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UNITED STATES

SECURITIES AND EXCHANGE COMMISSION

Washington, D. C. 20549

 

FORM 10-K

(Mark One)

 

 

☒

ANNUAL REPORT PURSUANT TO SECTION 13 OR 15(d) OF THE SECURITIES EXCHANGE ACT OF 1934

For the fiscal year ended June 30, 2026

OR

 

☐

TRANSITION REPORT PURSUANT TO SECTION 13 OR 15(d) OF THE SECURITIES EXCHANGE ACT OF 1934

 

For the transition period from to

 

Commission file number: 001-41655

 

 

img85804497_0.jpg

 

 

 

 

NioCorp Developments Ltd.

(Exact name of registrant as specified in its charter)

 

British Columbia, Canada

 

 

98-1262185

(State or other jurisdiction of incorporation or organization)

 

 

(I.R.S. Employer Identification No.)

 

 

7000 South Yosemite Street, Suite 115 Centennial, CO

(Address of principal executive offices)

80112

(Zip Code)

 

Registrant’s telephone number, including area code: (720) 334-7066

 

Securities registered pursuant to Section 12(b) of the Act:

 

Title of each class

Trading Symbol(s)

Name of each exchange on which registered

Common Shares, without par value

NB

The Nasdaq Stock Market LLC

Warrants, each exercisable for 1.11829212

Common Shares

NIOBW

The Nasdaq Stock Market LLC

Common Share Purchase Rights

N/A

The Nasdaq Stock Market LLC

 

Securities registered pursuant to section 12(g) of the Act: None.

 

Indicate by check mark if the registrant is a well-known seasoned issuer, as defined in Rule 405 of the Securities Act. Yes ☒ No ☐

 

Indicate by check mark if the registrant is not required to file reports pursuant to Section 13 or Section 15(d) of the Act. Yes ☐ No ☒

 

Indicate by check mark whether the registrant (1) has filed all reports required to be filed by Section 13 or 15(d) of the Securities Exchange Act of 1934 during the preceding 12 months (or for such shorter period that the registrant was required to file such reports), and (2) has been subject to such filing requirements for the past 90 days. Yes ☒ No ☐

 

Indicate by check mark whether the registrant has submitted electronically every Interactive Data File required to be submitted pursuant to Rule 405 of Regulation S-T (§232.405 of this chapter) during the preceding 12 months (or for such shorter period that the registrant was required to submit such files). Yes ☒ No ☐

 

Indicate by check mark whether the registrant is a large accelerated filer, an accelerated filer, a non-accelerated filer, a smaller reporting company, or an emerging growth company. See the definitions of “large accelerated filer,” “accelerated filer,” “smaller reporting company,” and “emerging growth company” in Rule 12b-2 of the Exchange Act.

 

 

Large Accelerated Filer

☐

Accelerated Filer

☐

 

Non-Accelerated Filer

☒

Smaller Reporting Company

☒

 

 

 

Emerging Growth Company

☐

 

If an emerging growth company, indicate by check mark if the registrant has elected not to use the extended transition period for complying with any new or revised financial accounting standards provided pursuant to Section 13(a) of the Exchange Act. ☐

 

Indicate by check mark whether the registrant has filed a report on and attestation to its management’s assessment of the effectiveness of its internal control over financial reporting under Section 404(b) of the Sarbanes-Oxley Act (15 U.S.C. 7262(b)) by the registered public accounting firm that prepared or issued its audit report. ☐

 

If securities are registered pursuant to Section 12(b) of the Act, indicate by check mark whether the financial statements of the registrant included in the filing reflect the correction of an error to previously issued financial statements. ☐

 

Indicate by check mark whether any of those error corrections are restatements that required a recovery analysis of incentive-based compensation received by any of the registrant’s executive officers during the relevant recovery period pursuant to §240.10D-1(b). ☐

 

Indicate by check mark whether the registrant is a shell company (as defined in Rule 12b-2 of the Exchange Act). Yes ☐ No ☒

 

At December 31, 2025, the aggregate market value of the registrant’s voting and non-voting common equity held by non-affiliates of the registrant was $622.4 million based on the closing sale price as reported on the Nasdaq Stock Market. There were 145,849,630 common shares outstanding on September 25, 2026.

 

 

DOCUMENTS INCORPORATED BY REFERENCE

 

Not applicable.

1


 

TABLE OF CONTENTS

Table of Contents

 

 

Select Mining Definitions

i

 

Mineral Reserves and Resources

v

 

Currency

v

 

Risk Factors Summary

v

PART I

1

 

ITEM 1.

BUSINESS

1

 

 

 

Introduction

1

 

 

 

Business Operations

1

 

 

 

Corporate Structure

2

 

 

 

Historical Development of the Business

2

 

 

 

Recent Corporate Events

3

 

 

 

Competitive Business Conditions

4

 

 

 

Cycles

4

 

 

 

Economic Dependence

5

 

 

 

Government Regulation

5

 

 

 

Human Capital

6

 

 

 

Forward-Looking Statements

7

 

 

 

Available Information

9

 

ITEM 1A.

RISK FACTORS

9

 

 

 

Risks Related to Our Business

9

 

 

 

Risks Related to Mining and Development

14

 

 

 

Risks Related to Government Regulation

20

 

 

 

Risks Related to Our Debt

22

 

 

 

Risks Related to the Common Shares

22

 

ITEM 1B.

UNRESOLVED STAFF COMMENTS

25

 

ITEM 1C.

CYBERSECURITY

25

 

ITEM 2.

PROPERTIES

25

 

ITEM 3.

LEGAL PROCEEDINGS

40

 

ITEM 4.

MINE SAFETY DISCLOSURES

40

PART II

41

 

ITEM 5.

MARKET FOR REGISTRANT’S COMMON EQUITY, RELATED STOCKHOLDER MATTERS, AND ISSUER PURCHASES OF EQUITY SECURITIES

41

 

 

 

Market Information

41

 

 

 

Holders

41

 

 

 

Dividends

41

 

 

 

Securities Authorized for Issuance Under Equity Compensation Plans

41

 

 

 

Purchases of Equity Securities by the Company

41

 

 

 

Recent Sales of Unregistered Securities

41

 

 

 

Exchange Controls

41

 

 

 

Certain Canadian Federal Income Tax Considerations for U.S. Residents

41

 

ITEM 6.

RESERVED

43

 

ITEM 7.

MANAGEMENT’S DISCUSSION AND ANALYSIS OF FINANCIAL CONDITION AND RESULTS OF OPERATIONS

44

 

 

 

Summary of Consolidated Financial and Operating Performance

44

 

 

 

Results of Operations

44

 

 

 

Liquidity and Capital Resources

45

 

 

 

Cash Flow Considerations

49

 

 

 

Environmental

50

 

 

 

Forward-Looking Statements

50

 

 

 

Accounting Developments

50

 

 

 

Critical Accounting Estimates and Recent Accounting Pronouncements

50

 

 

 

Other

51

 


 

 

ITEM 7A.

QUANTITATIVE AND QUALITATIVE DISCLOSURES ABOUT MARKET RISK

52

 

 

 

Interest rate risk

52

 

 

 

Foreign currency exchange risk

52

 

 

 

Commodity price risk

52

 

ITEM 8.

FINANCIAL STATEMENTS AND SUPPLEMENTARY DATA

52

 

ITEM 9.

CHANGES IN AND DISAGREEMENTS WITH ACCOUNTANTS ON ACCOUNTING AND FINANCIAL DISCLOSURE.

83

 

ITEM 9A.

CONTROLS AND PROCEDURES

83

 

ITEM 9B.

OTHER INFORMATION

85

 

ITEM 9C.

DISCLOSURE REGARDING FOREIGN JURISDICTIONS THAT PREVENT INSPECTION

85

PART III

86

 

ITEM 10.

DIRECTORS, EXECUTIVE OFFICERS AND CORPORATE GOVERNANCE

86

 

ITEM 11.

EXECUTIVE COMPENSATION

91

 

ITEM 12.

SECURITY OWNERSHIP OF CERTAIN BENEFICIAL OWNERS AND MANAGEMENT AND RELATED STOCKHOLDER MATTERS

100

 

ITEM 13.

CERTAIN RELATIONSHIPS AND RELATED TRANSACTIONS, AND DIRECTOR INDEPENDENCE

102

 

ITEM 14.

PRINCIPAL ACCOUNTANT FEES AND SERVICES

104

PART IV

105

 

ITEM 15.

EXHIBITS AND FINANCIAL STATEMENT SCHEDULES

105

 

ITEM 16.

FORM 10–K SUMMARY

109

SIGNATURES

110

 


 

Select Mining Definitions

 

2022 S-K 1300 Elk Creek Technical Report Summary

A technical report summary for the Elk Creek Project that conforms to S-K 1300 reporting standards, with an effective date of June 30, 2022, originally filed as Exhibit 96.1 to the Company’s Annual Report on Form 10-K for the year ended June 30, 2022.

2026 NI 43-101 Elk Creek Technical Report

The CIM-compliant NI 43-101 technical report for the Elk Creek Project with an effective date of August 10, 2026.

2026 S-K 1300 Elk Creek Technical Report Summary

A technical report summary for the Elk Creek Project that conforms to S-K 1300 reporting standards, with an effective date of June 30, 2026, filed as Exhibit 96.1 to this Annual Report on Form 10-K and incorporated by reference herein.

2026 Elk Creek Study

A pre-feasibility study, completed in 2026, prepared by qualified persons for the Elk Creek Project.

carbonatite

A type of intrusive or extrusive igneous rock defined by mineralogic composition consisting of greater than 50% carbonate minerals.

CIM

Canadian Institute of Mining and Metallurgy.

cut-off grade

The grade (i.e., the concentration of metal or mineral in rock) that determines the destination of the material during mining. For purposes of establishing “prospects of economic extraction,” the cut-off grade is the grade that distinguishes material deemed to have no economic value (it will not be mined in underground mining or if mined in surface mining, its destination will be the waste dump) from material deemed to have economic value (its ultimate destination during mining will be a processing facility). Other terms used in similar fashion as cut-off grade include net smelter return, pay limit, and break-even stripping ratio.

deposit

A mineralized body which has been physically delineated by sufficient drilling, trenching, and/or underground work, and found to contain a sufficient average grade of metal or metals to warrant further exploration and/or development expenditures. Such a deposit does not qualify as a commercially mineable ore body or as containing reserves or ore, unless final legal, technical, and economic factors are resolved.

development stage issuer

An issuer that is engaged in the preparation of mineral reserves for extraction on at least one material property.

development stage property

A property that has mineral reserves disclosed, pursuant to Regulation S-K 1300, but no material extraction.

diamond drilling

A type of rotary drilling in which diamond bits are used as the rock-cutting tool to produce a recoverable drill core sample of rock for observation and analysis.

dysprosium or Dy

The element dysprosium (atomic number 66), a rare-earth element in the lanthanide series.

dysprosium oxide

The chemical compound composed of dysprosium and oxygen with the formula Dy2O3.

economically viable

When used in the context of mineral reserve determination, means that the qualified person has determined, using a discounted cash flow analysis, or has otherwise analytically determined, that extraction of the mineral reserve is economically viable under reasonable investment and market assumptions.

Elk Creek Project

The Company’s critical minerals project located near Elk Creek, Nebraska that is expected to produce niobium, scandium, titanium, and several rare earth products, including neodymium-praseodymium oxide, dysprosium oxide, terbium oxide, SEG carbonate, and heavy rare earth carbonate

feasibility study

A comprehensive technical and economic study of the selected development option for a mineral project, which includes detailed assessments of all applicable modifying factors, as defined under S-K 1300, together with any other relevant operational factors, and detailed financial analysis that are necessary to demonstrate, at the time of reporting, that extraction is economically viable. The results of the study may serve as the basis for a final decision by a proponent or financial institution to proceed with, or finance, the development of the project.

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(1)
A feasibility study is more comprehensive, and with a higher degree of accuracy, than a pre-feasibility study. It must contain mining, infrastructure, and process designs completed with sufficient rigor to serve as the basis for an investment decision or to support project financing.
(2)
The confidence level in the results of a feasibility study is higher than the confidence level in the results of a pre-feasibility study. Terms such as full, final, comprehensive, bankable, or definitive feasibility study are equivalent to feasibility study.

ferroniobium or FeNb

An iron-niobium alloy, with a niobium content of 60-70%.

indicated mineral resource

That part of a mineral resource for which quantity and grade or quality are estimated on the basis of adequate geological evidence and sampling. The level of geological certainty associated with an indicated mineral resource is sufficient to allow a qualified person to apply modifying factors in sufficient detail to support mine planning and evaluation of the economic viability of the deposit. Because an indicated mineral resource has a lower level of confidence than the level of confidence of a measured mineral resource, an indicated mineral resource may only be converted to a probable mineral reserve.

inferred mineral resource

That part of a mineral resource for which quantity and grade or quality are estimated on the basis of limited geological evidence and sampling. The level of geological uncertainty associated with an inferred mineral resource is too high to apply relevant technical and economic factors likely to influence the prospects of economic extraction in a manner useful for evaluation of economic viability. Because an inferred mineral resource has the lowest level of geological confidence of all mineral resources, which prevents the application of the modifying factors in a manner useful for evaluation of economic viability, an inferred mineral resource may not be considered when assessing the economic viability of a mining project, and may not be converted to a mineral reserve.

LoM

Life of Mine, the period from the beginning of construction to the end of mine life.

measured mineral resource

That part of a mineral resource for which quantity and grade or quality are estimated on the basis of conclusive geological evidence and sampling. The level of geological certainty associated with a measured mineral resource is sufficient to allow a qualified person to apply modifying factors, as defined in this section, in sufficient detail to support detailed mine planning and final evaluation of the economic viability of the deposit. Because a measured mineral resource has a higher level of confidence than the level of confidence of either an indicated mineral resource or an inferred mineral resource, a measured mineral resource may be converted to a proven mineral reserve or to a probable mineral reserve.

mineral reserve

An estimate of tonnage and grade or quality of indicated and measured mineral resources that, in the opinion of the qualified person, can be the basis of an economically viable project. More specifically, it is the economically mineable part of a measured or indicated mineral resource, which includes diluting materials and allowances for losses that may occur when the material is mined or extracted.

mineral resource

A concentration or occurrence of material of economic interest in or on the Earth's crust in such form, grade or quality, and quantity that there are reasonable prospects for economic extraction. A mineral resource is a reasonable estimate of mineralization, taking into account relevant factors such as cut-off grade, likely mining dimensions, location or continuity, that, with the assumed and justifiable technical and economic conditions, is likely to, in whole or in part, become economically extractable. It is not merely an inventory of all mineralization drilled or sampled.

modifying factors

The factors that a qualified person must apply to indicated and measured mineral resources and then evaluate in order to establish the economic viability of mineral reserves. A qualified person must apply and evaluate modifying factors to convert measured and indicated mineral resources to proven and probable mineral reserves. These factors include, but are not restricted to: mining; processing; metallurgical; infrastructure; economic; marketing; legal; environmental compliance; plans, negotiations, or agreements with local individuals or groups; and governmental factors. The number, type and specific characteristics of the modifying factors applied will necessarily be a function of and depend upon the mineral, mine, property, or project.

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NI 43-101

National Instrument 43-101 of the Canadian Securities Administrators entitled “Standards of Disclosure for Mineral Projects”

niobium or Nb

The element niobium (atomic number 41), a transition metal primarily used in the production of high-strength, low-alloy steel

Nb2O5

Niobium pentoxide, a commercial form of refined niobium

neodymium oxide

The chemical compound composed of neodymium and oxygen with the formula Nd2O3

NSR

Net Smelter Return, the net revenue that the owner of a mining property receives from the sale of the mine's products less transportation and refining costs

praseodymium oxide

The chemical compound composed of praseodymium and oxygen with the formula Pr2O3

preliminary feasibility study

(or pre-feasibility study)
 

A comprehensive study of a range of options for the technical and economic viability of a mineral project that has advanced to a stage where a qualified person has determined (in the case of underground mining) a preferred mining method, or (in the case of surface mining) a pit configuration, and in all cases has determined an effective method of mineral processing and an effective plan to sell the product.

(1)
A pre-feasibility study includes a financial analysis based on reasonable assumptions, based on appropriate testing, about the modifying factors and the evaluation of any other relevant factors that are sufficient for a qualified person to determine if all or part of the indicated and measured mineral resources may be converted to mineral reserves at the time of reporting. The financial analysis must have the level of detail necessary to demonstrate, at the time of reporting, that extraction is economically viable.
(2)
A pre-feasibility study is less comprehensive and results in a lower confidence level than a feasibility study. A pre-feasibility study is more comprehensive and results in a higher confidence level than an initial assessment.

probable mineral reserve

The economically mineable part of an indicated and, in some cases, a measured mineral resource

production stage property

A property with material extraction of mineral reserves

proven mineral reserve

The economically mineable part of a measured mineral resource and can only result from conversion of a measured mineral resource

qualified person

An individual who is:

(1)
A mineral industry professional with at least five years of relevant experience in the type of mineralization and type of deposit under consideration and in the specific type of activity that person is undertaking on behalf of the registrant; and
(2)
An eligible member or licensee in good standing of a recognized professional organization at the time the technical report is prepared. For an organization to be a recognized professional organization, it must:
(i)
Be either:
(A)
An organization recognized within the mining industry as a reputable professional association; or
(B)
A board authorized by United States federal, state, or foreign statute to regulate professionals in the mining, geoscience, or related field;
(ii)
Admit eligible members primarily on the basis of their academic qualifications and experience;
(iii)
Establish and require compliance with professional standards of competence and ethics;
(iv)
Require or encourage continuing professional development;
(v)
Have and apply disciplinary powers, including the power to suspend or expel a member regardless of where the member practices or resides; and
(vi)
Provide a public list of members in good standing.

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rare earth elements, rare earths or REEs

A group of 17 elements, primarily the 15 lanthanide elements. Lanthanum, cerium, praseodymium, neodymium and promethium are considered “light” REE; samarium, europium and gadolinium are often referred to as “medium” REE; while terbium, dysprosium, holmium, erbium, thulium, ytterbium and lutetium are considered “heavy” REE (“HREE”). Two additional elements, yttrium and scandium, are often classified as HREE although they are not lanthanides. Yttrium and scandium are also included in this categorization because they exhibit similar properties to the lanthanides and are found in the same ore bodies. Individual mineral deposits may not contain all REEs in economically recoverable quantities.

rare earth products

Commercial rare earth products currently being examined for production by the Company, including neodymium-praseodymium oxide (sometimes referred to as didymium oxide), dysprosium oxide, and terbium oxide. These are the primary rare earths compounds used to manufacture the world’s most powerful permanent magnets.

relevant experience

For purposes of determining whether a party is a qualified person, that the party has experience in the specific type of activity that the person is undertaking on behalf of the registrant. If the qualified person is preparing or supervising the preparation of a technical report concerning exploration results, the relevant experience must be in exploration. If the qualified person is estimating, or supervising the estimation of mineral resources, the relevant experience must be in the estimation, assessment and evaluation of mineral resources and associated technical and economic factors likely to influence the prospect of economic extraction. If the qualified person is estimating, or supervising the estimation of mineral reserves, the relevant experience must be in engineering and other disciplines required for the estimation, assessment, evaluation, and economic extraction of mineral reserves.

(1)
Relevant experience also means, for purposes of determining whether a party is a qualified person, that the party has experience evaluating the specific type of mineral deposit under consideration (e.g., coal, metal, base metal, industrial mineral, or mineral brine). The type of experience necessary to qualify as relevant is a facts and circumstances determination. For example, experience in a high-nugget, vein-type mineralization such as tin or tungsten would likely be relevant experience for estimating mineral resources for vein-gold mineralization, whereas experience in a low grade disseminated gold deposit likely would not be relevant.

Note 1 to Paragraph (1) of the Definition of Relevant Experience: It is not always necessary for a person to have five years' experience in each and every type of deposit in order to be an eligible qualified person if that person has relevant experience in similar deposit types. For example, a person with 20 years' experience in estimating mineral resources for a variety of metalliferous hard-rock deposit types may not require as much as five years of specific experience in porphyry-copper deposits to act as a qualified person. Relevant experience in the other deposit types could count towards the experience in relation to porphyry-copper deposits.

(2)
For a qualified person providing a technical report for exploration results or mineral resource estimates, relevant experience also requires, in addition to experience in the type of mineralization, sufficient experience with the sampling and analytical techniques, as well as extraction and processing techniques, relevant to the mineral deposit under consideration. Sufficient experience means that level of experience necessary to be able to identify, with substantial confidence, problems that could affect the reliability of data and issues associated with processing.
(3)
For a qualified person applying the modifying factors, as defined by this section, to convert mineral resources to mineral reserves, relevant experience also requires:
(i)
Sufficient knowledge and experience in the application of these factors to the mineral deposit under consideration; and
(ii)
Experience with the geology, geostatistics, mining, extraction, and processing that is applicable to the type of mineral and mining under consideration.

S-K 1300

Subpart 1300 of Regulation S-K promulgated by the United States Securities and Exchange Commission

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scandium or Sc

The element scandium (atomic number 21), a transition metal used as an alloying agent with aluminum that provides high strength and lower weight for aerospace industry components and other applications that need lightweight metals. It also is used in the electrolyte layer of solid oxide fuel cells.

Sc2O3

Scandium trioxide, the primary form of refined scandium

SEG carbonate

Samarium-europium-gadolinium carbonate

terbium oxide

The chemical compound composed of terbium and oxygen with the formula Tb2O3

titanium or Ti

The element titanium (atomic number 22), a transition metal which in its oxide form is a common pigment in paper, paint, and plastic. In its metallic form, titanium is used in aerospace applications, armor, chemical processing applications, marine hardware applications, medical implants, power generation, and in sporting goods.

TiCl4

Titanium tetrachloride, an input for the production of high-purity titanium oxides and compounds

TiO2

Titanium dioxide, a commercial form of refined titanium

TREO

Total Rare Earth Oxides, the sum of all rare earth element oxides in a mineral deposit

 

Mineral Reserves and Resources

Information, including all mineral resource and mineral reserve estimates, concerning the Elk Creek Project in this Annual Report on Form 10-K has been prepared in accordance with the requirements of S-K 1300 and is based on the 2026 S-K 1300 Elk Creek Technical Report Summary, filed as Exhibit 96.1 to this Annual Report on Form 10-K. S-K 1300 requires us to disclose our mineral resources, in addition to our mineral reserves, as of the end of our most recently completed fiscal year. You are cautioned that mineral resources are subject to further exploration and development and are subject to additional risks and no assurance can be given that they will eventually convert to future reserves. Inferred resources, in particular, have a great amount of uncertainty as to their existence and their economic and legal feasibility. Investors are cautioned not to assume that any part or all of the inferred resource exists or is economically or legally mineable. In addition, the economic analysis described in the 2026 S-K 1300 Elk Creek Technical Report Summary was conducted in connection with the 2026 Elk Creek Study to demonstrate economic viability and support the determination of mineral reserves and is based on assumptions relating to discount rate, production rates, commodity prices, operating costs, capital expenditures, and other inputs that are subject to significant uncertainty. The results of the economic analysis are not a forecast or prediction of actual results for the periods covered, and actual results may differ materially from those projected by the economic analysis. There can be no assurance that the assumptions underlying the economic analysis will prove to be accurate or that the projected economics of the Elk Creek Project will be realized. See Item 1A., Risk Factors.

Currency

All dollar amounts in this Annual Report on Form 10-K are expressed in thousands of United States (“U.S.”) dollars unless otherwise indicated. The Company’s accounts are maintained in U.S. dollars and the Company’s consolidated financial statements are prepared in accordance with U.S. generally accepted accounting principles (“U.S. GAAP”).

 

Risk Factors Summary

Investing in common shares, no par value, of the Company (“Common Shares”) involves numerous risks and uncertainties, as more fully described below. You should read these risks before you invest in our Common Shares. In particular, risks associated with our business include, but are not limited to, the following:

Risks Related to Our Business

•
We will require significant additional capital to fund our business plan.
•
We have a limited operating history on which to base an evaluation of our business and prospects.
•
We have a history of losses and expect to continue to incur losses in the future.
•
We may be unable to successfully negotiate final, definitive offtake agreements, which could have a material adverse effect on our ability to secure project financing and establish the commercial viability of the Elk Creek Project.

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•
Any failure of our counterparties to meet their obligations to us or to third parties with respect to our offtake
agreements, supply agreements or other commercial agreements could have a material adverse effect on our ability
to secure project financing and establish the commercial viability of the Elk Creek Project.
•
We may not receive any proceeds from the exercise of our outstanding Common Share purchase warrants (“Warrants”), and the potential adverse effect on the prevailing market prices for our Common Shares as a result of sales, or the perception of future sales, of Common Shares could adversely affect our ability to raise additional capital.
•
The Company has identified a material weakness in its internal control over financial reporting. If not remediated, the Company’s failure to establish and maintain effective disclosure controls and procedures and internal control over financial reporting could result in material misstatements in its financial statements and a failure to meet its reporting and financial obligations, each of which could have a material adverse effect on the Company’s financial condition and the trading price of the Common Shares.

Risks Related to Mining and Development

•
We face numerous uncertainties in estimating our mineral reserves and resources and inaccuracies in our estimates could result in lower than expected revenues, higher than expected costs and decreased profitability.
•
Price volatility could have dramatic effects on our results of operations and our ability to obtain financing for the Elk
Creek Project and execute our business plan.
•
The nature of mineral exploration and production activities involves a high degree of risk and the possibility of uninsured losses.
•
We have no history of producing commercial products from our current mining properties and there can be no assurance that we will successfully establish mining operations or profitably produce minerals.
•
The success of our business will depend, in part, on the growth of existing and emerging uses for scandium and rare
earth products.
•
Any material changes in mineral resource/reserve estimates and grades of mineralization will affect the economic viability of placing a property into production and a property’s return on capital.
•
Our properties and operations may be subject to litigation or other claims.
•
We do not currently insure against all the risks and hazards of mineral exploration, development, and mining operations.

Risks Related to Government Regulation

•
We may not be able to obtain or renew all required permits and licenses to place any of our properties into production.
•
We are subject to significant governmental regulations that affect our operations and costs of conducting our business.
•
Land reclamation requirements for our properties may be burdensome and expensive.

Risks Related to Our Debt

•
The level of our indebtedness from time to time could impair our ability to obtain additional financing.

Risks Related to the Common Shares

•
Future sales, or the perception of future sales, of Common Shares by existing shareholders or by us, or future dilutive issuances of Common Shares by us, could adversely affect prevailing market prices for the Common Shares and cause investors to suffer dilution in their net book value per Common Share.
•
We are subject to the continued listing criteria of The Nasdaq Stock Market LLC (“Nasdaq”) and our failure to satisfy these criteria may result in delisting of the Common Shares.
•
Our Rights Plan (as defined below) includes terms and conditions that could discourage a take-over or other transaction that shareholders may consider favorable.

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PART I

ITEM 1. BUSINESS

Introduction

NioCorp Developments Ltd. (“NioCorp,” “we,” “us,” “our,” or the “Company”) was incorporated under the laws of the Province of British Columbia under the Business Corporations Act (British Columbia) on February 27, 1987, under the name “IPC International Prospector Corp.” On May 22, 1991, we changed our name to “Kingston Resources Ltd.” On June 29, 2001, we changed our name to “Butler Developments Corp.” On February 12, 2009, we changed our name to “Butler Resource Corp.” On March 4, 2010, we changed our name to “Quantum Rare Earth Developments Corp.” On March 4, 2013, we changed our name to “NioCorp Developments Ltd.”

NioCorp is a United States Securities and Exchange Commission (“SEC”) reporting company, and we are also a Canadian reporting issuer in British Columbia, Alberta, Saskatchewan, Ontario, and New Brunswick. Our registered and records office is located at 1133 Melville Street, Suite 3500, Vancouver, British Columbia V6E 4E5 (ATTN: Blake, Cassels & Graydon LLP). Our principal executive office is located at 7000 South Yosemite Street, Suite 115, Centennial, Colorado 80112.

Business Operations

NioCorp, through ECRC (as defined below), is developing a critical minerals project that, if and when developed, will produce niobium, scandium, titanium and several rare earth products, including neodymium-praseodymium oxide, dysprosium oxide, terbium oxide, samarium-europium-gadolinium (“SEG”) carbonate, and heavy rare earth carbonate. Known as the “Elk Creek Project,” it is located near Elk Creek, Nebraska, in the southeast portion of the state.

•
Niobium is used to produce various superalloys that are extensively used in high performance aircraft and jet turbines. It also is used in high-strength, low-alloy steel, a stronger steel used in automobiles, bridges, structural systems, buildings, pipelines, and other applications that generally enables those applications to be stronger and lighter in mass. This “lightweighting” benefit often results in environmental benefits, including reduced fuel consumption and material usage, which can result in fewer air emissions.
•
Scandium can be combined with aluminum to make super-high-performance alloys with increased strength and improved corrosion resistance. Scandium also is a critical component of advanced solid oxide fuel cells, which are increasingly being deployed to provide reliable, on-site power for energy-intensive artificial intelligence data centers.
•
Titanium is a component of various superalloys and other applications that are used for aerospace applications, weapons systems, protective armor, medical implants and many others. It also is used in pigments for paper, paint, and plastics.
•
Rare earth elements are critical minerals that are needed in virtually all U.S. defense systems and across the electronics, manufacturing, high-technology, transportation, and energy sectors. Magnetic rare earths, such as neodymium, praseodymium, terbium, and dysprosium are critical to the making of neodymium-iron-boron magnets, which are used in critical defense systems, electric vehicles, advanced automation, and robotics.

Our primary business strategy is to advance our Elk Creek Project to commercial production. We are focused on securing project financing sufficient to cover initial capital costs and other related expenses necessary for the commencement and completion of construction, and carrying out our near-term planned work programs necessary to complete detailed design, development, and construction of the Elk Creek Project, as well as the commencement of early elements of project construction.

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Corporate Structure

The Company’s business operations are conducted primarily through ECRC. The table below provides an overview of the Company’s current subsidiaries and their activities:

 

Name

 

State/Province of Formation

 

Ownership

 

Business

0896800 B.C. Ltd. (“0896800”)

 

British Columbia

 

100%

 

The only business of 0896800 is to hold the shares of Class A common stock of ECRC

Elk Creek Resources Corp. (“ECRC”)

 

Delaware

 

81.33%(1)

 

The business of ECRC is the development of the Elk Creek Project

NioCorp Advanced Metals and Alloys, LLC ("NAMA")

 

Delaware

 

100%

 

The business of NAMA is the production of scandium-containing aluminum master alloys

NioCorp Technologies Limited

 

United Kingdom

 

100%

 

The business of NioCorp Technologies Limited is the research and development of aluminum-scandium alloys and other business opportunities

 

(1)
Represents 100% of Class A common stock owned by 0896800, and 3,516,140 Vested Shares and 3,391,596 Earnout Shares (each as defined below) held by third parties, and outstanding as of June 30, 2026.

Historical Development of the Business

The acquisition of the carbonatite property located in Southeast Nebraska, USA (the “Elk Creek Property”) was closed in December 2010 and involved the purchase by NioCorp of all of the issued and outstanding common shares of a private British Columbia company, which in turn held 100% of the issued and outstanding shares of Elk Creek Resources Corp., a Nebraska corporation.

Between 2011 and 2020, the Company advanced the Elk Creek Project through the completion of field exploration programs, feasibility study development and reporting, updates to underground mine designs and supporting infrastructure, and the receipt of required permits from the State of Nebraska.

During fiscal year 2021, we obtained funding which allowed us to purchase land and mineral rights at the Elk Creek Property and continue early project execution activities. During fiscal year 2022, we focused efforts towards refining our Elk Creek Project mineral resource and mineral reserve estimates with respect to REEs. This work included additional assays of historical drill core to fill data gaps in the existing resource database and re-modeling. Based on this re-interpretation of the geologic data, an update to the mine plan was also completed. Based on this work, we issued a NI 43-101 technical report on June 28, 2022, and filed the 2022 S-K 1300 Elk Creek Technical Report Summary as an exhibit to our Annual Report on Form 10-K for the year ended June 30, 2022.

On March 17, 2023 (the “Closing Date”), the Company closed a series of transactions (the “GXII Transaction”) pursuant to the Business Combination Agreement, dated September 25, 2022 (the “Business Combination Agreement”), among the Company, GX Acquisition Corp. II (“GXII”), and Big Red Merger Sub Ltd (the “Closing”).

As a result of the GXII Transaction, among other matters, GXII became an indirect, majority-owned subsidiary of NioCorp and changed its name to “Elk Creek Resources Corp.”, which we refer to as “ECRC,” and the Common Shares and the Warrants that were assumed by NioCorp from GXII (the “NioCorp Assumed Warrants”) were listed for trading on Nasdaq under the symbols “NB” and “NIOBW,” respectively.

Pursuant to the Business Combination Agreement, the Sponsor Support Agreement, dated September 25, 2022, among GX Sponsor II LLC (the “Sponsor”), GXII, the Company and the other persons party thereto, and the Exchange Agreement, dated as of March 17, 2023, by and among NioCorp, ECRC and the Sponsor (the “Exchange Agreement”), after the Closing, the shares of Class B common stock of ECRC are exchangeable into Common Shares on a one-for-one basis, subject to certain equitable adjustments, under certain conditions. Of the issued and outstanding shares of Class B common stock of ECRC, 4,565,808 shares (the “Vested Shares”) were vested as of the Closing Date and are exchangeable at any time, and from time to time, until the tenth anniversary of the Closing Date and 3,391,596 shares (the “Earnout Shares”) are exchangeable until the tenth anniversary of the Closing Date, subject to certain vesting conditions. See Note 8 to the consolidated financial statements included in Part II, Item 8 hereof for additional information regarding the Class B common stock of ECRC.

In addition, during fiscal year 2026, the Company completed the acquisition of an additional 447.43 acres of land pursuant to existing option to purchase agreements ("OTPs"). As a result of these transactions, the Company now holds full ownership of all surface rights within the one-square-mile section in which it plans to construct both the underground critical minerals

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mine and integrated surface processing facility associated with the Elk Creek Project. These acquisitions also include 1.6 acres of land adjacent to Highway 50 and County Road 721 that will be used for improvements to both roadways in order to establish the entrance to the project site on the north side of the Company’s owned lands.

On December 4, 2025, the Company, through its newly-formed subsidiary, NAMA, completed the acquisition of the manufacturing assets and intellectual property of FEA Materials LLC for $8.4 million in cash. The acquired assets include equipment and proprietary technology used to produce aluminum-scandium ("Al-Sc") master alloy through an innovative process that converts scandium oxide directly into Al-Sc master alloy, eliminating the need to first manufacture scandium metal. This technology is expected to meaningfully reduce processing complexity and cost relative to traditional methods. The acquisition strengthens the Company’s downstream commercialization strategy by potentially enabling the future production of Al-Sc master alloy in the United States, subject to completion and financing of the Elk Creek Project.

On February 26, 2026, the Company announced that construction of the main access to the underground portion (the "Portal Project") of the Elk Creek Project had commenced. The construction of the Elk Creek Project mine’s main entrance, known as a “portal,” will serve as the primary access point for personnel, equipment, and materials, as well as to deliver ore from the underground mine to the surface production plant. The Company also filed a formal “Notice of Commencement” with the Mine Safety and Health Administration ("MSHA") in conjunction with this effort. The Portal Project has an overall budget of $44.6 million, and through June 30, 2026, the Company has incurred approximately $5.6 million in construction costs.

During fiscal year 2025, the Company initiated a drilling program at the Elk Creek Project to support the conversion of a portion of its current indicated resources into measured resources and the subsequent conversion of a portion of its current probable mineral reserves into proven mineral reserves. This drilling program and related assay work were completed in fiscal year 2026, and formed the basis of the updated 2026 Elk Creek Study, which is summarized in the 2026 S-K 1300 Elk Creek Technical Report Summary filed as Exhibit 96.1 to this Annual Report on Form 10-K and as more fully described below under Item 2. “Properties.”

Recent Corporate Events

EXIM Bank Financing Process

As previously disclosed, on March 6, 2023, the Company announced the receipt of a Letter of Interest from the Export-Import Bank of the United States (“EXIM”) for potential debt financing, which may include a loan or loan guarantee, through EXIM’s “Make More in America” initiative to fund a portion of the project costs of the Elk Creek Project (the “EXIM Financing”).

NioCorp submitted a formal application to EXIM under EXIM’s “Make More in America” initiative on June 6, 2023. The Company was informed that its application received approval by the first of three reviews by the EXIM Transaction Review Committee on October 2, 2023. EXIM deployed additional resources to the processing of the Company’s application during the quarter ended December 31, 2023, and has retained financial and legal consultants to support EXIM’s due diligence on the Elk Creek Project. On April 15, 2024, the Company received a Preliminary Project Letter (the “PPL”) from EXIM. The PPL is a summary of EXIM’s initial due diligence findings and also includes a preliminary Indicative Term Sheet. The PPL identified additional project activities to be undertaken by the Company in conjunction with the EXIM evaluation process. These include an updated mine plan and updated Elk Creek Project capital costs on a final or close-to-final basis reflecting updated process flows.

NioCorp continues to work with EXIM to advance the Elk Creek Project through EXIM’s due diligence and loan application process. The completion of the 2026 Elk Creek Study satisfies a key EXIM due diligence requirement reflected in the PPL, and the Company now expects to advance to the next steps of the process relating to detailed engineering, procurement and construction contracting. The PPL included an indicative term sheet, which left open the total estimated amount of the EXIM Financing and provided that the amount of the EXIM Financing that could be made available for the Elk Creek Project will be scaled based on the number of U.S. jobs supported, both during construction and over the life of EXIM’s financing, subject to certain expectations regarding the ratio of debt-to-equity financing for the Elk Creek Project. The Company believes that the updated 2026 Elk Creek Study, with its updated economic analysis, mineral resource and mineral reserve estimates, and increased job creation projections, demonstrates that the Elk Creek Project satisfies the criteria for increased financing as contemplated by the PPL. However, NioCorp is currently unable to estimate the total amount of the EXIM Financing, if any, as well as how long the application process, including additional project activities identified by EXIM, may take, and there can be no assurances that NioCorp will be able to successfully negotiate a final commitment for the EXIM Financing, on acceptable terms, or at all.

During the fiscal year ended June 30, 2026, the Company raised approximately $467.2 million in net proceeds from equity financing transactions, which involved the issuance and sale of Common Shares, and pre-funded warrants to purchase Common Shares, in a series of registered offerings. For further discussion, see Part II, Item 7, “Management’s Discussion and Analysis of Financial Condition and Results of Operations—Liquidity and Capital Resources.”

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DoW Agreement

On August 4, 2025, ECRC entered into a Project Sub-Agreement (the “DoW Agreement”) with Advanced Technology International, an entity acting on behalf of the Defense Industrial Base Consortium under the authority of the U.S. Department of War (“DoW”). Subject to the terms and conditions of the DoW Agreement, ECRC is entitled to receive up to an aggregate of approximately $10.0 million of reimbursement payments from the DoW upon the achievement of certain project milestones related to engineering and additional reserve drilling, as well as preparing updated cost estimates, for the Elk Creek Project. As of June 30, 2026, NioCorp has received approximately $8.1 million of reimbursement payments under the DoW Agreement.

Shareholder Rights Plan Agreement

On November 21, 2025, the Company adopted a limited-duration shareholder rights plan (the "Rights Plan") pursuant to a Shareholder Rights Plan Agreement dated November 21, 2025 (the "Original Rights Plan Agreement"), between the Company and Computershare Investor Services Inc., as rights agent (the "Rights Agent"). One right (a "Right") was issued for each Common Share outstanding as of December 4, 2025, and a Right automatically attaches to each Common Share subsequently issued until the expiration of the Rights Plan. The Rights generally become exercisable only if a person or group acquires, or announces the current intention of commencing a take-over bid to acquire, beneficial ownership of 20% or more of the Company's outstanding Common Shares, other than through a permitted bid made in compliance with applicable Canadian take-over bid rules. If the Rights become exercisable, each holder of a Right, other than the acquiring person, would be entitled to purchase additional Common Shares at a discount to the then-current market price. The Rights Plan was not adopted in response to any specific take-over proposal. On April 6, 2026, following approval by the Company's shareholders at the Company's annual general meeting held on April 6, 2026, the Company and the Rights Agent entered into an Amended and Restated Shareholder Rights Plan Agreement (the "Amended Rights Plan Agreement"), which amended and restated the Original Rights Plan Agreement in its entirety. Under the Original Rights Plan Agreement, the Rights Plan would have expired on May 21, 2026. Under the Amended Rights Plan Agreement, the Rights Plan now expires at 5:00 p.m. (Toronto time) on the date of the Company's next annual general meeting.

Competitive Business Conditions

There is significant competition within the minerals industry to discover, acquire, and obtain project financing for, mineral properties considered to have commercial potential. We compete with others in efforts to obtain project financing and resources to advance the Elk Creek Project to construction and commercial operation, acquire and utilize mining and processing equipment, and hire qualified personnel. These other companies may be better capitalized than us and we may have difficulty in obtaining the financing and resources necessary to advance the Elk Creek Project to construction and commercial operation. There is currently a significant focus on domestic critical mineral supply among potential producers, processors and the U.S. Government. This includes recent government financing and policy support announced for other potential sources of critical minerals, which may alter the strategic importance of the Elk Creek Project and impact our ability to access funding or potential future government support. In addition, in competing for qualified personnel, we may be required to pay compensation or benefits relatively higher than those paid in the past, and the availability of qualified personnel may be limited in high-demand periods.

Once the Elk Creek Project begins commercial operation, we expect to face significant competition both domestically and globally for our products. The most prominent global competitor is China, which controls a substantial majority of the world’s scandium and REE production. China’s scandium and rare earth industries benefit from extensive government support, allowing Chinese companies to offer scandium and REEs at subsidized prices, often undercutting other producers. Moreover, Chinese companies have invested heavily in improving their processing capabilities, giving them a technological and cost advantage in the global market, and we believe, at the expense of world sustainability and labor standards. In recent years, China has also begun to implement export controls limiting the amount of scandium and REE products that are sold into the global market outside of China. We believe these controls have created a bifurcated market for scandium, dysprosium and terbium, causing prices outside China to be significantly higher than prices within China.

Cycles

The mining business is subject to mineral price cycles. The marketability of minerals and mineral concentrates is also affected by worldwide economic cycles. Demand has in the past, and may in the future, be subject to those same worldwide economic cycles. Fluctuations in supply and demand in various regions throughout the world are common. In addition, the niobium, scandium, titanium, and rare earth products, that we intend to produce at the Elk Creek Project are subject to additional commodity-specific price cycles resulting from, among other factors, demand for specific products, export controls, taxes and other tariffs and fees.

As NioCorp is a development stage issuer and has not yet generated any revenue from the operation of the Elk Creek Project, it is not currently significantly affected by changes in commodity demand and prices, except to the extent that these changes may impact the development of the Elk Creek Project. As it does not carry on production activities, NioCorp’s ability

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to fund ongoing exploration is affected by the availability of financing, which is, in turn, affected by the strength of the economy and other general economic factors.

Economic Dependence

Other than land and mineral right option agreements and agreements between NioCorp and third parties for the purchase and sale of products to be produced from the Elk Creek Project (“offtake agreements”), NioCorp’s business is not substantially dependent on any contract such as a contract to sell the major part of its product or services or to purchase the major part of its requirements for goods, services or its raw materials, or any franchise or license or other agreement to use a patent, formula, trade secret, process or trade name upon which its business depends.

Government Regulation

The exploration and development of a mining prospect is subject to regulation by a number of federal and state government authorities. These include the United States Environmental Protection Agency (the “EPA”) and the United States Army Corps of Engineers (the “USACE”) as well as the various state and local environmental protection agencies. The regulations address many environmental issues relating to air, soil, and water contamination, and apply to many mining related activities including exploration, mine construction, mineral extraction, ore milling, water use, waste disposal, and use of toxic substances. In addition, we are subject to regulations relating to labor standards, occupational health and safety, mine safety, general land use, export of minerals, taxation, data protection, and data security. Many of the regulations require permits or licenses to be obtained, the absence of which and/or inability to obtain such permits or licenses will adversely affect our ability to conduct our exploration, development, and operation activities. The failure to comply with the regulations and terms of permits and licenses may result in fines or other penalties or in revocation of a permit or license or loss of a prospect.

General

While none of the lands on which the Elk Creek Project is proposed to be built are owned by the U.S. Government, mining rights on public lands are governed by the General Mining Law of 1872, as amended, which allows for the location of mining claims on certain federal lands upon the discovery of a valuable mineral deposit and compliance with location requirements. The exploration of mining properties and development and operation of mines is governed by both federal and state laws. Federal laws that govern mining claim location and maintenance and mining operations on federal lands are generally administered by the Bureau of Land Management. Additional federal laws, governing mine safety and health, also apply. State laws also require various permits and approvals before exploration, development or production operations can begin. Among other things, a reclamation plan must typically be prepared and approved, with financial assurance provided in the amount of projected reclamation costs. The financial assurance is used to ensure that proper reclamation takes place and will not be released until that time. Local jurisdictions may also impose permitting requirements, such as conditional use permits or zoning approvals.

Environmental Regulation

Our mineral projects are subject to various federal, state, and local laws and regulations governing protection of the environment. These laws are continually changing and, in general, are becoming more restrictive. The development, operation, closure, and reclamation of mining projects in the U.S. requires numerous notifications, permits, authorizations, and public agency decisions. Compliance with environmental and related laws and regulations requires us to obtain permits issued by regulatory agencies and to file various reports and keep records of our operations. Certain of these permits require periodic renewal or review of their conditions and may be subject to a public review process during which opposition to our proposed operations may be encountered. We are currently operating under various permits for activities connected to mineral exploration, reclamation, and environmental considerations. Our policy is to conduct business in a way that safeguards public health and the environment. We believe that our operations are conducted in material compliance with applicable laws and regulations.

Changes to current local, state, or federal laws and regulations in the jurisdictions where we operate could require additional capital expenditures and increased operating and/or reclamation costs. Although we are unable to predict what additional legislation, if any, might be proposed or enacted, additional regulatory requirements could impact the economics of our projects.

Environmental Regulation - U.S. Federal Laws

The Comprehensive Environmental Response, Compensation, and Liability Act (“CERCLA”), and comparable state statutes, impose strict, joint, and several liability on current and former owners and operators of sites and on persons who disposed of or arranged for the disposal of hazardous substances found at such sites. It is not uncommon for the government to file claims requiring clean-up actions and/or demands for reimbursement for government-incurred clean-up costs or natural resource damages. It is also not uncommon for neighboring landowners and other third parties to file claims for personal injury and property damage allegedly caused by hazardous substances released into the environment. The Resource Conservation and

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Recovery Act (“RCRA”), and comparable state statutes, govern the disposal of solid waste and hazardous waste and authorize the imposition of substantial fines and penalties for noncompliance, as well as requirements for corrective actions. CERCLA, RCRA, and comparable state statutes can impose liability for clean-up of sites and disposal of substances found on exploration, mining and processing sites long after activities on such sites have been completed.

The Clean Air Act, as amended (“CAA”), restricts the emission of air pollutants from many sources, including mining and processing activities. Any future mining operations by the Company may produce air emissions, including fugitive dust and other air pollutants from stationary equipment, storage facilities, and the use of mobile sources such as trucks and heavy construction equipment, which are subject to review, monitoring and/or control requirements under the CAA and state air quality laws. New facilities may be required to obtain permits before work can begin, and existing facilities may be required to incur capital costs in order to remain in compliance. In addition, permitting rules may impose limitations on our production levels or result in additional capital expenditures in order to comply with the rules.

The National Environmental Policy Act requires federal agencies to integrate environmental considerations into their decision-making processes by evaluating the environmental impacts of their proposed actions, including issuance of permits to mining facilities and assessing alternatives to those actions. If a proposed action could significantly affect the environment, the agency must prepare either a detailed statement known as an Environmental Impact Statement (“EIS”), or a less detailed statement known as an Environmental Assessment (“EA”). The EPA, other federal agencies, and any interested third parties can review and comment on the scope of the EIS or EA and the adequacy of any findings set forth in the draft and final EIS or EA. This process can cause delays in issuance of required permits or result in changes to a project to mitigate its potential environmental impacts, which can in turn impact the economic feasibility of a proposed project.

The Clean Water Act (“CWA”), and comparable state statutes, impose restrictions and controls on the discharge of pollutants into waters of the U.S. The discharge of pollutants into regulated waters is prohibited, except in accordance with the terms of a permit issued by the EPA or an analogous state agency. The CWA regulates storm water from mining facilities and requires a storm water discharge permit or Stormwater Pollution Prevention Plan for certain activities. Such a permit requires the regulated facility to monitor and sample storm water run-off from its operations. The CWA and regulations implemented thereunder also prohibit discharges of dredged and fill material in wetlands and other waters of the U.S. unless authorized by an appropriately issued permit. The CWA and comparable state statutes provide for civil, criminal, and administrative penalties for unauthorized discharges of pollutants, and impose liability on parties responsible for those discharges for the costs of cleaning up any environmental damage caused by the release and for natural resource damages resulting from the release.

The Safe Drinking Water Act (“SDWA”) and the Underground Injection Control (“UIC”) program promulgated thereunder, regulate the drilling and operation of subsurface injection wells. The EPA directly administers the UIC program in some states and in others the responsibility for the program has been delegated to the state. The program requires that a permit be obtained before drilling a disposal or injection well. Violation of these regulations and/or contamination of groundwater by mining-related activities may result in fines, penalties, and remediation costs, among other sanctions and liabilities under the SDWA and state laws. In addition, third-party claims may be filed by landowners and other parties claiming damages for alternative water supplies, property damages, and bodily injury.

Environmental Regulation − Nebraska

Nebraska has a well-developed set of environmental regulations and responsible agencies but does not have clearly defined regulations with respect to permitting mines. As such, review of the project and the issuance of permits by Nebraska agencies and regulatory bodies could potentially impact the total time to market for our Elk Creek Project. Other Nebraska regulations govern operating and design standards for the construction and operation of any source of air emissions and landfill operations. Any changes to these laws and regulations could have an adverse impact on our financial performance and results of operations by, for example, requiring changes to operating conditions, technical criteria, fees, or surety requirements. The most stringent permit related to air quality is known as a Prevention of Significant Deterioration (“PSD”) permit, which requires the applicant to demonstrate compliance with the National Ambient Air Quality Standards ("NAAQS") and Best Available Control Technology (“BACT”) for the control of air emissions. If the facility exceeds the potential to emit thresholds for such a permit and is thus subject to PSD requirements, permanent construction at the project site may not begin until the responsible agency issues the PSD permit. For facilities in Nebraska with potential emissions below PSD thresholds, a state air construction permit is needed. The state permit also requires a demonstration of compliance with NAAQS but does not require a BACT demonstration and further allows construction at a subject facility to proceed ahead of permit issuance through an established variance process. The Elk Creek Project has held a state air construction permit since June 2, 2020.

Human Capital

The Company’s ability to continue to progress the Elk Creek Project will depend on its ability to attract and retain individuals with (among other skills) financial, administrative, engineering, geological and mining skills, and knowledge of

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our industry and targeted markets. Much of the necessary specialized skills and knowledge required by the Company as a mineral exploration company are available from the Company’s current management team and Board of Directors (the “Board”). The Company retains outside consultants if additional specialized skills and knowledge are required.

As of June 30, 2026, we had fourteen full-time employees as well as four contract employees. In addition, we use consultants with specific skills to assist with various aspects of our corporate affairs, project evaluation, due diligence, corporate governance, and property management.

Our compensation programs are designed to align compensation of our employees with the Company’s performance and to provide the proper incentives to attract, retain, and motivate employees to achieve superior results. The structure of our compensation programs balances competitive wages and benefits and incentive earnings for both short-term and long-term performance.

Our priority to maintain a culture of ethical performance as a core value is reflected in the Company’s Code of Business Conduct and Ethics (the “Code of Conduct”) and other related policies. Oversight is provided by the Company’s Board and, for specific areas of performance, by committees of the Board. Employees are required to review the Code of Conduct on a periodic basis. Our compensation programs also include consideration of ethical performance in determining incentive awards.

The Company also provides a robust suite of benefits to our employees, including 401(k) participation, medical-insurance options, and programs to encourage and support the whole person.

Forward-Looking Statements

This Annual Report on Form 10-K and the exhibits attached hereto contain “forward-looking statements” within the meaning of Section 27A of the Securities Act of 1933, as amended (the “Securities Act”), and Section 21E of the Securities Exchange Act of 1934, as amended (the “Exchange Act”), and “forward-looking information” within the meaning of applicable Canadian securities legislation (collectively, “forward-looking statements”).

Forward-looking statements have been based upon our current business and operating plans, as approved by the Board, and may include statements regarding, among other matters, the financial and business performance of NioCorp; NioCorp’s anticipated results and developments in the operations of NioCorp in future periods; NioCorp’s planned exploration and development activities; the adequacy of NioCorp’s financial resources; NioCorp’s ability to secure sufficient project financing to complete construction and commence operation of the Elk Creek Project; NioCorp’s expectations on the form of future project financing; the necessity and impact of additional binding offtake agreements and the terms of such agreements, if any; NioCorp’s ability to receive a final commitment of financing from EXIM; future standards imposed by the U.S. federal government, if any; the estimated total upfront capital expenditure for the Elk Creek Project; NioCorp’s expectation and ability to produce niobium, scandium, titanium and the rare earth elements at the Elk Creek Project; NioCorp’s plans to produce and supply specific products and market demand for those products; NioCorp’s expectation that it will receive the full $10.0 million in reimbursement under the DoW Agreement; the intended use of our cash balance as of June 30, 2026, the proceeds from Warrant exercise issuances, and the reimbursement payments pursuant to the DoW Agreement; the Elk Creek Project’s ability to produce multiple critical metals; the Elk Creek Project’s projected ore production and mining operations over its expected mine life; statements with respect to the estimation of mineral resources and mineral reserves; statements with respect to projected product pricing, costs, and project economics; the exercise of options to purchase additional land parcels; the execution of contracts with engineering, procurement and construction companies; NioCorp’s possible future usage of artificial intelligence (“AI”) and the risks and challenges associated therewith; NioCorp’s ongoing evaluation of the impact of inflation, supply chain issues, tariffs, and geopolitical unrest on the Elk Creek Project’s economic model; construction of the Portal Project at the Elk Creek Project; and the creation of full time and contract construction jobs over the construction period of the Elk Creek Project.

Forward-looking statements are frequently, but not always, identified by words such as “expects,” “anticipates,” “believes,” “intends,” “estimates,” “potential,” “possible,” and similar expressions, or statements that events, conditions, or results “will,” “may,” “could,” or “should” (or the negative and grammatical variations of any of these terms) occur or be achieved. Any statements that express or involve discussions with respect to predictions, expectations, beliefs, plans, projections, objectives, assumptions, or future events or performance (often, but not always, using words or phrases such as “expects” or “does not expect,” “is expected,” “anticipates” or “does not anticipate,” “plans,” “estimates,” or “intends,” or stating that certain actions, events, or results “may,” “could,” “would,” “might,” or “will” be taken, occur or be achieved) are not statements of historical fact and may be forward-looking statements. Forward-looking statements reflect material expectations and assumptions, including, without limitation, expectations and assumptions relating to: NioCorp’s ability to receive sufficient project financing for the construction of the Elk Creek Project on acceptable terms, or at all; the future price of and demand for metals, including Al-Sc alloy; the impact that Chinese restrictions have on pricing and demand including the existence of a bifurcated market between China and the rest of the world; and the stability of the financial and capital

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markets. Such forward-looking statements reflect the Company’s current views with respect to future events and are subject to certain known and unknown risks, uncertainties, and assumptions. Many factors could cause actual results, performance, or achievements to be materially different from any future results, performance, or achievements that may be expressed or implied by such forward-looking statements, including, among others, risks related to the following: NioCorp’s requirement of significant additional capital; NioCorp’s ability to receive sufficient project financing for the construction of the Elk Creek Project on acceptable terms, or at all; NioCorp’s ability to achieve the required milestones and receive the full $10.0 million in reimbursement under the DoW Agreement; NioCorp’s ability to receive a final commitment of financing from EXIM or other debt financing or financial support on acceptable timelines, on acceptable terms, or at all; NioCorp’s ability to continue to meet Nasdaq listing standards; risks relating to the Common Shares, including price volatility, lack of dividend payments and dilution or the perception of the likelihood of any of the foregoing; the extent to which NioCorp’s level of indebtedness and/or the terms contained in agreements governing NioCorp’s indebtedness, if any, or other agreements may impair NioCorp’s ability to obtain additional financing, on acceptable terms, or at all; NioCorp’s limited operating history; NioCorp’s history of losses; the material weakness in NioCorp’s internal control over financial reporting, NioCorp’s efforts to remediate such material weakness and the timing of remediation; the possibility that NioCorp may qualify as a PFIC under the Code; the potential that the 2023 business combination with GXII could result in NioCorp becoming subject to materially adverse U.S. federal income tax consequences as a result of the application of Section 7874 and related sections of the Code; changes in tax laws and regulations; cost increases for NioCorp’s exploration and, if warranted, development projects; a disruption in, or failure of, NioCorp’s information technology systems, including those related to cybersecurity; equipment and supply shortages; variations in the market demand for, and prices of, niobium, scandium, titanium and rare earth products, including, without limitation, a reduction of demand for scandium from a downturn in capital spending for AI; impacts on the markets and pricing for scandium and rare earth products from the Chinese-based markets, including any future changes to export restrictions; current and future offtake agreements, joint ventures, and partnerships, including our ability to negotiate extensions to existing agreements or to enter into new agreements, on favorable terms or at all; NioCorp’s ability to negotiate definitive agreements for existing non-binding memoranda of understanding and non-binding term sheets; NioCorp's ability to attract qualified management; estimates of mineral resources and reserves; mineral exploration and production activities; technical and economic study results; the results of metallurgical testing; the results of technological research; unexpected variations in the quantity of ore, grade or recovery rates, or the presence of deleterious elements that would affect the process plant or waste removal; unexpected geotechnical and hydrogeological conditions from what was assumed in the mine designs; changes in demand for and price of commodities (such as fuel and electricity) and currencies; competition in the mining industry; changes or disruptions in the securities markets; legislative, political or economic developments, including changes in federal and/or state laws that may significantly affect the mining and scandium alloy industries; trade policies and tensions, including tariffs and other export controls; inflationary pressures; the impacts of climate change, as well as actions taken or required by governments related to strengthening resilience in the face of potential impacts from climate change; changes in other environmental and social factors; the need to obtain permits and comply with laws and regulations and other regulatory requirements; the timing and reliability of sampling and assay data; the possibility that actual results of work may differ from projections/expectations or may not realize the perceived potential of NioCorp’s projects; risks of accidents, equipment breakdowns, and labor disputes or other unanticipated difficulties or interruptions; the possibility of cost overruns or unanticipated expenses in development programs; operating or technical difficulties in connection with exploration, mining, development or scandium alloy production activities; management of the water balance at the Elk Creek Project site; land reclamation requirements related to the Elk Creek Project; the speculative nature of mineral exploration and development, including the risks of diminishing quantities or grades of reserves and resources; claims on the title to NioCorp’s properties; the infringement or loss of NioCorp's intellectual property rights; potential future litigation; NioCorp’s lack of insurance covering all of NioCorp’s operations; and changes in operating and capital costs, exchange rates, metallurgical performance, labor availability and other risks associated with the mining industry.

Should one or more of these risks or uncertainties materialize, or should underlying assumptions prove incorrect, actual results may vary materially from those described herein. This list is not exhaustive of the factors that may affect any of the Company’s forward-looking statements. Forward-looking statements are statements about the future and are inherently uncertain, and actual achievements of the Company or other future events or conditions may differ materially from those reflected in the forward-looking statements due to a variety of risks, uncertainties, and other factors, including without limitation those discussed under Item 1A., Risk Factors below.

The Company’s forward-looking statements contained in this Annual Report on Form 10-K are based on the beliefs, expectations, and opinions of management as of the date of this Annual Report on Form 10-K. The Company does not assume any obligation to update forward-looking statements if circumstances or management’s beliefs, expectations, or opinions should change, except as required by law. For the reasons set forth above, investors should not attribute undue certainty to, or place undue reliance on, forward-looking statements.

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Available Information

We maintain a website at http://www.niocorp.com. Our Common Shares are currently registered under Section 12(b) of the Exchange Act, and we are currently required to file reports on Forms 10-K, 10-Q, or 8-K. Our Annual Report on Form 10-K (which includes our audited consolidated financial statements), Quarterly Reports on Form 10-Q, Current Reports on Form 8-K and amendments to reports filed or furnished pursuant to Sections 13(a) and 15(d) of the Exchange Act, are available on our website, free of charge, as soon as reasonably practicable after we electronically file such reports with, or furnish those reports to, the SEC. The SEC maintains an internet site that contains reports, proxy and information statements, and other information regarding issuers that file electronically with the SEC (http://www.sec.gov). We do not intend to send security holders a printed version of our Annual Report as it will be available online.

We maintain a Code of Conduct, a copy of which may be found on our website in the “About Us” section under the main title “Corporate Governance.” Our Code of Conduct contains information regarding whistleblower procedures.

We are not including the information contained on or accessible through our website or the SEC’s website as a part of, or incorporating it by reference into, this Annual Report on Form 10-K.

ITEM 1A. RISK FACTORS

Our business activities are subject to significant risks, including those described below. You should carefully consider these risks. If any of the described risks occur, our business, financial position, and results of operations could be materially adversely affected. Such risks are not the only ones we face, and additional risks and uncertainties not presently known to us or that we currently deem immaterial may also affect our business. This report contains forward-looking statements that involve risks and uncertainties. Our actual results could differ materially from those anticipated in the forward-looking statements as a result of a number of factors, including the risks described below. See “Forward-Looking Statements” under Item 1., “Business.”

We will require significant additional capital to fund our business plan.

We will be required to make substantial capital expenditures to advance the Elk Creek Project to construction and commercial operation. We will also require funds for our ongoing capital needs and will be required to raise additional capital.

We expect that the Company will operate at a loss for the foreseeable future. The Company’s current planned cash needs are approximately $65 million to $75 million for the next twelve months. In addition to outstanding accounts payable and short-term liabilities, our planned expenditures over the next twelve months are expected to consist of expenditures relating to the advancement of the Elk Creek Project by NioCorp’s majority owned subsidiary, ECRC, corporate overhead costs, and estimated costs related to securing financing necessary for advancement of the Elk Creek Project.

We expect to use our cash balance as of June 30, 2026, as well as the proceeds from Warrant and options to purchase Common Shares ("Options") exercise issuances, and the reimbursement payments pursuant to the DoW Agreement, to fund our planned expenditures for the next twelve months. However, additional work is required in order to advance the Elk Creek Project, which will require additional financing. If the Company were able to obtain additional funding, the Company would be able to accelerate planned expenditures ahead of its current schedule. In addition, to the extent that EXIM requests further project activities to be undertaken in connection with the diligence process, the Company would require additional funding to complete such activities. The Company’s ability to continue operations and fund our current work plan is dependent on management’s ability to secure additional financing.

We have not yet commenced commercial production at any of our properties and, as such, have not generated positive cash flows to date and have no reasonable prospects of doing so unless successful commercial production can be achieved at our Elk Creek Project. We expect to continue to incur negative investing and operating cash flows until such time as we enter into successful commercial production. This will require us to deploy our working capital to fund such negative cash flow and to seek additional sources of financing. There is no assurance that any such financing sources will be available or sufficient to meet our requirements. There is no assurance that we will be able to continue to raise equity capital or to secure additional debt financing, or that we will not continue to incur losses.

The 2026 S-K 1300 Elk Creek Technical Report Summary includes an estimated total upfront capital expenditure for the Elk Creek Project of approximately $1,849 million. The actual amount of capital expenditure required to successfully achieve commercial production at the Elk Creek Project is subject to, among other factors, the timing and actual cost of further exploration, preparing feasibility studies, permitting, engineering, and the construction of infrastructure, mining and processing

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facilities. We anticipate financing the estimated total upfront capital expenditure for the Elk Creek Project with debt financing (including the potential EXIM Financing) and additional equity financing.

The potential EXIM Financing is subject to, among other matters, the satisfactory completion of due diligence, including the additional project activities identified in the PPL, the negotiation and settlement of final terms, and the negotiation of definitive documentation. The PPL included an indicative term sheet, which left open the total estimated amount of the EXIM Financing and provided that the amount of the EXIM Financing that could be made available for the Elk Creek Project will be scaled based on the number of U.S. jobs supported, both during construction and over the life of EXIM’s financing, subject to certain expectations regarding the ratio of debt-to-equity financing for the Elk Creek Project. However, NioCorp is currently unable to estimate the total amount of the EXIM Financing, if any, as well as how long the application process, including additional project activities identified by EXIM, may take, and there can be no assurances that NioCorp will be able to successfully negotiate a final commitment for the EXIM Financing, on acceptable terms, or at all.

Agreements we enter into may contain restrictions on our ability to raise additional financing on reasonable terms or at all. For example, pursuant to the Exchange Agreement, NioCorp is restricted from issuing equity or equity-linked securities (other than Common Shares) or any preferred equity or non-voting equity if such issuance would adversely impact the rights of the holders of the shares of Class B common stock of ECRC, without the consent of the holders of a majority of the shares of Class B common stock of ECRC. Additionally, sales of substantial amounts of securities may have a highly dilutive effect on our ownership or share structure. Sales of a large number of Common Shares in the public markets, or the potential for such sales, could decrease the trading price of the Common Shares and could impair our ability to raise capital through future sales of Common Shares. There is significant uncertainty that we will be able to secure any additional financing in the current equity or debt markets.

Our ability to obtain necessary funding depends upon a number of factors, including, without limitation, the status of the national and worldwide economy, including international trade restrictions and policies, the demand for and the price of the products we intend to produce and our ability to negotiate satisfactory offtake arrangements for the products we intend to produce at the Elk Creek Project. We are actively pursuing additional sources of debt and equity financing, and while we have been successful in doing so in the past, there can be no assurance we will be able to obtain any such additional financing on acceptable terms, if at all. Our inability to access sufficient capital for our operations and the Elk Creek Project could have a material adverse effect on our financial condition, results of operations, or prospects.

We have a limited operating history on which to base an evaluation of our business and prospects.

Since our inception, we have had no revenue from operations. We have no history of producing products from any of our properties, and our assumptions related to the risks we may face in the future related to the Elk Creek Project may change. Our Elk Creek Project is a development stage property. Advancing our Elk Creek Project from a development stage property to a production stage property will require significant capital and time, and successful commercial production from the Elk Creek Property will be subject to permitting and construction of the mine, processing plants, roads, and other related works and infrastructure. As a result, we are subject to all of the risks associated with developing and establishing new mining operations and business enterprises including:

•
the timing and cost, which can be considerable, of further exploration, preparing feasibility studies, permitting, engineering and construction of infrastructure, mining, and processing facilities;
•
the availability and costs of drilling equipment, exploration personnel, skilled labor, and mining and processing equipment, if required;
•
the availability and cost of appropriate smelting and/or refining arrangements, if required;
•
compliance with environmental and other governmental approval and permit requirements;
•
the availability of funds to finance exploration, development, permitting, and construction activities, as warranted;
•
potential opposition from non-governmental organizations, local groups, or local residents that may delay or prevent development activities;
•
potential increases in exploration, construction, and operating costs due to changes in the cost of fuel, power, materials, supplies or the encountering of unexpected conditions; and
•
potential shortages of mining, mineral processing, hydrometallurgical, pyrometallurgical, construction, and other facilities-related supplies.

The costs, timing, and complexities of exploration, development, engineering, and construction activities may be increased by the location of our properties and competition from other mineral exploration and mining companies. It is common for

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exploration companies to experience unexpected problems and delays during development, if commenced, including engineering, procurement, construction, commissioning, and ramp-up delays. Accordingly, our activities may not result in profitable operations and we may not succeed in establishing operations or profitably producing products at any of our current or future properties, including our Elk Creek Project.

We have a history of losses and expect to continue to incur losses in the future.

We have incurred losses since inception, have negative cash flow from operating activities, and expect to continue to incur losses in the future. We incurred a net loss attributable to the Company of $48.6 million for the year ended June 30, 2026, and $17.4 million for the year ended June 30, 2025.

We expect to continue to incur losses unless and until such time as one of our properties enters into commercial production and generates sufficient revenues to fund continuing operations. We recognize that if we are unable to generate significant revenues from operations and dispositions of our properties, we will not be able to earn profits or continue operations. At this early stage of our operation, we also expect to face the risks, uncertainties, expenses, and difficulties frequently encountered by companies at the start-up stage of their business development. We cannot be sure that we will be successful in addressing these risks and uncertainties and our failure to do so could have a materially adverse effect on our financial condition.

Increased costs could affect our financial condition.

We anticipate that costs at our projects that we may explore or develop, including the Elk Creek Project, will frequently be subject to variation from one year to the next due to a number of factors, such as changing ore grade, metallurgical performance, and revisions to mine plans, if any, in response to the physical shape and location of the ore body. In addition, costs are affected by the price of commodities such as fuel, steel, aluminum, iron, chemicals, natural gas, fresh water, and electricity, as well as by government actions such as tariffs. Such commodities are at times subject to volatile price movements, including increases that could make production at certain operations less profitable or not profitable at all. For example, the 2026 S-K 1300 Elk Creek Technical Report Summary includes an estimated total upfront capital expenditure for the Elk Creek Project of approximately $1,849 million, including a contingency of 14%, which is an increase of approximately $708 million compared to the estimated total upfront capital expenditure for the Elk Creek Project of approximately $1,141.0 million that was included in the 2022 S-K 1300 Elk Creek Technical Report Summary. The increase in estimated total upfront capital expenditure for the Elk Creek Project is primarily driven by a substantially redesigned processing plan and mining operation producing eight critical minerals and significant inflationary impacts since the 2022 S-K 1300 Elk Creek Technical Report Summary. The actual amount of capital expenditure required to successfully achieve commercial production at the Elk Creek Project is subject to, among other factors, the timing and actual cost of further exploration, preparing feasibility studies, permitting, engineering and the construction of infrastructure, mining, and processing facilities. A material increase in costs at any significant location could have a significant effect on our profitability.

We may be unable to successfully negotiate final, definitive offtake agreements, which could have a material adverse effect on our ability to secure project financing and establish the commercial viability of the Elk Creek Project.

We have entered into offtake agreements related to our Elk Creek Project, that cover the sale of 75% of our planned ferroniobium production for the first ten years of commercial operation. We expect that we will need to enter into additional offtake agreements to obtain sufficient project financing to cover initial capital costs and other related expenses, and to establish the commercial viability of the Elk Creek Project. We have entered into non-binding memoranda of understanding and non-binding term sheets related to the offtake of the remainder of the ferroniobium, as well as portions of our expected production of scandium and 100% of our titanium and rare earth production, that we expect to produce from the Elk Creek Project for the first ten years of commercial operation. We may be unable to negotiate final terms and agreements with these or other companies in a timely manner, or at all, and there is no guarantee that the terms of any final agreement will be the same or similar to those currently contemplated. Final terms may include less favorable pricing structures or volume commitments, reduced contract durations and other adverse changes. Delays in negotiating final agreements could slow our initial commercialization, and failure to agree to definitive terms for sales of sufficient volumes of our products could prevent us from growing our business. To the extent that terms in our initial purchase and offtake agreements may influence negotiations regarding future contracts, the failure to negotiate favorable final terms in respect of our current negotiations could have a material negative impact on our growth and profitability. Further, our prospective counterparties may cancel or delay entering into definitive agreements for a variety of reasons, some of which may be outside of our control. Any failure to enter into such definitive agreements on a timely basis, on favorable terms, or at all, could have a material adverse effect on our ability to secure project financing and establish the commercial viability of the Elk Creek Project.

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Any failure of our counterparties to meet their obligations to us or to third parties with respect to our offtake agreements, supply agreements or other commercial agreements could have a material adverse effect on our ability to secure project financing and establish the commercial viability of the Elk Creek Project.

We have entered into offtake agreements, and may enter into joint ventures or partnership arrangements, including additional offtake agreements, with other parties in relation to the exploration, development, and production of certain of the properties in which we have an interest. In addition, we expect to enter into other agreements, including Engineering, Procurement, and Construction (“EPC”) agreements, as well as agreements related to the supply of natural gas and electricity to the Elk Creek Project.

Any failure of our counterparties to meet their obligations to us or to third parties, or any disputes with respect to the parties’ respective rights and obligations, price fluctuations and termination provisions related to such agreements, or our ability to negotiate extensions to existing agreements or to enter into new agreements, on favorable terms or at all, could have a material adverse effect on us, the development and production at our properties, including the Elk Creek Project, the joint ventures, if any, or their properties and therefore could have a material adverse effect on our ability to secure project financing and establish the commercial viability of the Elk Creek Project.

A disruption in, or failure of our third-party service providers’ IT systems, including those related to cybersecurity, could adversely affect our business operations and financial performance.

We rely on the accuracy, capacity, and security of our third-party service providers’ IT systems for the operations of many of our business processes and to comply with regulatory, legal, and tax requirements. We are dependent on third parties to provide important IT services relating to, among other things, operational technology at our facilities, human resources, electronic communications, and certain finance functions. Despite the security measures that our third-party service providers have implemented, including those related to cybersecurity, we have experienced, and may experience in the future, cybersecurity incidents. Cybersecurity incidents and similar attacks vary in their form and can include the deployment of harmful malware or ransomware, denial-of-service attacks, and other attacks, which may affect business continuity and threaten the availability, confidentiality and integrity of our systems and information, and the systems and information of our third-party service providers. Cybersecurity incidents can also include employee or personnel failures, fraud, phishing or other social engineering attempts or other methods to cause confidential information, payments, account access or access credentials, or other data to be transmitted to an unintended recipient. Cybersecurity threat actors also may attempt to exploit vulnerabilities in software that is commonly used by companies in cloud-based services and bundled software. We have experienced cybersecurity threats and cybersecurity incidents in the past, and may experience cybersecurity threats and cybersecurity incidents in the future. To date, we have not identified any risks from cybersecurity threats, including as a result of previous cybersecurity incidents, that have had or are reasonably likely to have, a material impact on our business operations or financial condition.

Though our third-party service providers have controls in place, we cannot provide assurance that a cybersecurity incident will not occur in the future. Furthermore, we may have little or no oversight with respect to security measures employed by third-party service providers, which may ultimately prove to be ineffective at countering threats. Cybersecurity threats or incidents or disruptions of our third-party service providers’ IT systems could interrupt our ability to manage and operate our business, impact data, and adversely affect our business operations and financial performance, including major disruptions to business operations, loss of intellectual property, release of confidential information, alteration or corruption of data or systems, costs related to remediation or the payment of ransom, and litigation including individual claims or consumer class actions, commercial litigation, administrative, and civil or criminal investigations or actions, regulatory intervention and sanctions or fines, investigation and remediation costs and possible prolonged negative publicity. In addition, we have incurred costs in connection with the remediation of cybersecurity incidents in the past and we may be required to incur significant costs to protect against and, if required, remediate the damage caused by cybersecurity incidents, disruptions or system failures in the future.

We may also be required to comply with cybersecurity standards imposed by the U.S. Government as a condition of entering into government contracts or receiving federal financial assistance. Any failure to comply with these standards, whether or not resulting in a cybersecurity incident or disruption, could restrict our ability to receive financing from the U.S. Government or to bid for, be awarded and perform contracts with the U.S. Government.

A shortage of equipment and supplies could adversely affect our ability to operate our business.

We are dependent on various supplies and equipment to carry out our mining exploration and, if warranted, project development operations. The shortage of such supplies, equipment, and parts could have a material adverse effect on our ability to carry out our operations and could therefore limit, or increase the cost of, production. Ongoing disruptions to the world’s economy, including issues related to supply chains, inflation, tariffs and trade tensions, and increased raw material and labor costs, may delay our ability to secure supplies and equipment for the Elk Creek Project on a timely basis.

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We may use AI in our business, and challenges with properly managing its use could result in reputational harm, competitive harm and legal liability, and could have adverse effects on our results of operations, financial condition, liquidity and cash flows.

We may incorporate AI solutions into our business, and we may leverage AI, including generative and agentic AI, into our business operations. Our competitors or other third parties, may incorporate AI into their business more quickly or more successfully than we do, which could impair our ability to compete effectively and could adversely affect our results of operations. In addition, there are significant risks in using AI, and there can be no assurance that the use of AI will enhance our business or be beneficial to our business operations, including our efficiency or our profitability.

Additionally, if our AI applications, or the AI applications of third parties, are based on data, algorithms or other inputs that are flawed, or if our AI applications, or the AI applications of third parties, assist us in producing content, analyses or recommendations that are, or are alleged to be, deficient, inaccurate or biased, our business, results of operations and financial conditions may be adversely affected. The increased use of AI applications generally has resulted in, and may in the future result in, cybersecurity incidents that implicate the personal data of end users of such applications. Any such cybersecurity incidents related to our own use of AI applications may increase our cybersecurity risks, as well as the cybersecurity risks of third parties, which could adversely affect our reputation and results of operations. AI also presents emerging ethical issues, and if our use of AI becomes controversial, we may experience brand, reputational or competitive harm, or legal liability. The rapid evolution of AI, including the potential regulation of AI by governmental or other regulatory agencies, will require significant resources to develop, test and implement AI ethically and to minimize any unintended, harmful impacts.

We may experience difficulty attracting and retaining qualified management to meet the needs of our anticipated growth, and the failure to manage our growth effectively could have a material adverse effect on our business and financial condition.

We are dependent on a relatively small number of key employees, including our Chief Executive Officer. The loss of any officer could have an adverse effect on us. We have no life insurance on any individual, and we may be unable to hire a suitable replacement for them on favorable terms, should that become necessary. Further, the specialized nature of our model as summarized in the 2026 S-K 1300 Elk Creek Technical Report Summary may make qualified persons difficult to replace, which could have a material adverse effect on our business and financial condition.

The effect on the capital markets and the economy of recent global events, including inflation, volatility in commodity prices, supply chain uncertainty, tariffs and trade tensions, and increases in raw material and labor costs, could have an adverse effect on NioCorp’s business plans, financial condition, and liquidity.

Certain events have affected, and continue to affect, the global and United States economies, including increased inflation, volatility in commodity prices, supply chain uncertainty, tariffs and trade tensions, and increases in raw material and labor costs. We cannot predict how this will affect our business, but the impact may be adverse.

Although it is not possible to predict the ultimate impact of these factors on NioCorp’s business plans, financial position, or liquidity, such impacts that may be material include, but are not limited to: (i) delays in the completion of the mine and surface engineering designs and uncertainty regarding our ability to finalize necessary EPC agreements as a result of disruptions in the businesses of our engineering consultants and key contractors for the Elk Creek Project, (ii) reduced availability and increased costs of employees, (iii) a negative impact on our liquidity position, and (iv) increased costs and less ability to access funds in the capital markets. The full extent to which these factors may continue to impact our business will depend on future developments, which continue to be highly uncertain and cannot be predicted at this time.

In addition, we cannot predict the impact that recent global events, including inflation, volatility in commodity prices, supply chain uncertainty, tariffs and trade tensions, and increases in raw material and labor costs will have on our customers, suppliers, vendors, and other business partners, and each of their financial conditions; however, any material effect on these parties could adversely impact us.

It may be difficult to enforce judgments or bring actions outside the U.S. against us and certain of our directors.

We are a Canadian corporation and, as a result, it may be difficult or impossible for an investor to do the following:

•
enforce in courts outside the U.S. judgments obtained in U.S. courts based upon the civil liability provisions of U.S. federal securities laws against these persons and the Company; or
•
bring in courts outside the U.S. an original action to enforce liabilities based upon U.S. federal securities laws against these persons and the Company.

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We may not receive any proceeds from the exercise of our outstanding Warrants, and the potential adverse effect on the prevailing market prices for our Common Shares as a result of sales, or the perception of future sales, of Common Shares could adversely affect our ability to raise additional capital.

Upon exercise, we will receive the cash exercise price of our outstanding Warrants (assuming, that they are not exercised on a cashless basis, as applicable). We believe the likelihood that holders will exercise their Warrants, and therefore, the amount of cash proceeds that we would receive, is, among other things, dependent upon the market price of our Common Shares. For so long as the market price for our Common Shares is less than the applicable exercise price of the Warrants, we believe such holders will be unlikely to exercise their Warrants. The potential adverse effect on the prevailing market price of our Common Shares as a result of sales of Common Shares by us or by other security holders, or the perception that such sales may occur, could keep the market price for our Common Shares below the applicable exercise price of the Warrants. Accordingly, the holders of the Warrants may not exercise their Warrants before they expire, and we may not receive any proceeds from the exercise of the outstanding Warrants.

We may not recognize the full value of the DoW Agreement.

Subject to the terms and conditions of the DoW Agreement, the DoW will reimburse ECRC for a portion of the costs incurred by ECRC under the DoW Agreement and ECRC is entitled to receive up to an aggregate of approximately $10.0 million of reimbursement payments from the DoW upon the achievement of certain project milestones. If the Company is not successful in achieving the milestones required under the DoW Agreement or if the reimbursements sought by the Company are rejected or the DoW Agreement is terminated prior to completion of all milestones, the Company may not receive all of the payments as reimbursements for expenses incurred as expected under the DoW Agreement.

The Company has identified a material weakness in its internal control over financial reporting. If not remediated, the Company’s failure to establish and maintain effective disclosure controls and procedures and internal control over financial reporting could result in material misstatements in its financial statements and a failure to meet its reporting and financial obligations, each of which could have a material adverse effect on the Company’s financial condition and the trading price of the Common Shares.

Our management has identified a material weakness in its internal control over financial reporting relating to a deficiency in the principles associated with the control activities component of internal control based on the criteria established by the COSO Framework (as defined below), that constitute a material weakness. A material weakness is a deficiency, or a combination of deficiencies, in internal control over financial reporting, such that there is a reasonable possibility that a material misstatement of a company’s annual or interim financial statements will not be prevented or detected on a timely basis.

As discussed in Item 9A, “Controls and Procedures,” of this Annual Report on Form 10-K, the Company’s management has assessed the effectiveness of its internal control over financial reporting and its disclosure controls and procedures and concluded that they were not effective as of June 30, 2026.

The Company is committed to remediating its material weakness as promptly as possible. Management is in the process of implementing its remediation plan. However, there can be no assurance as to when the material weakness will be remediated or that additional material weaknesses will not arise in the future. If the Company is unable to maintain effective internal control over financial reporting, its ability to record, process and report financial information timely and accurately could be adversely affected, which could subject the Company to litigation or investigations, require management resources, increase costs, negatively affect investor confidence and adversely impact the trading price of the Common Shares.

We may face litigation and other risks as a result of the material weakness in our internal control over financial reporting.

We identified a material weakness in our internal control over financial reporting that existed as of June 30, 2026. As a result of such material weakness and other matters raised or that may in the future be raised by the SEC or the Canadian securities regulators, we face potential for litigation or other disputes, which may include, among others, claims invoking the federal and state securities laws, contractual claims or other claims arising from the material weakness in our internal control over financial reporting and the preparation of our financial statements. As of the date of this Annual Report on Form 10-K, we have no knowledge of any such litigation or dispute. However, we can provide no assurance that such litigation or dispute will not arise in the future. Any such litigation or dispute, whether successful or not, could adversely affect our business, financial condition and results of operations.

We face numerous uncertainties in estimating our mineral reserves and resources and inaccuracies in, or changes to, our estimates or the factors and assumptions on which they are based, including with respect to the economic analysis conducted

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in connection with the 2026 S-K 1300 Elk Creek Technical Report Summary, could result in lower than expected revenues, higher than expected costs, and decreased profitability.

A mineral is economically recoverable when the price at which we may sell the mineral exceeds the costs and expenses of mining and selling the mineral. Forecasts of our future performance are based on, among other things, estimates of our mineral reserves. We base our reserve and resource information on engineering, economic, and geological data assembled and analyzed by qualified persons, which include various engineers and geologists on our staff and with third parties. Our estimates are also subject to SEC regulations regarding classification of reserves and resources, including S-K 1300. Our reserve and resource estimates as to both quantity and quality are updated from time to time to reflect additional information received. There are numerous uncertainties inherent in estimating quantities and qualities of mineral reserves and resources, including many factors beyond our control.

Estimates of mineral reserves and resources necessarily depend upon a number of variable factors and assumptions, any one of which may, if incorrect, result in an estimate that varies considerably from actual results. These factors and assumptions include, but are not limited to:

•
geologic and mining conditions, which may not be fully identified by available exploration data and may differ from our experience;
•
demand for the minerals that we plan to produce;
•
current and future market prices for minerals and contractual arrangements;
•
current and future operating costs and capital expenditures may exceed estimates;
•
severance and excise taxes, royalties and development and reclamation costs;
•
future mining technology improvements;
•
the effects of regulation by governmental agencies;
•
the ability to obtain, maintain and renew all required permits;
•
employee health and safety; and
•
historical production from the area compared with production from other producing areas.

The conversion of reported mineral resources to mineral reserves should not be assumed, and the reclassification of reported mineral resources from lower to higher levels of geological confidence should not be assumed. As such, actual mineral tonnage recovered from identified reserves, and revenues and expenditures with respect to our reserves, may vary materially from estimates. Thus, these estimates may not accurately reflect our actual reserves. Any material inaccuracy in, or changes to, our estimates related to our reserves, or the underlying factors and assumptions, could result in lower-than-expected revenues, higher-than-expected costs, or decreased profitability, which could materially and adversely affect our business, results of operations, financial position, and cash flows.

In addition, the economic analysis described in the 2026 S-K 1300 Elk Creek Technical Report Summary that was conducted in connection with the 2026 Elk Creek Study to demonstrate economic viability and support the determination of mineral reserves may be impacted by the variables listed above, as well as assumptions relating to discount rates, future production rates, commodity prices, operating costs, capital expenditures, and other inputs that are subject to significant uncertainty. For example, the initial capital cost estimate for the Elk Creek Project as described in the 2026 S-K 1300 Elk Creek Technical Report Summary has a contingency level of 14%. The results of the economic analysis are not a forecast or prediction of actual results for the periods covered, and actual results may differ materially from those projected by the economic analysis. There can be no assurance that the assumptions underlying the economic analysis will prove to be accurate or that the projected economics of the Elk Creek Project will be realized. Any material inaccuracy in, or change to, our estimates related to our economic analysis could result in lower than expected revenues, higher than expected costs, or decreased profitability, which could materially and adversely affect our business, results of operations, financial position, and cash flows.

Price volatility could have dramatic effects on our results of operations and our ability to obtain financing for the Elk Creek Project and execute our business plan.

The price of commodities varies on a daily basis. Niobium is a specialty metal and not a commonly traded commodity such as copper, zinc, gold, or iron ore. The price of niobium tends to be set through a limited long-term offtake market, contracted between very few suppliers and purchasers. The world’s largest supplier of niobium, Companhia Brasileira de Metalurgia e Mineração, supplies approximately 85% of the world’s niobium. Any attempt to suppress the price of niobium by such supplier, or an increase in production by any supplier in excess of any increased demand, would have negative

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consequences on the price of niobium and, potentially, on our value. The price of niobium may also be reduced by the discovery of new niobium deposits, which could not only increase the overall supply of niobium (causing downward pressure on its price) but could draw new firms into the niobium industry that would compete with us.

Sc2O3 is used in solid oxide fuel cells and has the potential to become a valuable alloy with aluminum in the aerospace and automotive industries. Supply of scandium has been sporadic in recent years, and there are no primary scandium mines in the world at present. Production primarily occurs as a by-product from existing metallurgical plants, primarily in Russia, Canada, the Philippines, and China. Our management believes the Elk Creek Project would significantly increase the world’s supply of scandium trioxide. Although the Company’s market studies indicate a positive outlook for demand, there is no assurance at present that the Company could sell all of its production. In addition, the sale of scandium represents a significant portion of the Elk Creek Project revenue; achieving the revenue projected in the Company’s studies is subject to market growth in scandium, which is a developing market with a risk of oversupply and/or undersupply disrupting pricing.

Titanium metal is used in various superalloys and other applications for aerospace applications, armor, and medical implants, and in oxide form is a key component of pigments used in paper, paint, and plastics. The Elk Creek Project would produce a small quantity of TiCl4 relative to other producers. As a small producer, we would be subject to fluctuations in the price of TiCl4 that would result from normal variations in supply and demand for this commodity.

In addition, the niobium, scandium, titanium, neodymium-praseodymium oxide, dysprosium oxide, terbium oxide, SEG carbonate and heavy rare earth carbonate, that we intend to produce at the Elk Creek Project are also subject to additional commodity-specific price cycles resulting from, among other factors, export controls, taxes and other tariffs and fees. Volatility in the demand for, and prices of, the niobium, scandium, titanium, and potentially, rare earth products, that we intend to produce at the Elk Creek Project may adversely affect the overall value of the Elk Creek Project and impact our ability to obtain financing for the Elk Creek Project on acceptable terms, or at all.

Furthermore, supply-side factors have a significant influence on price volatility for our planned products. Production of scandium and REEs is dominated by Chinese producers. The Chinese Central Government regulates production through quotas and environmental standards and, to a lesser extent, import regulation. It has changed, and may continue to change, those production quotas, environmental standards and import regulations. Over the past few years, the Chinese market has undergone significant restructuring in line with Chinese Central Government policy. However, periods of oversupply or speculative trading in scandium and REEs can lead to significant fluctuations in the market prices of these products. In recent years, China has also begun to implement export controls. We believe these controls have created a bifurcated market for scandium, dysprosium and terbium, causing prices outside China to be significantly higher than prices within China. Any easing of these export controls by China, or the development of alternative sources of supply, could have a material adverse effect on our business, financial condition and results of operations.

The nature of mineral exploration and production activities involves a high degree of risk and the possibility of uninsured losses.

Exploration for and the production of minerals is highly speculative and involves much greater risk than many other businesses. Most exploration programs do not result in the discovery of mineralization, and any mineralization discovered may not be of sufficient quantity or quality to be profitably mined. Our operations are, and any future development or mining operations we may conduct will be, subject to all of the operating hazards and risks normally incident to exploring for and developing mineral properties, such as, but not limited to:

•
economically insufficient mineralized material;
•
fluctuation in production costs that make production uneconomical;
•
labor disputes;
•
unanticipated variations in grade and other geologic problems;
•
environmental hazards;
•
water conditions;
•
difficult surface or underground conditions;
•
industrial accidents;
•
metallurgical, pyrometallurgical, and other processing problems;
•
mechanical and equipment performance problems;

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•
failure of dams, stockpiles, wastewater transportation systems, or impoundments;
•
unusual or unexpected rock formations; and
•
personal injury, fire, flooding, cave-ins, and landslides.

Any of these risks can materially and adversely affect, among other things, the development of properties, production quantities and rates, costs and expenditures, potential revenues, and production dates. We currently have very limited insurance to guard against some of these risks. If we determine that capitalized costs associated with any of our mineral interests are not likely to be recovered, we would incur a write-down of our investment in these interests. All of these factors may result in losses in relation to amounts spent that are not recoverable, or that result in additional expenses.

We have no history of producing commercial products from our current mining properties and there can be no assurance that we will successfully establish mining operations or profitably produce minerals.

We have no history of producing commercial products from our current mining properties. We do not produce commercial products and do not currently generate operating earnings. While we seek to move our Elk Creek Project from a development stage property to a production stage property, such efforts will be subject to all of the risks associated with establishing new mining operations and business enterprises, including:

•
the timing and cost, which are considerable, of the construction of mining and processing facilities;
•
the availability and costs of skilled labor and equipment;
•
compliance with environmental and other governmental approval and permit requirements;
•
the availability of funds to finance construction and development activities;
•
potential opposition from non-governmental organizations, local groups, or local residents that may delay or prevent development activities; and
•
potential increases in construction and operating costs due to changes in the cost and availability of labor, fuel, power, materials, and equipment and supplies, and the time elapsed since the most recent estimates of cost and availability were made.

It is common in new mining and processing operations to experience unexpected problems and delays during engineering, procurement, construction, commissioning, and initial operations. In addition, our management and workforce will need to be expanded, and sufficient housing and other support systems for our workforce will have to be established. This could result in delays in the commencement of production and increased costs of production. Accordingly, we cannot assure you that our activities will result in profitable operations or that we will successfully establish mining and processing operations.

Results of metallurgical testing by us may not be favorable to, or as expected by, us.

We have completed significant bench, mini-pilot, and pilot scale metallurgical testing on material from the Elk Creek Project and will continue to complete necessary metallurgical testing at the bench, mini-pilot, and pilot scale as the exploration and, if warranted, development of the Elk Creek Project progresses. There can be no assurance that the results of such metallurgical testing will be favorable to, or will be as expected by, us. Furthermore, there can be no certainty that metallurgical recoveries obtained in bench or pilot scale tests will be achieved in either subsequent testing or commercial operations. The development of a complete metallurgical process to produce saleable final products from the Elk Creek Project is a complex and resource-intensive undertaking that may result in overall schedule delays and increased project costs for us.

The success of our business will depend, in part, on the growth of existing and emerging uses for scandium and rare earth products.

We intend to produce scandium and rare earth products at the Elk Creek Project that are used in critical industries, including AI data centers, electronics, aerospace and defense systems, robotics, and other advanced technologies. The success of our business depends, in part, on the continued growth of these end-markets and the successful commercialization of scandium and rare earth products. If the market for these existing and emerging technologies does not grow as we expect, grows slower than we expect, or if the demand for our products in these markets decreases, then our business, prospects, financial condition and operating results could be harmed. Although periods of high market prices would generally be beneficial to our financial performance, any such period could also create economic pressure to identify or create alternate technologies that ultimately could depress the long-term demand for our products. Any unexpected costs or delays in the production of scandium or rare earth products, or less than expected demand for the existing and emerging technologies that use scandium or rare earth products, could have a material adverse effect on the results of our operations.

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Our recovery process for our planned products has been evaluated at a demonstration scale but has not been fully validated on a commercial scale.

The 2026 S-K 1300 Elk Creek Technical Report Summary describes the process by which we expect to recover scandium, niobium, titanium and the rare earth products from the Elk Creek Project’s ore body. Although demonstration-scale testing has achieved the targeted recovery rates, the full recovery and separation process has not been operated on a commercial scale or with actual production-stream materials at commercial throughput, and commercial samples of separated products have not yet been produced through the complete process. There can be no assurance that the recovery process will perform as designed on a commercial scale, produce products meeting required purity and quality specifications, or achieve the recoveries assumed in the 2026 S-K 1300 Elk Creek Technical Report Summary. Failure to validate the recovery process on a commercial scale could reduce the Elk Creek Project’s revenue, adversely affect the commercial viability of the Elk Creek Project, and have a material adverse effect on our business, results of operations, and financial condition.

Estimates of resources and reserves are subject to evaluation uncertainties that could result in project failure.

Our exploration and future mining operations, if any, are and would be faced with risks associated with being able to accurately predict the quantity and quality of resources/reserves within the earth using statistical sampling techniques. Estimates of any resources/reserves on any of our properties would be made using samples obtained from appropriately placed trenches, test pits, underground workings, and intelligently designed drilling. There is an inherent variability of assays between check and duplicate samples taken adjacent to each other and between sampling points that cannot be reasonably eliminated. Additionally, there also may be unknown geologic details that have not been identified or correctly appreciated at the current level of accumulated knowledge about our properties. This could result in uncertainties that cannot be reasonably eliminated from the process of estimating resources/reserves. If these estimates were to prove to be unreliable, we could implement an exploitation plan that may not lead to commercially viable operations in the future.

Any material changes in mineral resource/reserve estimates and grades of mineralization will affect the economic viability of placing a property into production and a property’s return on capital.

Mineral resource/reserve estimates may require adjustments or downward revisions. In addition, the grade of ore ultimately mined, if any, may differ from that indicated in the 2026 S-K 1300 Elk Creek Technical Report Summary. Minerals recovered in small scale tests may not be duplicated in large scale tests under on-site conditions or at commercial production scale.

The mineral resource and mineral reserve estimates included in the 2026 S-K 1300 Elk Creek Technical Report Summary and contained in this Annual Report on Form 10-K have been determined based on assumed future prices, cut-off grades, and operating costs that may prove to be inaccurate. Extended declines in market prices for our products may render portions of our resource/reserve estimates uneconomic and may result in reduced reported resources/reserves or may adversely affect any commercial viability determinations we may reach. Any material reductions in estimates of resources/reserves could have a material adverse effect on our Common Share price and on the value of our properties.

We face intense competition in the mining industry.

The mining industry is intensely competitive in all of its phases, and we compete with other companies for capital. In particular, the U.S. Government has made, and may continue to make, significant investments in other companies engaged in the mining of scandium, REEs, and other critical minerals, which may provide those companies with greater access to capital, resources, and operational support. As a result of this competition, some of which is with large established mining companies with substantial capabilities and with greater financial and technical resources than ours, we may be unable to obtain financing for the Elk Creek Project on terms we consider acceptable, or at all, or to acquire and develop additional properties in the future. Government investment in competing projects may also accelerate the development of alternative sources of supply for our products, which could reduce the prices we are able to realize for our products, and diminish our ability to negotiate offtake or supply agreements on favorable terms. In addition, we compete with others in efforts to obtain resources to advance the Elk Creek Project to construction and commercial operation, including mining and processing equipment, as well as qualified managerial and technical employees. If we are unable to successfully compete for required resources, including qualified employees, we may have difficulty in advancing the Elk Creek Project to construction and commercial operation. In addition, in competing for qualified personnel, we may be required to pay compensation or benefits relatively higher than those paid in the past, and the availability of qualified personnel may be limited in high-demand periods.

Changes in geopolitical conditions and U.S. critical minerals policy could reduce the strategic importance of our planned products and adversely affect our business.

A part of our business strategy is supported by the current geopolitical and national security environment, including ongoing trade tensions between the United States and China, China’s restrictions on exports of certain strategic minerals, and U.S. Government initiatives to strengthen domestic supply chains for critical minerals. These developments have increased interest in and public support for U.S.-based critical mineral projects like the Elk Creek Project.

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There is no assurance that these conditions will persist or that the Elk Creek Project will benefit from this strategic focus. Certain government agencies may possess the means to finance only a limited number of critical minerals projects, which could result in fewer projects being funded and increased competition for such support. Our ability to obtain funds or incentives from U.S. Government sources is subject to the availability of funds under applicable government programs and there is no guarantee that there will be opportunities for us to receive such financing or support or that we will be successful in obtaining any grants, awards, loans, or other incentives.

Any improvement in U.S.-China relations, reduction or removal of tariffs or export controls, a shift in U.S. Government priorities regarding access to critical minerals, or identification of other readily available sources of our planned products, could decrease or eliminate the perceived strategic value of domestic production of certain strategic minerals, including scandium, dysprosium and terbium. Similarly, if China were to resume or expand exports of certain strategic minerals, including scandium, dysprosium and terbium, global supply and pricing dynamics could change materially, which could reduce the focus on developing U.S.-based projects.

In addition, U.S. Government agencies, including the DoW, may decide not to continue, or may significantly reduce efforts, to promote domestic critical minerals development. If U.S. Government interest or policy support for domestic critical mineral projects declines, our ability to secure project financing and establish the commercial viability of the Elk Creek Project could be adversely affected. Any such decline could have a material adverse effect on our business, results of operations, and financial condition.

Difficulties in water balance management at our Elk Creek Project could negatively affect our potential production and economics at the project.

The Company has conducted three field investigations and two major technical studies into the hydrogeology of the Elk Creek carbonatite, which is the geologic formation which hosts the mineralized material that would be extracted by the Company’s mining operations. The Company expects to encounter significant amounts of water in the carbonatite, which will need to be pumped out of the formation to facilitate a mining operation. Water quality analyses have demonstrated that this water will have elevated temperature and salt content when compared to other water resources in the area. While the Company has developed plans to treat water produced from the mine for use in its operations, there is no guarantee that the permits needed for the treatment of the water or the disposal of the resultant waste products will be issued by the State of Nebraska, nor is there any guarantee that such permits will be issued in a timely fashion. Further, based on such plans, the operations will rely on a water treatment system to achieve zero discharge of wastewater, and there is no guarantee that this system will function as designed or achieve nameplate treatment capacity.

Title to our properties may be subject to other claims that could affect our property rights and claims.

There are risks that title to our properties may be challenged or impugned. Our Elk Creek Project is located in Nebraska and may be subject to prior unrecorded agreements or transfers or native land claims, and title may be affected by undetected defects. The property we already own will allow us to construct the Elk Creek Project once sufficient project financing is obtained. Our current land and/or mineral rights lease agreements between ECRC and individual landowners give us an OTP, which may be used to support potential future operations, additional mineral exploration activities, and expansion. The rights of the current owners to sell the property subject to these options may be subject to prior unrecorded or unknown claims to title. Further, our current OTP agreements are of fixed duration and expire between December 2029 and May 2040, and we may incur additional cost and delays in securing renewals of such OTPs. We have investigated our rights to explore and exploit the Elk Creek Project resource/reserve and, to the best of our knowledge, our rights in relation to lands covering the Elk Creek Project resource/reserve are in good standing. However, there may be valid challenges to the title of our properties that, if successful, could impair development and/or operations.

Our properties and operations may be subject to litigation or other claims.

From time to time our properties or operations may be subject to disputes that may result in litigation or other legal claims. We may be required to assert or defend against these claims, which will divert resources and management time from operations. The costs of these claims or adverse filings may have a material effect on our business and results of operations.

We do not currently insure against all the risks and hazards of mineral exploration, development, and mining operations.

Exploration, development, mining, and surface operations involve various hazards, including environmental hazards, industrial accidents, metallurgical and other processing problems, unusual or unexpected rock formations, structural cave-ins or slides, flooding, fires, and periodic interruptions due to inclement or hazardous weather conditions. These risks could result in damage to or destruction of mineral properties, facilities, or other property, personal injury, environmental damage, delays in operations, increased cost of operations, monetary losses, and possible legal liability. We may not be able to obtain insurance to cover these risks at economically feasible premiums or at all. We may elect not to insure where premium costs are

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disproportionate to our perception of the relevant risks. The payment of such insurance premiums and of such liabilities would reduce the funds available for exploration and production activities.

We may not be able to obtain or renew all required permits and licenses to place any of our properties into production.

Our current and future operations, including development activities and commencement of production, if warranted, on the Elk Creek Project, require permits from governmental authorities and such operations are and will be governed by laws and regulations governing prospecting, development, mining, production, exports, taxes, labor standards, occupational health, waste disposal, toxic substances, land use, environmental protection, mine safety, and other matters. Companies engaged in mineral property exploration and the development or operation of mines and related facilities generally experience increased costs, as well as delays in production and other schedules as a result of the need to comply with applicable laws, regulations, and permits. We cannot predict if all permits that we may require for continued exploration, development, or construction of mining facilities and conduct of mining operations will be obtainable or renewable on reasonable terms, if at all. Costs related to applying for and obtaining permits and licenses may be prohibitive and could delay our planned exploration and development activities. Failure to comply with applicable laws, regulations, and permitting requirements may result in enforcement actions, including orders issued by regulatory or judicial authorities causing operations to cease or be curtailed, and may include corrective measures requiring capital expenditures, installation of additional equipment, or remedial actions.

Facilities associated with the Elk Creek Project, such as the mine, surface plant, tailings facilities, stockpiles and supporting infrastructure, are likely to either temporarily or permanently impact water bodies and wetlands that are subject to regulation by the USACE as Waters of the United States (“WOUS”). We believe that we have obtained the necessary USACE permits to construct the project, but changes to the design or layout of the facility may trigger the USACE to require us to obtain and maintain additional permits for the Elk Creek Project. The duration of this permitting exercise is dictated by the USACE and would need to be completed before facilities that would impact WOUS could be constructed. We may experience delays or additional costs in relation to obtaining the necessary permits and these delays and additional costs could negatively affect the economics of the Elk Creek Project and our results of operations.

Parties engaged in mining operations may be required to compensate those suffering loss or damage by reason of the mining activities and may have civil or criminal fines or penalties imposed for violations of applicable laws or regulations. Amendments to current laws, regulations, and permits governing operations and activities of mining companies, or more stringent implementation thereof, could have a material adverse impact on our operations and cause increases in capital expenditures or production costs or reduction in levels of production at producing properties or require abandonment or delays in development of new mining properties.

We are subject to significant governmental regulations that affect our operations and costs of conducting our business.

Our current and future operations, including development of the Elk Creek Project, are and will be governed by laws and regulations, including:

•
laws and regulations governing mineral concession acquisition, prospecting, development, mining, and production;
•
laws and regulations related to exports, taxes, and fees;
•
labor standards and regulations related to occupational health and mine safety; and
•
environmental standards and regulations related to waste disposal, toxic substances, land use reclamation, and environmental protection.

Companies engaged in development activities often experience increased costs and delays in production and other schedules as a result of the need to comply with applicable laws, regulations, and permits. Failure to comply with applicable laws, regulations, and permits may result in enforcement actions, including the forfeiture of mineral claims or other mineral tenures and/or orders issued by regulatory or judicial authorities requiring operations to cease or be curtailed, and may include corrective measures requiring capital expenditures, installation of additional equipment, or costly remedial actions. We may be required to compensate those suffering loss or damage by reason of our development activities and may have civil or criminal fines or penalties imposed for violations of such laws, regulations, and permits.

Existing and possible future laws, regulations, and permits governing operations and activities of mineral development companies, or more stringent implementation, could have a material adverse impact on our business and cause increases in capital expenditures or require abandonment or delays in development. Our Elk Creek Project is located in Nebraska, and while the State does have a comprehensive and modern set of environmental regulations, it does not have specific regulations with respect to permitting or reclaiming mines which could potentially impact the total time to market for the project.

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Our activities are subject to environmental laws and regulations that may change, thereby increasing our costs of doing business and restricting our operations.

All phases of our operations are subject to environmental regulation in the jurisdictions in which we operate. Environmental legislation is evolving in a manner that may require stricter standards and enforcement, increased fines and penalties for non-compliance, more stringent environmental assessments of proposed projects, and a heightened degree of responsibility for companies and their officers, directors, and employees. These laws address emissions into the air, discharges into water, management of waste, management of hazardous substances, protection of natural resources, antiquities and endangered species, and reclamation of lands disturbed by mining operations. Compliance with environmental laws and regulations, and future changes in these laws and regulations, may require significant capital outlays and may cause material changes or delays in our operations and future activities. It is possible that future changes in these laws or regulations could have a significant adverse impact on our properties or some portion of our business, causing us to re-evaluate those activities at that time.

Regulations and pending legislation governing issues involving climate change could result in increased operating costs, which could have a material adverse effect on our business.

A number of governments or governmental bodies have introduced or are contemplating legislative and/or regulatory changes in response to concerns about the potential impact of climate change. Legislation and increased regulation regarding climate change could impose significant costs on us, on our future venture partners, if any, and on our suppliers, including costs related to increased energy requirements, capital equipment, environmental monitoring and reporting, and other costs necessary to comply with such regulations. Any adopted future climate change regulations could also negatively impact our ability to compete with companies situated in areas not subject to such limitations. Given the emotion, political significance, and uncertainty surrounding the impact of climate change and how it should be dealt with, we cannot predict how legislation and regulation will affect our financial condition, operating performance, and ability to compete. Furthermore, even without such regulation, increased awareness and any adverse publicity in the global marketplace about potential impacts on climate change by us or other companies in our industry could harm our reputation. The potential physical impacts of climate change on our operations are highly uncertain and could be particular to the geographic circumstances in areas in which we operate and may include changes in rainfall and storm patterns and intensities, water shortages, changing sea levels, and changing temperatures. These impacts may adversely impact the cost, production, and financial performance of our operations.

Our failure to comply with applicable anti-corruption, anti-bribery, anti-money laundering and similar laws and regulations could negatively impact our reputation and results of operations.

Our governance and compliance policies and processes may not prevent potential breaches of law or accounting or other governance practices. Our operating and ethical codes, among other standards and guidance, may not prevent instances of fraudulent behavior and dishonesty, nor guarantee compliance with legal and regulatory requirements.

We may be required to comply with anti-corruption laws and regulations imposed by governments with jurisdiction over our operations, which may include U.S. and Canadian anti-bribery and corruption legislation, as well as the laws of other countries where we do business or have a close connection. These laws and regulations may restrict our operations, trade practices, investment decisions, and partnering activities. We are subject to the jurisdiction of various governments and regulatory agencies around the world, which may bring our personnel and representatives into contact with “foreign officials” responsible for issuing or renewing permits, licenses or approvals or for enforcing other governmental regulations.

Our failure to successfully comply with these laws and regulations may expose us to reputational harm, as well as significant sanctions, including criminal fines, imprisonment, civil penalties, disgorgement of profits, injunctions, and debarment from government contracts, as well as other remedial measures. Investigations of alleged violations can be expensive and disruptive. Compliance, on the other hand, often adds cost and complexity to the permitting process and subsequent operations. There can be no guarantee that we will effectively prevent violations by our employees or business partners acting on our behalf, for which we may be held responsible, and any such violation could adversely affect our reputation, business, results of operations and financial condition.

Land reclamation requirements for our properties may be burdensome and expensive.

Although variable depending on location and the governing authority, land reclamation requirements are generally imposed on mineral exploration companies (as well as companies with mining operations) in order to minimize long-term effects of land disturbance.

Reclamation may include requirements to:

•
control dispersion of potentially deleterious effluents;
•
treat ground and surface water to achieve water quality standards; and

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•
reasonably re-establish pre-disturbance landforms and vegetation.

In order to carry out reclamation obligations imposed on us in connection with our potential development activities, we must allocate financial resources that might otherwise be spent on further exploration and development programs. We plan to set up a provision for our reclamation obligations on our properties, as appropriate, but this provision may not be adequate. If we are required to carry out unanticipated reclamation work, our financial position could be adversely affected.

We expect to incur substantial debt in connection with the Elk Creek Project, which will require a significant amount of cash to service, require us to comply with certain covenants and restrictions, and could impair our ability to obtain additional financing.

We expect to incur substantial debt as part of our plan to obtain project financing sufficient to cover initial capital costs and other related expenses necessary to the commencement and completion of construction of the Elk Creek Project, which may include, but is not limited to, the EXIM Financing. We currently anticipate that the upfront capital expenditure amount for the Elk Creek Project will be funded through a combination of debt and equity financing, with approximately 65% of such amount being funded from the net proceeds of debt financing. We will require a significant amount of cash to service any future debt obligations and our ability to generate cash will depend on our future operations, which are subject to prevailing industry conditions and other factors, many of which are beyond our control. We also expect that any agreements governing our future indebtedness will require us to comply with certain covenants and restrictions that limit our ability to engage in activities that may be in our long-term best interests. Any failure to comply with such covenants and restrictions could adversely affect our reputation, business, results of operations and financial condition.

In addition, our articles of incorporation do not limit the amount of indebtedness that we may incur. Any substantial indebtedness could impair our ability to obtain additional financing on a timely basis, or at all, for working capital or to take advantage of business opportunities that may arise.

NioCorp may be a “passive foreign investment company” for the current taxable year and for one or more future taxable years, which may result in materially adverse U.S. federal income tax consequences for U.S. investors.

If NioCorp is a passive foreign investment company (“PFIC”) for any taxable year, or portion thereof, that is included in the holding period of a U.S. holder of Common Shares or other securities of NioCorp, such U.S. holder may be subject to certain adverse U.S. federal income tax consequences. These adverse tax consequences include requirements to treat any gain realized upon a disposition of Common Shares or other securities, or any “excess distribution” received on Common Shares, as ordinary income, to pay an interest charge on a portion of such gain or distribution, and certain additional reporting requirements. Such consequences may be mitigated with respect to Common Shares (but not with respect to Warrants or other securities of NioCorp) if the holder thereof makes a timely and effective “qualified electing fund” or “QEF” election or a “mark-to-market” election. A U.S. holder of Common Shares that makes a QEF election generally must include in income on a current basis for U.S. federal income tax purposes its share of NioCorp’s net capital gain and ordinary earnings for any taxable year in which it is a PFIC, whether or not NioCorp distributes any amount to its shareholders. A U.S. holder of Common Shares that makes a mark-to-market election generally must include as ordinary income each year the excess of the fair market value of the Common Shares over the taxpayer’s basis therein.

NioCorp generally will be classified as a PFIC for a taxable year if (a) 75% or more of its gross income for such year is “passive income” (generally, dividends, interest, rents, royalties, and gains from the disposition of assets producing passive income) or (b) at least 50% or more of the value of its assets produce, or are held for the production of, passive income, based on the quarterly average of the fair market value of such assets. NioCorp believes that it was classified as a PFIC for its taxable years ended June 30, 2026 and 2025 and, based on the current composition of its income and assets, as well as current business plans and financial expectations, may be classified as a PFIC for its current or future taxable years. Any conclusion regarding PFIC status is a factual determination that must be made annually at the close of each taxable year and, thus, is subject to change. In addition, even if NioCorp concluded it did not qualify as a PFIC, it is possible that the U.S. Internal Revenue Service (the “IRS”) could assert, and that a court could sustain, a determination that NioCorp is a PFIC. Accordingly, there can be no assurance that NioCorp will not be treated as a PFIC for any taxable year. The PFIC rules are complex and each holder of Common Shares or other securities of NioCorp should consult its own tax advisors regarding these rules and the U.S. federal income tax consequences of the acquisition, ownership, and disposition of such securities.

The 2023 business combination with GXII could result in NioCorp becoming subject to materially adverse U.S. federal income tax consequences.

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Section 7874 and related sections of the U.S. Internal Revenue Code of 1986, as amended (the “Code”), provide for certain adverse tax consequences when the stock of a U.S. corporation is acquired by a non-U.S. corporation in certain transactions in which former shareholders of the U.S. corporation come to own 60% or more of the stock of the non-U.S. corporation (by vote or value, and applying certain specific counting and ownership rules). These adverse tax consequences include (i) potential additional required gain recognition by the U.S. corporation, (ii) treatment of certain payments to the non-U.S. corporation that reduce gross income as “base erosion payments,” (iii) an excise tax on certain options and stock-based compensation of the U.S. corporation, (iv) disallowance of “qualified dividend” treatment for distributions by the non-U.S. corporation, and (v) if former shareholders of the U.S. corporation come to own 80% or more of the stock of the non-U.S. corporation, treatment of the non-U.S. corporation as a U.S. corporation subject to U.S. federal income tax on its worldwide income (in addition to any tax imposed by non-U.S. jurisdictions). If the 2023 business combination with GXII results in the application of any of these, or any other, adverse tax consequences, NioCorp could incur significant additional tax costs. While NioCorp currently does not believe the 2023 business combination with GXII will cause such adverse tax consequences as a result of Section 7874 and related sections of the Code, this determination is subject to significant legal and factual uncertainty. NioCorp has not sought and will not seek any rulings from the IRS as to the tax treatment of the 2023 business combination with GXII or any related transactions. Further, there can be no assurance that your tax advisor, the IRS, or a court, will agree with the position that NioCorp is not subject to these adverse tax consequences.

Our Common Share price may be volatile and as a result you could lose all or part of your investment.

In addition to volatility associated with equity securities in general, the value of your investment could decline due to the impact of any of the following factors upon the market price of the Common Shares:

•
material changes to mineral resource/reserve estimates, grades of mineralization or economic viability of the Elk Creek Project;
•
our ability to obtain sufficient financing for the Elk Creek Project;
•
decline in demand for Common Shares;
•
downward revisions in securities analysts’ estimates or changes in general market conditions;
•
technological innovations by competitors or in competing technologies;
•
investor perception of our industry or our prospects;
•
the impact of trade policies and tariffs, or changes and uncertainties related thereto; and
•
general economic trends.

In particular, any material reductions in resource/reserve estimates, material increases in capital or operating costs relative to those reflected in the 2026 S-K 1300 Elk Creek Technical Report Summary, or other adverse changes to project economics could have a material adverse effect on the value of our properties and the market price of our Common Shares. See “We face numerous uncertainties in estimating our mineral reserves and resources and inaccuracies in our estimates could result in lower than expected revenues, higher than expected costs, and decreased profitability” in Item 1A., Risk Factors above.

From July 1, 2025, to the date of this report, the trading price of our stock on the Nasdaq has ranged from a low of $2.19 to a high of $11.67.

In addition, stock markets in general have experienced extreme price and volume fluctuations, and the market prices of securities have been highly volatile. These fluctuations are often unrelated to operating performance and may adversely affect the market price of the Common Shares. As a result, you may be unable to sell any Common Shares you acquire at a desired price.

We have never paid dividends on the Common Shares.

We have not paid dividends on the Common Shares to date, and we may not be in a position to pay dividends for the foreseeable future. Our ability to pay dividends with respect to the Common Shares will depend on our ability to successfully develop one or more properties and generate earnings from operations. Further, our initial earnings, if any, will likely be retained to finance our operations. Any future dividends on Common Shares will depend upon our earnings, our then-existing financial requirements, and other factors, and will be at the discretion of our Board.

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Future sales, or the perception of future sales, of Common Shares by existing shareholders or by us, or future dilutive issuances of Common Shares by us, or future exercises or exchanges of outstanding Warrants or securities exchangeable for Common Shares, could adversely affect prevailing market prices for the Common Shares and cause investors to suffer dilution in their net book value per Common Share.

In addition to potential debt financing, our plan to obtain project financing sufficient to cover initial capital costs and other related expenses necessary to the commencement and completion of construction of the Elk Creek Project includes the sale and issuance of equity securities which may include, but is not limited to, Common Shares, Warrants, or pre-funded Warrants. Sales of a substantial number of Common Shares in the public market could occur at any time, including issuances and sales of additional Common Shares by us and sales by other security holders. These sales, or the market perception that the holders of a large number of Common Shares or securities convertible, exercisable, or exchangeable into Common Shares intend to sell Common Shares, could reduce the prevailing market price of the Common Shares. The effect, if any, that future public sales of these securities or the availability of these securities for sale will have on the market price of the Common Shares is uncertain. If the market price of the Common Shares were to drop as a result, this might impede our ability to raise additional capital and might cause remaining shareholders to lose all or part of their investment.

The Articles of NioCorp, as amended, permit us to issue an unlimited number of Common Shares. Subject to the requirements of the British Columbia Business Corporations Act and Nasdaq, we will not be required to obtain the approval of the NioCorp shareholders for the issuance of additional Common Shares. We have issued Common Shares in the past and intend to continue to issue Common Shares to finance our activities in the future. In addition, outstanding Options and Warrants and securities convertible into or exchangeable for Common Shares may be exercised, converted, or exchanged resulting in the issuance of additional Common Shares. If we issue additional Common Shares or decide to enter into joint ventures with other parties in order to raise financing through the sale of equity securities, investors’ interests in the Company will be diluted and investors may suffer dilution in their net book value per Common Share depending on the price at which such securities are sold.

We are subject to the continued listing criteria of the Nasdaq and our failure to satisfy these criteria may result in delisting of the Common Shares.

Our Common Shares are currently listed on the Nasdaq under the symbol “NB”. The public NioCorp Assumed Warrants are currently listed on Nasdaq under the symbol “NIOBW.” The Nasdaq has rules for continued listing. In order to maintain the listings, we must maintain certain financial and share distribution targets, including maintaining a minimum number of public shareholders.

If Nasdaq delists the Common Shares, investors may face material adverse consequences, including, but not limited to, a lack of a trading market for the Common Shares, reduced liquidity, a determination that our Common Shares are a “penny stock,” decreased analyst coverage of the Company, and an inability for us to obtain additional financing to fund our operations.

Our Rights Plan includes terms and conditions that could discourage a take-over or other transaction that shareholders may consider favorable.

On November 21, 2025, the Company adopted the Rights Plan pursuant to the Original Rights Plan Agreement, between the Company and the Rights Agent. One Right was issued for each Common Share outstanding as of December 4, 2025, and a Right automatically attaches to each Common Share subsequently issued until the expiration of the Rights Plan. The Rights generally become exercisable only if a person or group acquires, or announces the current intention of commencing a take-over bid to acquire, beneficial ownership of 20% or more of the Company's outstanding Common Shares, other than through a permitted bid made in compliance with applicable Canadian take-over bid rules. If the Rights become exercisable, each holder of a Right, other than the acquiring person, would be entitled to purchase additional Common Shares at a discount to the then-current market price.

On April 6, 2026, following approval by the Company's shareholders at the Company's annual general meeting held on April 6, 2026, the Company and the Rights Agent entered into the Amended Rights Plan Agreement, which amended and restated the Original Rights Plan Agreement in its entirety. Under the Original Rights Plan Agreement, the Rights Plan would have expired on May 21, 2026. Under the Amended Rights Plan Agreement, the Rights Plan now expires at 5:00 p.m. (Toronto time) on the date of the Company's next annual general meeting.

The Board adopted the Rights Plan to help ensure that all shareholders of the Company are treated equally and fairly in the event of any unsolicited take-over bid or other attempt to acquire control of the Company (including by way of a “creeping take-over bid”). The Rights Plan was not adopted in response to any specific take-over bid or other proposal to acquire control of the Company.

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The Rights Plan will cause substantial dilution to any person, entity or group that acquires beneficial ownership of 20% or more of the outstanding Common Shares. As a result, the overall effect of the Rights Plan and the issuance of the Rights may be to discourage any person, entity or group from gaining a control or control-like position in the Company or engaging in other tactics, potentially disadvantaging the interests of the Company’s shareholders, without negotiating with the Board and without paying an appropriate control premium to all shareholders. The Rights Plan is intended to, among other things, (i) encourage potential bidders to treat the Company’s shareholders fairly and equally and preserve control premiums and value for shareholders and (ii) provide the Board and shareholders adequate time to appropriately respond on an informed basis. Nevertheless, the Rights Plan may be considered to have certain anti-take-over effects, including potentially discouraging a third party from attempting to obtain a substantial position in the Common Shares or seeking to obtain control of the Company and discouraging a take-over attempt that shareholders may consider favorable or that could result in a premium over the market price of the Common Shares. Even in the absence of a take-over attempt, the Rights Plan may adversely affect the prevailing market price of Common Shares if it is viewed as discouraging take-over attempts in the future.

ITEM 1B. UNRESOLVED STAFF COMMENTS

None.

ITEM 1C. CYBERSECURITY

Cybersecurity risk management is integrated into the Company’s enterprise-wide risk management. Our Board has overall oversight responsibility for our risk management and management is responsible for identifying, considering, and assessing material risks to the Company. Our Chief Financial Officer is responsible for assessing and managing cybersecurity risks; however, as a smaller reporting company, we currently do not have a dedicated cybersecurity team. Our Chief Financial Officer reports to the Board regarding financial and operating risks, including cybersecurity risks. Our Chief Financial Officer has experience in managing public companies and assessing financial and operating risks.

Our cybersecurity risk management is designed to provide a framework for assessing, identifying, and managing material risks from cybersecurity threats and to respond to cybersecurity incidents, including material risks associated with the use of services provided by third-party service providers. We rely on the cybersecurity protections of many of our third-party service providers. Our primary third-party service providers utilize two-factor authentication as well as login and password protections with email verifications.

We are in the process of evaluating our cybersecurity needs and developing appropriate measures to enhance our cybersecurity posture. Our goal is to establish a cybersecurity framework that is commensurate with our size, complexity, and nature of our operations.

We have experienced cybersecurity threats and cybersecurity incidents in the past, and may experience cybersecurity threats and cybersecurity incidents in the future. For the year ended June 30, 2026, the Company had no material cybersecurity incidents or threats that have materially affected or were reasonably likely to materially affect our business strategy, results of operations or financial condition. Despite our efforts, we cannot eliminate all risks from cybersecurity threats or provide assurances that we have not experienced an undetected cybersecurity incident.

ITEM 2. PROPERTIES

Elk Creek Project, Nebraska

Our principal mineral property is the Elk Creek Property, a development stage property that is expected to produce eight commercial mineral products: ferroniobium, scandium oxide, titanium tetrachloride, neodymium-praseodymium (“NdPr”) oxide, dysprosium oxide, terbium (“Tb”) oxide, SEG carbonate, and heavy rare earth ("heavies") carbonate. As discussed in greater detail below, the Elk Creek Project has established measured, indicated, and inferred resources along with proven and probable reserves. The below information is in part summarized or extracted from our 2026 S-K 1300 Elk Creek Technical Report Summary, which is filed as Exhibit 96.1 to this Annual Report on Form 10-K. The 2026 S-K 1300 Elk Creek Technical Report Summary has an overall effective date of June 30, 2026. The Company does not have any other material properties.

The qualified persons responsible for the 2026 S-K 1300 Elk Creek Technical Report Summary are:

•
Dahrouge Geological Consulting USA Ltd.;
•
SMH Process Innovation;

25


 

•
Dumas Contracting USA Inc.;
•
Amplify Mine Planning LLC;
•
BBA Consultants International LP (formerly Tierra Group International, Ltd.);
•
Olsson;
•
Adrian Brown Consultants Inc.;
•
Andrieux & Associates Geomechanics Consulting, L.P.;
•
Tetra Tech;
•
Metallurgy Concept Solutions;
•
Magemi Mining Inc.;
•
T Engineering; and
•
Scott Honan, M.Sc., SME-RM, NioCorp.

A table of the sections for which each qualified person is responsible is included in Section 2.6 of the 2026 S-K 1300 Elk Creek Technical Report Summary. Except for Scott Honan, none of the qualified persons is affiliated with the Company. Mr. Honan is the Chief Operating Officer of the Company. The disclosure of scientific or technical information in this Annual Report on Form 10-K was reviewed and approved by Mr. Honan who is a qualified person as defined in NI 43-101, and Mr. Honan has verified the data disclosed herein.

The 2026 S-K 1300 Elk Creek Technical Report Summary summarizes the 2026 Elk Creek Study, which, among other matters, updates the Elk Creek Project’s economics to incorporate the expanded product offering, including REEs, revises mine and processing design, and updates mineral resource and mineral reserve estimates and current capital and operating cost estimates. The 2026 Elk Creek Study comprises the results of the technical and economic analyses conducted by the qualified persons, which were also presented in the 2026 NI 43-101 Elk Creek Technical Report. The 2026 Elk Creek Study qualifies as a feasibility study within the meaning given to such term under the CIM Definition Standards (2014) for purposes of NI 43-101 and qualifies as a pre-feasibility study within the meaning given to such term under S-K 1300. The reason that the 2026 Elk Creek Study does not qualify as a feasibility study under S-K 1300 is because additional work with respect to the engineering of and procurement for the planned surface plant is required to allow the qualified person to reduce the overall contingency range attributed to the initial capital expenditure estimate for the Elk Creek Project from the current 14% to less than or equal to 10%. Even as additional work is completed and the contingency range is reduced, accordingly, there can be no assurance that the actual initial capital expenditure requirements will not materially exceed estimates.

Property Description and Location

The Elk Creek Property consists of certain interests of NioCorp in land and mineral rights located in Johnson and Pawnee Counties, southeast Nebraska, USA. The carbonatite contains elements of economic significance, including niobium, titanium, and scandium, as well as several REEs. The Elk Creek Property is situated as shown below and is located within the USGS Tecumseh Quadrangle Nebraska SE (7.5 minute series) mapsheet in Sections 1-6, 9-11; Township 3N; Range 11E and Sections 19-23, 25-36; Township 4N, Range 11E, at approximately 40°16’ north and 96°11’ west in the State of Nebraska, in central USA. The Elk Creek Property is approximately 47 miles southeast of Lincoln, Nebraska, the state capital of Nebraska.

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img85804497_1.gif

Title and Ownership

Land in the project area is exclusively owned by private entities, and there is no federal or state land in the project area. The Company has secured its rights to the project area by purchasing land from private landowners or by entering into agreements with the landowners as described below.

Following the acquisition of an additional approximately 447 acres of land pursuant to existing OTPs during fiscal year 2026, the Company, through its subsidiary ECRC, owns the surface rights and/or mineral rights to approximately 710 acres of land in and around the project area. This includes an approximately one-square-mile (approximately 630-acre) section of which it owns the mineral rights to all but approximately 80 acres and all of the surface rights, all within the carbonatite footprint. The Elk Creek Project’s mine infrastructure and a portion of the supporting operations is planned to be located within this section. Ownership of the mineral rights in this section includes a 2% NSR royalty and grants us access to all of the Elk Creek Project’s mineral resources and mineral reserves.

The land owned by ECRC currently houses the Company’s drill core inventory and geological sample repository in two steel core shed buildings, and the Company maintains vegetative cover on portions of the property that were formerly used for growing row crops. Additionally, the Company has begun construction of the main access, known as a “portal,” to the underground portion of the Elk Creek Project on the land owned by ECRC. The portal will serve as the primary access point for personnel, equipment, and materials, as well as to deliver ore from the underground mine to the surface production plant.

As of June 30, 2026, the total book value of the Elk Creek Property and associated buildings and equipment was approximately $37.3 million.

The Company also currently holds six OTPs that are associated with the Elk Creek Project and one perpetual easement on a land parcel adjacent to the Missouri River. The current optioned land package covers an area of approximately 1,011 acres and includes the land needed for the development of tailings storage facilities that are expected to be developed in phases over the Elk Creek Project’s proposed 40-year operating life. Details on the current OTPs held by the Company are shown in the table below.

Active Lease Agreements (OTPs) Covering the Elk Creek Project as of September 2026

Agreement Identifier

 

Acres

 

Agreement Expiry

Beethe007

 

163.75

 

January 20, 2031

Heidemann005

 

196.57

 

March 16, 2030

Nielsen001

 

249.82

 

June 25, 2030

Woltemath002

 

257.03

 

December 4, 2029

Krueger001

 

63.79

 

November 12, 2030

Shuey001

 

80.00

 

May 27, 2040

 

27


 

The OTPs are between NioCorp’s subsidiary ECRC and the individual landowners. Land subject to the OTP agreements is currently used for agricultural purposes, including growing row crops (corn and soybeans) and pasturing livestock. The OTPs grant the Company an exclusive right to explore and evaluate the property during the term thereof, with an option to purchase the surface rights or a combination of the mineral and surface rights at any time during the term. The OTPs that involve mineral rights provide for a 2% NSR royalty.

In general, exercise of an OTP is accomplished by paying the greater of a fixed amount per acre or a multiple of the appraised value at the time of purchase. If the land is not purchased by the Company during the term of the OTP and the land in question is needed for the Elk Creek Project, the Company intends to negotiate a new OTP with the landowner. Each OTP is accompanied by a negotiated payment to the landowner that is paid upon execution of the OTP by the Company and the landowner. As of June 30, 2026, the Company was obligated to make payments totaling approximately $48 over the next 9 years to maintain our rights under these OTPs.

Land Tenure Map as of September 2026

img85804497_2.jpg

Accessibility, Climate, Local Resources, Infrastructure and Physiography

The Elk Creek Property is easily accessible year-round as it is situated approximately 47 miles southeast of Lincoln, Nebraska, the state capital, and approximately 68 miles south of Omaha, Nebraska. Access to the site can be completed via interstates and state highways or from one of the regional airports. There are several regularly scheduled flights to both Lincoln and Omaha, with Omaha providing more regular commercially serviced options. From Eppley Airfield in Omaha, Nebraska, the Elk Creek Property is accessed via paved roads on the main network. The section in which the Company plans to construct both the underground critical minerals mine and integrated surface processing facility associated with the Elk Creek Project, and where the mineral resource and mineral reserve are centered, is in Section 33, Township 4N, Range 11E within the USGS Tecumseh Quadrangle Nebraska SE (7.5 minute series) mapsheet. This section is immediately southwest of the junction of Nebraska state highways 50 and 62, which turns into county road 721 west of state highway 50. The Elk Creek Project will be accessed from the north from county road 721. A secondary access point is available on the east side of the project from state highway 50. Rail access is available in the town of Elk Creek, which is located 3 miles east of the project area.

Southeast Nebraska is situated in a humid continental climate (Dfa) on the Köppen climate classification system. In eastern Nebraska, this climate is generally characterized by hot, humid summers and cold winters. Average winter temperatures vary between 13°F to 35°F. Average summer temperatures vary between 65°F to 88°F. Exploration and mining-related activities may be conducted all year round although severe winter weather and spring/early-summer thunderstorm activity can periodically affect operations.

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Average monthly precipitation (rain and liquid-equivalent snowfall) varies between 0.8 and 5.3 inches, with a mean annual total of approximately 32.3 inches. Average snowfall is approximately 22 inches. Nebraska is located within a region of the central United States that experiences severe thunderstorms and tornadoes, with peak tornado occurrence generally during May through July, although events can occur outside this period.

The area is well developed with direct access to roads, rail, supply and distribution companies, and a local workforce, including heavy equipment operators. There are several local communities near the Elk Creek Property, including Elk Creek, Syracuse, Tecumseh and Pawnee City, that are capable of providing local housing for the Elk Creek Project construction and operating staff. There are several other communities within driving distance and the large cities of Lincoln and Omaha are also within reasonable driving distance. Both cities have substantial regional airports.

The Elk Creek Project is expected to incorporate surface and underground infrastructure, as well as surface tailings and salt storage facilities. The offsite infrastructure is expected to include a water supply pipeline from the City of Tecumseh and temporary and permanent natural gas pipelines. On-site power is expected to be provided by a third-party microgrid using modular 2.5 megawatts ("MW") natural gas generators, rated at approximately 50 MW. Initially, a 15 MW construction microgrid is expected to be supplied, with gas from trucked liquefied natural gas and/or a temporary pipeline connection approximately 5 miles east. A permanent gas pipeline from a main distribution line approximately 30 miles west is expected to be connected around the end of the second construction year. Before the end of construction, the larger 50 MW microgrid is expected to replace the construction microgrid. Approximately 200 kilowatts ("kW") of grid power from the local power utility is also expected to be utilized via an existing connection. Water used for all on-site process needs and activities is expected to be supplied from mine dewatering activities, recycling, and from a local water utility. See “Planned Operations” below for additional information regarding proposed infrastructure related to the Elk Creek Project.

The local topography of eastern Nebraska is relatively low-relief with shallow rolling hills intersected by shallow river valleys. Elevation varies from about 1,066 feet ("ft") to 1,276 ft above mean sea level. Bedrock outcrop exposure is nonexistent in the Elk Creek Project area.

The majority of the area around the Elk Creek Project is used for cultivation of corn and soybeans, along with uses as grazing land. Native vegetation typical of eastern Nebraska is upland tall-grass, prairie and upland deciduous forests.

Geology and Mineralization

Geology

The Elk Creek Property includes a carbonatite that has intruded older Precambrian granitic and low- to medium-grade metamorphic basement rocks. The carbonatite is an elliptical magmatic body with a northwest-trending long axis perpendicular to the strike of the Midcontinent Rift System, near the northern part of the Nemaha uplift. The carbonatite consists predominantly of dolomite, calcite and ankerite, with lesser chlorite, barite, phlogopite, pyrochlore, serpentine, fluorite, sulfides and quartz. It is, however, believed from stratigraphic reconstruction based on drill core observation in the area that the carbonatite is unconformably overlain by approximately 656 ft of essentially flat-lying Paleozoic marine sedimentary rocks, including carbonates, sandstones and shales of Pennsylvanian age.

Mineralization

The property hosts niobium, titanium, and scandium mineralization as well as REE mineralization that occurs within the Elk Creek carbonatite. The current extent of modeled mineralization is 3,937 ft (1,200 meters ("m")) along strike, 1,640 ft (500 m) wide, and 2,461 ft (750 m) in dip extent below the unconformity. Niobium, titanium, scandium, and rare earth elements are considered the main elements of interest.

The deposit contains significant concentrations of niobium. Based on the metallurgical test work completed to date at several laboratories using QEMSCAN® analysis, the niobium mineralization is known to be fine grained, and that 77% of the niobium occurs in the mineral pyrochlore, while the balance occurs in an iron-titanium-niobium oxide mineral of varying composition.

Within the Elk Creek carbonatite, a host of other elements exist with varying degrees of concentration. The Company has completed both whole rock analysis and multi-element analysis on all samples for the 2014 drilling program, described below, plus resampling of selected historical core/pulps between 2011 and 2021.

Historical Exploration

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Drilling at the Elk Creek Property has been conducted in four phases. The first was during the 1970’s and 1980’s by the Molybdenum Company of America (“Molycorp”), the second in 2011 by Quantum Rare Earth Developments Corp (“Quantum” - NioCorp under its former name), the third in 2014 and 2015 by NioCorp and the fourth and latest program in 2025 by NioCorp. To date, 94 drill holes have been completed on the section in which NioCorp plans to construct both the underground critical minerals mine and integrated surface processing facility associated with the Elk Creek Project for a total of 196,114 ft (59,775 m), including 16 drill holes totaling 37,861 ft (11,540 m) completed in 2025. A further five holes totaling 11,001 ft (3,353.1 m) were drilled in 2015 for hydrogeological and geotechnical studies but were not used for resource estimation.

All drilling has been completed using a combination of Tricone, Reverse Circulation (“RC”) or diamond drilling in the upper portion of the hole within the Pennsylvanian sediments. A portion of the 2014 drill holes used RC drilling within the Pennsylvanian sediments to increase drilling efficiency through cover material within areas of strong geological confidence. All drilling within the underlying carbonatite has been completed using diamond drilling methods.

Summary of Drilling Database within Elk Creek Deposit Area

 

Year

Company

Number of Holes in Carbonatite Complex

 

Number of Holes on Project

 

Project Hole Average Depth (m)

 

Project Hole Average Depth (ft)

 

Total Length (ft) Drillholes on Project

 

Total Length (m) Drillholes on Project

 

1971-1986

Molycorp

 

114

 

 

49

 

 

530

 

 

1,738

 

 

85,171

 

 

25,960

 

2011

Quantum

 

5

 

 

4

 

 

739

 

 

2,423

 

 

9,692

 

 

2,954

 

2014-2015

NioCorp

 

24

 

 

24

 

 

805

 

 

2,641

 

 

63,390

 

 

19,321

 

2025

NioCorp

 

17

 

 

17

 

 

679

 

 

2,227

 

 

37,861

 

 

11,540

 

Total

 

 

160

 

 

94

 

 

688

 

 

2,257

 

 

196,114

 

 

59,775

 

Exploration History

Private mineral leasing and exploration began in the early 1970s at the Elk Creek Property. Cominco American Inc. acquired mineral rights in 1973 and undertook exploration work, after which the rights were acquired by Molycorp in 1974. Molycorp completed detailed aeromagnetic surveying in 1973 and, in 1980, carried out a regional exploration program including gravity work, magnetic surveying, geologic mapping, surface sampling, and drilling. Between 1973 and 1986, Molycorp completed a regional drill program over an approximately 7 kilometers ("km") × 7 km gravity anomaly, totaling 114 drill holes for approximately 157,992 ft (48,156 m). Within the Elk Creek Deposit area, 27 holes totaling 52,848 ft (16,108 m) were drilled during the 1970–1980 period, forming the foundation of the historical drilling database.

No known exploration was completed on the Elk Creek Property between 1986 and 2011. In 2010–2011, Quantum initiated verification and modernization of the historical dataset through Dahrouge Geological Consulting Ltd., compiling and checking historical drilling, lithology, and assay information, and completing resampling of historical material to assess comparability with historical results. Quantum then completed a 2011 diamond drilling program consisting of five inclined holes totaling 11,220 ft (3,420 m) of HQ core; three holes 7,605 ft (2,318 m) targeted the Elk Creek deposit and two holes tested regional REE targets. These holes were not used for mineral resource estimation.

Following the acquisition of the Elk Creek Property, NioCorp advanced the Elk Creek Project through additional diamond drilling programs to improve confidence and support updated technical studies. Between 2014 and 2015 NioCorp drilled a total of 24 holes within the Elk Creek Deposit totaling approximately 63,390 ft (19,321 m). The program included data validation, metallurgical and mineralogical studies, geotechnical and hydrogeological studies all in support of resource estimation.

During fiscal year 2022, NioCorp collected a total of 1,095 samples originating from 18 diamond drill holes completed by Molycorp, as discussed above. These samples were collected, and subsequently assayed, in order to fill in gaps in our records regarding REE grades and tonnage that may exist in the deposit. Assaying was conducted at Activation Laboratories (“ActLabs”) in Ancaster, Ontario. The assay results were subjected to a Quality Assurance and Quality Control (“QA/QC”) program consistent with industry best practices.

During fiscal year 2026, NioCorp completed its previously announced drilling program at the Elk Creek Project (the “2025 Drilling Program”). The 2025 Drilling Program was specifically designed to target gaps within the mineral resource in support of converting a portion of the mineral resource from indicated and inferred to measured, indicated and inferred. During this campaign a total of 16 HQ diamond drillholes were completed totaling 37,861 ft (11,540 m). Assay results from the 2025 Drilling Program were added to the existing assay database and were used in the mineral resource estimate described below.

30


 

Samples from the 2025 Drilling Program were prepared and analyzed by SGS North America in Lakefield, ON. Selected pulp duplicates were submitted to ActLabs for external check analysis, with a total of 490 external pulps analyzed to test for laboratory bias. Both laboratories’ procedures were consistent with previous drilling and sampling programs.

Internal Controls

NioCorp integrated a series of routine QA/QC procedures throughout the sampling and analysis portion of the drilling programs to ensure the highest level of quality was maintained throughout the process leading to the estimate of mineral reserves and mineral resources for the Elk Creek Project. This included the insertion of duplicate samples taken from various stages of the process, insertion of known control samples (standard reference materials, certified reference materials (“CRM”), and blanks) and sending third-party pulps to a secondary lab.

To meet planned QA/QC insertion rates, the following guidelines were followed:

•
Field quartz blanks (1 in 20, or 5%) were inserted within or immediately after samples collected from mineralized intervals, targeting zones of elevated visual mineralization, where possible.
•
CRMs (1 in 20, or 5%) were inserted in the field with the sample sequence.
•
Field quarter-core duplicates (1 in 20, or 5%) were inserted to test mineralization and sampling variability.

Additional details on the QA/QC program can be found in Section 8 of the 2026 S-K 1300 Elk Creek Technical Report Summary.

Mineral deposits, including the Elk Creek deposit, are inherently uncertain because of variability at all scales and sparse sampling. In addition to uncertainty associated with estimation, there are specific risks and sources of uncertainty associated with the Elk Creek deposit. See Item 1A., Risk Factors.

S-K 1300 and other similarly purposed International Codes (JORC, 2012; NI 43-101, 2014) are designed to require disclosure to the public of risks relating to mineral resource and reserve estimation as identified and evaluated by a qualified person. The qualified persons responsible for the 2026 S-K 1300 Elk Creek Technical Report Summary address the technical risks in various sections and identify the principal sources of uncertainty as geological confidence at depth and along the margins of the peripheral carbonatite domain, the size of the inferred mineral resource relative to the measured and indicated mineral resources, and the sensitivity of the NSR cut-off to metallurgical recovery and to commodity prices, particularly niobium and scandium. Additional descriptions of the risks and uncertainty associated with reported mineral reserves and resources can be found in Section 11 of the 2026 S-K 1300 Elk Creek Technical Report Summary.

Economic Analysis Included in the 2026 S-K 1300 Elk Creek Technical Report Summary

The metrics reported in the 2026 S-K 1300 Elk Creek Technical Report Summary are based on the cash flow model results. The metrics are on both a pre-tax and after-tax basis, on a 100% equity basis with no Elk Creek Project financing inputs and are in first quarter 2027 U.S. constant dollars. Key criteria used in the analysis are discussed in detail throughout this section.

Principal Project Assumptions

Description

 

Value

 

 

Pre-Production Period

 

35 months

 

 

Process Plant Life

 

40 years

 

 

Mine Operating Days per Year

 

365

 

 

Mill Operating Days per Year

 

365

 

 

Discount Rate, End of Period

 

 

8

%

 

 

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Summary of Key Evaluation Metrics

The following table sets forth mine and process plant production estimates for the Elk Creek Project over the 40-year operating life of the mine. Ore mined and ore processed refer to proven and probable mineral reserves.

 

Description

 

Value

 

Ore Mined (short tons ("tons"))

 

45,929,462

 

Ore Mining Rate (tons/day)

 

3,047

 

Niobium Grade

 

0.76%

 

Scandium Grade (parts per million, “ppm”)

 

69.3

 

TiO2 Grade

 

2.68%

 

TREO Grade

 

0.34%

 

Contained Nb (tons)

 

205,464

 

Contained Sc2O3 (tons)

 

4,585

 

Contained TiCl4 (tons)

 

2,341,367

 

Contained TREO (tons)

 

53,309

 

Total Ore Processed (tons 000s)

 

45,929

 

Recovery, Nb

 

84.70%

 

Recovery Sc

 

94.30%

 

Recovery Ti

 

80.50%

 

Recovery NdPr

 

93.04%

 

Recovery Tb

 

94.40%

 

Recovery Dy

 

94.60%

 

Summary Pricing Assumptions

The following table sets forth applicable benchmark product pricing assumptions used in the economic analysis. Except with respect to scandium trioxide, the economic analysis assumes constant prices with no inflationary adjustments. The realized pricing used in the economic analysis was based on a combination of third-party market studies, qualified person judgment, and management expertise to establish appropriate market pricing projections. The planned products of the Elk Creek Project, especially niobium and Sc2O3, are thinly traded without an established publicly available price discovery mechanism. Hence, detailed third-party market studies were completed for all four of the major product groups that are expected to be produced from the Elk Creek Project: niobium, titanium, scandium and rare earths. These market studies analyzed relevant factors, including supply and demand trends, in order to forecast market pricing. For scandium and the heavy rare earths dysprosium and terbium, for example, the relevant market studies describe a bifurcated market between China and the rest of the world as a result of export controls implemented by China, which has resulted in prices outside of China to be significantly higher than prices within China. In the judgment of the qualified person, various assumptions were applied to the forecasted market pricing to arrive at the realized pricing used in the economic analysis, including, without limitation, terms of the offtake arrangements pursuant to which NioCorp expects to sell its products. Refer to Sections 16 and 19 of the 2026 S-K 1300 Elk Creek Technical Report Summary for additional information regarding market and netback pricing assumptions for each product.

Description

Realized Price
 $/lb product

 

FeNb

$

23.59

 

Sc2O3 (LoM average)

 

1,562.90

 

TiCl4

 

0.84

 

NdPr Oxide

 

62.78

 

Tb2O3

 

2,048.21

 

Dy2O3

 

593.30

 

SEG Carbonate

 

4.07

 

Heavies Carbonate

 

2.29

 

 

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Capital Cost Estimates

The following table shows the breakout in LoM initial capital and sustaining capital cost estimates (including closure and reclamation of $96 million), which total $4,019 million. This includes a total initial capital cost of $1,849 million, including a $233 million contingency, equal to an overall contingency of 14% on initial capital.

($millions)

 

 

Description

 

Initial

 

 

 

Sustaining

 

 

 

Total

 

 

Capitalized Preproduction Expenses

 

$

3

 

 

 

$

—

 

 

 

$

3

 

 

Site Preparation and Infrastructure

 

 

25

 

 

 

 

42

 

 

 

 

67

 

 

Processing Plant

 

 

870

 

 

 

 

309

 

 

 

 

1,180

 

 

Water Management & Treatment

 

 

13

 

 

 

 

0

 

 

 

 

13

 

 

Mining Infrastructure

 

 

145

 

 

 

 

382

 

 

 

 

527

 

 

Tailings Management

 

 

57

 

 

 

 

169

 

 

 

 

226

 

 

Site Wide Indirects

 

 

4

 

 

 

 

—

 

 

 

 

4

 

 

Processing Indirects

 

 

34

 

 

 

 

—

 

 

 

 

34

 

 

Mining Indirects

 

 

169

 

 

 

 

1,000

 

 

 

 

1,169

 

 

Owner's Costs Indirects

 

 

296

 

 

 

 

3

 

 

 

 

299

 

 

Closure and Reclamation

 

 

—

 

 

 

 

96

 

 

 

 

96

 

 

Contingency

 

 

233

 

 

 

 

169

 

 

 

 

402

 

 

Total Capital Costs

 

$

1,849

 

 

 

$

2,170

 

 

 

$

4,019

 

 

Totals may not sum due to rounding.

Operating Cost Estimates

The following LoM unit operating cost estimates include the pre-production and first/last years of production.

 

Description

 

LoM $/ton ore

 

 

Mining Cost

 

$

70.95

 

 

Process Cost

 

 

151.96

 

 

Water Mgmt

 

 

13.72

 

 

Tailings

 

 

8.08

 

 

Other Infrastructure

 

 

9.52

 

 

Site G&A

 

 

0.32

 

 

Subtotal

 

 

254.56

 

 

Royalties/Annual Bond Premium

 

 

11.38

 

 

Total LoM Operating Costs

 

$

265.94

 

 

Totals may not sum due to rounding.

33


 

Summary Projected Economic Results

Description

 

Value

 

 

Pre-Tax NPV8% ($ millions)

 

$

4,111

 

 

Pre-Tax IRR

 

 

24.0

%

 

After-Tax NPV8% ($ millions)

 

$

3,441

 

 

After-Tax IRR

 

 

22.8

%

 

After-Tax Payback Period (years)

 

 

2.93

 

 

Total Upfront Capital Expenditures ($ millions)

 

$

1,849

 

 

Mine Life (years)

 

 

40

 

 

LoM Gross Revenue ($ millions)

 

$

37,435

 

 

     Niobium

 

 

9,781

 

 

     Scandium

 

 

14,331

 

 

     Titanium

 

 

3,946

 

 

     Rare Earths

 

 

9,378

 

 

          NdPr Oxide

 

 

3,255

 

 

          Dy Oxide

 

 

3,137

 

 

          Tb Oxide

 

 

2,827

 

 

          SEG Carbonate

 

 

113

 

 

          Heavy Rare Earth Carbonate

 

 

46

 

 

Average Annual EBITDA over Full Production Years ($ millions)(1)

 

$

608

 

 

Average EBITDA Margin over LoM (EBITDA as a % of total revenue)(1)

 

 

67

%

 

Revenue Per Ton ($/ton)

 

$

815

 

 

Average Annual Operating Cost ($/ton)

 

$

(255

)

 

Effective Tax Rate

 

 

14.3

%

 

Development Timeline (months)

 

 

35

 

 

Totals may not sum due to rounding.

(1)
The term “EBITDA” refers to earnings before interest, taxes depreciation and amortization. See “Non-GAAP Financial Performance Measures” below for a discussion of the use of non-GAAP financial measures.
(2)
Taxes that may be levied on the Elk Creek Project include corporate income tax rates of 21% for federal and 3.99% for Nebraska. The Elk Creek Project is eligible for federal depletion allowances and credits, as well as various state incentives. The calculated effective income tax rate for the Elk Creek Project is 14.3% for the 2026 Elk Creek Study.

Planned Operations

Planned Mining Operations

The Elk Creek Project is planned as an underground mining operation using a long-hole stoping mining method and paste backfill, with ramp access from the surface. The mine will utilize jumbo drills for lateral development and tophammer and down-the-hole drills for vertical development and production stoping. Rock bolters will be used for ground support and probe holes will be used to support mine grouting where required. Ore will be remotely mucked from the bottom stope accesses using 10.3 cubic yard (7.9 cubic meter) battery-electric load-haul-dump units with an 18 metric tonne ("tonne") (19.8 ton) payload capacity and remote-operation capability. Ore will be transported to ore passes equipped with grizzly screens. The ore passes will report to the bottom of each of three mining horizons where the ore will be loaded on to the Railveyor system for transport to the surface plant. The Railveyor is a series of connected ore cars mounted on a rail system that move ore and waste rock from three loading stations underground to two stockpiles on the surface.

Planned Processing Operations

Planned ore processing operations include mineral processing, hydrometallurgical processing (“Hydromet”), and pyrometallurgical processing (“Pyromet”) housed in separate buildings.

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The mineral processing building will house all of its equipment within a single large building. Ore from the Primary Crusher (located adjacent to the mineral processing plant on the surface) will be fed to the secondary cone crusher system, operating in closed circuit with a double deck screen. The screen undersize from the cone crusher system will be fed to a high-pressure grinding roll unit (“HPGR”), operating in closed circuit with another double deck screen. The HPGR screen undersize is the comminution product that will report to the Hydromet process.

The Hydromet plant building will be a multi-level engineered steel structure, which will house equipment on two levels. Ore from mineral processing will be fed through a series of processes required to separate the niobium, scandium, titanium and rare earths from the rest of the ore. Outputs from the Hydromet process include saleable TiCl4 and Sc2O3 along with five rare earth oxide/carbonate products, with Nb2O5 reporting to the Pyromet plant for final processing. The Hydromet plant will be supported by a hydrochloric acid regeneration operation.

The Pyromet building will house its equipment within a single building. The purpose of the Pyromet plant is to reduce the Nb2O5 coming from the Hydromet plant by converting it into a saleable FeNb metal. Aluminum shots and iron oxide pellets will be introduced to an electric arc furnace on a continuous basis along with fluxing agents and Nb2O5 to produce a saleable ferroniobium metal.

Proposed Production Plan and Schedule

Based on the 2026 S-K 1300 Elk Creek Technical Report Summary, the operating mine life is approximately 40 years with a nominal processing rate of 3,047 tons per day. The Elk Creek Project timeline is based on 30 months to mechanical completion after authorization to proceed, plus an additional five months of commissioning and ramp-up to 100% of production capacity for a total of 35 months and assumes no financing constraints. The Board must approve a construction program and budget before construction of the Elk Creek Project can begin. This approval, along with the receipt of all required governmental permits and approvals and the completion of project financing, will determine whether and when construction of the Elk Creek Project can begin.

Proposed Tailings Storage

The tailings produced by the process plant will consist of calcium carbonate, magnesium carbonate, iron oxide, leach residue, gypsum, and slag. Six engineered and lined tailings storage facilities (“TSFs”) will be constructed sequentially to contain the tailings over the life of the Elk Creek Project and have a design capacity of approximately 33.7 million tonnes, against a required capacity over the life of the Elk Creek Project of approximately 31 million tonnes. A composite lining system with leak detection and monitoring systems will be installed in each tailings impoundment.

Tailings will be delivered to the TSFs from the paste tailings plant as paste containing low quantities of binder (cement and flyash) to limit seepage. Facility closure is considered in the design.

Proposed Salt Management

The crystalline salt produced as a waste product of heating and evaporating brine from the reverse osmosis (“RO”) water treatment plant will be transported to a dedicated salt management cell. A single lined surface impoundment, which will also serve as the mine water holding pond during construction, will be constructed to contain the salt over the life of the project and is designed with a volume of approximately 16 million cubic feet. Based on expected flows, the cell is expected to reach its nominal storage capacity, inclusive of a 15% safety factor, in approximately 15 years. NioCorp expects to reduce and reuse salt from the wastewater treatment process and to contract with local landfills to accept a portion of this waste as needed. The cell will incorporate a synthetic liner meeting the requirements of Nebraska Title 123 governing the design, operation and maintenance of wastewater works.

Proposed Water Management

For the first several years of construction, the advancement of the underground workings will require limited dewatering, anticipated to be through lower-level sumping and pumping for surface collection and disposal. Formation water produced during construction is expected to be brackish and unsuitable for direct discharge and will be stored in the lined salt management cell or trucked off-site for treatment at a local publicly owned treatment works. Excess water in the salt management cell will be spray evaporated within its footprint using turbomister spray evaporators, to avoid the reintroduction of soluble salts into the water treatment system. Temporary on-site storage or off-site shipment and disposal of the crystallized solid waste may be necessary until construction of the salt management cell is completed.

35


 

Once full operations commence, a shortfall of approximately 1,000 gallons per minute of operational and processing water is anticipated. To make up this shortfall, NioCorp would purchase fresh water from a local utility and from local landowners.

Once tailings begin being deposited in the TSF, internal contact water (from residual moisture in the tailings and precipitation falling within the impoundment footprint) will need to be actively managed. This water will be collected and treated using lime softening to precipitate hydroxide and carbonate solid forms for many of the inorganic constituents. The treated water will be filtered to remove the solids (which will be returned to the TSF for disposal), and the clean water will be pumped to the process plant RO system for further treatment. The clean water from the process plant RO unit will be used in the process plant, and the reject concentrate will be crystallized and deposited into the salt management cell.

Proposed Source of Power

On-site power will be provided by a third-party microgrid based off modular 2.5 MW natural gas fired generators, rated at approximately 50 MW. A small amount of grid power (200 kW) will also be used.

Proposed Source of Natural Gas

Natural gas, to be used throughout the Elk Creek Project during the construction and operation phases of the project, will be brought to the site via pipeline from the local gas utilities. NioCorp will connect to existing distribution pipelines located 5 miles east and approximately 30 miles west of the project site. Natural gas will be distributed to all on-site facilities utilizing buried high-density polyethylene natural gas distribution pipe. Natural gas piping above ground and located inside of the facilities will consist predominately of carbon steel pipe. Natural gas will be used for power generation, facility heating, water heating, and for gas-fired process equipment.

Environmental, Permitting, and Social

The current mine design incorporates the following strategies and technologies designed to minimize environmental impacts of operation:

•
Zero Process Liquid Discharge: The Elk Creek facility will now operate as a “Zero Process Liquid Discharge” facility, with no releases of process liquids. Instead, both naturally occurring, brackish (slightly salty) water produced during mining operations, and water used in ore processing, will be treated on site for use in operations. A solid salt will be produced from water treatment operations which will be stored on site.
•
Additional Protection of Groundwater Resources Through Grouting: The Elk Creek Project’s new mine design will utilize grouting during mine development and mine operations to protect groundwater resources in the area and limit the amount of groundwater that will report to the underground mine.
•
Avoidance of Permanent Impacts to Federally Jurisdictional Waters: The layout of the Elk Creek Project was designed to minimize permanent impacts to any federally jurisdictional waters and/or wetlands on the property. The proposed design of TSF Cell #3 would result in permanent impacts to a federally jurisdictional intermittent channel requiring CWA Section 404 permitting. If the design remains unchanged and the channel status remains jurisdictional at the time of construction, the permanent impacts would require federal permitting. This overall layout minimized the expected environmental impacts. No other federal permits are now expected to be required for the Elk Creek Project.
•
Utilizing Tailings as Underground Mine Backfill: The plan to fill underground voids concurrently with mining operations using a paste backfill material that contains mine waste material that typically would be stored in above-ground tailings storage areas. The tailings will be combined with cement and/or flyash to provide a structural backfill in the mine which allows for a more efficient extraction of the mineral reserve.

A number of key permits and environmental management requirements have been identified for the Elk Creek Project, some of which need to be implemented as soon as practicable in order to maintain the proposed Elk Creek Project schedule.

•
While not necessarily complex, the timing generally required to complete permitting through any federal regulatory agency requires that NioCorp engage key agencies (in this case the USACE and possibly the EPA) early on in Elk Creek Project development and consider the siting and orientation of facilities carefully to minimize the risk of a protracted National Environmental Policy Act analysis of the Elk Creek Project. At the present time, the Company believes that we have completed the major federal permitting actions needed for project construction, although changes to the design or location of project facilities may require that additional federal permits be obtained.

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•
Construction at the facility requires an Air Permit from the State of Nebraska, which was issued to the Company on June 2, 2020. The Air Permit describes all the prospective air emissions from the facility and required the completion of an air quality model that demonstrates compliance with the NAAQS. On April 15, 2022, the Company announced that the Nebraska Department of Environment and Energy advised the Company that periodic extensions to the Elk Creek Project’s Air Permit are no longer required because the Company has met the regulatory definition of “construction, reconstruction, or modification of the source” since the permit was issued.
•
Documentation of existing baseline environmental conditions at the Elk Creek Project site was initiated in 2014 and will continue as needed throughout the permitting process.
•
Surface water monitoring will continue as needed throughout the permitting process and extend into construction and operations as part of the Environmental Management System and likely State of Nebraska permit requirements.
•
The major land-use authorization for the project was received from Johnson County, Nebraska, on December 24, 2019, in the form of a Special Use Permit for the project. This land-use permit is a necessary precursor to any project-related construction activities. County zoning permits will be required for individual buildings constructed at the site, and the County requirement is that such applications must be submitted five days before construction commences.
•
Closure costs for the Elk Creek Project have been estimated at $106 million, including contingency, which covers all aspects of closure and site reclamation and includes a three-year closure period and a 30-year post-closure monitoring period.

The Company has not identified any significant encumbrances to the property it owns or holds under OTP agreements. Other than for the MSHA assessment described in Exhibit 95.1 to this Annual Report on Form 10-K, the Company has not had any permit violations or fines since the filing of our Annual Report on Form 10-K for the fiscal year ended June 30, 2025.

Permitting requirements for the project have been identified. The Company holds an Air Construction Permit from the State of Nebraska and a Special Use Permit from Johnson County, both of which are necessary to allow the start of project construction. In addition, the Elk Creek Project will be required to obtain a series of permits for operations from federal, state, and local agencies. The majority of these permits are ministerial in nature and present minimal risk to the Company and typically involve the completion of an application and the payment of a nominal fee. Four permits from the State of Nebraska are discretionary in nature, where an application and fee are provided to the state and the state must make a decision as to whether or not the permit will be granted. In addition, one federal permit, from the USACE is discretionary as well. While the risk involved in these five permits is low, such discretionary permits require more processing time and do require the agency (either the State of Nebraska or the USACE) to make a decision in favor of issuance of the permit. These five permits include the following:

•
Solid Waste Permit;
•
Air Construction Permit for the microgrid, the obtaining, maintenance and costs of which will be the responsibility of the third-party microgrid operator;
•
Air Operating Permits for the facility;
•
Air Operating Permit for the microgrid; and
•
USACE permit for the diversion channel associated with the construction of TSF #3

The cost and schedule for obtaining both the discretionary and ministerial permits is included in the overall execution plan for the Elk Creek Project. Additional details on the project’s permitting requirements can be found in Section 17 of the 2026 S-K 1300 Elk Creek Technical Report Summary.

Mineral Reserves and Resources

Mineral reserves and mineral resources at the Elk Creek Project as of June 30, 2026, are summarized in the tables below. Further discussion and background regarding the approaches used to establish mineral reserves and mineral resources is contained in Sections 11 and 12 of the 2026 S-K 1300 Elk Creek Technical Report Summary.

 

Elk Creek Project In Situ Mineral Resource Estimate Excluding Reserves

as of June 30, 2026

 

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Classification

Cut-off NSR ($/ton)

Tonnage (Mtons)

Nb₂O₅ (%)

TiO₂ (%)

Sc (ppm)

TREO (%)

Measured

218

14.1

0.53

2.05

47.60

0.39

Indicated

218

149.0

0.43

1.70

42.50

0.39

Measured + Indicated

218

163.1

0.44

1.89

45.30

0.39

Inferred

218

169.2

0.38

2.14

51.02

0.39

Notes:

(1)
Mineral resources are not mineral reserves and do not have demonstrated economic viability. There is no certainty that all or any part of the mineral resource will be converted to mineral reserves.
(2)
Prepared in accordance with S-K 1300.
(3)
NSR cut-off of $218/ton ($240/tonne) based on longhole stoping underground mining; incorporates metallurgical recoveries of Nb 86.72%, TiO₂ 83.65%, Sc 92.00%, and REE by-products 92.00%, at metal prices of $52.00/kg Nb, $2,000.00/kg Sc, $1.86/kg TiCl4, $1,845.00/kg Tb₂O₃, $125.00/kg NdPr, and $8.97/kg SEG carbonate.
(4)
TREO = Light Rare Earth Metals and Oxides + Heavy Rare Earth Metals and Oxides expressed as a percentage (TREO% = TREO ppm ÷ 10,000).
(5)
Tonnages in millions of short tons (Mtons). Grades rounded to reflect the approximate nature of resource estimates.
(6)
Totals may not sum due to rounding.
(7)
Qualified Person: Dahrouge Geological Consulting USA Ltd., effective date June 30, 2026.

Elk Creek Project Underground In Situ Mineral Reserves Estimate for Elk Creek

as of June 30, 2026

 

Mineral Reserve Classification

Cut-off NSR

Tonnage

Grade

Grade

Grade

Grade

($/ton)

(ton)

(Nb2O5%)

(TiO2%)

(Sc ppm)

(TREO %)

Proven

218

7,570,098

0.760

2.70

71.5

0.32

Probable

218

38,359,365

0.759

2.67

68.8

0.35

Total

218

45,929,462

0.759

2.68

69.3

0.34

 

Classification

Tonnage
(ton)

 

Nb2O5 Grade
(%)

 

FeNb
(ton)

 

Payable Nb
(ton)

 

TiO2 Grade
(%)

 

Payable TiCl4 
(ton)

 

Sc Grade
(ppm)

 

Payable Sc2O3 
(ton)

 

TREO Grade
(ppm)

 

Payable TREO
(ton)

 

Proven

 

7,570,098

 

 

0.76

 

 

53,651

 

 

34,873

 

 

2.70

 

 

405,938

 

 

71.5

 

 

762

 

 

3,232

 

 

22,509

 

Probable

 

38,359,365

 

 

0.76

 

 

271,386

 

 

176,401

 

 

2.67

 

 

2,036,334

 

 

68.8

 

 

3,717

 

 

3,489

 

 

123,115

 

Total

 

45,929,462

 

 

0.76

 

 

325,038

 

 

211,274

 

 

2.68

 

 

2,442,272

 

 

69.3

 

 

4,479

 

 

3,446

 

 

145,625

 

Notes:

(1)
All figures are rounded to reflect the accuracy of the estimates. Totals may not sum due to rounding.
(2)
The Qualified Person for the mineral reserve estimate is Amplify Mine Planning. The estimate has an effective date of June 30, 2026.
(3)
The mineral reserve is based on the mine design and mine plan, utilizing an average cut-off grade of 0.650% Nb2O5 with an NSR of $ 218/ton.
(4)
The estimate of mineral reserves may be materially affected by metal prices, environmental, permitting, legal, title, taxation, socio-political, marketing, infrastructure development, or other relevant issues.
(5)
Annual LoM average production rate of ~8,282 tons of FeNb/annum in the years of full production.
(6)
Mining dilution of ~6% was applied to all stopes and development, based on 3% for the primary stopes, 9% for the secondary stopes, and 5% for ore development.
(7)
Mining recoveries of 95% were applied in longhole stopes and 62.5% in sill pillar stopes.
(8)
Price assumptions for FeNb, Sc2O3, TiO2 and TREO metals are based upon independent market analyses for each product.
(9)
Price and cost assumptions are based on the pricing of products at the “mine-gate,” with no additional down-stream costs required. The assumed products are a ferroniobium product (metallic alloy shots consisting of 65%Nb and 35% Fe), titanium in the form of TiCl4, scandium trioxide in powder form and rare earth oxides in either purified oxide or carbonate form. The mineral reserve has an average LoM NSR of $590.84/ton.
(10)
The economic assumptions used to define the mineral reserve cut-off grade are as follows:

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Parameter

 

Value

 

 

Unit

Mining Cost

 

$46.14

 

 

$/ton mined

Processing

 

125.04

 

 

$/ton mined

Water Management and Infrastructure

 

16.58

 

 

$/ton mined

Tailings Management

 

2.00

 

 

$/ton mined

Other Infrastructure

 

5.46

 

 

$/ton mined

General and Administrative

 

8.89

 

 

$/ton mined

Royalties/Annual Bond Premium

 

8.32

 

 

$/ton mined

Other Costs

 

6.28

 

 

$/ton mined

Total Cost

 

$218.71

 

 

$/ton mined

Nb2O5 to Niobium conversion

 

69.9

 

 

%

Niobium Process Recovery

 

86.72

 

 

%

Niobium Price

 

$23.59

 

 

$/lb

TiCl4 Process Recovery

 

83.65

 

 

%

TiCl4 Price

 

$0.84

 

 

$/lb

Sc Process Recovery

 

92

 

 

%

Sc to Sc2O3 conversion

 

153.4

 

 

%

Sc Price

 

$891.76

 

 

$/lb

Dy2O3 Process Recovery

 

92

 

 

%

Dy2O3 Price

 

$185.97

 

 

$/lb

Nd2O3 Process Recovery

 

92

 

 

%

Nd2O3 Price

 

$56.70

 

 

$/lb

Pr2O3 Process Recovery

 

92

 

 

%

Pr2O3 Price

 

$56.70

 

 

$/lb

Tb2O3 Process Recovery

 

92

 

 

%

Tb2O3 Price

 

$836.88

 

 

$/lb

Comparison of Mineral Resources and Mineral Reserves to Previous Estimates

The mineral resource and mineral reserve estimates reported in the 2026 S-K 1300 Elk Creek Technical Report Summary supersede the previous mineral resource and mineral reserve estimates reported in our Annual Report on Form 10-K for the fiscal year ended June 30, 2025, which was based on the 2022 S-K 1300 Elk Creek Technical Report Summary.

The principal changes between the 2025 and 2026 resource estimates are as follows. The NSR cut-off was raised from $164/ton ($180/tonne) to $218/ton ($240/tonne), reflecting updated operating cost estimates from the 2026 Elk Creek Study. A measured mineral resource category of 14.1 Mtons (12.8 million metric tonnes ("Mtonnes")) was introduced in the 2026 estimate, representing areas where infill drilling achieved sufficient density to support measured classification; no measured resource was classified in 2025. Indicated tonnage decreased from 167.2 Mtons (151.7 Mtonnes) in the 2025 estimate to 149.0 Mtons (135.2 Mtonnes) in the 2026 estimate (-10.8%), primarily due to the reclassification of indicated resources uplifted into the measured classification. Inferred tonnage increased from 119.4 Mtons (108.3 Mtonnes) in the 2025 estimate to 169.2 Mtons (153.5 Mtonnes) in the 2026 estimate (+41.7%), reflecting additional drilling that extended the geological understanding of the peripheral carbonatite capturing a greater volume of lower-grade peripheral material. Mean grades are broadly consistent between estimates; the slight improvement in indicated TiO₂ (2.24% to 2.36%) and TREO (0.34% to 0.36%) reflects the higher NSR cut-off removing lower-grade diluting blocks from the reported indicated resource.

In terms of the mineral reserve, a proven reserve of 7.6 Mtons (6.9 Mtonnes) was established for the 2026 estimate; no proven reserve was classified in 2025. Probable reserves decreased from 40.4 Mtons (36.6 Mtonnes) in the 2025 estimate to 38.4 Mtons (34.8 Mtonnes) in the 2026 estimate (-5.1%). Grades were broadly comparable between the 2025 and 2026 reserve estimates. The change between the two estimates is a reflection of the infill drilling program completed in 2025, which specifically targeted uplifting a portion of the probable reserves into the proven category.

Non-GAAP Financial Performance Measures

Non-GAAP financial performance measures are intended to provide additional information only and do not have any standard meaning prescribed by U.S. GAAP. These measures should not be considered in isolation or as a substitute for performance measures prepared in accordance with U.S. GAAP.

The 2026 S-K 1300 Elk Creek Technical Report Summary uses non-GAAP financial performance measures, such as EBITDA, Averaged Annual EBITDA, and Averaged EBITDA Margin, for purposes of projecting the economic results of the Elk Creek Project. We are unable to provide a reconciliation of these forward-looking non-GAAP measures to the most comparable U.S. GAAP financial performance measures because certain information needed to reconcile those non-GAAP measures to the most comparable U.S. GAAP financial performance measures is dependent on future events, some of which are outside the control of the Company, such as FeNb, Sc2O3, and TiO2 prices, interest rates, and exchange rates. Moreover,

39


 

estimating such U.S. GAAP measures with the required precision necessary to provide a meaningful reconciliation is extremely difficult and could not be accomplished without unreasonable effort.

Proposed Activities

The Elk Creek Property is characterized as a development stage property. The Company is currently progressing the property toward construction while it works to secure the remaining project financing required to fund the construction, commissioning, and operation of the Elk Creek Project. The property is expected to be characterized as a production stage property upon the commencement of production.

Using cash on hand, the Company expects to undertake the following activities:

•
Continuation of the Company's efforts to secure federal, state and local operating permits;
•
Negotiation and completion of offtake agreements for the remaining uncommitted production of Nb, Sc, and Ti from the Elk Creek Project, including the potential sale of Ti as titanium tetrachloride, as well as REE production;
•
Negotiation and completion of engineering, procurement, and construction agreements;
•
Completion of the final detailed engineering for the underground portion of the Elk Creek Project;
•
Continuation and completion of the final detailed engineering for surface project facilities;
•
Completion of water supply agreements and related infrastructure to deliver fresh water to the project site; and
•
Continuation of revised mine groundwater investigation and control activities.

Securing the remaining project financing is a condition to the Company making a final investment decision to proceed with full construction of the Elk Creek Project. Upon obtaining such financing, we expect to undertake the following activities:

•
Construction of natural gas and electrical infrastructure under existing agreements to serve the Elk Creek Project site;
•
Initiation of long-lead equipment procurement activities; and
•
Initiation of initial construction work at the project site.

Corporate Headquarters

We lease our principal executive office space at 7000 South Yosemite Street, Suite 115, Centennial, Colorado.

As of September 25, 2026, we are not a party to any legal proceedings that could have a material adverse effect on the Company’s business, financial condition, or operating results. Further, to the Company’s knowledge, no such proceedings have been threatened against the Company.

ITEM 4. MINE SAFETY DISCLOSURES

Pursuant to Section 1503(a) of the United States Dodd-Frank Wall Street Reform and Consumer Protection Act of 2010 (the “Dodd-Frank Act”), issuers that are operators, or that have a subsidiary that is an operator, of a coal or other mine in the U.S. are required to disclose specified information about mine health and safety in their periodic reports. These reporting requirements are based on the safety and health requirements applicable to mines under the Federal Mine Safety and Health Act of 1977 (the “Mine Act”) which is administered by MSHA. The information concerning mine safety violations and other regulatory matters required by Section 1503(a) of the Dodd-Frank Wall Street Reform and Consumer Protection Act and Item 104 of Regulation S-K is included in Exhibit 95.1 to this Annual Report on Form 10-K.

 

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PART II

ITEM 5. MARKET FOR REGISTRANT’S COMMON EQUITY, RELATED STOCKHOLDER MATTERS, AND ISSUER PURCHASES OF EQUITY SECURITIES

Market Information

The Common Shares are listed for trading on the Nasdaq under the trading symbol “NB.” The Company also trades on the Frankfurt Stock Exchange as “BR30.”

Holders

As of September 25, 2026, we had 140 holders of record of our Common Shares.

Dividends

We have not paid any cash dividends on the Common Shares since our inception and do not anticipate paying any cash dividends in the foreseeable future. We plan to retain our earnings, if any, to provide funds for the expansion of our business.

Securities Authorized for Issuance Under Equity Compensation Plans

See Equity Compensation Plan Information under Item 12, “Security Ownership of Certain Beneficial Owners and Management and Related Stockholder Matters,” for information on plans approved by our shareholders.

Purchases of Equity Securities by the Company

We did not make any repurchases in the quarter ended June 30, 2026.

Recent Sales of Unregistered Securities

The Company did not make any unregistered sales of equity securities during the quarter ended June 30, 2026.

Exchange Controls

There are no governmental laws, decrees, or regulations in Canada that restrict the export or import of capital, including foreign exchange controls, or that affect the remittance of dividends, interest or other payments to non-resident holders of the securities of NioCorp, other than Canadian withholding tax. See “Certain Canadian Federal Income Tax Considerations for U.S. Residents” below.

Certain Canadian Federal Income Tax Considerations for U.S. Residents

The following generally summarizes certain Canadian federal income tax consequences generally applicable under the Income Tax Act (Canada) and the regulations enacted thereunder (collectively, the “Canadian Tax Act”) and the Canada-United States Tax Convention (1980) (the “Convention”) to the holding and disposition of Common Shares.

Comment is restricted to holders of Common Shares each of whom, at all material times for the purposes of the Canadian Tax Act and the Convention, (i) is resident solely in the U.S. for tax purposes, (ii) is a “qualifying person” under and entitled to the benefits of the Convention, (iii) holds all Common Shares as capital property, (iv) deals at arm’s length with and is not affiliated with NioCorp, (v) does not and is not deemed to use or hold any Common Shares in a business carried on in Canada (including an adventure or concern in the nature of trade), (vi) is not an insurer that carries on business in Canada and elsewhere, (vii) is not an “authorized foreign bank” (as defined in the Canadian Tax Act), (viii) has not entered into a “derivative forward agreement,” “synthetic equity arrangement,” or “synthetic disposition arrangement” (each as defined in the Canadian Tax Act) with respect to the Common Shares, and (ix) does not have and has not had, at any time, a “permanent establishment” (as defined in the Convention) of any kind in Canada (each such holder, a “U.S. Resident Holder”).

Certain U.S.-resident entities that are fiscally transparent for U.S. federal income tax purposes (including limited liability companies) may not in all circumstances be entitled to the benefits of the Convention. Members of or holders of an interest in such an entity that holds Common Shares should consult their own tax advisers regarding the extent, if any, to which the benefits of the Convention will apply to the entity in respect of its Common Shares.

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Generally, a U.S. Resident Holder’s Common Shares will be considered to be capital property of such holder provided that the U.S. Resident Holder is not a trader or dealer in securities, did not acquire, hold, or dispose of the Common Shares in one or more transactions considered to be an adventure or concern in the nature of trade (i.e. speculation), and does not hold the Common Shares in the course of carrying on a business.

This summary is based on the current provisions of the Canadian Tax Act and the Convention in effect as of the date prior to the date hereof, all specific proposals to amend the Canadian Tax Act and the Convention publicly and officially announced by or on behalf of the Minister of Finance (Canada) prior to the date hereof (the "Tax Proposals"), and the current administrative policies and assessing practices of the Canada Revenue Agency (the “CRA”) published in writing and made publicly available by the CRA prior to the date hereof. This summary assumes that the Tax Proposals will be enacted as currently proposed, and that there will be no other material change to any applicable law or administrative policy or assessing practice, whether by way of judicial, legislative or governmental decision or action, although no assurance can be given in these respects. Except as otherwise expressly provided, this summary does not take into account any provincial, territorial, or foreign tax considerations, which may differ materially from those set out herein.

This summary is of a general nature only, is not exhaustive of all possible Canadian federal income tax considerations and is not intended to be and should not be construed as legal or tax advice to any particular U.S. Resident Holder, and no representations with respect to the tax consequences to any U.S. Resident Holder are made herein. The tax consequences of holding and disposing of Common Shares will vary according to the U.S. Resident Holder’s particular circumstances. U.S. Resident Holders are urged to consult their own tax advisers for advice with respect to their particular circumstances. The discussion below is qualified accordingly.

Currency Conversion

In general, for purposes of the Canadian Tax Act, all amounts relating to the holding or disposition of Common Shares must be converted into Canadian dollars based on the relevant exchange rate as determined in accordance with the Canadian Tax Act.

Disposition of Common Shares

A U.S. Resident Holder generally will not be subject to tax under the Canadian Tax Act in respect of a capital gain realized on the disposition or deemed disposition of one or more Common Shares, nor will a capital loss arising therefrom be recognized under the Canadian Tax Act, unless such Common Shares constitute “taxable Canadian property” (as defined in the Canadian Tax Act) of the U.S. Resident Holder at the time of disposition and the U.S. Resident Holder is not entitled to relief under the Convention.

Generally, a U.S. Resident Holder’s Common Shares will not constitute “taxable Canadian property” of such holder at a particular time at which the Common Shares are listed on a “designated stock exchange” (which currently includes Nasdaq) unless at any time during the 60-month period that ends at the particular time both of the following conditions are concurrently met:

1.
25% or more of the issued shares of any class of the capital stock of NioCorp were owned by or belonged to one or any combination of:
a.
the U.S. Resident Holder,
b.
persons with whom the U.S. Resident Holder did not deal at arm’s length, and
c.
partnerships in which the U.S. Resident Holder or a person referred to in clause (b) holds a membership interest directly or indirectly through one or more partnerships, and
2.
more than 50% of the fair market value of the Common Shares was derived directly or indirectly from, one or any combination of, real or immovable property situated in Canada, “Canadian resource properties” (as defined in the Canadian Tax Act), “timber resource properties” (as defined in the Canadian Tax Act), or options in respect of, or interests in, or for civil law rights in, any of the foregoing, whether or not the property exists.

Notwithstanding the foregoing, Common Shares may also be deemed to be “taxable Canadian property” in certain circumstances set out in the Canadian Tax Act.

U.S. Resident Holders whose Common Shares are or may be “taxable Canadian property” should consult their own tax advisors with respect to the tax and compliance considerations that may be relevant to them, including with respect to any potential relief under the Convention.

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Dividends on Common Shares

A U.S. Resident Holder to whom NioCorp pays or credits or is deemed to pay or credit a dividend on such holder’s Common Shares will be subject to Canadian withholding tax, and NioCorp will be required to withhold the tax from the dividend and remit it to the CRA for the holder’s account. The rate of withholding tax under the Canadian Tax Act is 25% of the gross amount of the dividend, but should generally be reduced under the Convention to 15% (or, if the U.S. Resident Holder is a company which is the beneficial owner of at least 10% of the voting stock of NioCorp, 5%) of the gross amount of the dividend. For this purpose, a company that is a resident of the United States for purposes of the Canadian Tax Act and the Convention and is entitled to the benefits of the Convention shall be considered to own the voting stock of NioCorp owned by an entity that is considered fiscally transparent under the laws of the United States and that is not a resident of Canada, in proportion to such company’s ownership interest in that entity.

ITEM 6. RESERVED

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ITEM 7. MANAGEMENT’S DISCUSSION AND ANALYSIS OF FINANCIAL CONDITION AND RESULTS OF OPERATIONS

The following Management’s Discussion and Analysis (“MD&A”) provides information that management believes is relevant to an assessment and understanding of the consolidated financial condition and results of operations of NioCorp and subsidiaries. This item should be read in conjunction with our consolidated financial statements and the notes thereto included in this Annual Report on Form 10-K.

Summary of Consolidated Financial and Operating Performance

The Company had no revenues from mining operations during the fiscal years presented below. Operating expenses incurred related primarily to performing exploration and feasibility study related activities, as well as the activities necessary to support corporate and shareholder duties.

 

For the year ended June 30,

 

 

2026

 

 

2025

 

 

($000)

 

Operating expenses

 

$

38,309

 

 

$

11,958

 

Net loss attributable to the Company

 

 

(48,555

)

 

 

(17,405

)

Net loss per share (basic and diluted)

 

 

(0.41

)

 

 

(0.36

)

The net loss attributable to the Company increased to $48.6 million for fiscal year 2026 from $17.4 million for fiscal year 2025. This is primarily due to spending on the 2026 Elk Creek Study, the recognition of non-cash expenses related to share-based compensation and the valuation of the Earnout Shares and Warrant liabilities, and increased compensation expenses, partially offset by interest income. Net loss per share increased due to an increase in net loss, offset by an increase in weighted average Common Shares outstanding since June 30, 2025.

Results of Operations

The Company had no revenues from mining operations during the fiscal years presented below. Operating expenses incurred related primarily to performing exploration and study related activities, and the activities necessary to support corporate and shareholder duties, as detailed in the following table:

 

 

For the year ended June 30,

 

 

2026

 

 

2025

 

 

($000)

 

Operating expenses:

 

 

 

 

 

 

Exploration expenditures

 

$

16,076

 

 

$

4,135

 

General and administrative expenditures

 

 

22,233

 

 

 

7,823

 

Total operating expenses

 

 

38,309

 

 

 

11,958

 

Change in fair value of earnout shares liability

 

 

8,571

 

 

 

2,063

 

Change in fair value of warrant liabilities

 

 

13,034

 

 

 

4,093

 

Change in fair value of convertible notes

 

 

—

 

 

 

40

 

Interest expense

 

 

—

 

 

 

48

 

Interest income

 

 

(9,146

)

 

 

(94

)

Other non-operating expense (income)

 

 

13

 

 

 

(126

)

Income tax benefit

 

 

—

 

 

 

—

 

Less: Net loss attributable to redeemable noncontrolling interest

 

 

(2,226

)

 

 

(577

)

Net loss attributable to the Company

 

$

(48,555

)

 

$

(17,405

)

Fiscal Year 2026 as Compared to Fiscal Year 2025

Significant items affecting operating expenses are noted below:

Exploration expenditures increased for fiscal year 2026 as compared to fiscal year 2025 primarily due to field-based costs associated with the 2025 Drilling Program, which was substantially completed by September 30, 2025, as well as expenses related to the Company’s ongoing efforts to prepare the 2026 Elk Creek Study.

 

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General and administrative expenditures increased in fiscal year 2026 as compared to fiscal year 2025, reflecting an overall increase in corporate compliance, governance, financing, and other Elk Creek Project advancement activities. This includes increased expenses related to share-based compensation and employee compensation costs, legal fees to support financing initiatives and Elk Creek Project advancement, and costs associated with the advancement of scandium product initiatives.

Other significant items impacting the change in the Company’s net loss are noted below:

Change in fair value of earnout shares liability represents the impact of changes in fair value related to valuation of the Earnout Shares. The increase in fair value for fiscal year 2026 as compared to fiscal year 2025 primarily reflects the increase in the Company’s Common Share price in the financial modeling used to determine the period end fair value.

Change in fair value of warrant liabilities represents the impact of changes in fair value of Warrants recorded as liabilities in the consolidated balance sheet. The increase in fair value for fiscal year 2026 as compared to fiscal year 2025 primarily reflects the increase in the Company’s Common Share price used in the Black-Scholes valuation of outstanding Warrant liabilities.

Interest income represents earnings from the investment of excess cash balances in a commercial money market account. The increase for fiscal year 2026 as compared to fiscal year 2025 is attributable to our higher cash balance resulting from our financing efforts during fiscal year 2026.

Loss attributable to noncontrolling interest represents the portion of net loss in ECRC attributable to the Vested Shares, which are not owned by the Company. The increase in loss for fiscal year 2026 as compared to fiscal year 2025 is related to the increased consolidated net loss, as noted above, incurred by ECRC.

Liquidity and Capital Resources

Overview

As of June 30, 2026, the Company had cash of $415.0 million and working capital of $402.3 million, compared to cash of $25.6 million and working capital of $24.8 million as of June 30, 2025. This increase reflects net proceeds of approximately $375.1 million from five equity offerings completed between July 2025 and February 2026, together with approximately $23.3 million of proceeds from the exercise of Warrants and Options and approximately $38.7 million of proceeds from advances under the Standby Equity Purchase Agreement, dated January 26, 2023 (the “Yorkville Equity Facility Financing Agreement”) between the Company and YA II PN, Ltd., an investment fund managed by Yorkville Advisors Global, LP. The Company has no outstanding long-term debt. For additional details on the equity transactions that occurred during the year-ended June 30, 2026, see Note 9 to the consolidated financial statements included in this Annual Report on Form 10-K.

During fiscal year 2026 and the period through the date of this Annual Report on Form 10-K, the Company completed the 2025 Drilling Program that supported updated mineral resource and mineral reserve estimates for the Elk Creek Project, commenced excavation of the mine portal at the Elk Creek Project in February 2026, and completed the 2026 Elk Creek Study. The Company is now focused on securing project financing sufficient to cover initial capital costs and other related expenses necessary for the commencement and completion of construction, and carrying out our near-term planned work programs necessary to complete detailed design, development and construction of the Elk Creek Project, as well as the commencement of early elements of project construction. The Company does not intend to commence full construction of the Elk Creek Project until sufficient project financing is in place to cover initial capital costs and other related expenses necessary for the commencement and completion of construction of the Elk Creek Project.

Short-Term Liquidity and Planned Expenditures

We expect that the Company will operate at a loss for the foreseeable future. The Company’s current planned cash outflows are approximately $65 million to $75 million for the next twelve months. In addition to the settlement of outstanding accounts payable and other short-term liabilities, our planned cash outflows over the next twelve months are expected to consist of expenditures relating to the advancement of the Elk Creek Project by NioCorp’s majority-owned subsidiary, ECRC, corporate overhead costs, and estimated costs related to securing the financing necessary for construction of the Elk Creek Project.

We expect our cash balance as of June 30, 2026, together with the proceeds from the exercise of Warrants and Options, if any, and the reimbursement payments to which ECRC is entitled pursuant to the DoW Agreement, to be sufficient to fund our planned cash outflows for at least the next twelve months from the date of this Annual Report on Form 10-K. That expectation relates to the activities described above and does not extend to the capital required to construct the Elk Creek Project and achieve commercial production, which the Company must finance separately as described under “Long-Term Liquidity

45


 

Requirements” below. If project financing is delayed, the Company has the ability to defer or reduce a substantial portion of its planned expenditures until such financing is in place.

The planned expenditures relating to the advancement of the Elk Creek Project over the next twelve months include, but are not limited to, continued construction of the mine portal at the Elk Creek Project, which the Company’s Board of Directors approved in December 2025 and for which the current remaining estimated capital cost is approximately $38.7 million; detailed engineering; procurement and construction contracting activities; planning and deposits for long-lead equipment; metallurgical test work; environmental and permitting activities; community and stakeholder engagement programs; and advisory costs relating to securing project financing. The planned corporate overhead costs over the next twelve months are approximately $19 million, including Elk Creek property lease commitments, and the settlement of outstanding accounts payable as of June 30, 2026.

Long-Term Liquidity Requirements

Our long-term liquidity requirements consist principally of the capital required to construct the Elk Creek Project and to fund the Company’s operations through the commencement of commercial production. On August 10, 2026, the Company announced the results of the 2026 Elk Creek Study, which is summarized in the 2026 S-K 1300 Elk Creek Technical Report Summary. The 2026 S-K 1300 Elk Creek Technical Report Summary includes an estimated total upfront capital expenditure for the Elk Creek Project of approximately $1,849 million, including a contingency of 14%, which is an increase of approximately $708 million compared to the estimated total upfront capital expenditure for the Elk Creek Project of approximately $1,141.0 million that was included in the 2022 S-K 1300 Elk Creek Technical Report Summary. The increase reflects, among other things, a substantially redesigned processing plant and mining operation that is intended to produce eight critical mineral products, from the previous plan to produce three critical mineral products, as well as significant inflationary impacts since the previous feasibility study.

The total amount of financing the Company will require is greater than the estimated total upfront capital expenditure for the Elk Creek Project, because the Company must also fund costs that are not included in that estimate. These include financing fees and transaction costs; interest accruing during the development period; working capital required at start-up; reclamation and other financial assurance obligations; corporate overhead costs through the commencement of commercial production; and any cost escalation or cost overruns in excess of the contingency included in the 2026 S-K 1300 Elk Creek Technical Report Summary. The Company would therefore require additional financing to fund that estimated capital expenditure alone, before giving effect to the additional costs described above. The Company does not expect to fund it from any single source. Management currently anticipates that it would be provided by a combination of sources of financing, in the targeted proportions and from the categories of sources described below.

The actual amount of capital expenditure required to successfully achieve commercial production at the Elk Creek Project is subject to, among other factors, the timing and actual cost of detailed engineering, procurement, construction contracting, permitting and the construction of infrastructure, mining and processing facilities, as well as prevailing interest rates and the terms on which financing is available to the Company. In addition, to the extent that EXIM or any other prospective lender requests further project activities to be undertaken in connection with its diligence process, the Company would require additional funding to complete such activities. The Company’s ability to construct and operate the Elk Creek Project is dependent on management’s ability to secure such financing.

Management currently anticipates that it will fund the upfront capital expenditure amount for the Elk Creek Project through a combination of debt and equity financing, with approximately 65% of such amount being funded from the net proceeds of debt financing, including the amount of debt that would be represented by the EXIM Financing, if any. The balance, representing approximately 35% of such amount, is expected to be funded from the net proceeds of equity financing or other funding available to the Company. The debt component contemplated by this funding mix may exceed the EXIM Financing, as described under “Proposed Project Financing from EXIM” below. In addition to the EXIM Financing, the Company may also seek to fund a portion of the debt component from other export credit agencies and from commercial lenders. The ultimate composition of the debt component has not been determined and may or may not include lenders other than EXIM. The Company has not obtained a commitment for any portion of the debt financing required to construct the Elk Creek Project, and there can be no assurance that debt financing will be available in the amount, or on the terms, that management currently anticipates, or at all. Management is actively pursuing additional sources of debt and equity financing to meet its long-term funding requirements, and while it has been successful in doing so in the past, there is no assurance that we will be able to obtain any such additional financing on acceptable terms, if at all. See Item 1A., Risk Factors – We expect to incur substantial debt in connection with the Elk Creek Project, which will require a significant amount of cash to service, require us to comply with certain covenants and restrictions, and could impair our ability to obtain additional financing.

Because the funding mix that management currently anticipates contemplates that approximately 35% of the upfront capital expenditure for the Elk Creek Project would be funded with equity or other funding available to the Company, and because the

46


 

Company’s cash on hand as of June 30, 2026 represents less than 35% of the estimated total upfront capital expenditure for the Elk Creek Project, the Company expects that it may be required to raise additional equity capital in order to fund this portion of the Elk Creek Project’s upfront capitalization. The amount of equity capital the Company will be required to raise will depend on, among other things, the final upfront capital cost of the Elk Creek Project, the amount and terms of the debt financing the Company is able to obtain, and the minimum equity contribution, leverage limitations and coverage ratios that prospective lenders require. See Item 1A., Risk Factors –We will require significant additional capital to fund our business plan.

Proposed Project Financing from EXIM

The estimated financing costs associated with the Elk Creek Project over the next twelve months include, but are not limited to, costs relating to the EXIM application process, the scope of which remains under discussion with EXIM. On June 6, 2023, the Company announced that it had submitted an application to EXIM for debt financing, which may include a loan or loan guarantee, to fund the project costs for the Elk Creek Project, under EXIM’s “Make More in America” initiative. The Company was informed that its application received approval by the first of three reviews by the EXIM Transaction Review Committee ("TRC") on October 2, 2023. In April 2024, EXIM provided the Company with a PPL, which also conveyed EXIM’s initial due diligence findings on the Company’s application. The PPL did not state a total amount of the EXIM Financing. Instead, the PPL provided that the amount of the EXIM Financing that could be made available for the Elk Creek Project will be scaled based on the number of U.S. jobs supported, both during construction and over the life of EXIM’s financing, and subject to certain expectations regarding the ratio of debt-to-equity financing for the Elk Creek Project. PPL also identified additional project activities to be undertaken by the Company as part of EXIM’s due diligence process, including, among other things, an updated mine plan and updated Elk Creek Project capital costs on a final or close-to-final basis reflecting updated process flows. On February 4, 2025, EXIM advanced the Company’s application to the next stage of the TRC’s reviews and selected RPMGlobal USA, Inc. whose mining advisory business has since been acquired by SLR Consulting, to conduct an independent technical review of the Elk Creek Project, and in October 2025 the Company executed a professional services agreement with SLR Consulting to conduct an independent environmental and social review as part of EXIM’s ongoing due diligence. The Company’s application remains at the next stage of the TRC’s review process. If the application is approved and supported by EXIM staff, it would be subject to a final decision by EXIM’s Board of Directors.

The amount of the EXIM Financing, if any, will be determined by EXIM. As described above, the PPL provided that the amount of the EXIM Financing that could be made available for the Elk Creek Project will be scaled based on the number of U.S. jobs supported, both during construction and over the life of EXIM’s financing, subject to certain expectations regarding the ratio of debt-to-equity financing for the Elk Creek Project. That determination will be made by EXIM on the basis of its own analysis and its own application of its underwriting criteria and internal policies. The Company does not control that analysis, is not able to predict its outcome, and accordingly is unable to estimate the amount of the EXIM Financing that may ultimately be made available to it, if any.

The Company believes that the completion of the 2026 Elk Creek Study satisfies a key EXIM due diligence requirement reflected in the PPL, and the Company expects to advance to the next steps of the process relating to detailed engineering, procurement and construction contracting. The Company further believes that the 2026 Elk Creek Study, with its updated economic model, mineral resource and mineral reserve estimates and increased job creation projections, demonstrates that the Elk Creek Project satisfies the criteria for increased financing as contemplated by the PPL.

The EXIM Financing remains subject to, among other matters, the satisfactory completion of EXIM’s due diligence, the completion of EXIM’s internal review and approval process, the negotiation and settlement of final terms, and the negotiation and execution of definitive documentation. Neither the letter of interest the Company received from EXIM in March 2023 nor the PPL represents a financing commitment from EXIM. Certain of these conditions, including the timing and sequencing of EXIM’s internal review and approval process, are outside the Company’s control, and the conditions to which any commitment would be subject are customary for financings of a similar nature by U.S. Government or other public lending institutions. The Company continues to meet with EXIM, to respond to requests for additional information from EXIM and from the consultants conducting due diligence on the Company’s application on behalf of EXIM, and to take steps to complete the additional project activities identified by the PPL. There can be no assurance as to what further project activities or matters EXIM may request in connection with the application process. Accordingly, the Company is currently unable to estimate the total amount of the EXIM Financing, if any, or how long the application process may take, and there can be no assurances that the Company will be able to successfully negotiate a final commitment of debt financing from EXIM, on acceptable terms, or at all.

Other Government and Export Credit Support

In addition to the EXIM Financing, the Company has pursued other government-supported sources of capital for the Elk Creek Project. For example, on August 4, 2025, ECRC entered into the DoW Agreement, a Project Sub-Agreement with Advanced Technology International, an entity acting on behalf of the Defense Industrial Base Consortium under the authority of the DoW, pursuant to which ECRC is entitled to receive up to an aggregate of approximately $10.0 million of reimbursement

47


 

payments from the DoW upon the achievement of certain project milestones. The DoW Agreement has an initial term through December 30, 2028. As of June 30, 2026, approximately $8.1 million of such reimbursement payments had been received and approximately $1.9 million remained available upon the achievement of the remaining milestones. In addition, we are seeking other alternative sources of debt financing, which may include loans or loan guarantees from commercial or government-supported sources. The Company can provide no assurance as to the timing or outcome of any additional debt financing arrangements, or that any other loans or loan guarantees will ultimately be obtained. See Item 1A., "Risk Factors – Changes in geopolitical conditions and U.S. critical minerals policy could reduce the strategic importance of our planned products and adversely affect our business."

In March 2015, the Company obtained in-principle eligibility approval for a loan guarantee to be provided by the Federal Republic of Germany under its untied loan guarantee program, which supports financing for projects that contribute to securing supplies of strategic raw materials in the economic interest of Germany. That approval was based on the Company’s offtake agreement with ThyssenKrupp Metallurgical Products GmbH for the purchase of approximately 50% of planned ferroniobium production from the Elk Creek Project, and constituted the first of the approvals required under the program. The Company received a reiteration of in-principle eligibility in 2017 following completion of the then-current feasibility study for the Elk Creek Project, and received a further reiteration of in-principle eligibility in June 2026. No subsequent approvals under the program have been obtained, and the amount of loan guarantees, if any, that may be made available has not been determined. Any such guarantee would be coordinated with the EXIM Financing and with any other debt financing obtained for the Elk Creek Project. The Company can provide no assurance as to the timing or outcome of any further review under the program, or that any loan guarantee will ultimately be provided.

On May 16, 2025, UK Export Finance issued to the Company an expression of interest with respect to a potential debt guarantee of up to $200 million in support of the Elk Creek Project, which is non-binding and is conditioned upon, among other things, the execution of an offtake agreement for one or more of NioCorp’s planned products with UK-based companies that in turn can be shown to support UK exports. A debt guarantee issued by UK Export Finance, if any, would be coordinated with the EXIM Financing and with any loan guarantee provided under the German program described above.

The DoW Agreement does not provide funding for the construction of the Elk Creek Project, and neither the UK Export Finance expression of interest nor the in-principle eligibility approval from the Federal Republic of Germany represent a financing commitment.

Financing and Strategic Alternatives

The Company remains open to financing and strategic opportunities that support its overall financing and development objectives for the Elk Creek Project, which may include the issuance of additional equity; corporate or project-level debt; government and export credit agency financing; offtake, prepayment, royalty or streaming arrangements; and joint venture, strategic investment or other strategic transactions. In evaluating any such opportunity, management intends to consider, among other factors, the total cost of capital, the certainty and timing of funding, the effect on the Company’s ability to construct and operate the Elk Creek Project on its anticipated schedule, and the value delivered to the Company’s shareholders.

Capital Resources and Restrictions on Financing

The Yorkville Equity Facility Financing Agreement expired by its terms on April 1, 2026, and, as of the date of this Annual Report on Form 10-K, the Company has not entered into a replacement equity facility. On October 10, 2025, the Company filed an automatic shelf registration statement on Form S-3ASR, which became effective upon filing and under which the Company may offer and sell securities from time to time.

Except for the potential funding from the exercise of Options and Warrants and the reimbursement payments available to ECRC under the DoW Agreement, we currently have no further funding commitments or arrangements for additional financing as of the date of this Annual Report on Form 10-K. Pursuant to the Exchange Agreement, NioCorp is restricted from issuing equity or equity-linked securities (other than Common Shares) or any preferred equity or non-voting equity if such issuance would adversely impact the rights of the holders of the shares of Class B common stock of ECRC, without the consent of the holders of a majority of the shares of Class B common stock of ECRC. Notwithstanding the restrictions set forth in the Exchange Agreement, there can be no assurance that we will be able to secure additional financing on acceptable terms, or at all. The quantity of funds to be raised and the terms of any proposed equity or debt financing that may be undertaken will be negotiated by management as opportunities to raise funds arise. Management may pursue funding sources of both debt and equity financing, including but not limited to the issuance of equity securities in the form of Common Shares, Warrants, subscription receipts, or any combination thereof in units of the Company pursuant to private placements to accredited investors or pursuant to public offerings in the form of underwritten/brokered offerings, registered direct offerings, or other forms of equity financing and public or private issuances of debt securities, including secured and unsecured convertible debt instruments, or secured debt project financing.

48


 

Management does not currently know the terms pursuant to which such financings may be completed in the future, but any such financings will be negotiated at arm’s-length. Future financings involving the issuance of equity securities or derivatives thereof may be completed at a discount to the then-current market price of the Company’s securities and would be dilutive to current shareholders. In addition, we could raise funds through the sale of interests in our mineral properties. However, we cannot provide any assurances that we will be able to be successful in raising such funds.

Additional Capital Requirements

As defined under S-K 1300, we are a development stage issuer, and we have incurred losses since our inception. The Company will require additional capital to construct the Elk Creek Project and to meet its long-term operating requirements. Based on its current liquidity position and planned expenditures, management believes the Company has sufficient resources to meet its obligations as they become due within one year from the issuance date of the consolidated financial statements included in this Annual Report on Form 10-K, which have been prepared on a going concern basis. Management expects that future capital requirements will be met through a combination of debt financing, equity financing and other funding sources. Uncertainty in capital markets, supply chain disruptions, increased interest rates and inflation, and the potential for regional recessions have contributed to general global economic uncertainty. During fiscal year 2026, these events continued to create uncertainty with respect to overall project funding and timelines.

Cash Management and Credit Risk

We have no exposure to any asset-backed commercial paper. Other than cash held by our subsidiaries for their immediate operating needs in Colorado and Nebraska, all of our cash reserves are on deposit with major U.S. and Canadian chartered banks. We do not believe that the credit, liquidity, or market risks with respect thereto have increased as a result of the current market conditions. However, in order to achieve greater security for the preservation of our capital, we have held our cash reserves in deposit accounts and other highly liquid instruments, which may result in lower rates of interest, and therefore lower interest income, than alternative investments.

Operating Activities

During the year ended June 30, 2026, the Company’s operating activities consumed $15.9 million of cash (2025: $10.7 million). Overall, operational outflows during fiscal year 2026 increased from fiscal year 2025 primarily due to increased exploration and general and administrative expenditures, offset by non-cash activity related to changes in valuation of earnout shares and warrant liabilities. Going forward, the Company’s working capital requirements are expected to increase substantially in connection with the development of the Elk Creek Project.

Investing Activities

During the year ended June 30, 2026, the Company's investing activities consumed $29.7 million of cash (2025: $0.0 million), which included the acquisition of additional land and mineral rights, certain Scandium alloy manufacturing assets, and construction expenditures for the Company's Portal Project.

Financing Activities

Net cash provided by financing activities was $437.1 million in fiscal year 2026 (2025: $34.2 million). This increase in financing inflows primarily reflects the timing of cash inflows from the financing transactions disclosed above under “Liquidity and Capital Resources—Overview.”

Cash Flow Considerations

The Company has historically relied upon debt and equity financing to finance its activities. Subject to the restrictions set forth in the Exchange Agreement, the Company may pursue additional debt and/or equity financing in the medium term; however, there can be no assurance the Company will be able to obtain any required financing in the future on acceptable terms.

49


 

The Company has limited financial resources compared to its proposed expenditures, no source of operating income, and no assurance that additional funding will be available to it for current or future projects, although the Company has been successful in the past in financing its activities through the sale of equity securities.

The ability of the Company to arrange additional financing in the future will depend, in part, on the prevailing capital market conditions, and its success in developing the Elk Creek Project. Any quoted market for the Common Shares may be subject to market trends generally, notwithstanding any potential success of the Company in creating revenue, cash flows, or earnings, and any depression of the trading price of the Common Shares could impact its ability to obtain equity financing on acceptable terms.

Historically, the Company has used net proceeds from issuances of Common Shares to provide sufficient funds to meet its near-term exploration and development plans and other contractual obligations when due. However, development and construction of the Elk Creek Project will require substantial additional capital resources. This includes near-term funding and, ultimately, funding for Elk Creek Project construction and other costs. See “Liquidity and Capital Resources” above, for the Company’s discussion of arrangements related to possible future financings.

Environmental

Our mining and exploration activities are subject to various federal and state laws and regulations governing the protection of the environment. We have made, and expect to make in the future, expenditures to comply with such laws and regulations, but cannot predict the full amount of such future expenditures. As of June 30, 2026 and 2025, we had accrued $48 and $48, respectively, related to estimated environmental obligations.

Forward-Looking Statements

The foregoing discussion and analysis, as well as certain information contained elsewhere in this Annual Report on Form 10-K, contain “forward-looking statements” within the meaning of Section 27A of the Securities Act and Section 21E of the Exchange Act, and are intended to be covered by the safe harbor created thereby. See the discussion in “Forward-Looking Statements” in Item 1., “Business.”

Accounting Developments

For a discussion of Recently Adopted Accounting Pronouncements and Recently Issued Accounting Pronouncements, see Note 3 to the consolidated financial statements included in this Annual Report on Form 10-K.

Critical Accounting Estimates and Recent Accounting Pronouncements

Our significant accounting policies are described in Note 3 to the Consolidated Financial Statements included in this Annual Report on Form 10-K. As described in Note 3, we are required to make estimates and assumptions that affect the reported amounts and related disclosures of assets, liabilities, revenue, and expenses. Our estimates are based on our experience and our interpretation of economic, political, regulatory, and other factors that affect our business prospects. Many of the inputs into our estimation process are subjective and are subject to uncertainty over time and therefore, actual results may differ significantly from our estimates. Note 3 also discloses recent accounting pronouncements applicable to the Company.

We believe that our most critical accounting estimates are related to the carrying value of our long term assets, intangible assets and goodwill; accounting for income taxes and the valuation of deferred tax assets; and the valuation of liabilities associated with Warrants and Earnout Shares, as they require us to make assumptions that are highly uncertain at the time the accounting estimates are made and changes in them are reasonably likely to occur from period to period. Management has discussed the development and selection of these critical accounting estimates with the Audit Committee of our Board (the “Audit Committee”), and the Audit Committee has reviewed the disclosures presented below. In addition, there are other items within our financial statements that require estimation, but are not deemed to be critical. However, changes in estimates used in these and other items could have a material impact on our consolidated financial statements.

Carrying Value of Long-Lived Assets, Intangible Assets, and Goodwill

The recoverability of the carrying values of mineral properties is dependent upon economic reserves being discovered or developed on the properties, permitting, financing, start-up, and commercial production from, or the sale/lease of, or other strategic transactions related to these properties. Development and/or start-up of a project will depend on, among other things, management’s ability to raise sufficient capital for these purposes. We assess the carrying cost of our mineral properties for impairment whenever information or circumstances indicate the potential for impairment. Key inputs include events and circumstances such as our inability to obtain all the necessary permits, changes in the legal status of our mineral properties, government actions, the results of exploration activities and technical evaluations and changes in economic conditions, including the price of commodities or input prices. Many of these inputs are subjective and are subject to uncertainty over time. Such evaluations compare estimated future net cash flows with our carrying costs and future obligations on an undiscounted

50


 

basis. If it is determined that the estimated future undiscounted cash flows are less than the carrying value of the property, an impairment loss will be recorded, measured by the amount by which the carrying amount of the assets exceeds the fair value of the assets. Where estimates of future net cash flows are not determinable and where other conditions indicate the potential for impairment, management uses available market information and/or third-party valuation experts to assess if the carrying value can be recovered and to estimate fair value.

Long-lived assets, other than mineral properties, held and used by the Company are reviewed for impairment whenever events or changes in circumstances indicate that the carrying amount of an asset may not be recoverable. For purposes of evaluating the recoverability of long-lived assets, the recoverability test is performed using undiscounted net cash flows related to the long-lived assets. If such assets are considered to be impaired, the impairment recognized is measured by the amount by which the carrying amount of the assets exceeds the fair value of the assets.

The fair value of the acquired technology was estimated using the multi-period excess earnings method. Significant inputs include estimated future cash flows attributable to the acquired technology, an appropriate discount rate, and assumptions regarding technological obsolescence. The intangible asset is amortized on a straight-line basis over an estimated useful life of ten years and is reviewed for impairment whenever events or changes in circumstances indicate that the carrying value may not be recoverable. Assumptions used in the model are subjective and require significant judgment.

Goodwill is assessed for impairment annually, or more frequently upon the occurrence of a triggering event. The Company operates as a single reporting unit, as our scandium commercialization activities are not managed or reviewed as a discrete component by the Chief Operating Decision Maker and no discrete financial information is prepared at that level. Accordingly, goodwill is tested at the consolidated reporting unit level. This determination will be reassessed as our scandium commercialization activities mature.

Income Taxes

We have assets, hold interests, and conduct activities in the U.S. and Canada and are subject to their tax regimes. Tax laws are complex and continue to evolve. While we have a history of losses, our assumptions made in tax returns are subject to review and interpretation by taxing authorities and could be modified. Management judgment is required in determining our provision for income taxes, our deferred tax assets and liabilities, and any valuation allowance recorded against our deferred tax assets. We consider factors such as the cumulative income or loss in recent years; reversal of deferred tax liabilities; projected future taxable income exclusive of temporary differences; the character of the income tax asset, including income tax positions; tax planning strategies and the period over which we expect the deferred tax assets to be recovered in the determination of the valuation allowance. In the event that actual results differ from these estimates or we adjust our estimates in the future, we may need to adjust our valuation allowance, which could materially impact our financial position and results of operations.

Financial Instruments Carried at Fair Value

The fair value of our Earnout Shares was determined using various significant unobservable inputs, including a discount rate and our best estimate of expected volatility and expected holding periods. The fair value of our private Warrants was determined using quoted prices or inputs that are observable, either directly or indirectly. Changes in the estimated fair values of these liabilities may have material impacts on our results of operations in any given period, as any increases in these liabilities have a corresponding negative impact on our U.S. GAAP results of operations. See Notes 8 and 9 to our consolidated financial statements included in this Annual Report on Form 10-K for additional details.

Other

The Company has one class of shares, being Common Shares. A summary of outstanding Common Shares, Vested Shares, Options, and Warrants as of September 25, 2026, is set out below, on a fully diluted basis.

 

 

Common
Shares
Outstanding
(fully diluted)

 

Common Shares

 

 

145,849,630

 

Vested Shares of ECRC Class B common stock(1)

 

 

3,516,140

 

Options(2)

 

 

5,052,901

 

Warrants(3)

 

 

18,696,530

 

 

(1)
Each exchangeable into one Common Share at any time, and from time to time, until the tenth anniversary of the Closing Date.
(2)
Each exercisable for one Common Share.
(3)
Includes 15,666,526 NioCorp Assumed Warrants that are each exercisable for 1.11829212 Common Shares, and 3,041,254 Warrants that are each exercisable into one Common Share.

51


 

ITEM 7A. QUANTITATIVE AND QUALITATIVE DISCLOSURES ABOUT MARKET RISK

Interest rate risk

The Company’s exposure to changes in market interest rates, relates primarily to the Company’s earned interest income on cash deposits and short-term investments. The Company maintains a balance between the liquidity of cash assets and the interest rate return thereon. The carrying amount of financial assets, net of any provisions for losses, represents the Company’s maximum exposure to credit risk.

Foreign currency exchange risk

The Company incurs expenditures in both U.S. and Canadian dollars. Canadian dollar expenditures are primarily related to engineering and metallurgical expenses, as well as certain professional services. As a result, currency exchange fluctuations may impact the costs of our operating activities. To reduce this risk, we maintain sufficient cash balances in Canadian dollars to fund expected near-term expenditures.

Commodity price risk

The Company is exposed to commodity price risk related to the elements associated with the Elk Creek Project. A significant decrease in the global demand for these elements may have a material adverse effect on our business. The Elk Creek Project is not in production, and the Company does not currently hold any commodity derivative positions.

ITEM 8. FINANCIAL STATEMENTS AND SUPPLEMENTARY DATA

52


 

REPORT OF INDEPENDENT REGISTERED PUBLIC ACCOUNTING FIRM

To the shareholders and the Board of Directors of NioCorp Developments Ltd.

Opinion on the Financial Statements

We have audited the accompanying consolidated balance sheets of NioCorp Developments Ltd. and subsidiaries (the "Company") as of June 30, 2026 and 2025, the related consolidated statements of operations and comprehensive loss, cash flows, and shareholders' equity and redeemable noncontrolling interest, for each of the two years in the period ended June 30, 2026, the related notes (collectively referred to as the "financial statements"). In our opinion, the financial statements present fairly, in all material respects, the financial position of the Company as of June 30, 2026 and 2025, and the results of its operations and its cash flows for each of the two years in the period ended June 30, 2026 in conformity with accounting principles generally accepted in the United States of America.

Basis for Opinion

These financial statements are the responsibility of the Company's management. Our responsibility is to express an opinion on the Company's financial statements based on our audits. We are a public accounting firm registered with the Public Company Accounting Oversight Board (United States) (PCAOB) and are required to be independent with respect to the Company in accordance with the U.S. federal securities laws and the applicable rules and regulations of the Securities and Exchange Commission and the PCAOB.

We conducted our audits in accordance with the standards of the PCAOB. Those standards require that we plan and perform the audit to obtain reasonable assurance about whether the financial statements are free of material misstatement, whether due to error or fraud. The Company is not required to have, nor were we engaged to perform, an audit of its internal control over financial reporting. As part of our audits, we are required to obtain an understanding of internal control over financial reporting but not for the purpose of expressing an opinion on the effectiveness of the Company’s internal control over financial reporting. Accordingly, we express no such opinion.

Our audits included performing procedures to assess the risks of material misstatement of the financial statements, whether due to error or fraud, and performing procedures that respond to those risks. Such procedures included examining, on a test basis, evidence regarding the amounts and disclosures in the financial statements. Our audits also included evaluating the accounting principles used and significant estimates made by management, as well as evaluating the overall presentation of the financial statements. We believe that our audits provide a reasonable basis for our opinion.

Critical Audit Matter

The critical audit matter communicated below is a matter arising from the current-period audit of the financial statements that was communicated or required to be communicated to the audit committee and that (1) relates to accounts or disclosures that are material to the financial statements and (2) involved our especially challenging, subjective, or complex judgments. The communication of critical audit matters does not alter in any way our opinion on the financial statements, taken as a whole, and we are not, by communicating the critical audit matter below, providing a separate opinion on the critical audit matter or on the accounts or disclosures to which it relates.

Carrying value of Mineral Properties and Long-Lived Assets – Refer to Notes 3(d) through 3(g) to the financial statements

Critical Audit Matter Description

As of June 30, 2026, the Company held mineral properties and long-lived assets (which includes property and equipment, intangible assets, and goodwill).

The Company assesses mineral properties, property and equipment, and intangible assets for impairment whenever events or changes in circumstances indicate respective carrying amounts may not be recoverable. For goodwill, the Company assesses impairment at least annually, or more frequently upon the occurrence of a triggering event, to determine if it is more likely than not that the asset is impaired. The recoverability of the carrying values of mineral properties, property and equipment, and intangible assets, along with the impairment of goodwill, depends on the development of economic reserves, permitting, financing, start-up, and commercial production from the properties, amongst other factors.

53


 

If impairment indicators are present when evaluating impairment of goodwill or recoverability of mineral properties, property and equipment, and intangible assets, the respective assets are tested for impairment. For mineral properties, property and equipment, and intangible assets, estimated undiscounted future net cash flows of the assets are compared to their respective carrying amounts, with an impairment loss recognized against the assets for any excess of the carrying amount over the respective estimated undiscounted future net cash flows. For goodwill, the fair value of the reporting unit is compared to the carrying value of the reporting unit, with an impairment loss recognized against goodwill for any excess of the carrying value of the reporting unit over fair value of the reporting unit, limited to the total amount of goodwill.

Given the significant assumptions made by management in determining if events or changes indicated that the carrying amounts of the long-live assets were impaired during the current year, performing audit procedures to evaluate the reasonableness of management's conclusions required a high degree of auditor judgment and an increased extent of effort.

How the Critical Audit Matter Was Addressed in the Audit

Our audit procedures related to the recoverability of mineral properties and long-lived assets, including impairment of goodwill, consisted of risk assessment and testing management’s impairments analyses through the following, among other procedures:

•
We evaluated management’s assessment of recoverability of mineral properties, property and equipment, and intangible assets through the following procedures:
o
We evaluated the reasonableness of management’s assessment over ASC 360, Property, Plant, and Equipment, qualitative impairment indicators regarding recoverability of the carrying amounts of the assets.
o
We performed a qualitative assessment as of June 30th to evaluate whether events or changes in circumstances indicated that the carrying amounts of the assets may not be recoverable, considering information in industry reports and the Company’s future business strategies.
o
Tested the design and implementation of management’s controls over the recoverability of mineral properties, property and equipment, and intangible assets.
•
We evaluated management’s assessment of impairment of goodwill through the following procedures:
o
We evaluated the reasonableness of management’s annual assessment over ASC 350, Intangibles – Goodwill and Other, qualitative impairment indicators regarding whether it is more likely than not that the carrying amount of the associated reporting unit, including goodwill, exceeds the fair value of the reporting unit as of the Company’s annual assessment date of April 1st.
o
We performed a qualitative assessment as of June 30th to evaluate potential impairment indicators during the period from management’s April 1st annual goodwill impairment assessment date to the June 30th balance sheet date, considering information in industry reports and the Company’s future business strategies.
o
Tested the design and implementation of management’s controls over the impairment of goodwill.
•
Evaluated the completeness and accuracy of the disclosures related to the recoverability of the mineral properties and long-lived assets, including impairment of goodwill.

 

 

/s/ DELOITTE & TOUCHE LLP
 

Denver, Colorado

September 25, 2026

 

We have served as the Company's auditor since fiscal year 2024.

54


 

NioCorp Developments Ltd.

Consolidated Balance Sheets

(expressed in thousands of U.S. dollars, except share data)

 

 

As of June 30,

 

 

2026

 

 

2025

 

ASSETS

 

 

 

 

 

 

Current

 

 

 

 

 

 

Cash and cash equivalents

 

$

415,004

 

 

$

25,554

 

Restricted cash

 

 

2,102

 

 

 

—

 

Prepaid expenses and other

 

 

1,740

 

 

 

1,183

 

Total current assets

 

 

418,846

 

 

 

26,737

 

Non-current

 

 

 

 

 

 

Right-of-use assets

 

 

91

 

 

 

118

 

Property and equipment, net

 

 

11,569

 

 

 

839

 

Mineral properties

 

 

25,726

 

 

 

16,085

 

Intangible assets, net

 

 

5,672

 

 

 

—

 

Goodwill

 

 

2,220

 

 

 

—

 

Other assets

 

 

2,776

 

 

 

40

 

Total assets

 

$

466,900

 

 

$

43,819

 

 

 

 

 

 

 

 

LIABILITIES

 

 

 

 

 

 

Current

 

 

 

 

 

 

Accounts payable and accrued liabilities

 

$

5,638

 

 

$

1,795

 

Deferred reimbursements

 

 

6,177

 

 

 

—

 

Warrant liabilities, at fair value

 

 

4,606

 

 

 

—

 

Operating lease liability

 

 

94

 

 

 

98

 

Total current liabilities

 

 

16,515

 

 

 

1,893

 

Non-current

 

 

 

 

 

 

Warrant liabilities, at fair value

 

 

6,140

 

 

 

6,852

 

Earnout liability, at fair value

 

 

14,451

 

 

 

5,880

 

Operating lease liability

 

 

—

 

 

 

33

 

Total liabilities

 

 

37,106

 

 

 

14,658

 

Commitments and contingencies (Note 3r, 6)

 

 

 

 

 

 

Redeemable noncontrolling interest

 

 

(1,446

)

 

 

838

 

SHAREHOLDERS' EQUITY

 

 

 

 

 

 

Common stock, no par value, unlimited shares authorized; 145,838,380
 and
58,491,196 shares outstanding, respectively

 

 

660,049

 

 

 

208,551

 

Accumulated deficit

 

 

(227,872

)

 

 

(179,317

)

Accumulated other comprehensive loss

 

 

(937

)

 

 

(911

)

Total shareholders’ equity

 

 

431,240

 

 

 

28,323

 

Total liabilities, redeemable noncontrolling interest, and shareholders’ equity

 

$

466,900

 

 

$

43,819

 

 

The accompanying notes are an integral part of these consolidated financial statements

55


 

NioCorp Developments Ltd.

Consolidated Statements of Operations and Comprehensive Loss

(expressed in thousands of U.S. dollars, except share and per share data)

 

 

For the year ended June 30,

 

 

2026

 

 

2025

 

Operating expenses

 

 

 

 

 

 

Exploration expenditures

 

$

16,076

 

 

$

4,135

 

General and administrative expenditures

 

 

22,233

 

 

 

7,823

 

Total operating expenses

 

 

38,309

 

 

 

11,958

 

Change in fair value of earnout shares liability

 

 

8,571

 

 

 

2,063

 

Change in fair value of warrant liabilities

 

 

13,034

 

 

 

4,093

 

Change in fair value of convertible notes

 

 

—

 

 

 

40

 

Interest expense

 

 

—

 

 

 

48

 

Interest income

 

 

(9,146

)

 

 

(94

)

Other non-operating expense (income)

 

 

13

 

 

 

(126

)

Loss before income taxes

 

 

(50,781

)

 

 

(17,982

)

Income tax benefit

 

 

—

 

 

 

—

 

Net loss

 

 

(50,781

)

 

 

(17,982

)

Less: Net loss attributable to redeemable noncontrolling interest

 

 

(2,226

)

 

 

(577

)

Net loss attributable to the Company

 

$

(48,555

)

 

$

(17,405

)

 

 

 

 

 

Reporting currency translation

 

 

(26

)

 

 

—

 

Total comprehensive loss

 

 

(50,807

)

 

 

(17,982

)

Less: Comprehensive loss attributable to redeemable noncontrolling interest

 

 

(2,226

)

 

 

(577

)

Comprehensive loss attributable to the Company

 

$

(48,581

)

 

$

(17,405

)

 

 

 

 

 

 

 

Loss per common share, basic and diluted

 

$

(0.41

)

 

$

(0.36

)

 

 

 

 

 

 

Weighted Average Shares Outstanding

 

 

117,214,449

 

 

 

45,072,895

 

 

The accompanying notes are an integral part of these consolidated financial statements

56


 

NioCorp Developments Ltd.

Consolidated Statements of Cash Flows

(expressed in thousands of U.S. dollars)

 

 

For the year ended June 30,

 

 

2026

 

 

2025

 

CASH FLOWS FROM OPERATING ACTIVITIES

 

 

 

 

 

 

Net loss for the period

 

$

(50,781

)

 

$

(17,982

)

Adjustments for:

 

 

 

 

 

 

Change in valuation of earnout shares liability

 

 

8,571

 

 

 

2,063

 

Change in valuation of warrant liabilities

 

 

13,034

 

 

 

4,093

 

Change in fair value of convertible note

 

 

—

 

 

 

40

 

Accretion of convertible debt

 

 

—

 

 

 

43

 

Share-based compensation

 

 

4,441

 

 

 

789

 

Loss on equity facility issuances

 

 

724

 

 

 

589

 

Fair value of insider warrants

 

 

—

 

 

 

144

 

Depreciation

 

 

359

 

 

 

3

 

Unrealized (gain) loss on equity securities

 

 

(1

)

 

 

1

 

Noncash lease activity

 

 

(10

)

 

 

(6

)

Other gains

 

 

—

 

 

 

(122

)

 

 

(23,663

)

 

 

(10,345

)

Change in working capital items:

 

 

 

 

 

 

Prepaid expenses and other

 

 

(459

)

 

 

(267

)

Deposits

 

 

(44

)

 

 

(2

)

Deferred reimbursements

 

 

6,177

 

 

 

—

 

Accounts payable and accrued liabilities

 

 

2,091

 

 

 

(48

)

Net cash used in operating activities

 

 

(15,898

)

 

 

(10,662

)

 

 

 

 

 

 

CASH FLOWS FROM INVESTING ACTIVITIES

 

 

 

 

 

 

Assets acquired in business combination

 

 

(8,400

)

 

 

0

 

Capitalized expenditures

 

 

(21,257

)

 

 

(5

)

Net cash used in investing activities

 

 

(29,657

)

 

 

(5

)

 

 

 

 

 

 

CASH FLOWS FROM FINANCING ACTIVITIES

 

 

 

 

 

 

Proceeds from issuance of capital stock

 

 

467,202

 

 

 

45,666

 

Issuance of debt, net of costs

 

 

—

 

 

 

—

 

Related party debt draws

 

 

—

 

 

 

504

 

Related party debt repayments

 

 

—

 

 

 

(504

)

Debt repayments

 

 

—

 

 

 

(7,223

)

Share issue costs

 

 

(30,069

)

 

 

(4,234

)

Net cash provided by financing activities

 

 

437,133

 

 

 

34,209

 

Exchange rate effect on cash and cash equivalents

 

 

(26

)

 

 

—

 

Change in cash and cash equivalents and restricted cash during period

 

 

391,552

 

 

 

23,542

 

Cash and cash equivalents and restricted cash, beginning of period

 

 

25,554

 

 

 

2,012

 

Cash and cash equivalents and restricted cash, end of period

 

$

417,106

 

 

$

25,554

 

 

 

 

 

 

 

Supplemental cash flow information:

 

 

 

 

 

 

Amounts paid for interest

 

$

—

 

 

$

4

 

Non-cash investing and financing transactions:

 

 

 

 

 

 

Conversion of debt for common shares

 

 

—

 

 

$

501

 

Additions to construction in progress not yet paid

 

 

1,753

 

 

 

—

 

Value of warrants issued

 

 

—

 

 

 

2,262

 

Reclassification of warrant liabilities to equity

 

 

9,141

 

 

 

820

 

 

The accompanying notes are an integral part of these consolidated financial statements

57


 

NioCorp Developments Ltd.

Consolidated Statements of Shareholders’ Equity and Redeemable Noncontrolling Interest

(expressed in thousands of U.S. dollars, except share data)

 

 

Common
Shares
Outstanding

 

 

Common
Stock

 

 

Accumulated
Deficit

 

 

Accumulated
Other
Comprehensive
Loss

 

 

Total
Shareholders'
Equity

 

 

Redeemable
Noncontrolling
Interest

 

Balance, June 30, 2024

 

 

38,062,647

 

 

$

163,823

 

 

$

(161,912

)

 

$

(911

)

 

$

1,000

 

 

$

1,534

 

Equity placements

 

 

13,321,628

 

 

 

30,059

 

 

 

—

 

 

 

—

 

 

 

30,059

 

 

 

—

 

Yorkville equity facility draws

 

 

5,671,742

 

 

 

12,941

 

 

 

—

 

 

 

—

 

 

 

12,941

 

 

 

—

 

Warrant exercises

 

 

828,235

 

 

 

1,809

 

 

 

—

 

 

 

—

 

 

 

1,809

 

 

 

—

 

Option exercises

 

 

512

 

 

 

—

 

 

 

—

 

 

 

—

 

 

 

—

 

 

 

—

 

Redemption of vested shares

 

 

348,085

 

 

 

119

 

 

 

—

 

 

 

—

 

 

 

119

 

 

 

(119

)

Debt conversions

 

 

258,347

 

 

 

501

 

 

 

—

 

 

 

—

 

 

 

501

 

 

 

—

 

Issuance of Lind Consent warrants

 

 

—

 

 

 

2,262

 

 

 

—

 

 

 

—

 

 

 

2,262

 

 

 

—

 

Conversion of private warrants

 

 

—

 

 

 

482

 

 

 

—

 

 

 

—

 

 

 

482

 

 

 

—

 

Share-based compensation

 

 

—

 

 

 

789

 

 

 

—

 

 

 

—

 

 

 

789

 

 

 

—

 

Share issuance costs

 

 

—

 

 

 

(4,234

)

 

 

—

 

 

 

—

 

 

 

(4,234

)

 

 

—

 

Loss for the year

 

 

—

 

 

 

—

 

 

 

(17,405

)

 

 

—

 

 

 

(17,405

)

 

 

(577

)

Balance, June 30, 2025

 

 

58,491,196

 

 

$

208,551

 

 

$

(179,317

)

 

$

(911

)

 

$

28,323

 

 

$

838

 

Equity placements

 

 

58,406,915

 

 

 

405,195

 

 

 

—

 

 

 

—

 

 

 

405,195

 

 

 

—

 

Yorkville equity facility draws

 

 

5,727,662

 

 

 

39,434

 

 

 

—

 

 

 

—

 

 

 

39,434

 

 

 

—

 

Warrant exercises

 

 

22,308,264

 

 

 

28,557

 

 

 

—

 

 

 

—

 

 

 

28,557

 

 

 

—

 

Option exercises

 

 

486,452

 

 

 

1,381

 

 

 

—

 

 

 

—

 

 

 

1,381

 

 

 

—

 

Redemption of vested shares

 

 

417,891

 

 

 

58

 

 

 

—

 

 

 

—

 

 

 

58

 

 

 

(58

)

Conversion of private warrants

 

 

—

 

 

 

2,501

 

 

 

—

 

 

 

—

 

 

 

2,501

 

 

 

—

 

Share-based compensation

 

 

—

 

 

 

4,441

 

 

 

—

 

 

 

—

 

 

 

4,441

 

 

 

—

 

Share issuance costs

 

 

—

 

 

 

(30,069

)

 

 

—

 

 

 

—

 

 

 

(30,069

)

 

 

—

 

Change in accumulated other comprehensive income

 

 

—

 

 

 

—

 

 

 

—

 

 

 

(26

)

 

 

(26

)

 

 

 

Loss for the year

 

 

—

 

 

 

 

 

 

(48,555

)

 

 

—

 

 

 

(48,555

)

 

 

(2,226

)

Balance, June 30, 2026

 

 

145,838,380

 

 

$

660,049

 

 

$

(227,872

)

 

$

(937

)

 

$

431,240

 

 

$

(1,446

)

 

 

The accompanying notes are an integral part of these consolidated financial statements

58


 

NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

1.
DESCRIPTION OF BUSINESS

NioCorp Developments Ltd. (the “Company” or “NioCorp”) was incorporated on February 27, 1987, under the laws of the Province of British Columbia and currently operates in one reportable operating segment consisting of exploration and development of mineral deposits in the United States, specifically, the Elk Creek Niobium/Scandium/Titanium property (the “Elk Creek Project”) located in southeastern Nebraska.

On March 17, 2023 (the “Closing Date”), the Company closed a series of transactions pursuant to the Business Combination Agreement, dated September 25, 2022 (the “Business Combination Agreement”), among the Company, GX Acquisition Corp. II (“GXII”), and Big Red Merger Sub Ltd. (the closing of such transactions, the “Closing”).

The Company currently earns no operating revenues and will require additional capital in order to advance the Elk Creek Project to construction and commercial operation.

Liquidity

As of June 30, 2026, the Company had cash and cash equivalents of $415,004 and working capital of $402,331. Based on its current liquidity position and planned expenditures, management believes the Company has sufficient resources to meet its obligations as they become due within one year from the issuance date of these consolidated financial statements, which have been prepared on a going concern basis.

The Company will require additional capital to fully develop, construct, and operate the Elk Creek Project. Management expects that future capital requirements will be met through a combination of debt financing, equity financings, and other funding sources.

2.
BASIS OF PREPARATION
a)
Basis of Preparation and Consolidation

These consolidated financial statements have been prepared in conformity with generally accepted accounting principles of the United States of America (“U.S. GAAP”) and the rules and regulations of the U.S. Securities and Exchange Commission. The consolidated financial statements include the consolidated accounts of the Company and its wholly owned subsidiaries with all significant intercompany transactions eliminated. Certain transactions include reference to Canadian dollars (“C$”) where applicable. Certain reclassifications were made to the prior year's consolidated statement of operations and comprehensive loss to conform to the current year's presentation, combining professional fees, employee-related costs, and other operating expenses into a single line item, general and administrative expenditures.

These consolidated financial statements include the accounts of the Company and the subsidiaries listed in the following table. All intercompany transactions and balances have been eliminated.

 

 

 

 

Ownership at June 30,

Subsidiary

 

Jurisdiction of
incorporation

 

2026

 

2025

0896800 B.C. Ltd. (“0896800”)

 

British Columbia, Canada

 

100%

 

100%

Elk Creek Resources Corp. (“ECRC”) (1)

 

Delaware, USA

 

81.33%

 

80.42%

NioCorp Advanced Metals and Alloys, LLC (“NAMA”)

 

Delaware, USA

 

100%

 

—

NioCorp Technologies Limited

 

United Kingdom

 

100%

 

100%

(1) Represents 100% of Class A common stock owned by 0896800, and 3,516,140 and 3,934,031 Vested Shares and 3,391,596 and 3,391,596 Earnout Shares (each as defined below) held by third parties, and outstanding as of June 30, 2026 and 2025, respectively.

 

b)
Use of Estimates

The preparation of consolidated financial statements in conformity with U.S. GAAP requires management to make estimates and assumptions that affect the reported amounts of assets and liabilities and the disclosure of contingent assets and liabilities at the date of the consolidated financial statements, and the reported amounts of expenses during the reporting period. The Company regularly evaluates estimates and assumptions related to the

59


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

valuation of property and equipment, mineral properties, intangible assets, goodwill, deferred income tax asset valuations, earnout and warrant liabilities, and share-based compensation. The Company bases its estimates and assumptions on current facts, historical experience, and various other factors that it believes to be reasonable under the circumstances, the results of which form the basis for making judgments about the other sources. The actual results experienced by the Company may differ materially and adversely from the Company’s estimates. To the extent there are material differences between estimates and the actual results, future results of operations will be affected.

3.
SIGNIFICANT ACCOUNTING POLICIES
a)
Development Stage Issuer

The Company is considered to be a development stage issuer under Subpart 1300 of Regulation S-K of the United States Securities Act of 1933, as amended (“S-K 1300”), and it devotes substantially all of its efforts to acquiring and exploring mining interests that management believes should eventually provide sufficient net profits to sustain the Company’s existence. Until such interests are engaged in commercial production, the Company will continue to seek additional funding to support the completion of its exploration and development activities. The Company’s activities are subject to significant risks and uncertainties, including its ability to secure sufficient funding to continue operations, to obtain proven and probable reserves, to comply with industry regulations and obtain permits necessary for development of the Elk Creek Project, as well as environmental risks and market conditions.

b)
Cash and Cash Equivalents

Cash and cash equivalents include cash on hand, cash in banks, investments in certificates of deposit with original maturities of 90 days or less, and money market funds. The Company maintains the majority of its cash balances with two financial institutions. Accounts at banks in the United States (“U.S.”) are insured by the Federal Deposit Insurance Corporation (“FDIC”) up to $250, while accounts at banks in Canada are insured by the Canada Deposit Insurance Corporation (“CDIC”) up to C$100. At June 30, 2026, the Company had $413,932 and $129 in excess of the FDIC and CDIC insured limits, respectively.

As of June 30, 2026, total cash, cash equivalents, and restricted cash was $417,106, consisting of cash and cash equivalents of $415,004 and restricted cash of $2,102. As of June 30, 2025, there was no restricted cash, and the total of $25,554 consisted entirely of cash and cash equivalents. Restricted cash consists primarily of funds held in escrow pursuant to an agreement with Johnson County, Nebraska for road improvements adjacent to the Elk Creek Project site.

c)
Foreign Currency Translation

Functional and reporting currency

Items included in the financial statements of each of the Company’s entities are measured using the currency of the primary economic environment in which the entity operates (“the functional currency”). The functional currency for all entities is the U.S. Dollar except for NioCorp Technologies Limited, which is measured in British Pounds.

The reporting currency for these consolidated financial statements is U.S. dollars.

Transactions in foreign currency

Transactions made in a currency other than the functional currency are remeasured to the functional currency at exchange rates at the dates of the transactions. Monetary assets and liabilities denominated in foreign currencies at the reporting date are remeasured to the functional currency at the exchange rate at that date and non-monetary assets and liabilities are remeasured at historical rates. Foreign currency translation gains and losses are included in profit or loss.

60


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

Translation to reporting currency

Translation gains and losses from the application of the U.S. dollar as the reporting currency, if any, are included as part of cumulative currency translation adjustment, which is reported as a component of shareholders’ equity under accumulated other comprehensive loss.

d)
Mineral Properties

Mineral property acquisition costs, including indirectly related acquisition costs, are capitalized when incurred. Acquisition costs include cash consideration and the fair market value of common shares, no par value, of the Company (“Common Shares”) issued as consideration. Properties acquired under option agreements, whereby payments are made at the sole discretion of the Company, are capitalized as mineral property acquisition costs at such time as the payments are made. Exploration costs are expensed as incurred. When it is determined that a mining deposit can be economically and legally extracted or produced based on established proven and probable reserves under S-K 1300, and the Company’s board of directors (the “Board”) has approved the commencement of formal development activities, development costs related to such reserves and incurred after such board approval will be considered for capitalization. The establishment of proven and probable reserves is based on results of feasibility studies, which indicate whether a property is economically feasible. Upon commencement of commercial production, capitalized costs will be amortized over their estimated useful lives or units of production, whichever is a more reliable measure. Capitalized amounts relating to a property that is abandoned or otherwise considered uneconomic for the foreseeable future are written off.

Direct costs incurred in connection with the construction of the Elk Creek Project mine portal, including construction contractor costs and directly attributable construction management costs, are capitalized as construction in progress ("CIP") within property and equipment. CIP assets are not depreciated or amortized during the construction period. Upon substantial completion, accumulated CIP costs will be transferred to mine development assets and amortized using the units-of-production method over proven and probable reserves upon commencement of commercial production.

The recoverability of the carrying values of mineral properties is dependent upon economic reserves being discovered or developed on the properties, permitting, financing, start-up, and commercial production from, or the sale/lease of, or other strategic transactions related to these properties. Development and/or start-up of a project will depend on, among other things, management’s ability to raise sufficient capital for these purposes. We assess the carrying cost of our mineral properties for impairment whenever information or circumstances indicate the potential for impairment. This would include events and circumstances such as our inability to obtain all the necessary permits, changes in the legal status of our mineral properties, government actions, the results of exploration activities and technical evaluations and changes in economic conditions, including the price of commodities or input prices. Such evaluations compare estimated future net cash flows with our carrying costs and future obligations on an undiscounted basis. If it is determined that the estimated future undiscounted cash flows are less than the carrying value of the property, an impairment loss will be recorded. Where estimates of future net cash flows are not determinable and where other conditions indicate the potential for impairment, management uses available market information and/or third-party valuation experts to assess if the carrying value can be recovered and to estimate fair value. There was no impairment recorded to mineral properties as of June 30, 2026 or 2025, respectively.

e)
Long Lived Assets

Long-lived assets, other than mineral properties, held and used by the Company are reviewed for impairment whenever events or changes in circumstances indicate that the carrying amount of an asset may not be recoverable. For purposes of evaluating the recoverability of long-lived assets, the recoverability test is performed using undiscounted net cash flows related to the long-lived assets. If such assets are considered to be impaired, the impairment recognized is measured by the amount by which the carrying amount of the assets exceeds the fair value of the assets. Assets to be disposed of are reported at the lower of the carrying amount or fair value less costs to sell. There was no impairment recorded to long-lived assets as of June 30, 2026 or 2025, respectively.

f)
Intangible Assets

The fair value of the acquired technology was estimated using the multi-period excess earnings method. Significant inputs include estimated future cash flows attributable to the acquired technology, an appropriate

61


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

discount rate, and assumptions regarding technological obsolescence. The intangible asset is amortized on a straight-line basis over an estimated useful life of ten years and is reviewed for impairment whenever events or changes in circumstances indicate that the carrying value may not be recoverable. Assumptions used in the model are subjective and require significant judgment. There was no impairment recorded to intangible assets as of June 30, 2026 or 2025, respectively.

g)
Goodwill

Goodwill is assessed for impairment annually on April 1, or more frequently upon the occurrence of a triggering event. The Company operates as a single reporting unit, as our scandium commercialization activities are not managed or reviewed as a discrete component by the CODM (as defined below) and no discrete financial information is prepared at that level. Accordingly, goodwill is tested at the consolidated reporting unit level. This determination will be reassessed as our scandium commercialization activities mature. There was no impairment recorded to goodwill as of June 30, 2026 or 2025, respectively.

h)
Leases

Under Accounting Standards Codification (“ASC”) 842, Leases, we determine if a contractual arrangement is, or contains, a lease at the inception date. Right-of-use ("ROU") assets and liabilities related to operating leases are separately reported in the consolidated balance sheets. The Company currently has no finance leases.

ROU assets and lease liabilities are recognized at the lease commencement date based on the present value of the future lease payments over the lease term. When the rate implicit to the lease cannot be readily determined, we utilize our incremental borrowing rate in determining the present value of the future lease payments. The incremental borrowing rate is derived from information available at the lease commencement date and represents the rate of interest that a lessee would have to pay to borrow an amount equal to the lease payments on a collateralized basis over a similar term in a similar economic environment. Operating lease ROU assets also include any cumulative prepaid or accrued rent when the lease payments are uneven throughout the lease term. The ROU assets and lease liabilities may include options to extend or terminate the lease when it is reasonably certain that we will exercise that option.

Lease liabilities are increased by interest and reduced by payments each period, and the ROU asset is amortized over the lease term. For operating leases, interest on the lease liability and the amortization of the ROU asset result in straight-line rent expense over the lease term. Variable lease expenses are recorded when incurred.

i)
Warrants

We apply relevant accounting guidance for warrants to purchase our Common Shares (“Warrants”) based on the nature of the relationship with the counterparty. The Company has made an accounting policy election that the “greater of” Share-Price Input to the Black-Scholes Value would not preclude equity classification. The Company has not had any historical transactions that include the “greater of” Share-Price Input feature. For Warrants issued to investors or lenders in exchange for cash or other financial assets, we follow guidance issued within ASC 480, Distinguishing Liabilities from Equity, and ASC 815, to assist in the determination of whether the Warrants should be classified as liabilities or equity. The fair value of Warrants is estimated using Black Scholes modeling or Monte Carlo modeling, depending on the settlement features embedded in the Warrant. Inputs under both models include inputs such as NioCorp’s Common Share price, the risk-free interest rate, the expected term, the volatility, and the dividend rate. Warrants that are determined to require liability classifications are measured at fair value upon issuance and are subsequently remeasured to their then fair value at each subsequent reporting period with changes in fair value recorded in current earnings. Warrants that are determined to require equity classifications are measured at fair value upon issuance and are not subsequently remeasured unless they are required to be reclassified.

j)
Earnout Shares

Earnout Shares are classified as a liability due to failure to meet the equity classification criteria under ASC 815-40. The Earnout Shares are measured at fair value upon issuance and subsequently remeasured at each reporting period using a Monte Carlo simulation methodology, which includes inputs such as NioCorp’s Common Share price, the risk-free interest rate, the expected term, the weighted average of historical Common Share volatility and implied volatility underlying the Company’s publicly traded Warrants, the dividend rate, the conversion price,

62


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

and the number of Earnout Shares outstanding. Assumptions used in the model are subjective and require significant judgment.

k)
Financial Instruments

The Company’s financial instruments consist of cash and cash equivalents, receivables, equity securities, and accounts payable and accrued liabilities. It is management’s opinion that the Company is not exposed to significant interest, currency or credit risks arising from its financial instruments. The fair values of these instruments approximate their carrying value unless otherwise noted.

l)
Concentration of Credit Risk

The financial instrument which potentially subjects the Company to credit risk is cash and cash equivalents. The Company holds investments or maintains available cash primarily in two commercial banks located in Vancouver, British Columbia and Columbus, Ohio. As part of its cash management process, the Company regularly monitors the relative credit standing of these institutions.

m)
Asset Retirement Obligation

The Company is subject to various government laws and regulations relating to environmental disturbances caused by exploration and evaluation activities. The estimated costs associated with environmental remediation obligations are accrued in the period in which the liability is incurred if it is reasonably estimable or known. Until such time that a project life is established, the Company records the corresponding cost as an exploration stage expense and has accrued $48 for estimated obligations as of both June 30, 2026 and June 30, 2025.

Future reclamation and environmental-related expenditures are difficult to estimate in many circumstances due to the early-stage nature of the Elk Creek Project, the uncertainties associated with defining the nature and extent of environmental disturbance, the application of laws and regulations by regulatory authorities and changes in reclamation or remediation technology. The Company periodically reviews accrued liabilities for such reclamation and remediation costs as evidence indicating that the liabilities have potentially changed becomes available. Changes in estimates are reflected in the consolidated statement of operations and comprehensive loss in the period an estimate is revised.

n)
Income Taxes

Income taxes are provided based upon the liability method of accounting pursuant to ASC 740-10-25, “Income Taxes – Recognition.” Under the approach, deferred income taxes are recorded to reflect the tax consequences in future years of differences between the tax basis of assets and liabilities and their financial reporting amounts at each year-end. A valuation allowance is recorded against deferred tax assets if management does not believe the Company has met the “more likely than not” standard imposed by ASC 740-10-25-5 to allow recognition of such an asset. ASC 740-10-50, “Income Taxes – Disclosure,” requires the Company to evaluate its income tax positions and recognize a liability for uncertain tax positions that are not more likely than not to be sustained by tax authorities. As of June 30, 2026 and 2025, the Company believes it had no income tax uncertainties that required recognition of a liability. If the Company were to determine that uncertain tax positions meet the criteria for recognition, an estimated liability and related interest and penalties would be recognized as income tax expense.

o)
Redeemable Noncontrolling Interest

Redeemable Noncontrolling Interest refers to non-controlling interest associated with the Vested Shares that are redeemable upon the occurrence of an event that is not solely within the Company’s control and is reported in the mezzanine section between total liabilities and shareholders’ equity, as temporary equity in the Company’s consolidated balance sheets. The Company’s non-controlling interest is redeemable at fair value, and no adjustment to the earnings per share numerator is required because redemption at fair value is not considered an economic distribution different from other common stockholders.

p)
Basic and Diluted Per Share Disclosure

Basic earnings (loss) per share represents net earnings (loss) attributable to common shareholders divided by the weighted average number of Common Shares outstanding during the period. The Company considers Vested

63


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

Shares and Released Earnout Shares (each as defined in Note 8), to be participating securities, requiring the use of the two-class method. Diluted earnings (loss) per share represents net earnings (loss) attributable to common shareholders divided by the weighted average number of Common Shares outstanding, inclusive of the dilutive impact of all potentially dilutive securities outstanding during the period, as applicable.

The Company utilizes the weighted average method to determine the impact of changes in a participating security on the calculation of loss per share. The following table sets forth the computation of the Company’s basic and diluted net loss per share attributable to common shareholders:

 

 

For the year ended June 30,

 

 

2026

 

 

2025

 

Net loss

 

$

(50,781

)

 

$

(17,982

)

Adjust: Net loss attributable to noncontrolling interest

 

 

(2,226

)

 

 

(577

)

Net loss available to participating securities

 

 

(48,555

)

 

 

(17,405

)

Net loss attributable to Vested Shares

 

 

(875

)

 

 

(1,102

)

Net loss attributed to common shareholders - basic and diluted

 

$

(47,680

)

 

$

(16,303

)

Denominator:

 

 

 

 

 

 

Weighted average shares outstanding – basic and diluted

 

 

117,214,449

 

 

 

45,072,895

 

Loss per Common Share outstanding – basic and diluted

 

$

(0.41

)

 

$

(0.36

)

 

The following shares underlying options to purchase Common Shares (“Options”) and Warrants were antidilutive due to a net loss in the periods presented and, therefore, were excluded from the dilutive securities computation for the periods indicated below:

 

 

For the year ended June 30,

 

Excluded potentially dilutive securities (1)(2):

 

2026

 

 

2025

 

Options

 

 

4,147,500

 

 

 

3,020,000

 

Warrants

 

 

20,561,006

 

 

 

31,839,152

 

Total potentially dilutive securities

 

 

24,708,506

 

 

 

34,859,152

 

 

(1)
The number of shares is based on the maximum number of shares issuable on exercise or conversion of the related securities as of the period end. Such amounts have not been adjusted for the treasury stock method or weighted average outstanding calculations as required if the securities were dilutive.
(2)
Earnout Shares (as defined below) are excluded as the vesting terms were not met as of the end of the reporting period.
q)
Share Based Compensation

The Company grants Options to directors, officers, employees, and business advisors. Option terms and vesting conditions are at the discretion of the Board. The Option exercise price is equal to the closing market price on the Nasdaq Stock Market LLC (“Nasdaq”) on the day preceding the date of the grant.

The Company estimates the fair value of Options using the Black-Scholes option pricing model. The Company recognizes forfeitures as they occur.

 

r)
Retirement Plan

The Company sponsors a 401(k) savings plan covering substantially all eligible employees. Beginning January 1, 2026, the Company began matching participant contributions equal to 100% of the participant's contributions up to 4% of eligible compensation, with such matching contributions vesting immediately. The Company recognized $35 of expense for matching contributions for the year ended June 30, 2026. There is no comparable

64


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

amount for the prior year, as the Company's matching contribution program was not in effect prior to January 1, 2026.

s)
Recent Accounting Standards

Recently Adopted Accounting Standards

In December 2025, the Financial Accounting Standards Board ("FASB") issued Accounting Standards Update ("ASU") No. 2025-10, Government Grants (Topic 832): Accounting for Government Grants Received by Business Entities. The guidance establishes authoritative accounting and disclosure requirements for government grants received by business entities, permits early adoption, and is effective for annual reporting periods beginning after December 15, 2028, with application on a prospective basis. The Company early adopted ASU 2025-10 effective July 1, 2025. Upon adoption, the Company concluded that the DoW Agreement (as defined in Note 11 below) represents a government grant within the scope of Topic 832. Adoption of the guidance did not have a material impact on the Company’s consolidated financial statements, as the Company’s existing accounting policies for accounting for such grants are consistent with the guidance.

In December 2023, the FASB issued ASU 2023-09, Improvements to Income Tax Disclosures (Topic 740), which establishes new income tax disclosure requirements in addition to modifying and eliminating certain existing ones. The new guidance requires consistent categorization and greater disaggregation of information in the income tax rate reconciliation, as well as further disaggregation of income taxes paid. We adopted ASU 2023-09 for the year ended June 30, 2026, and applied the guidance retrospectively for all periods presented in the notes to the consolidated financial statements. The adoption did not have a material impact on our consolidated financial statements for the year ended June 30, 2026, but did require additional disclosures.

Issued and Not Effective

In November 2024, the FASB issued ASU 2024-03, Income Statement - Reporting Comprehensive Income -Expense Disaggregation Disclosures (Subtopic 220-40): Disaggregation of Income Statement Expenses. ASU 2024-03 requires the disclosure of additional information related to certain costs and expenses, including amounts of inventory purchases, employee compensation, and depreciation and amortization included in each income statement line item. This ASU also requires disclosure of the total amount of selling expenses and our definition of selling expenses. This ASU is effective for our annual report for the period ending June 30, 2028, and for interim period reports beginning thereafter on a prospective or retrospective basis. Early adoption is permitted. We are currently evaluating the impact of adopting this ASU on our consolidated financial statements and disclosures.

From time to time, new accounting pronouncements are issued by the FASB that are adopted by the Company as of the specified effective date. Unless otherwise discussed, recently issued accounting pronouncements are not expected to have a material impact on the Company's consolidated financial statements.

4.
ACQUISITION

On December 4, 2025, the Company completed the acquisition of certain manufacturing assets and intellectual property of FEA Materials LLC, a producer of scandium-containing aluminum master alloys. The Company did not acquire any equity or other legal interest in FEA Materials LLC in connection with the transaction. The transaction was accounted for as a business combination under ASC 805 as the acquired assets and processes constituted a business. The acquisition was made to obtain proprietary technology and manufacturing capabilities to support the Company’s scandium alloy commercialization strategy, and control was obtained through the purchase of the acquired assets.

 

The following table summarizes the fair values of the assets acquired at the acquisition date:

 

 

Fair Value

 

Accounts receivable and prepaids

 

$

7

 

Inventory

 

 

88

 

Fixed assets

 

 

63

 

Security deposit

 

 

5

 

Intangible asset – technology

 

 

6,017

 

65


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

Goodwill

 

 

2,220

 

Assets acquired

 

$

8,400

 

The excess of the purchase consideration over the fair value of net assets acquired, totaling $2,220, was recorded as goodwill. The goodwill primarily reflects expected future growth opportunities and anticipated synergies resulting from the integration of the acquired technology and production capabilities into the Company’s scandium alloy commercialization strategy. The goodwill is expected to be deductible for income tax purposes. The purchase price allocation is based on management’s estimates as of the acquisition date, and management has completed its evaluation of the fair values of the assets acquired.

The Company recognized identifiable intangible assets related to acquired technology, consisting of a group of patented and proprietary intellectual property. The intangible assets were valued using an income approach, specifically the multi-period excess earnings method, which incorporates significant unobservable inputs (Level 3), including management’s estimates of future cash flows, discount rates, and assumptions related to obsolescence. The acquired intangible assets are being amortized on a straight-line basis over their estimated weighted-average remaining useful life of 10 years. The Company has recognized $345 of amortization expense through June 30, 2026, and expects to recognize amortization expense of approximately $602 annually for each of fiscal years 2027 through 2031, with the remaining $2,662 recognized thereafter.

The Company incurred $131 of transaction costs related to the acquisition, which were expensed as incurred and recognized in other operating expenses. Pro forma financial information has not been presented as the acquisition was not deemed significant under Securities and Exchange Commission Regulation S-X.

5.
PROPERTY AND EQUIPMENT, NET

 

 

As of June 30,

 

 

2026

 

 

2025

 

Construction in progress

 

$

5,651

 

 

$

—

 

Fixed assets and vehicles

 

 

204

 

 

 

46

 

Total depreciable assets

 

 

5,855

 

 

 

46

 

Accumulated depreciation

 

 

(24

)

 

 

(14

)

Net depreciable assets

 

 

5,831

 

 

 

32

 

Land

 

 

5,738

 

 

 

807

 

Property and equipment, net

 

$

11,569

 

 

$

839

 

Property Acquisitions

In connection with the development of the Elk Creek Project, ECRC, an indirect majority-owned subsidiary of the Company, acquired additional land and associated mineral rights in Johnson County, Nebraska, as described below.

August Property Purchases

On August 1, 2025, ECRC closed its options to purchase three parcels of land consisting of (i) an 80-acre parcel of surface rights and (ii) two smaller parcels totaling approximately 1.66 acres that included both surface rights and associated mineral rights. The total purchase price was approximately $2,699, including $35 of indirect costs. Of this amount, $2,650 was allocated to land and $49 was allocated to mineral properties.

September Property Purchases

On September 30, 2025, ECRC closed on its options to purchase two additional parcels of land consisting of (i) a 105.77-acre parcel and (ii) a 220-acre parcel, each including both surface rights and associated mineral rights (the "September Property Purchases"). The total purchase price was approximately $11,325, including $29 of indirect costs. Of this amount, $2,263 was allocated to land and $9,062 was allocated to mineral properties.

66


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

November Property Purchase

On November 7, 2025, ECRC acquired a 40-acre parcel of land and associated mineral rights located within the one-square-mile section that comprises the Elk Creek Project area. The acquisition was completed through (i) the transfer of surface rights to a separate 40-acre tract previously acquired as part of the September Property Purchases, (ii) cash consideration of $500 for the mineral rights, and (iii) the grant of a 2% net smelter return ("NSR") royalty on the acquired parcel. The surface-rights exchange involved parcels of substantially identical value, resulting in no gain or loss recognized. The total purchase price was $551, including $51 of indirect costs, with $531 allocated to mineral properties and $20 allocated to land.

Construction in Progress

Construction in progress consists of costs incurred for the development of the mine portal and related infrastructure at the Elk Creek Project.

6.
MINERAL PROPERTIES

Mineral properties consist of original acquisition costs and purchased mineral rights related to the Elk Creek Project, as discussed in Note 5. The Company currently owns approximately 550 acres of land and associated mineral rights, an additional 80 acres of mineral rights, and an additional 80 acres of surface rights. The mineral rights include a 2% NSR royalty.

In addition to the land and mineral rights currently owned by the Company, the property interests of Elk Creek include six mineral exploration option-to-purchase agreements which include a pre-determined buyout for permanent ownership of the mineral and/or surface rights. Terms of the agreements require no further significant payments, and the Company may terminate the leases, negotiate lease extensions, or elect to purchase the mineral and/or surface rights any time. Agreements that allow for the purchase of mineral rights contain provisions whereby the landowners would retain a 2% NSR royalty.

During the year ended June 30, 2025, the Company completed negotiations with landowners in Nebraska and entered into contract amendments which extended the option periods by approximately five years for option to purchase agreements (“OTP”) covering six parcels of land for project construction and operation which the Company does not already own. The Company recorded an exploration expense in the year ended June 30, 2025, for $310 for OTP extension payments made.

7.
ACCOUNTS PAYABLE AND ACCRUED LIABILITIES

 

 

As of June 30,

 

2026

 

2025

Accounts payable, trade

 

$997

 

$692

Trade payable accruals

 

2,557

 

1,055

Employee salary, benefit, and bonus accruals

 

2,036

 

—

Environmental accruals

 

48

 

48

Total accounts payable and accrued liabilities

 

$5,638

 

$1,795

 

8.
CLASS B COMMON STOCK OF ECRC

Holders of the Class B common stock of ECRC have the right to exchange such shares for Common Shares on a one-for-one basis, subject to certain equitable adjustments, under certain conditions. Of the issued and outstanding shares of Class B common stock of ECRC, 4,565,808 shares (the “Vested Shares”) were vested as of the Closing Date and are exchangeable at any time, and from time to time, until the tenth anniversary of the Closing Date (the “Ten-Year Anniversary”) and 3,391,596 shares (the “Earnout Shares”) are exchangeable until the Ten-Year Anniversary, subject to certain vesting conditions. Under certain circumstances, and subject to certain exceptions, NioCorp may instead settle all or a portion of any exchange pursuant to the terms of the Exchange Agreement, dated as of March 17, 2023, by and among NioCorp, ECRC, and GX Sponsor II LLC (the “Sponsor”) in cash, in lieu of Common Shares, based on a volume-weighted average price of Common Shares.

During the years ended June 30, 2026 and 2025, 417,891 and 348,085 Vested Shares, respectively, were exchanged for an equivalent number of Common Shares, and as of June 30, 2026, 3,516,140 Vested Shares remain outstanding. These

67


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

exchanges resulted in a change in the Company’s ownership interest in ECRC and were accounted for as an equity transaction in accordance with ASC 810-10-45-23, with no gain or loss recognized. Accordingly, the carrying amount of the noncontrolling interest was adjusted to reflect the change in the Company’s ownership interest with a corresponding offset to equity.

Both Vested Shares and Released Earnout Shares (as defined below) may be exchanged by the holders into Common Shares at any time. All Vested Shares and Earnout Shares must be exchanged for Common Shares by the Ten-Year Anniversary except for Released Earnout Shares that have been vested for a period of fewer than twenty-four months as of the Ten-Year Anniversary. Such Released Earnout Shares will be forfeited if not exchanged for Common Shares by the date that is twenty-four months after the vesting date.

Vested Shares

As the exchange of Vested Shares are contingently redeemable at the option of the noncontrolling interest shareholders, the Company classifies the carrying amount of the redeemable noncontrolling interest in the mezzanine section on the consolidated balance sheet, which is presented above the equity section and below liabilities. Adjustments to the carrying value of the redeemable noncontrolling interest associated with redemptions are recorded by reclassifying the proportionate amount of mezzanine equity to permanent equity.

Earnout Shares

The Earnout Shares vest (the “Released Earnout Shares”) in two equal tranches based upon achieving market share price milestones of approximately $12.00 per Common Share and approximately $15.00 per Common Share, respectively, prior to the Ten-Year Anniversary, or upon a change in control as defined in the underlying agreement. These shares will be forfeited if the market share price milestones or an acceleration event is not reached prior to the Ten-Year Anniversary. At such time that the Earnout Shares shall become vested, and therefore, become Released Earnout Shares, the shares will be transferred to the redeemable noncontrolling interest in the mezzanine section of the Consolidated Balance Sheet.

The Earnout Shares were classified as a liability due to failure to meet the equity classification criteria under ASC 815-40, as Level 3 instruments under the fair value hierarchy and are considered a financial liability under ASC 480, Distinguishing Liabilities from Equity. The Earnout Shares were measured at fair value on the Closing Date with subsequent changes in fair value recorded in earnings. The Earnout Shares were valued utilizing a Monte Carlo simulation pricing model with an expiry date of March 17, 2033. The following table discloses the primary inputs into the Monte Carlo models:

 

Key Valuation Input

 

June 30,
2026

 

June 30,
2025

 

June 30,
2024

Closing Common Share price

 

$4.82

 

$2.33

 

$1.73

Term (expiry)

 

March 17, 2033

 

March 17, 2033

 

March 17, 2033

Implied volatility of the 2023 Public Warrants

 

84.0%

 

75.0%

 

65.0%

Risk-free rate

 

4.28%

 

4.04%

 

4.35%

 

 

 

 

 

 

The following table sets forth a summary of the changes in the fair value of the Earnout Shares liability for the year ended June 30, 2026:

 

68


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

 

Amount

 

Fair value as of June 30, 2024

 

$

3,817

 

Change in fair value

 

 

2,063

 

Fair value as of June 30, 2025

 

 

5,880

 

Change in fair value

 

 

8,571

 

Fair value as of June 30, 2026

 

$

14,451

 

 

9.
COMMON SHARES
a)
Issuances

Fiscal Year 2026 Issuances

On July 18, 2025, the Company issued and sold 13,850,000 Common Shares, at an offering price of $3.25 per Common Share, in a registered offering (the “July 2025 Offering”) under the Company’s registration statement on Form S-3 (Registration No. 333-280176), pursuant to the Placement Agency Agreement between the Company and Maxim Group LLC (“Maxim”), dated July 17, 2025. The Company received net proceeds from the July 2025 Offering, after deducting placement agent fees and other offering expenses payable by the Company, of approximately $41,335.

On September 19, 2025, the Company issued and sold 10,000,000 Common Shares, at an offering price of $5.00 per Common Share, in a registered direct offering (the “September 2025 Registered Direct Offering”) under the Company’s registration statement on Form S-3 (Registration No. 333-280176), pursuant to the Placement Agency Agreement between the Company and Maxim, dated September 17, 2025. The Company received net proceeds from the September 2025 Registered Direct Offering, after deducting placement agent fees and other offering expenses payable by the Company, of approximately $46,048.

On September 29, 2025, the Company issued and sold (a) 7,004,740 Common Shares at a public offering price of $6.15 per Common Share and (b) 2,755,260 pre-funded Warrants to purchase an aggregate of 2,755,260 Common Shares (the “September Pre-Funded Warrants”) at a public offering price of $6.1499 per September Pre-Funded Warrant in a confidentially marketed public offering (the “September 2025 Public Offering”) under the Company’s registration statement on Form S-3 (Registration No. 333-280176), pursuant to the Placement Agency Agreement between the Company and Maxim, dated September 26, 2025. On September 30, 2025, the Company issued 2,755,218 Common Shares in connection with the cashless exercise of all of the outstanding September Pre-Funded Warrants. The Company received net proceeds from the September 2025 Public Offering, after deducting placement agent fees and other offering expenses payable by the Company, of approximately $55,365.

On October 15, 2025, the Company issued and sold (a) 10,152,175 Common Shares at an offering price of $9.34 per Common Share and (b) 5,925,000 pre-funded Warrants (the “October Pre-Funded Warrants”) to purchase up to an additional 5,925,000 Common Shares at an offering price of $9.3399 per October Pre-Funded Warrant in a registered offering (the “October 2025 Offering”) under the Company's registration statement on Form S-3 (Registration No. 333-290837), pursuant to the Placement Agency Agreement between the Company and Maxim, dated October 13, 2025. On October 17, 2025, the Company issued 5,924,942 Common Shares in connection with the cashless exercise of all of the outstanding October Pre-Funded Warrants. The Company received net proceeds from the October 2025 Offering, after deducting placement agent fees and other offering expenses payable by the Company, of approximately $138,974.

On February 25, 2026, the Company issued and sold (a) 17,400,000 Common Shares at an offering price of $5.00 per Common Share and (b) 2,600,000 pre-funded Warrants (the “February Pre-Funded Warrants”) to purchase up to an additional 2,600,000 Common Shares at an offering price of $4.9999 per February Pre-Funded Warrant in a registered offering (the “February 2026 Offering”) under the Company's registration statement on Form S-3 (Registration No. 333-290837), pursuant to the Placement Agency Agreement between the Company and Maxim, dated February 24, 2026. On February 25, 2026 and March 4, 2026, the Company issued a total of 2,599,951 Common Shares in connection with the cashless exercise of all of the outstanding February Pre-Funded Warrants. The Company received net proceeds from the February 2026 Offering, after deducting placement agent fees and other offering expenses payable by the Company, of approximately $93,406.

Fiscal Year 2025 Issuances

69


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

On November 5, 2024, the Company closed an underwritten public offering (the “November 2024 Registered Offering”), pursuant to the underwriting agreement, dated November 3, 2024 (the “November 2024 Underwriting Agreement”), with Maxim, as underwriter, which consisted of 1,592,356 Common Shares, 1,672,090 Warrants (the “Series A Public Warrants”) to purchase up to an additional 1,672,090 Common Shares and 836,045 Warrants (the “Series B Public Warrants” and, together with the Series A Public Warrants, the “November 2024 Public Warrants”) to purchase up to an additional 836,045 Common Shares. Each Common Share was sold together with one Series A Public Warrant and one-half of one Series B Public Warrant at a combined public offering price of $1.57. The gross proceeds from the November 2024 Registered Offering were $2,501 before deducting underwriting discounts and offering expenses. The November 2024 Public Warrants were classified as equity instruments and accordingly, the net proceeds were allocated based on the relative fair values of the Common Shares and the November 2024 Public Warrants on the date of issuance, with $943 allocated to the fair value of the November 2024 Public Warrants and the balance of the proceeds of $1,558 allocated to Common Shares. The Company incurred total transaction costs related to the November 2024 Registered Offering of $1,226, which were treated as share issuance costs at closing. The Series A Public Warrants have an exercise price of $1.75 per underlying Common Share, are exercisable immediately, and will expire on November 5, 2026. The Series B Public Warrants have an exercise price of $2.07 per underlying Common Share, are exercisable beginning six months and one day from the date of issuance and will expire on November 5, 2029. In addition, pursuant to the November 2024 Underwriting Agreement, the Company granted Maxim a 45-day over-allotment option to purchase (i) 238,853 additional Common Shares and (ii) 358,280 Option Warrants (as defined below) to purchase up to an aggregate of 358,280 Common Shares. “Option Warrant” means one Series A Public Warrant combined with one-half of one Series B Public Warrant. On November 4, 2024, Maxim partially exercised its over-allotment option to purchase 79,734 additional Series A Public Warrants and 39,867 additional Series B Public Warrants, which amounts are included in the amounts discussed above and were issued at closing of the November 2024 Registered Offering.

The following table discloses the primary inputs for the Black-Scholes model used in valuing the November 2024 Public Warrants:

 

 

 

November 5, 2024

 

November 2024 Public Warrants:

 

Series A Public Warrants

 

 

Series B Public Warrants

 

Closing Common Share price

 

$

1.455

 

 

$

1.455

 

Term (years)

 

 

4.5

 

 

 

2.0

 

Historic equity volatility

 

 

67.43

%

 

 

67.13

%

Risk-free rate

 

 

4.14

%

 

 

4.20

%

 

On November 13, 2024, the Company closed a non-brokered private placement (the “November 2024 Private Offering”), pursuant to binding subscription agreements with certain accredited investors as part of a non-brokered private placement of 2,199,602 units of the Company (the “November 2024 Units”). Each November 2024 Unit consisted of one Common Share, one Warrant (a “Series A Private Warrant”) to purchase one Common Share, and one-half of one Warrant (each whole such Warrant, a “Series B Private Warrant” and, together with the Series A Private Warrants, the “November 2024 Private Warrants”), with each Series B Private Warrant entitling the holder thereof to purchase one additional Common Share. Each November 2024 Unit was issued and sold at a price of $1.57. The gross proceeds of the November 2024 Private Offering were approximately $3,500 before deducting offering expenses. Certain directors and officers of the Company (the “Insider Investors”) purchased November 2024 Units at a price of $1.7675 per November 2024 Unit, which price includes $0.1975 per November 2024 Private Warrant and allowed such directors and officers to participate in the November 2024 Private Offering in accordance with the rules of the Nasdaq. The Series A Private Warrants have an exercise price of $1.75 per underlying Common Share, are exercisable immediately, and will expire on November 13, 2026. The Series B Private Warrants have an exercise price of $2.07 per underlying Common Share, are exercisable beginning six months and one day from the date of issuance and will expire on November 13, 2029. The Company recorded a non-cash expense of $34 and $110 to other operating expenses and employee related costs, respectively, representing the excess of fair value of the November 2024 Units over the purchase price paid by Insider Investors.

Based upon the Company’s analysis of the criteria contained in ASC 815, the Company determined that the November 2024 Private Warrants met the definition of a derivative liability, as any Warrant exercise that could

70


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

cause the holder to exceed 19.9% ownership of NioCorp Common Shares would require shareholder approval. As such, the November 2024 Private Warrants were recognized as warrant liabilities on the consolidated balance sheet and were measured at their issuance date fair value of $1,928 and subsequently remeasured at each reporting period with changes being recorded as a non-operating gain or loss in the consolidated statement of operations and comprehensive loss. The remaining proceeds of the November 2024 Private Offering of $1,573 were allocated to Common Shares. The Company incurred total transaction costs related to the November 2024 Private Offering of $161, of which $60 was allocated to the November 2024 Private Warrants and was expensed at closing.

The following tables disclose the primary inputs for the Black-Scholes model used in valuing the November 2024 Private Warrants:

 

 

 

November 13, 2024

 

November 2024 Private Warrants:

 

Series A Private Warrants

 

 

Series B Private Warrants

 

Closing Common Share price

 

$

1.49

 

 

$

1.49

 

Term (years)

 

 

2.0

 

 

 

4.5

 

Historic equity volatility

 

 

67.26

%

 

 

67.52

%

Risk-free rate

 

 

4.20

%

 

 

4.30

%

 

 

 

June 30, 2026

 

November 2024 Private Warrants:

 

Series A Private Warrants

 

 

Series B Private Warrants

 

Closing Common Share price

 

$

4.82

 

 

$

4.82

 

Term (years)

 

 

0.37

 

 

 

3.38

 

Historic equity volatility

 

 

65.66

%

 

 

81.83

%

Risk-free rate

 

 

3.89

%

 

 

4.20

%

 

The following table sets forth a summary of the changes in the fair value of the November 2024 Private Warrants liabilities.

 

 

 

November 2024 Private Warrants

 

Fair value at issuance (November 13, 2024)

 

$

1,929

 

Fair value of Warrants exercised

 

 

(338

)

Change in fair value

 

 

2,240

 

Fair value as of June 30, 2025

 

 

3,831

 

Fair value of Warrants exercised

 

 

(4,833

)

Change in fair value

 

 

8,353

 

Fair value as of June 30, 2026

 

$

7,351

 

 

On January 31, 2025, the Company closed an underwritten registered direct offering (the “January 2025 Offering”), pursuant to an underwriting agreement, dated January 29, 2025, with Maxim, as underwriter, pursuant to which the Company issued and sold 2,577,320 Common Shares, 2,577,320 Series A Warrants to purchase up to 2,577,320 Common Shares (the “January 2025 Series A Warrants”) and 1,288,660 Series B Warrants to purchase up to an additional 1,288,660 Common Shares (the “January 2025 Series B Warrants” and, together with the January 2025 Series A Warrants, the “January 2025 Warrants”). Each Common Share was sold together with one January 2025 Series A Warrant and one-half of one January 2025 Series B Warrant at a combined public offering price of $1.94. The gross proceeds from the January 2025 Offering were approximately $5,000 before deducting underwriting discounts and offering expenses. The January 2025 Warrants were classified as equity instruments, and accordingly, the net proceeds were allocated based on the relative fair values of the Common Shares and the January 2025 Warrants on the date of issuance, with $2,200 allocated to the fair value of the January 2025 Warrants and the balance of the proceeds of $2,800 allocated to Common Shares. The Company incurred total transaction costs related to the January 2025 Offering of $799, which were treated as share issuance costs at closing. The January

71


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

2025 Series A Warrants have an exercise price of $1.98 per underlying Common Share, are exercisable immediately, and will expire on August 2, 2027. The January 2025 Series B Warrants have an exercise price of $2.05 per underlying Common Share, are exercisable immediately, and will expire on January 31, 2029.

The following primary inputs were used in the Black-Scholes model for valuing the January 2025 Warrants:

 

 

 

January 2025
Series A Warrants

 

 

January 2025
Series B Warrants

 

Closing Common Share price

 

$

2.25

 

 

$

2.25

 

Term (years)

 

 

2.5

 

 

 

4.0

 

Historic equity volatility

 

 

73.18

%

 

 

73.36

%

Risk-free rate

 

 

4.23

%

 

 

4.31

%

 

On April 21, 2025, the Company closed an underwritten public offering (the “April 2025 Offering”), pursuant to an underwriting agreement, dated April 17, 2025, with Maxim, as underwriter, pursuant to which the Company issued and sold (i) 6,628,846 Common Shares at a public offering price of $2.60 per Common Share and (ii) 1,063,462 pre-funded Warrants (the “April 2025 Pre-Funded Warrants”) to purchase up to an additional 1,063,462 Common Shares at a public offering price of $2.5999. The April 2025 Pre-Funded Warrants have an exercise price of $0.0001 per underlying Common Share, are exercisable immediately, and do not have an expiration date. On April 17, 2025, Maxim partially exercised its over-allotment option to purchase 323,504 additional Common Shares at closing. The gross proceeds from the April 2025 Offering were approximately $20,841 before deducting underwriting discounts and offering expenses. The April 2025 Pre-Funded Warrants were classified as equity instruments and accordingly, the net proceeds were allocated based on the relative fair values of the Common Shares and the April 2025 Pre-Funded Warrants on the date of issuance, with $2,765 allocated to the fair value of the April 2025 Pre-Funded Warrants (based on the value of the underlying Common Shares at closing) and the balance of the proceeds of $18,076 allocated to Common Shares. The Company incurred total transaction costs related to the April 2025 Offering of $2,102, which were treated as share issuance costs at closing.

Yorkville Equity Facility Financing Agreement Issuances

The Company entered into a Standby Equity Purchase Agreement, dated January 26, 2023 (the “Yorkville Equity Facility Financing Agreement”) between the Company and YA II PN, Ltd., an investment fund managed by Yorkville Advisors Global, LP (“Yorkville”) which expired on April 1, 2026. The Company issued the following Common Shares under the Yorkville Equity Facility Financing Agreement during the periods presented below:

 

 

 

For The Year
Ended June 30,

 

 

 

2026

 

 

2025

 

Common Shares issued

 

 

5,727,662

 

 

 

5,671,742

 

Gross funds received

 

$

38,710

 

 

$

12,352

 

Market value of Common Shares issued

 

 

39,434

 

 

 

12,941

 

Loss on issuance(1)

 

$

724

 

 

$

589

 

 

(1)
Loss on issuance represents a non-cash amount equal to the difference between the proceeds received and the fair value of the Common Shares issued based on the Nasdaq closing price per Common Share on the issuance date and is recorded in general and administrative expenditures in the consolidated statement of operations and comprehensive loss.
b)
Stock Options

On April 6, 2026, the Company’s shareholders voted to approve an amendment and restatement of its long-term incentive plan, the NioCorp Developments Ltd. Long Term Incentive Plan (as amended, the “2017 Amended Long-Term Incentive Plan”). Under the 2017 Amended Long-Term Incentive Plan, the Board may, in its discretion from time to time, grant Options and share units (in the form of restricted share units and performance share units), plus dividend equivalents, to non-employee directors, employees and certain other service providers (as described in the 2017 Amended Long-Term Incentive Plan) of the Company and affiliated entities selected by the Board.

72


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

Subject to adjustment as described in the 2017 Amended Long-Term Incentive Plan, and subject to the plan's share counting rules, the aggregate number of Common Shares available for awards under the 2017 Amended Long-Term Incentive Plan may not exceed 11,300,000 Common Shares, minus, as of April 5, 2026, one Common Share for every one Common Share subject to an award granted under the 2017 Amended Long-Term Incentive Plan after February 9, 2026 and before April 6, 2026. The 2017 Amended Long-Term Incentive Plan also limits the maximum annual compensation that may be granted to our non-employee directors for service on the Board to $750 (measured as described in the plan document), subject to exceptions for distributions of previously deferred compensation for services as an executive officer or employee, and non-preferential dividends or dividend equivalents.

The Board has power over the granting, amendment, administration, or settlement of any award.

Option transactions are summarized as follows:

 

 

 

Number of Options

 

Weighted Average Exercise Price

 

Aggregate Intrinsic Value

 

Weighted Average Remaining Contractual Life

Balance, June 30, 2024

 

2,495,500

 

4.78

 

 

 

 

Granted

 

945,000

 

1.41

 

 

 

 

Exercised

 

(512)

 

1.40

 

 

 

 

Cancelled/expired

 

(419,988)

 

9.44

 

 

 

 

Balance, June 30, 2025

 

3,020,000

 

3.09

 

 

 

 

Granted

 

2,282,500

 

4.68

 

 

 

 

Exercised

 

(567,000)

 

3.28

 

 

 

 

Cancelled/expired

 

(588,000)

 

6.77

 

 

 

 

Balance, June 30, 2026

 

4,147,500

 

3.42

 

$6,210

 

3.5 Years

 

As of June 30, 2026, 53.3% of the outstanding Options were fully vested. The total intrinsic value of Options exercised during the year ended June 30, 2026 was $1,654, and as of June 30, 2026, there was $1,540 of unrecognized compensation costs related to unvested share-based compensation arrangements granted. The Company recognized share-based compensation expense of $4,441 and $789 for the years ended June 30, 2026 and 2025, respectively.

 

 

 

 

The following table summarizes the weighted average information and assumptions used to determine Option costs:

 

 

 

For the year ended June 30,

 

 

2026

 

2025

Fair value per option granted during the period

 

$2.84

 

$0.84

Risk-free interest rate

 

3.84%

 

4.44%

Expected dividend yield

 

0%

 

0%

Expected stock price volatility (historical basis)

 

76.8%

 

67.3%

Expected option life in years

 

4.6

 

5.0

 

73


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

c)
Warrants

Warrant transactions are summarized as follows. Weighted average exercise prices related to Canadian dollar denominated Warrants were converted to U.S. dollars using end of period foreign currency exchange rates.

 

 

 

Warrants

 

Weighted Average Exercise Price

Balance, June 30, 2024

 

18,563,561

 

$10.53

Granted

 

13,553,714

 

2.05

Exercised

 

(828,235)

 

1.78

Expired

 

(1,303,118)

 

7.72

Balance, June 30, 2025

 

29,985,922

 

$7.06

Granted

 

11,280,260

 

0.0001

Exercised

 

(22,308,402)

 

0.98

Expired

 

(250,000)

 

4.60

Balance, June 30, 2026

 

18,707,780

 

$9.94

 

At June 30, 2026, the Company has outstanding exercisable Warrants, as follows:

 

Number

 

 

Exercise Price

 

Expiry Date

279,000

 

 

1.75

 

November 5, 2026

1,487,111

 

 

1.75

 

November 13, 2026

15,666,526

(1)

 

11.50

 

March 17, 2028

296,742

 

 

2.31

 

September 17, 2028

217,295

 

 

2.07

 

November 5, 2029

761,106

 

 

2.07

 

November 13, 2029

18,707,780

 

 

 

 

 

 

(1)
Includes 13,447,105 and 2,219,421 2023 Public Warrants and 2023 Private Warrants, respectively, as defined below. Each 2023 Public Warrant and 2023 Private Warrant is exercisable into 1.11829212 Common Shares.

In connection with the Closing, pursuant to the Business Combination Agreement, the Company assumed GXII’s obligations under the agreement (the “GXII Warrant Agreement”) governing the GXII share purchase Warrants (the “GXII Warrants”) and each GXII Warrant thereunder that was issued and outstanding immediately prior to the Closing Date was converted into one Warrant to purchase 1.11829212 Common Shares (the “NioCorp Assumed Warrants”) pursuant to the GXII Warrant Agreement, as amended by an Assignment, Assumption and Amendment Agreement, dated March 17, 2023, among the Company, GXII, Continental Stock Transfer & Trust Company, as the existing warrant agent, and Computershare Inc. and its affiliate, Computershare Trust Company, N.A, together as the successor warrant agent (the “NioCorp Assumed Warrant Agreement”). In connection with the Closing, NioCorp issued (a) 9,999,959 public NioCorp Assumed Warrants (the “2023 Public Warrants”) in respect of the GXII Warrants that were publicly traded prior to the Closing and (b) 5,666,667 NioCorp Assumed Warrants (the “2023 Private Warrants”) to the Sponsor in respect of the GXII Warrants that it held prior to the Closing, which NioCorp Assumed Warrants were subsequently distributed by the Sponsor to its members in connection with the Closing.

Each NioCorp Assumed Warrant entitles the holder to the right to purchase 1.11829212 Common Shares at an exercise price of $11.50 per 1.11829212 Common Shares (subject to adjustments for stock splits, stock dividends, reorganizations, recapitalizations and the like). No fractional shares will be issued upon exercise of any NioCorp Assumed Warrants, and fractional shares that would otherwise be due to the exercising holder will be rounded down to the nearest whole Common Share. In no event will the Company be required to net cash settle any NioCorp Assumed Warrant.

2023 Public Warrants

The Company may elect to redeem the 2023 Public Warrants subject to certain conditions, in whole and not in part, at a price of $0.01 per 2023 Public Warrant if (i) 30 days’ prior written notice of redemption is provided to the

74


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

holders, (ii) the last reported sale price of the Common Shares equals or exceeds approximately $16.10 per share (as adjusted for stock splits, stock dividends, reorganizations, recapitalizations and the like) for any 20 trading days within a 30-trading day period ending on the third business day prior to the date on which the Company sends the notice of redemption to the Warrant holders and (iii) there is an effective registration statement covering the Common Shares issuable upon exercise of the 2023 Public Warrants, and a current prospectus relating thereto, available through the redemption date. Upon issuance of a redemption notice by the Company, the Warrant holders will have until the redemption date to exercise for cash, or, at the Company’s election, on a cashless basis.

2023 Private Warrants

The 2023 Private Warrants: (i) will be exercisable either for cash or on a cashless basis at the holder’s option and (ii) will not be redeemable by the Company, in either case as long as the 2023 Private Warrants are held by the initial purchasers or their permitted transferees. Any 2023 Private Warrants that are held by someone other than the initial purchasers or their permitted transferees are treated as 2023 Public Warrants.

The Company accounts for the 2023 Private Warrants in accordance with the guidance contained in ASC 815-40. Such guidance provides that because the 2023 Private Warrants do not meet the criteria for equity treatment thereunder, the 2023 Private Warrants must be recorded as a liability. This liability is carried as a component of Warrant liabilities on the consolidated balance sheet and is subject to re-measurement at each balance sheet date. With each such re-measurement, the warrant liability will be adjusted to its current fair value, with the change in fair value recognized in the consolidated statement of operations and comprehensive loss. The Company will reassess the classification at each balance sheet date.

As provided for in the NioCorp Assumed Warrant Agreement, through June 30, 2026, a total of 3,447,246 2023 Private Warrants were exchanged for 2023 Public Warrants. The Company recorded a non-cash loss of $1,217 and $26 for the years ending June 30, 2026 and 2025, respectively, in change in fair value of warrant liabilities in the consolidated statement of operations, representing the change in fair value of the 2023 Private Warrants through the respective exercise dates.

The Company classifies the 2023 Private Warrants as Level 2 instruments under the fair value hierarchy and estimated the fair value using a Black Scholes model with the following assumptions:

 

Key Valuation Input

 

June 30, 2026

 

 

June 30, 2025

 

Stock price on valuation date

 

$

4.82

 

 

$

2.33

 

Strike price

 

$

11.50

 

 

$

11.50

 

Implied volatility of the 2023 Public Warrants

 

 

99.0

%

 

 

90.0

%

Risk free rate

 

 

4.14

%

 

 

3.70

%

Dividend yield

 

 

0

%

 

 

0

%

Expected Warrant life in years

 

 

1.7

 

 

 

2.7

 

 

The change in the 2023 Private Warrants liability is presented below:

 

 

 

Amount

 

Valuation at June 30, 2024

 

$

1,353

 

Exchange of 2023 Private Warrants for 2023 Public Warrants

 

 

(482

)

Change in valuation

 

 

1,661

 

Valuation at June 30, 2025

 

$

2,532

 

Exchange of 2023 Private Warrants for 2023 Public Warrants

 

 

(2,501

)

Change in valuation

 

 

3,364

 

Valuation at June 30, 2026

 

$

3,395

 

Contingent Consent Warrants

As consideration for entering into the previously publicly disclosed Waiver and Consent Agreement, dated September 25, 2022 (the “Lind Consent”), between the Company and Lind Global Asset Management III, LLC (“Lind III”), Lind III received, amongst other things, the right to receive additional Warrants (the “Contingent

75


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

Consent Warrants”) if on September 17, 2024, the closing trading price of the Common Shares on the Toronto Stock Exchange or such other stock exchange on which such shares may then be listed, is less than C$10.00, subject to adjustments. The number of Contingent Consent Warrants to be issued, if any, is based on the Canadian dollar equivalent (based on the then current Canadian to U.S. dollar exchange rate as reported by Bloomberg, L.P.) of $5,000 divided by the five-day volume weighted average price of the Common Shares on the date of issuance. Further, the number of Contingent Consent Warrants issued would be proportionately adjusted based on the percentage of Warrants currently held by Lind III that are exercised, if any, prior to the issuance of any Contingent Consent Warrants.

On September 17, 2024, the Company’s Common Share price was below the threshold price set forth in the Lind Consent, and accordingly, the Company issued 2,816,742 Contingent Consent Warrants to Lind III. Each Contingent Consent Warrant is exercisable for one Common Share at an exercise price of $2.308 and may be exercised at any time prior to their expiration on September 17, 2028. The number of Contingent Consent Warrants issued was based on $5,000 divided by the five-day volume weighted average price of the Common Shares on September 16, 2024. The Company valued the Contingent Consent Warrants at $2,262 based on a Black-Scholes valuation with the following inputs:

 

Key Valuation Input

 

September 17,
2024

Closing Common Share price

 

$1.74

Term (years)

 

4.0

Historic equity volatility

 

67.14%

Risk-free rate

 

3.44%

 

The change in the fair value of the Contingent Consent Warrants liability is presented below:

 

 

 

Amount

 

Valuation at June 30, 2024

 

$

2,365

 

Fair value of Warrants issued

 

 

(2,262

)

Gain on issuance of Warrants

 

 

(103

)

Ending balance

 

$

—

 

 

The Company recognized a gain of $103 on the issuance of the Contingent Consent Warrants. This gain was recorded as a part of other non-operating expense (income) in the consolidated statements of operations and comprehensive loss.

 

 

April 2024 Warrants

As previously disclosed, on April 12, 2024, the Company issued and sold to Yorkville and Lind Global Fund II LP (together with Yorkville, the “April 2024 Purchasers”) $8,000 aggregate principal amount of unsecured notes (the “April 2024 Notes”), pursuant to a securities purchase agreement, dated April 11, 2024, between the Company and each of the April 2024 Purchasers. The Company also issued to the April 2024 Purchasers, in proportion to the aggregate principal amount of April 2024 Notes issued to each April 2024 Purchaser, Warrants (the “April 2024 Warrants”) to purchase up to 615,385 Common Shares, which are equal to 25% of the aggregate principal amount of April 2024 Notes issued to the April 2024 Purchasers divided by the exercise price of $3.25, subject to any adjustment to give effect to any stock dividend, stock split or recapitalization. The Company accounted for the April 2024 Warrants in accordance with ASC Topic 815, Derivatives and Hedging, and determined that at issuance, the April 2024 Warrants should be classified as a warrant liability. During the three-month period ended September 30, 2025, all of the outstanding April 2024 Warrants were exercised.

76


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

The change in the April 2024 Warrant liability is presented below:

 

Amount

 

Fair value as of June 30, 2024

 

$

298

 

Change in fair value

 

 

191

 

Fair value as of June 30, 2025

 

 

489

 

Fair value of Warrants exercised

 

 

(1,807

)

Change in fair value

 

 

1,318

 

Fair value as of June 30, 2026

 

$

—

 

 

d)
Shareholder Rights Plan

On November 21, 2025, the Company adopted a limited-duration shareholder rights plan (the "Rights Plan") pursuant to a Shareholder Rights Plan Agreement dated November 21, 2025 (the "Original Rights Plan Agreement"), between the Company and Computershare Investor Services Inc., as rights agent (the "Rights Agent"). One right (a "Right") was issued for each Common Share outstanding as of December 4, 2025, and a Right automatically attaches to each Common Share subsequently issued until the expiration of the Rights Plan. The Rights generally become exercisable only if a person or group acquires, or announces the current intention of commencing a take-over bid to acquire, beneficial ownership of 20% or more of the Company's outstanding Common Shares, other than through a permitted bid made in compliance with applicable Canadian take-over bid rules. If the Rights become exercisable, each holder of a Right, other than the acquiring person, would be entitled to purchase additional Common Shares at a discount to the then-current market price. The Rights Plan was not adopted in response to any specific take-over proposal.

On April 6, 2026, following approval by the Company's shareholders at the Company's annual general meeting, the Company and the Rights Agent entered into an Amended and Restated Shareholder Rights Plan Agreement (the "Amended Rights Plan Agreement"), which amended and restated the Original Rights Plan Agreement in its entirety. Under the Amended Rights Plan Agreement, the Rights Plan expires at 5:00 p.m. (Toronto time) on the date of the Company's annual general meeting of shareholders to be held in 2027, or earlier upon the redemption of the Rights or, provided that a triggering event has not occurred, at such earlier date or time as the Board of Directors may determine in its sole discretion.

Neither the adoption of the Original Rights Plan Agreement nor the subsequent entry into the Amended Rights Plan Agreement had an impact on the Company's consolidated financial statements for the year ended June 30, 2026.

10.
RELATED PARTY TRANSACTIONS AND BALANCES

On September 11, 2024, the Company and Mark Smith, Chief Executive Officer, President, Executive Chairman, and Director of NioCorp, entered into a loan agreement (the “Smith Loan Agreement”), which provided for a $2,000 non-revolving, multi-draw credit facility (the “Smith Loan”). The Smith Loan had an interest rate of 10% per annum, calculated monthly in arrears, through the date of repayment of the Smith Loan. The Company could pre-pay the Smith Loan at any time without notice and without penalty, but any amount of principal or interest repaid by the Company prior to the earlier of the date of expiration of the Smith Loan Agreement, on June 30, 2025, and the occurrence of an event of default under the Smith Loan Agreement was subject to an early payment fee of 2.5% of the value of any such payment. The Smith Loan was secured by all of the Company’s assets pursuant to a general security agreement between the Company and Mr. Smith dated September 11, 2024.

Through October 30, 2024, the Company borrowed a total of $504 under the Smith Loan and subsequently the Company repaid $508, representing the balance of interest and principal outstanding under the Smith Loan, together with $41 related to loan origination fees payable. The Smith Loan expired on June 30, 2025.

77


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

11.
EXPLORATION EXPENDITURES

 

 

For the year ended June 30,

 

2026

 

2025

Feasibility study and engineering

 

$10,354

 

$1,112

Field management and other

 

2,765

 

900

Drilling

 

2,527

 

1,456

Metallurgical

 

1,355

 

214

Geologists and field staff

 

1,038

 

453

Subtotal

 

18,039

 

4,135

Less: reimbursements recognized

 

(1,963)

 

—

Total

 

$16,076

 

$4,135

 

On August 4, 2025, ECRC entered into a Project Sub-Agreement (the “DoW Agreement”) with Advanced Technology International, an entity acting on behalf of the Defense Industrial Base Consortium under the authority of the U.S. Department of War (“DoW”). The DoW Agreement commenced upon full execution and has an initial term through December 30, 2028, with an option to extend the term for an additional five-year period through December 30, 2033. Subject to the terms and conditions of the DoW Agreement, ECRC is entitled to receive up to an aggregate of approximately $10.0 million of reimbursement payments from the DoW upon the achievement of certain project milestones. These milestones include, among other matters, the completion of new drilling operations at the Elk Creek Project to support the conversion of a portion of the current indicated mineral resources into measured mineral resources and the subsequent conversion of a portion of the current probable mineral reserves into proven mineral reserves, the production of samples of scandium metal and aluminum-scandium master alloys, and the completion of a new feasibility study for the Elk Creek Project. Reductions to exploration expenditures for reimbursement under the DoW Agreement will be recognized based on management’s assessment regarding the achievement of milestones set forth in the DoW Agreement. Since inception of the DoW Agreement, the Company recognized a total of $1,963 as a reduction to exploration expenditures. As of June 30, 2026, the Company’s deferred reimbursements balance is $6,177.

12.
LEASES

The Company has one immaterial operating lease for office space. In October 2025 the lease was amended and in May 2026 the Company exercised an option to shorten the lease term to January 31, 2027. These lease remeasurements were made in accordance with ASC 842.

 

The Company incurred lease costs as follows:

 

For the year ended June 30,

 

 

2026

 

 

2025

 

Fixed rent expense

 

$

184

 

 

$

94

 

Variable rent expense

 

 

15

 

 

 

13

 

Short term lease cost

 

 

11

 

 

 

10

 

Sublease income

 

 

(59

)

 

 

(41

)

Net lease cost – other operating expense

 

$

151

 

 

$

76

 

 

The maturity of lease liabilities is as follows at June 30, 2026:

 

 

Fiscal Year Lease Maturities

 

2027

 

$

96

 

Less amount of payments representing interest

 

 

(2

)

Lease liability

 

$

94

 

 

78


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

13.
INCOME TAXES

Domestic and foreign components of loss before income taxes for the years ended June 30, 2026 and 2025 are as follows:

 

 

For the year ended June 30,

 

2026

 

2025

Canada

 

$(29,649)

 

$(13,089)

United States

 

(21,053)

 

(4,818)

United Kingdom

 

(79)

 

(75)

Total

 

$(50,781)

 

$(17,982)

 

The following table is a reconciliation of income taxes at statutory rates:

 

 

For the year ended June 30,

 

 

2026

 

2025

 

$

 

%

 

$

 

%

Income tax benefit at Canadian federal statutory rate

 

$(7,617)

 

15.00%

 

$(2,697)

 

15.00%

Provincial income tax

 

(3,558)

 

7.01%

 

$(1,571)

 

8.74%

Non-taxable/non-deductible items:

 

 

 

 

 

 

 

 

Stock issuance costs in equity

 

(8,119)

 

15.99%

 

$(1,143)

 

6.36%

Warrant liabilities

 

3,519

 

(6.93)%

 

$1,105

 

(6.15)%

Earnout share liability

 

2,314

 

(4.56)%

 

$557

 

(3.10)%

Share based payments

 

822

 

(1.62)%

 

$194

 

(1.08)%

Other

 

208

 

(0.41)%

 

$5

 

(0.03)%

Change in valuation allowance

 

9,249

 

(18.21)%

 

2,804

 

(15.59)%

Other

 

12

 

(0.02)%

 

13

 

(0.07)%

Foreign Tax Effects

 

 

 

 

 

 

 

 

United States:

 

 

 

 

 

 

 

 

Foreign rate differences

 

(2,105)

 

4.15%

 

(482)

 

2.68%

Change in valuation allowance

 

4,908

 

(9.67)%

 

1,159

 

(6.45)%

Other

 

355

 

(0.71)%

 

45

 

(0.25)%

Other foreign jurisdictions

 

12

 

(0.02)%

 

11

 

(0.06)%

Total

 

$—

 

0.00%

 

$—

 

0.00%

The provincial income tax rate reflects the statutory general corporate income tax rate of 12% applicable in the Province of British Columbia. Income tax benefit was $0 in each of the Canadian federal, Canadian provincial, U.S., and U.K. jurisdictions for the years ended June 30, 2026 and 2025. In addition, during the years ended June 30, 2026 and 2025, the Company did not pay any income taxes, net of refunds received, in Canada, the United States, or the United Kingdom.

 

 

Deferred income taxes reflect the net tax effects of temporary differences between the carrying amounts of assets and liabilities for financial reporting purposes and the amounts used for income tax purposes. The significant components of deferred taxes are as follows:

79


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

 

 

As of June 30,

 

2026

 

2025

Deferred tax assets

 

 

 

 

Mineral interests

 

$13,562

 

$10,438

Net operating losses available for future periods

 

20,424

 

16,125

Startup and organizational costs

 

1,697

 

1,842

Research and development costs

 

2,120

 

1,295

Share issuance/financing costs

 

7,420

 

1,357

Canadian restricted interest and financing carryforward

 

605

 

605

Capital losses available for future periods

 

457

 

456

Other

 

50

 

41

Total deferred tax assets

 

46,335

 

32,159

Valuation allowance

 

(46,335)

 

(32,159)

Net deferred tax assets

 

$—

 

$—

 

Changes in the valuation allowance are as follows:

 

 

For the year ended June 30,

 

2026

 

2025

Valuation allowance, beginning of year

 

$(32,159)

 

$(28,181)

Current year additions

 

(14,176)

 

(3,978)

Valuation allowance, end of year

 

$(46,335)

 

$(32,159)

 

The Company establishes a valuation allowance against future income tax assets if, based on available information, it is more likely than not that all of the assets will not be realized. The valuation allowance of $46,335 at June 30, 2026, relates mainly to net operating loss carryforwards in Canada and mineral interests due to deferred exploration expenditures in the United States, where the utilization of such attributes is not more likely than not.

The Company has the following cumulative net operating losses for Canadian and U.S. Federal income tax purposes. Canadian tax loss carryforwards will generally expire between 2028 and 2045. U.S. tax losses incurred through June 30, 2018, totaled $981 and will generally expire between 2031 and 2038. As a result of the Tax Cuts and Jobs Act of 2017, U.S. tax losses incurred for our tax years ending on and after June 30, 2019, totaling $10,027, have no expiration.

 

 

 

As of June 30,

Jurisdiction

 

2026

 

2025

Canada

 

$64,990

 

$53,194

United States

 

11,008

 

6,627

United Kingdom

 

208

 

112

Total

 

$76,206

 

$59,933

 

In addition, the Company has a Canadian capital loss carryforward of $3,388 as of June 30, 2026, which has no expiration date and can be used to offset future capital gains, and U.S. state net operating loss carryforwards of $13,124 as of June 30, 2026 which generally expire between 2031 and 2046.

At June 30, 2026 and 2025, we had no undistributed earnings of foreign subsidiaries that would be subject to income tax upon distribution to Canada from a foreign subsidiary. As such, as of June 30, 2026 and 2025, we did not provide for deferred taxes on any such earnings of our foreign subsidiaries.

The Company had no unrecognized tax benefits as of June 30, 2026 or 2025. The Company has not recognized any interest or penalties in the fiscal years presented in these consolidated financial statements. The Company is subject to income tax in the U.S. federal jurisdiction, the United Kingdom, and Canada. Certain years remain subject to examination by the applicable tax authorities.

80


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

On July 4, 2025, the One Big Beautiful Bill Act (“OBBBA”) was enacted in the U.S., which includes a broad range of tax reform provisions affecting businesses. The OBBBA includes numerous changes to existing tax law including extending or making permanent certain business and international tax measures initially established under the 2017 Tax Cuts and Jobs Act, which were set to expire. The OBBBA contains several changes to corporate taxation including modifications to capitalization of research and development expenses, modifications to deductions for interest expense, and accelerated depreciation on certain asset additions. The OBBBA was enacted during the year ended June 30, 2026. Given the Company's full valuation allowance against its net deferred tax assets, the enactment of the OBBBA did not have a material impact on the Company's income tax provision or effective tax rate for the year ended June 30, 2026.

14.
FAIR VALUE MEASUREMENTS

The Company measures the fair value of financial assets and liabilities in accordance with ASC 820, Fair Value Measurement, which establishes a framework for measuring fair value and a three-tier hierarchy that prioritizes the inputs used in valuation techniques. Level 1 inputs are unadjusted quoted prices in active markets for identical assets or liabilities. Level 2 inputs are observable inputs other than quoted prices included in Level 1, including quoted prices for similar instruments in active markets and quoted prices for identical or similar instruments in markets that are not active. Level 3 inputs are unobservable and reflect the Company's own assumptions about the assumptions market participants would use in pricing the asset or liability.

Cash and cash equivalents, restricted cash, receivables, accounts payable, and accrued liabilities are carried at amortized cost, which management believes approximates fair value due to the short-term nature of these instruments.

The following tables present information about the assets and liabilities measured at fair value on a recurring basis as of June 30, 2026 and 2025.

 

 

As of June 30, 2026

 

 

Total

 

 

Level 1

 

 

Level 2

 

 

Level 3

 

Assets:

 

 

 

 

 

 

 

 

 

 

 

 

Cash and cash equivalents

 

$

415,004

 

 

$

415,004

 

 

$

—

 

 

$

—

 

Restricted cash

 

 

2,102

 

 

 

2,102

 

 

 

—

 

 

 

—

 

Total

 

$

417,106

 

 

$

417,106

 

 

$

—

 

 

$

—

 

Liabilities:

 

 

 

 

 

 

 

 

 

 

 

 

Earnout Shares liability

 

$

14,451

 

 

$

—

 

 

$

—

 

 

$

14,451

 

Warrant liabilities

 

 

10,746

 

 

 

—

 

 

 

10,746

 

 

 

—

 

Total

 

$

25,197

 

 

$

—

 

 

$

10,746

 

 

$

14,451

 

 

 

As of June 30, 2025

 

 

Total

 

 

Level 1

 

 

Level 2

 

 

Level 3

 

Assets:

 

 

 

 

 

 

 

 

 

 

 

 

Cash and cash equivalents

 

$

25,554

 

 

$

25,554

 

 

$

—

 

 

$

—

 

Investment in equity securities

 

 

3

 

 

 

3

 

 

 

—

 

 

 

—

 

Total

 

$

25,557

 

 

$

25,557

 

 

$

—

 

 

$

—

 

Liabilities:

 

 

 

 

 

 

 

 

 

 

 

 

Earnout Shares liability

 

$

5,880

 

 

$

—

 

 

$

—

 

 

$

5,880

 

Warrant liabilities

 

 

6,852

 

 

 

—

 

 

 

6,852

 

 

 

—

 

Total

 

$

12,732

 

 

$

—

 

 

$

6,852

 

 

$

5,880

 

 

15.
SEGMENT INFORMATION

The Company has one reportable segment: the United States. The United States segment conducts exploration, development, and care and maintenance activities at the Elk Creek Project. This segment holds substantially all of the Company’s non-current assets and does not presently report any revenues from operations. Through this segment, the Company seeks to position the Elk Creek Project as a development opportunity in the strategic minerals sector. The Company’s Chief Operating Decision Maker ("CODM") is the Chief Executive Officer.

81


NioCorp Developments Ltd.

Notes to the Consolidated Financial Statements

June 30, 2026

(expressed in thousands of U.S. dollars, except share and per share data or as otherwise stated)

 

Financial information and annual operating plans and forecasts are prepared and reviewed by the CODM at a consolidated level. The CODM assesses performance for the single operating segment and decides how to better allocate resources based on total operating expenses, net loss, changes in cash and cash equivalents, and cash and cash-equivalent balances that are reported on the Consolidated Statement of Operations and Consolidated Statement of Cash Flows. The Company's objective in making resource allocation decisions is to optimize the Company’s ability to develop and operate the Elk Creek Project. In addition, the CODM reviews the segment’s assets based on total assets reported on the consolidated balance sheet, and the accounting policies of our single operating segment are the same as those described in the Summary of Significant Accounting Policies herein. For additional reportable single operating segment level financial information, see the Consolidated Financial Statements.

82


 

ITEM 9. CHANGES IN AND DISAGREEMENTS WITH ACCOUNTANTS ON ACCOUNTING AND FINANCIAL DISCLOSURE.

None.

ITEM 9A. CONTROLS AND PROCEDURES

Evaluation of Disclosure Controls and Procedures

The management of NioCorp Developments Ltd. has evaluated, under the supervision and with the participation of our Chief Executive Officer (“CEO”) and Chief Financial Officer (“CFO”), the effectiveness of our disclosure controls and procedures (as defined in Rules 13a-15(e) and 15d-15(e) under the Exchange Act) as of June 30, 2026. Based on that evaluation, the CEO and the CFO have concluded that, as of June 30, 2026, our disclosure controls and procedures were not effective due to a material weakness in internal control over financial reporting described below.

Notwithstanding the material weakness in our internal control over financial reporting, our CEO and CFO have concluded that the audited consolidated financial statements included in this Annual Report on Form 10-K fairly present, in all material respects, our financial position, results of operations and cash flows for the periods presented in conformity with U.S. GAAP.

The Company’s disclosure controls and procedures have been designed to ensure that: (i) information required to be disclosed by us in reports that we file or submit to the SEC under the Exchange Act is recorded, processed, summarized, and reported within the time periods specified in applicable rules and forms and (ii) material information required to be disclosed in our reports filed under the Exchange Act is accumulated and communicated to management, including the CEO and the CFO, as appropriate, to allow for accurate and timely decisions regarding required disclosures.

Management does not expect that our disclosure controls and procedures will prevent all errors and all fraud. The effectiveness of our or any system of disclosure controls and procedures, however well designed and operated, can provide only reasonable assurance that the objectives of the system will be met and is subject to certain limitations, including the exercise of judgment in designing, implementing, and evaluating controls and procedures and the assumptions used in identifying the likelihood of future events.

Management’s Report on Internal Control over Financial Reporting

The management of NioCorp Developments Ltd. is responsible for establishing and maintaining adequate internal control over financial reporting as defined in Rules 13a-15(f) and 15d-15(f) of the Exchange Act for the Company. Management assessed the effectiveness of our internal control over financial reporting as of June 30, 2026. In making this assessment, our management used the criteria set forth in the Internal Control - Integrated Framework (2013) issued by the Committee of Sponsoring Organizations of the Treadway Commission (the “COSO Framework”). Based on that evaluation, the CEO and the CFO have concluded that, as of June 30, 2026, our internal control over financial reporting was not effective due to the material weakness in internal control over financial reporting described below. For a discussion of the previously reported material weaknesses that management has concluded were remediated during fiscal year 2026, see “Remediation of Previously Reported Material Weaknesses” below.

Remaining Material Weakness

A material weakness is a deficiency, or a combination of deficiencies, in internal control over financial reporting, such that there is a reasonable possibility that a material misstatement of our annual or interim consolidated financial statements will not be prevented or detected on a timely basis.

Management concluded that, of the material weaknesses disclosed in the Company’s Annual Report on Form 10-K for the fiscal year ended June 30, 2025, one material weakness continued to exist as of June 30, 2026. That material weakness relates to a deficiency in the principles associated with the control activities component of internal control, based on the criteria established by the COSO Framework:

•
Control Activities: Management did not maintain effective controls over the design and implementation of process-level control activities related to vendor banking information.

The remaining material weakness described above could result in a misstatement of account balances or disclosures that would result in a material misstatement to the annual or interim consolidated financial statements that would not be prevented or timely detected. The remaining material weakness did not result in any misstatement of the Company’s consolidated financial statements.

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Remediation of Previously Reported Material Weaknesses

During fiscal year 2026, management, with oversight from the Audit Committee, completed and tested a series of remediation actions directed at the material weaknesses previously reported in the control environment, risk assessment, control activities and monitoring activities components of internal control. The actions completed include the following:

•
Control environment - We added two positions to the accounting and financial reporting function, including a VP of Accounting and Senior Accountant. We also engaged outside accounting and internal control consultants with relevant expertise to supplement internal resources.
•
Risk assessment - We designed and implemented a formal financial reporting risk assessment process requiring periodic review and updating of current risks, internal controls and financial reporting risks, including risks arising from changes in the Company’s business practices and from complex or non-routine transactions. The results of the risk assessment are reviewed with management and communicated to the Audit Committee quarterly.
•
Control activities - We designed and implemented controls over the monitoring and assessment of the work of third-party specialists, including a documented evaluation of the specialist’s scope of work, competence and objectivity, the completeness and accuracy of the data provided to the specialist, and the appropriateness of the resulting accounting conclusions, and over the evaluation of inputs and assumptions used to estimate the fair value of instruments and features associated with complex debt and equity transactions, including independent review and approval of key assumptions prior to recording.
•
Monitoring activities - We designed and implemented a monitoring program under which management performs ongoing and separate evaluations to ascertain whether the components of internal control are present and functioning, retains contemporaneous evidence of the performance of key controls, and evaluates and communicates internal control deficiencies, together with an assessment of their severity, in a timely manner to those parties responsible for taking corrective action, including senior management and the Audit Committee.

Management tested the design and operating effectiveness of the remediated controls during the year ended June 30, 2026, using sample sizes commensurate with the frequency of each control. Based on that testing, management determined that the remediated controls were appropriately designed and implemented and operated effectively for a sufficient period of time. Accordingly, management concluded that the material weaknesses in the control environment, risk assessment and monitoring activities components of internal control, and the material weaknesses in the control activities component relating to (i) monitoring and assessing the work of third-party specialists, including the evaluation of the appropriateness of accounting conclusions, and (ii) the evaluation of certain inputs and assumptions used to estimate the fair value of instruments and features associated with complex debt and equity transactions, were remediated as of June 30, 2026.

Remediation Plan

To address the remaining material weakness existing as of June 30, 2026 described above, we are continuing to implement a remediation plan. These actions include the following:

•
We have designed and implemented process-level controls over the initiation, verification, approval and recording of changes to vendor banking information, including independent verification of each change request through a call-back or comparable out-of-band confirmation to a previously validated contact, segregation of duties between the requestor and the approver of changes to vendor data, and periodic management review of a system-generated report of all changes to vendor master data.

The process of designing and maintaining effective internal control over financial reporting is a continuous effort that requires management to anticipate and react to changes in our business, economic and regulatory environments and to expend significant resources. As we continue to evaluate our internal control over financial reporting, we may take additional actions to remediate the material weakness or modify the remediation actions described above.

While we continue to devote significant time and attention to these remediation efforts, the remaining material weakness will not be considered remediated until the controls operate for a sufficient period of time, and management has concluded, through testing, that these controls are effective. Management currently expects to complete these actions during fiscal year 2027.

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Changes in Internal Control over Financial Reporting

Other than the remediation of previously disclosed material weaknesses as discussed above, there has been no change in our internal control over financial reporting during the quarter ended June 30, 2026, that has materially affected, or is reasonably likely to materially affect, our internal control over financial reporting.

ITEM 9B. OTHER INFORMATION

During the quarter ended June 30, 2026, no director or officer (as defined in Rule 16a-1(f) promulgated under the Exchange Act) of the Company adopted or terminated a “Rule 10b5-1 trading arrangement” or “non-Rule 10b5-1 trading arrangement” (as each term is defined in Item 408 of Regulation S-K).

ITEM 9C. DISCLOSURE REGARDING FOREIGN JURISDICTIONS THAT PREVENT INSPECTION

Not applicable.

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PART III

ITEM 10. DIRECTORS, EXECUTIVE OFFICERS AND CORPORATE GOVERNANCE

Directors and Executive Officers

The following table sets forth as of September 25, 2026, the names and ages of, and position or positions held by, our executive officers and directors, the employment background of these persons, and any directorships held by the current directors during the last five years.

 

Name

 

Age

 

Position

 

Date of Appointment

Mark A. Smith

 

67

 

Chief Executive Officer, President, Executive Chairman, and Director

 

Chief Executive Officer and Director:

   September 23, 2013

President and Executive Chairman:

   May 31, 2015

Neal Shah

 

52

 

Chief Financial Officer and Corporate Secretary

 

Chief Financial Officer:

   July 1, 2016

Corporate Secretary:

   December 3, 2021

Scott Honan

 

55

 

Chief Operating Officer

 

May 6, 2014

Jim Sims

 

65

 

Chief Communications Officer

 

November 2, 2015

Ernest Cleave

 

56

 

Senior Vice President of Business Development

 

August 15, 2025

Anthony W. Fulton

 

53

 

Director

 

August 9, 2025

Nilsa Guerrero-Mahon

 

65

 

Director

 

September 28, 2017

Dean C. Kehler

 

69

 

Director

 

March 17, 2023

Michael G. Maselli

 

66

 

Director

 

March 17, 2023

Peter Oliver

 

63

 

Director

 

May 25, 2022

 

The following sets forth a brief description of the business experience of each executive officer and director of the Company, including current directorships and directorships held in, at least, the past five years for each director:

Mark A. Smith – Chief Executive Officer, President, Executive Chairman, and Director

Mr. Smith has over 44 years of experience in operating, developing, and financing mining and strategic materials projects in the Americas and abroad. In September 2013, he was appointed CEO and a Director of NioCorp. From April 2015 to September 2019, Mr. Smith served as the President and Director for Largo Resources Ltd. (“Largo”), a mineral company with an operating property in Brazil and projects in Brazil and Canada. In addition, from April 2015 to October 2018, Mr. Smith also served as the CEO of Largo. Mr. Smith has also served on the board of directors of IBC Advanced Alloys Corp., a leading copper advanced alloys company (“IBC”), since May 2016 and as CEO of IBC since July 2020. From October 2008 through December 2012, Mr. Smith served as President, CEO and Director of Molycorp, where he was instrumentally involved in taking it from a private company to a publicly traded company with a producing mine. From November 2011 through May 2015, he served on the board of directors at Avanti Mining, a mining company (TSX-V: AVT; Avanti Mining changed its name to AlloyCorp in early 2015). From December 2012 through September 2013, he served as the Managing Director of KMSmith LLC, a business strategy and finance advisory firm, where he served as a consultant.

Prior to Molycorp, Mr. Smith held numerous engineering, environmental, and legal positions within Unocal Corporation, a former petroleum explorer and marketer (“Unocal”), and later served as the President and CEO of Chevron Mining Inc., a coal and metal mining company and wholly owned subsidiary of Chevron Corporation (“Chevron Mining”). Mr. Smith also served for over seven years as the shareholder representative of Companhia Brasileira Metalúrgica e Mineração, a private company that currently produces approximately 85% of the world supply of niobium. During his tenure with Chevron Mining, Mr. Smith was responsible for Chevron Mining’s three coal mines, one molybdenum mine, a petroleum coke calcining operation and Molycorp’s Mountain Pass mine. At Unocal, he served as the Vice-President from June 2000 to April 2006, and managed the real estate, remediation, mining and carbon divisions. Mr. Smith is a Registered Professional Engineer and serves as an active member of the State Bars of California and Colorado. He received his Bachelor of Science degree in Agricultural Engineering from Colorado State University in 1981 and his Juris Doctor, cum laude, from Western State University, College of Law, in 1990.

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Neal Shah – Chief Financial Officer and Corporate Secretary

Mr. Shah joined NioCorp in September 2014 as Vice President of Finance, and now serves as the Company’s CFO and Corporate Secretary. Mr. Shah served as Finance Manager at Covidien Ltd., a medical device company since acquired by Medtronic, from May 2014 through September 2014. From April 2011 until May 2014, he held the positions of Senior Manager of Corporate Development and M&A and more recently the Director of Strategy and Business Planning at Molycorp. Mr. Shah graduated from the University of Colorado with a BSc in Mechanical Engineering in 1996, and from Purdue University with an MBA in 2002. Since the completion of his MBA, Mr. Shah also held key finance roles with Intel Corporation and IBM.

Scott Honan – Chief Operating Officer

Mr. Honan joined NioCorp in May 2014 as Vice President, Business Development, and since July 2020, has served as the Company’s Chief Operating Officer (“COO”). He also serves as President of Elk Creek Resources Corporation, the NioCorp subsidiary that is developing the Elk Creek Project in Nebraska. Prior to his work at NioCorp, Mr. Honan served in several leadership capacities at Molycorp from February 2001 until May 2014, including as Vice President/Director Health, Environment, Safety and Sustainability and General Manager and Environmental Manager from July 2011 to May 2014. With over 32 years of experience in the gold and rare earth industries, Mr. Honan is a graduate of Queen’s University in Mining Engineering in both Mineral Processing (B.Sc. Honors) and Environmental Management (M.Sc.) disciplines.

Jim Sims – Chief Communications Officer

Mr. Sims has more than 33 years of experience in devising and executing marketing, media relations, public affairs, and investor relations operations for companies in the mining, chemical, manufacturing, utility, and renewable energy sectors. He joined NioCorp in November 2015 as Vice President, External Affairs, and now serves in a different role for the Company as its Chief Communications Officer, effective June 7, 2022. Prior to NioCorp, Mr. Sims served for more than five years as Director (and then Vice President) of Corporate Communications for Molycorp from March 2010 through November 2015. Since May 2016, Mr. Sims has also served as Director of Investor and Public Relations for IBC. Mr. Sims was President and CEO of Policy Communications, Inc. from 1998 until 2010 and served as White House Director of Communications for the Energy Policy Development Group. A former U.S. Senate Chief of Staff, he is the co-founder and former Executive Director of the Geothermal Energy Association, and he has served as Board Chairman of the Rare Earth Technology Alliance. He is an honors graduate of Georgetown University.

Ernest Cleave – Senior Vice President of Business Development

Mr. Cleave joined NioCorp in August 2025 as Senior Vice President of Business Development. Mr. Cleave has more than 21 years of experience in the mining, mineral processing, and energy industries. Prior to his work at NioCorp, Mr. Cleave served as the President and CEO of Tinova Resources Corp., a critical minerals exploration company, from June 2024 to August 2025. From September 2013 to June 2024, Mr. Cleave served as the Chief Financial Officer of Largo Inc., a supplier of vanadium and ilmenite products. Additionally, Mr. Cleave served as the Interim President of Largo Clean Energy Corp. (a subsidiary of Largo Inc.) from November 2022 to June 2023. Mr. Cleave’s career has also spanned leadership positions in several other mining and energy companies, including as Chief Financial Officer of Cline Mining, Chief Financial Officer of Petrolympic, Global Lead of Sarbanes-Oxley Compliance at Glencore (previously Falconbridge), and Treasurer and Director of Financial Planning and Analysis at Goldcorp. Mr. Cleave is a Chartered Accountant (AUS & NZL) and is a registered CPA in both Canada and Australia. Mr. Cleave earned his M.B.A. from Deakin University of Victoria, Australia and has undergraduate degrees in computational science and commerce, respectively.

Anthony W. Fulton – Director

A former Nebraska State Senator and successful business entrepreneur, Mr. Fulton previously served on the Board from 2013 until 2016, when he left to serve as Nebraska Tax Commissioner and Director of the Nebraska Department of Revenue, a 400-employee, $9 billion enterprise from January 2016 to December 2022. A mechanical engineer by training, Mr. Fulton has been the President of the Nevada-based Hallmark Homecare, LLC, an independent domestic caregiver referral agency since May 2023 and is the Founder and Owner of Guardian Angels Homecare, Inc. of Lincoln, Nebraska, an in-home senior care company, where he has served as the President and CEO since March 2003. In addition to his work in the senior care industry, Mr. Fulton serves as the Chairman of the Diocesan Finance Council for the Catholic Diocese of Lincoln (Southern Nebraska) and is the recipient of numerous awards throughout his professional career. He received his B.S. in Mechanical Engineering from the University of Nebraska-Lincoln, with studies in Philosophy at Newman University in Wichita, Kansas and Theology at Mount Saint Mary’s University in Emmitsburg, Maryland.

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Nilsa Guerrero-Mahon – Director

A former CFO and Controller for global corporations in the technology, energy, and government sectors, Ms. Guerrero-Mahon provides consulting services to domestic and international corporations as the principal at NGM Business Consulting, LLC, a business consulting service, since 2008. In addition, Ms. Guerrero-Mahon was appointed to the board of directors of FinGoal, Inc. in April 2022, a finance technology company building artificial intelligence tools for the financial services industry and other financial technology developers. She also serves as the Chair of the Finance and Audit Committee for the Financial Data Exchange (“FDX”). FDX unifies the financial industry around a common standard for secure and convenient access of permissioned consumer and business financial data. From 2014 to 2019, she served as the Vice Chair of the Board and Chaired the Strategy Committee for the Mountains & North Denver Operating Group, the largest division in the Common Spirit Health System (formerly Centura Health). From 2009 to 2025, Ms. Guerrero-Mahon served as a gubernatorial appointed Board Member of the State of Colorado Securities Commission and the Financial Services Commission. Among other prior positions, from 2004 to 2007, she was the Global Services Controller at Microsoft Corporation, overseeing internal controls, compliance and corporate finance activities.

Ms. Guerrero-Mahon stays current with the latest Corporate Governance practices serving as a member of the Nasdaq Center for Board Excellence. She is an NACD Board Leadership Fellow and a member of the SASB Alliance. She holds a CERT Certificate in Cybersecurity Oversight from Carnegie Mellon University. Ms. Guerrero-Mahon is a Certified Public Accountant and a Certified Fraud Examiner. She received an Executive MBA from the Daniels College of Business at the University of Denver, a BS in Business Administration - Accounting from the Interamerican University in San Juan, Puerto Rico, and an AS in Computer Science from the EDP University of Puerto Rico.

Peter Oliver – Director

With a background in chemistry, Mr. Oliver began working at Greenbushes, Western Australia, for Sons of Gwalia, a mining company, in May 2003. After Sons of Gwalia went into administration in 2004, Mr. Oliver was hired by Talison Lithium Limited (“Talison”), a mining company, where he served as General Manager of Talison’s Greenbushes and Wodgina Mines and as Talison’s COO, until Mr. Oliver was appointed as the CEO/Managing director. As Talison’s CEO/Managing director, Mr. Oliver led the listing of Talison on the Toronto Stock Exchange in September 2010.

Mr. Oliver guided Talison through its acquisition in 2013 by Tianqi Lithium Corporation (“Tianqi”). He then served as a corporate adviser to Tianqi, focusing on M&A opportunities and global expansion, including advising on the sale of 49% of Talison to Albemarle Corp. and the acquisition of 24% of Sociedad Quimica y Minera de Chile S.A., as well as significant expansions of Talison’s Greenbushes lithium concentrate production.

Mr. Oliver also was a founding member of Tianqi Lithium Energy Australia Pty Ltd, a wholly owned subsidiary of Tianqi, which was established to build a major Lithium Hydroxide manufacturing facility in Western Australia. Until June 2021, Mr. Oliver remained as a director of Talison, a joint venture between Tianqi and Albemarle Corp. In September 2022, Mr. Oliver was appointed to the Board of Latin Resources, a lithium exploration company in Australia. Mr. Oliver was appointed to the role of Executive Director of Latin Resources in 2024 and helped lead the successful acquisition of Latin Resources by Pilbara Minerals LTD (ASX: PLS) in March 2025.

Dean C. Kehler – Director

Mr. Kehler co-founded Trimaran Fund Management, L.L.C. ("Trimaran Fund") in 1998, where he is a Managing Partner. Mr. Kehler was also the Co-Chairman and Chief Executive Officer of GX Acquisition Corp. II, a position he held from August 2018 to March 2023. From 1995 to 2000, Mr. Kehler held senior positions at Canadian Imperial Bank of Commerce ("CIBC"), including Vice Chairman of CIBC World Markets Corp. Mr. Kehler currently serves on the Board of Directors of BCP Investment Corporation (formerly Portman Ridge Finance Corporation). Within the last five years, he has served as a director of Celularity Inc. and El Pollo Loco Holdings, Inc. He holds a bachelor's degree from the Wharton School of the University of Pennsylvania.

Michael G. Maselli – Director

Mr. Maselli is a managing director of Trimaran Fund, a position he has held since 2006, and was the President of Acquisitions of GX Acquisition Corp. II from August 2018 to March 2023. Before joining Trimaran Fund in February 2006, Mr. Maselli worked in the Corporate and Leverage Finance Groups of CIBC World Markets. Prior to joining CIBC in 1997, Mr. Maselli served as a Managing Director in Bear Stearns’ corporate finance group and, prior to that, as a Vice President at Kidder Peabody & Co. Incorporated. Mr. Maselli served on the board of directors of El Pollo Loco Holdings from 2010 to 2024, and he served as their Chairman of the Board from 2011 to 2023. He served on the board of ChanceLight, Inc. (f/k/a Educational Services of America, Inc.) until 2018. From 2013 to 2015, he served on the board of directors of Norcraft Companies, Inc., and

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also served on the board of managers of its predecessor company beginning in 2003. Additionally, Mr. Maselli served on the board of directors of Standard Steel, LLC, and was director as well as Chairman of the Board of CB Holding Corp. Mr. Maselli received an MBA with distinction from The A.B. Freeman School at Tulane University and a bachelor’s degree in economics from the University of Colorado.

Other Directorships

The following is a list of directorships held over the past five years by our directors. Except as listed below, no directors of the Company are also directors of reporting issuers.

 

Name of Director

Other Reporting Issuer (or equivalent)

 

Exchange

 Mark A. Smith

IBC Advanced Alloys Corp.

 

TSX-V

Peter Oliver

Latin Resources

 

ASX

Dean C. Kehler

El Pollo Loco Holdings, Inc.

BCP Investment Corporation

Celularity Inc.

GX Acquisition Corp. II

 

Nasdaq

Nasdaq

Nasdaq

Nasdaq

Michael G. Maselli

El Pollo Loco Holdings, Inc.

 

Nasdaq

Legal Proceedings

No director or executive officer of the Company is a party adverse to the Company or any of its subsidiaries or has a material interest adverse to the Company or any of its subsidiaries.

During the past ten years, none of the persons serving as executive officers and/or directors of the Company and, with respect to promoters or control persons, for the past five years, none have been the subject matter of any of the legal proceedings that are required to be disclosed pursuant to Item 401(f) of Regulation S-K. Further, no such legal proceedings are believed to be contemplated by governmental authorities against any director or executive officer.

Ethical Business Conduct

The Board expects management to operate the business of the Company in a manner that enhances shareholder value and is consistent with the highest level of integrity. Management is expected to execute the Company’s business plan and to meet performance goals and objectives according to the highest ethical standards.

In addition, directors and senior officers are bound by the provisions of the Company’s Articles and the British Columbia Business Corporations Act (“BCBCA”), which set forth how any conflicts of interest are to be dealt with. In particular, any director who has a material interest in a particular transaction is required to disclose such interest and to refrain from voting with respect to the approval of any such transaction.

Insider Trading Policy

We have insider trading policies and procedures, as described below, applicable to our directors, officers, and employees, and have implemented processes for the Company, that we believe are reasonably designed to promote compliance with insider trading laws, rules, and regulations, and the Nasdaq listing standards.

The Board has adopted an insider trading policy (the “Insider Trading Policy”) to help ensure, among other things: (i) that persons to whom the policy applies understand their obligations to preserve the confidentiality of “Material Nonpublic Information” (as defined in the Insider Trading Policy); (ii) strict compliance by all insiders with all requirements relating to the reporting of insider trading and with respect to trading when in possession of “Material Nonpublic Information”; and (iii) that individuals subject to scheduled and unscheduled blackout periods adhere to the restrictions on trading as set out in the Insider Trading Policy.

Code of Business Conduct and Ethics

Our Board has adopted a written Code of Business Conduct and Ethics applicable to our employees, officers, and directors, including those officers responsible for financial reporting. The Code of Business Conduct and Ethics is available on our website at www.niocorp.com. If the Board amends the Code of Business Conduct and Ethics or grants a waiver, including an implicit waiver, from the Code of Business Conduct and Ethics, the Company will disclose the information on its internet website. The waiver information will remain on the website for at least 12 months after the initial disclosure of such waiver. Given the current

89


 

size of the Company workforce, and the lack of significant operations, the Board monitors compliance through periodic discussions with executive management.

Audit Committee and Audit Committee Financial Experts

Our Audit Committee is currently comprised of Nilsa Guerrero-Mahon, as Chair, Dean Kehler, and Michael Maselli, all of whom are independent directors. Our Board has determined that each of the three members are audit committee financial experts, as defined by the rules of the SEC. Further, all Audit Committee members are financially literate as defined in NI 52-110. The Audit Committee was established in accordance with Section 3(a)(58)(A) of the Exchange Act.

Delinquent Section 16(a) Reports

Section 16(a) of the Exchange Act requires the Company’s officers and directors, and persons who own more than ten percent of a registered class of the Company’s equity securities, to file reports of ownership and changes in ownership of such securities with the SEC.

Based upon the review of the copies of Section 16(a) forms received by the Company, and upon written representations from reporting persons concerning the necessity of filing a Form 5 Annual Statement of Changes in Beneficial Ownership, the Company believes that, during fiscal 2026, all required reports were filed on a timely basis, other than the filing of a Form 3 and a Form 4 for each of Mr. Fulton and Mr. Cleave, which were filed late because of delays in processing of Form IDs due to new EDGAR Next requirements. The Form 4s each reported a single transaction on August 18, 2025.

 

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ITEM 11. EXECUTIVE COMPENSATION

 

Unless otherwise indicated, all compensation amounts in this Item 11 are presented in whole dollars.

The following table sets out the compensation for the fiscal years ended June 30, 2026 and 2025 for the individual who served as the Company’s CEO during fiscal year 2026, as well as the Company’s two other most highly compensated executive officers other than the CEO who were serving at the end of the last fiscal year (collectively, the “named executive officers” or "NEOs"):

Fiscal 2026 Summary Compensation Table

 

Name and Principal Position

 

Fiscal
Year

 

Salary
($)

 

 

Bonus (1)
($)

 

 

Option
Awards (2)
($)

 

 

All Other Compensation (3) ($)

 

 

Total
($)

 

Mark A. Smith,
Chief Executive Officer, President, Executive Chairman, and Director (4)

 

2026

 

$

355,625

 

 

$

712,784

 

 

$

1,027,500

 

 

$

—

 

 

$

2,095,909

 

 

2025

 

 

325,000

 

 

 

—

 

 

 

126,000

 

 

 

—

 

 

 

451,000

 

Scott Honan,
Chief Operating Officer

 

2026

 

 

297,500

 

 

 

453,197

 

 

 

685,000

 

 

 

6,000

 

 

 

1,441,697

 

 

2025

 

 

280,000

 

 

 

—

 

 

 

84,000

 

 

 

—

 

 

 

364,000

 

Neal Shah,
Chief Financial Officer and Corporate Secretary

 

2026

 

 

271,875

 

 

 

420,621

 

 

 

685,000

 

 

 

5,500

 

 

 

1,382,996

 

 

2025

 

 

250,000

 

 

 

—

 

 

 

84,000

 

 

 

—

 

 

 

334,000

 

 

(1)
The amounts in this column for fiscal 2026 include the payouts to the named executive officers under the 2026 AIP (defined below) and special recognition bonus amounts approved by the Board in August 2025, each as discussed below.
(2)
Reflects the grant date fair value of the Options granted during the reported fiscal years. Fiscal year 2026 grants consisted of 375,000 Options for Mr. Smith and 250,000 Options for each of Messrs. Honan and Shah, in each case at an exercise price of $4.35 per share. Grant date fair values were computed in accordance with Financial Accounting Standards Board Accounting Standards Codification ("FASB ASC") Topic 718. Assumptions used in the calculation of these amounts are described in Note 9b in the Company’s consolidated financial statements included in this Annual Report on Form 10-K. These Options were vested 34% on the grant date (August 18, 2025) and an additional 33% of the Options will vest on each of the first two anniversaries of the grant date. These Options generally remain exercisable until the fifth anniversary of the grant date.
(3)
The fiscal year 2026 row includes the Company’s matching contributions made under the Company’s 401(k) Retirement Savings Plan, which are provided to eligible participants in accordance with the terms of the plan.
(4)
Disclosed amounts were paid to 76 Resources, LLC, an entity controlled by Mr. Smith, as further described below under “Employment Agreements and Severance Arrangements.”

Narrative Disclosure to Summary Compensation Table

Compensation Governance

The Company’s Compensation and Organization Committee of the Board (the “Compensation Committee”) generally determines the amount of compensation for the Company’s executives, which is designed to reflect the need to provide incentives and compensation for the time and effort expended by the executives while taking into account the financial and other resources of the Company. The Compensation Committee has the authority to engage and compensate, at the expense of the Company, any outside advisor that it determines to be necessary to permit it to carry out its duties (including compensation consultants and advisors).

In fiscal 2026, the Compensation Committee engaged Semler Brossy Consulting Group, LLC (“Semler Brossy”) as its independent compensation consultant. Semler Brossy was retained to assist the Compensation Committee in developing an executive compensation peer group and market compensation comparisons and in designing a Company-wide annual incentive program. Semler Brossy reports directly to the Compensation Committee, which has the sole authority to retain, terminate and approve the fees of its compensation consultant. Semler Brossy provided no services to the Company during fiscal 2026 other than those provided at the direction of the Compensation Committee. The Compensation Committee has assessed the independence of Semler Brossy as required under Nasdaq listing rules. Based on this review, the Compensation Committee has determined that Semler Brossy's work has not raised any conflict of interest.

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The Compensation Committee has reviewed the Company’s compensation policies and practices and does not believe that they create any risks that are reasonably likely to have a material adverse effect on the Company.

Compensation Program Design

The Board, in conjunction with the Compensation Committee, determines compensation and rewards to senior management on the basis of individual and corporate performance, both in the short term and the long term, while at the same time being mindful of the responsibility that the Company has to its shareholders. The Compensation Committee believes that the Company’s compensation program should remain straightforward in design, consistent with the Company’s current stage of development, and that it should balance reasonable current compensation against longer-term compensation tied to the performance of the Company as a whole. As described under “Changes for Fiscal 2027” below, the Compensation Committee took a number of steps during fiscal 2026 to formalize the program while preserving that design philosophy.

Fiscal Year 2026 Actions

Historically, the Compensation Committee had not established a formal set of benchmarks or performance criteria to be met by the Company’s named executive officers; rather, the members of the Compensation Committee used their own subjective assessments of the level of success of the Company to determine, collectively, whether or not the named executive officers had successfully achieved the Company’s business plan and strategy and the degree to which they performed in that regard. The Compensation Committee also had not established any pre-determined formula for determining named executive officer compensation, either as to the amount thereof or the specific mix of compensation elements. Instead, compensation (and adjustments from time to time) was set through discussions and subjective assessments at the Compensation Committee level.

Compensation decisions for fiscal 2026 outlined below generally reflect this historical approach; that said, the Compensation Committee took steps in fiscal 2026 to adopt a more formal market analysis and pay determination process. Beginning in fiscal 2027, the Compensation Committee intends to consider its own subjective assessments of Company and individual performance alongside a formal set of market assessments and pre-set performance objectives – see “Changes for Fiscal 2027” below for additional detail.

Salaries

The Compensation Committee sets base salaries (or, for Mr. Smith, base consulting fees) for the Company’s named executive officers generally at a level it deems appropriate to attract and retain capable individuals while taking into account the total compensation provided to each individual. Each year, the Compensation Committee determines if adjustments are appropriate based upon executive performance, role scope, and market context. No changes were made to any executive’s annualized salary for fiscal 2025 compared to fiscal 2024. For fiscal 2026, the Compensation Committee determined to make a number of adjustments in consideration of Company and individual performance, as well as competitive market dynamics:

 

Executive

Fiscal Year 2025 Salary Rate

Fiscal Year 2026 Salary Rate

% Increase

Fiscal Year 2026 Actual Salary

Mark A. Smith

Chief Executive Officer, President, Executive Chairman, and Director

$325,000

$360,000

10.8

$355,625

Scott Honan

Chief Operating Officer

280,000

300,000

7.1

297,500

Neal Shah

Chief Financial Officer and Corporate Secretary

250,000

275,000

10.0

271,875

Amounts shown as salary rates represent annualized base salary rates and not amounts actually earned. The fiscal 2026 increases were effective August 15, 2025, and the amounts actually earned during fiscal 2026 are reported in the Summary Compensation Table. Amounts shown for Mr. Smith represent base consulting fees payable under his consulting arrangement rather than base salary.

Annual Incentive Plan

In fiscal 2026, the Compensation Committee designed and adopted the Company’s annual incentive plan (“AIP”), which is intended to operate as a Company-wide, performance-based, annual cash incentive award program in which substantially all of the Company’s and its subsidiaries’ regular full-time employees participate, including each of the Company’s named executive officers. Annual AIP award opportunities are established generally by employee role considerations, so that annual

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AIP award opportunities are generally based on the scope of an employee’s role on a consistent, Company-wide basis rather than negotiated individually. The Company adopted the AIP to help attract, motivate, and retain employees at all levels and to align the interests of its workforce, including senior management, with the long-term interests of the Company’s shareholders.

In general, under the AIP, each participant has a target annual incentive award opportunity expressed as a percentage of base salary, with award payouts generally ranging from 0% to 200% of target based on performance against pre-established measures. The AIP was adopted during late fiscal 2026 and was applied to fiscal 2026 on a transitional basis. Beginning in fiscal 2027, the AIP operates on a full fiscal-year basis, with performance measures and individual objectives established at or near the beginning of each fiscal year — see “Changes for Fiscal 2027” below for additional detail. For fiscal 2026, performance for all eligible employees was weighted: 45% on the achievement of pre-established, Board-approved corporate milestones tied to project development, financing, and execution readiness; 10% on safety performance, measured by reference to the presence or absence of lost-time incidents and OSHA-reportable incidents; and 45% on individual performance. Because the AIP was adopted during late fiscal 2026, individual performance for fiscal 2026 was assessed on a qualitative basis rather than against pre-established individual objectives. Beginning in fiscal 2027, individual objectives will be established at or near the beginning of each performance period.

The Board evaluates the performance of the Chief Executive Officer, and the Chief Executive Officer evaluates the performance of the other named executive officers. Annual incentive awards under the AIP, if any, are generally payable in cash following the end of the applicable fiscal year, subject to the participant’s continued service through the payment date and the other terms of the AIP.

For fiscal 2026, target award opportunities were applied to each named executive officer’s eligible earnings for the fiscal year rather than to his annualized base salary rate. The Compensation Committee determined that the following amounts were payable under the AIP to the named executive officers:

 

Executive

Eligible Earnings

Target (% of Eligible Earnings)

Target Award

Achievement (% of Target)

Payout

Mark A. Smith

Chief Executive Officer, President, Executive Chairman, and Director

$355,625

100%

$355,625

169.5

$602,784

Scott Honan

Chief Operating Officer

$297,500

75%

$223,125

169.5

$378,197

Neal Shah

Chief Financial Officer and Corporate Secretary

$271,875

75%

$203,906

169.5

$345,621

The Compensation Committee determined the achievement levels above based on the following performance assessment:

Corporate Milestones (45% weighting, 161.1% achievement percentage)

•
Advancement of the drilling program in support of future mineral reserve estimation
•
Substantial progress toward completion of the feasibility study, notwithstanding laboratory processing bottlenecks
•
Advancement of land parcel acquisition for surface and/or mineral rights
•
Capital raises substantially above expectations, positioning the Company advantageously for its broader project financing objectives

Safety Performance (10% of final payout is fully achieved)

•
No lost-time incidents and no OSHA-reportable incidents were recorded in fiscal 2026, measured on a quarterly basis. A strong safety culture was maintained throughout site drilling operations and the transition to construction of the project portal.
•
The Compensation Committee structured the safety measure so that safety performance, when fully achieved, would be set at an amount that would represent approximately 10% of the final total annual incentive award payout. Safety is assessed quarterly, and one-quarter of the component is earned for each quarter in which no lost-time or OSHA-reportable incident occurs. All four quarters qualified in fiscal 2026, and the component was therefore earned in full.

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Individual Performance (45% weighting, 177.8% achievement percentage)

•
Individual objectives were not pre-established for fiscal 2026 because the AIP was adopted during late fiscal year 2026. The Compensation Committee assessed this component qualitatively and determined that the named executive officers performed effectively as a team in delivering the corporate results described above and in establishing recommendations regarding the AIP framework and related compensation governance enhancements. A consistent achievement level was applied across the named executive officers. At the Board’s direction, specific individual objectives will be established for each named executive officer for fiscal 2027 at the beginning of fiscal 2027.

Aggregate Achievement – Applying the weightings above, the corporate milestone and individual performance components contributed 72.5 and 80.0 percentage points, respectively, and the safety component contributed 17.0 percentage points (so that it would represent approximately 10% of the final payout), resulting in an overall achievement of 169.5% for fiscal 2026.

Bonus Compensation

The Compensation Committee has discretion, where deemed appropriate and financially affordable for the Company, to grant a cash bonus to a named executive officer based on the performance of both the individual named executive officer and the Company. In early fiscal 2026, the Board approved special cash bonuses for each of the named executive officers, in the amount of $110,000 for Mr. Smith, $75,000 for Mr. Honan, and $75,000 for Mr. Shah. These bonuses were approved generally in recognition of the named executive officers’ performance.

Long-Term Incentives

The incentive portion of each named executive officer’s compensation package consists primarily of Options awarded under the 2017 Amended Long-Term Incentive Plan. Share ownership opportunities through the grant of Options are provided to align the interests of senior management of the Company with the longer-term interests of the shareholders of the Company.

The Compensation Committee reviews the overall number of Options held by an individual (including the exercise prices and remaining terms of outstanding Options and whether previously granted Options have expired out of the money or were exercised) and takes such information into consideration when reviewing proposed new grants. After considering the Chief Executive Officer’s recommendations, if any, and the foregoing factors, the resulting proposed Option grant is submitted to the Board for final approval.

During the fiscal year ended June 30, 2026, the Board, upon the recommendation of the Compensation Committee, approved the grant of Options proposed by management, and the named executive officers were granted the following number of Options effective August 18, 2025, each with an exercise price of $4.35 per share: Mr. Smith, 375,000 Options; Mr. Honan, 250,000 Options; and Mr. Shah, 250,000 Options. Options vest in three installments: 34% on the grant date, 33% on the first anniversary of the grant date, and 33% on the second anniversary of the grant date. The Options expire five years after the grant date, subject to earlier expiration upon a cessation of service.

Option grants made in fiscal 2026 were awarded primarily in recognition of overall Company and individual performance as described above and to align executives' interests with the future performance of the Company.

In response to shareholder feedback and the Compensation Committee’s market assessment conducted in fiscal 2026, equity awards granted beginning in fiscal 2027 will be determined (i) based on long-term incentive target grant values set in consideration of both internal Company context and market data from the Company’s compensation peer group, and (ii) in the form of awards that may vest ratably over three years from the date of the grant – see “Changes for Fiscal 2027” below for additional detail.

Changes for Fiscal 2027

With the assistance of Semler Brossy, the Compensation Committee established an executive compensation peer group and conducted a thorough market review of executive pay levels, compensation designs, and governance practices, and adopted a number of program enhancements to better align the Company’s programs with market practice and respond to feedback from our shareholders.

Compensation Peer Group

The Compensation Committee selected the peer group from U.S.- and Canada-listed mining and mineral development companies that are comparable to NioCorp in industry, stage of development, and scale of operations, with an emphasis on

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companies advancing large-scale critical minerals or precious metals projects that have not yet reached commercial production. Because the Company is pre-revenue and operates with a small corporate workforce, the Compensation Committee focused on factors it believes most directly affect the Company's ability to attract and retain executive talent — as such, the review emphasized project development, employee headcount, and geographic footprint in addition to giving consideration to financial metrics such as revenue. The Compensation Committee uses the peer group as one reference point among several in evaluating the competitiveness of executive pay, and does not target compensation at any specific percentile of the peer group. The peer group includes the following companies:

 

•
American Battery Technology Company
•
Dakota Gold Corp.
•
Idaho Strategic Resources Inc.
•
Centerra Gold Inc.
•
enCore Energy Corp
•
Perpetua Resources Corp.
•
Compass Minerals International, Inc.
•
Hycroft Mining Holding Corporation
•
United States Antimony Corporation
•
Contango Silver & Gold Inc.
•
i-80 Gold Corp.
•
Ucore Rare Metals Inc.

Annual Incentive Plan

As discussed above, the Company adopted the AIP during fiscal 2026 as a formal cash-based annual incentive plan. Beginning in fiscal 2027, the AIP will operate on a full fiscal-year basis, with performance measures established at the beginning of each fiscal year, in order to strengthen the pay-for-performance character of the Company’s compensation programs and to tie executive compensation outcomes more directly to accomplishments in the interests of shareholders. Key aspects of the program include:

•
Target award opportunities for each named executive officer expressed as a percentage of base salary, with a potential payout range from 0% to 200% of target based on performance;
•
Performance measured against a mixture of financial, strategic, and operational goals determined by the Compensation Committee and established at the beginning of each fiscal year; and
•
Specific individual performance objectives established for each named executive officer at the beginning of each fiscal year.

Long-Term Incentives

For fiscal 2027, the Compensation Committee has established annual long-term incentive target grant values for each named executive officer based on market data. To better align the interests of executives with those of shareholders and support retention, long-term incentive awards for fiscal 2027 are expected to consist of stock options that vest ratably over a two-year period.

Based on shareholder feedback, the Compensation Committee also evaluated the feasibility of introducing performance-based equity for future executive long-term incentive awards. The Compensation Committee ultimately determined not to adopt performance-based equity at this time as (i) the Company’s current stage of development makes it difficult to establish meaningful multi-year performance goals, and (ii) the Company’s equity awards are made in the form of stock options, which deliver value only to the extent the Company’s share price appreciates following the grant date and therefore provide inherent performance alignment. That said, the Compensation Committee intends to periodically revisit and assess the feasibility of adopting performance-based equity in future years.

Stock Ownership Guidelines

The Company adopted formal stock ownership guidelines for its executive officers and independent directors during fiscal 2026, effective June 26, 2026. Under the guidelines, each covered executive officer or director is required to hold shares of the Company’s common stock with a value equal to a multiple of his or her base salary (6.0x for the Chief Executive Officer and 3.0x for the other named executive officers) or annual cash retainer (5.0x for independent directors). Each covered individual has five years from the later of the date the guidelines were adopted and the date on which he or she first becomes subject to the guidelines to satisfy the applicable requirement.

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Employment Agreements and Severance Arrangements

Agreement Regarding Mr. Smith

The Company is currently a party to a Consulting Agreement with 76 Resources, LLC (an entity controlled by Mr. Smith) under which (as currently in effect, the “Smith Agreement”) 76 Resources, LLC, through Mr. Smith, performs the duties and responsibilities of the CEO of the Company and related services, for an indefinite term at a base rate of $360,000 per year as of June 30, 2026, generally payable in equal semi-monthly installments of $15,000. Any bonuses and incentive payments are payable at the discretion of the Board. Mr. Smith is eligible to receive Options under the 2017 Amended Long-Term Incentive Plan, as determined by the Board.

The Company may terminate the Smith Agreement at any time without notice or payment if (1) 76 Resources, LLC commits a material breach of the Smith Agreement (subject to a cure period in certain circumstances), (2) Mr. Smith dies or becomes permanently disabled, or (3) certain other “for cause” scenarios occur (as further described in the Smith Agreement). In the event the Smith Agreement is terminated by the Company for any other reason or if 76 Resources, LLC terminates the Smith Agreement on the occurrence of a Triggering Event, the Company shall pay 76 Resources, LLC a lump sum termination fee equal to the base fee in effect at the termination date as well as the average of any annual bonuses or other cash incentive payments for two calendar years immediately preceding the year the termination occurs. A Triggering Event is defined as: a substantial change in the nature of services to be performed by 76 Resources, LLC; a material breach by the Company of the Smith Agreement that is not remedied within 30 days of notice; the cessation of the Company as a going concern; the failure of the Company to pay a material amount due pursuant to the Smith Agreement within 30 days of the due date; or a material reduction in base fee or any other form of compensation payable by the Company to 76 Resources, LLC, except where all senior executives or consultants of the Company are subject to relatively similar reductions in such values. 76 Resources, LLC may terminate the Smith Agreement for a reason other than a Triggering Event on 90 days’ written notice and, should the Company immediately accept such termination notice, it shall pay 76 Resources, LLC the sum of $69,904. Should a change of control of the Company occur (as that term is defined in the Smith Agreement) and, within one year, either a Triggering Event occurs and 76 Resources, LLC terminates the Smith Agreement or 76 Resources, LLC’s engagement is terminated by the Company under circumstances that would give rise to a termination payment in the absence of a change of control, then 76 Resources, LLC shall be entitled to receive an amount equal to the base fee in effect at the termination date as well as the average of any annual bonuses or other cash payments for two calendar years immediately preceding the year the termination occurs. In the event 76 Resources, LLC is entitled to a termination payment with respect to a change of control, any Options previously granted to Mr. Smith shall become fully vested and shall remain exercisable for the original term of grant despite a termination of the services of 76 Resources, LLC. Termination payments under the Smith Agreement are generally contingent on a release of claims by 76 Resources, LLC. The Smith Agreement also includes customary confidentiality and six-month employee non-solicitation provisions.

If the Smith Agreement had been terminated by the Company for any reason other than as set out in the Smith Agreement, if 76 Resources, LLC terminated the Smith Agreement on the occurrence of a Triggering Event, or had a change of control of the Company occurred and within one year, either a Triggering Event occurred and 76 Resources, LLC terminated the Smith Agreement or 76 Resources, LLC’s engagement was terminated by the Company without the occurrence of a Triggering Event for any reason other than as set out in the Smith Agreement, effective as of June 30, 2026, 76 Resources, LLC (as ultimate successor in interest to KMSmith, LLC) would have been entitled to a payment of $415,000.

Agreements Regarding Messrs. Shah and Honan

As previously disclosed, on September 25, 2022, in connection with our entry into the Business Combination Agreement, Messrs. Shah and Honan (the “Covered Officers”) entered into employment agreements with a U.S. affiliate (the “U.S. Affiliate”) of the Company (the “Employment Agreements”). The Employment Agreements became effective as of March 17, 2023, and will continue until either the Covered Officer or the U.S. Affiliate terminates the Covered Officer’s employment for any reason. Pursuant to the Employment Agreements, Mr. Shah continues to serve as CFO of the Company, and Mr. Honan continues to serve as the COO of the Company and serves as President of the U.S. Affiliate.

The Employment Agreement for Mr. Shah provided for an initial annual base salary of $220,000 per year, and Mr. Honan’s Employment Agreement provided for an initial annual base salary of $260,000 per year. The annual base salary rates for the Covered Officers are reviewed at least annually for potential increases. The base salary rates of Messrs. Shah and Honan were increased in fiscal 2023 to $250,000 for Mr. Shah and $280,000 for Mr. Honan. There were no increases in base salary rates for fiscal 2024 or 2025. In fiscal 2026, Mr. Shah's base salary rate increased to $275,000 per year and Mr. Honan's base salary rate increased to $300,000 per year. The Employment Agreements also provide each of the Covered Officers with eligibility to participate in (1) any annual cash bonus plan and/or any long-term incentive compensation plan as may be established by the U.S. Affiliate or its affiliates, and (2) any employee benefit plan, program, or policy of the U.S. Affiliate or its affiliates as may

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be in effect for senior executives of the U.S. Affiliate or its affiliates generally. The Employment Agreements also include the following additional features: (1) severance benefits upon certain qualifying terminations of employment, consisting of: (a) for a qualifying termination of the Covered Officer’s employment by the U.S. Affiliate without Cause (as such term is defined in the Employment Agreements) that does not occur within two years after a Change in Control of the U.S. Affiliate (as defined in the Employment Agreements), certain accrued obligations, plus 12 months of salary continuation, and (b) for a qualifying termination of the Covered Officer’s employment by the U.S. Affiliate without Cause or by the Covered Officer for Good Reason (as such term is defined in the Employment Agreements) that occurs within two years after a Change in Control (a “Change in Control Termination”), certain accrued obligations, and a lump sum cash amount equal to two times the Covered Officer’s annual base salary as in effect at the time of such termination; and (2) a requirement that each Covered Officer execute a customary release of claims in favor of the U.S. Affiliate to receive severance compensation. In connection with the Covered Officers entering into the Employment Agreements each Covered Officer also entered into a restrictive covenant agreement (a “Restrictive Covenant Agreement”). The Restrictive Covenant Agreements include customary restrictive covenants, including non-competition and non-solicitation obligations that remain in effect both during the employment term and for one year following termination of the Covered Officer’s employment other than a Change in Control Termination (in which case the period will be two years following such Change in Control Termination), as well as other customary restrictive covenants, such as confidentiality provisions.

Stock Options Under the 2017 Amended Long-Term Incentive Plan

In accordance with the 2017 Amended Long-Term Incentive Plan, the Company granted Options to its named executive officers during the Company’s 2026 fiscal year; no other equity-based awards were granted to the named executive officers during the 2026 fiscal year.

The following table sets forth the outstanding equity awards for each named executive officer at June 30, 2026. The Company has not granted full value stock-based awards to any of its named executive officers.

Outstanding Equity Awards at 2026 Fiscal Year-End

 

 

Option Awards

Name

 

Grant Date (1)

 

Number of
Securities
Underlying
Unexercised
Options
(#)
Exercisable

 

Number of
Securities
Underlying
Unexercised
Options
(#)
Unexercisable

 

Option
Exercise
Price ($)

 

Option
Expiration
Date

Mark A. Smith

 

02/15/2024

 

375,000

 

—

 

2.99

 

02/15/2029

 

12/23/2024

 

150,000

 

—

 

1.40

 

12/21/2029

 

8/18/2025

 

127,500

 

247,500

 

4.35

 

8/19/2030

 

 

 

 

 

 

 

 

 

 

 

Scott Honan

 

02/15/2024

 

250,000

 

—

 

2.99

 

02/15/2029

 

12/23/2024

 

100,000

 

—

 

1.40

 

12/21/2029

 

8/18/2025

 

85,000

 

165,000

 

4.35

 

8/19/2030

 

 

 

 

 

 

 

 

 

 

 

Neal Shah

 

02/15/2024

 

250,000

 

—

 

2.99

 

02/15/2029

 

12/23/2024

 

100,000

 

—

 

1.40

 

12/21/2029

 

8/18/2025

 

85,000

 

165,000

 

4.35

 

8/19/2030

(1) The Options granted on August 18, 2025 vested 34% at grant, and will vest 33% on each of August 18, 2026 and August 18, 2027.

Retirement Plan Benefits

Messrs. Honan and Shah are each eligible to participate in the Company’s 401(k) savings plan on the same basis as our other eligible employees. The 401(k) savings plan is designed to reward continued employment with the Company and assist participants with financial preparation for retirement. Participants can defer a portion of their eligible compensation under the plan, subject to Code limits. Beginning January 1, 2026, the Company began providing matching contributions to the 401(k) savings plan. Matching contributions equal 100% of the participant’s contributions up to 4% of eligible compensation and vest immediately.

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Termination and Change of Control Benefits

Except as described above, the Company is not a party to any plans or arrangements regarding the named executive officers under which they may receive enhanced or incremental compensation or benefits in the event of a change of control, termination of employment (as a result of resignation, retirement, change of control, etc.) or a change in responsibilities following a change of control. Options are generally subject to clawback provisions, and provide for post-employment exercise periods, pursuant to the terms of such awards and the 2017 Amended Long-Term Incentive Plan.

Practices Related to the Grant of Equity Awards

Under our policies and practices, the approval of Options (including any Option grants to our named executive officers and directors) is typically provided at a Board or Compensation Committee meeting or via unanimous written action on the part of the Board or Compensation Committee. In the past, such grants were not generally made on any kind of predetermined, regular schedule. Instead, our award recipients (including the named executive officers and directors) generally received annual grants at various times each year, including as recommended by the CEO to the Board or Compensation Committee. Board or Compensation Committee meetings or written actions to approve such grants were scheduled on an ad hoc, as-needed basis, generally prompted by a determination by the Board or Compensation Committee that such grants should be made (or a request by management or the Board that such grants be made). Going forward, it is the Company's intention that equity award grants will generally be made on a predetermined annual cycle in connection with the Compensation Committee's annual compensation review.

Including for grants made during fiscal year 2026, we do not time the disclosure of material non-public information for purposes of affecting the value of executive compensation, and we do not make any grants while in the possession of material non-public information.

During fiscal year 2026, we did not grant Options (or similar awards) to any of our named executive officers during the period beginning four business days before and ending one business day after the filing of any Company periodic report on Form 10-Q or Form 10-K, or the filing or furnishing of any Company Form 8-K, that disclosed any material non-public information.

Fiscal 2026 Director Compensation

One of the directors serving on the Board (Mr. Smith) is also a named executive officer. For a description of the compensation paid to Mr. Smith, see “Fiscal 2026 Summary Compensation Table” and the accompanying narrative provided above.

The following table sets forth all compensation the Company granted to our directors, other than Mr. Smith, for the fiscal year ended June 30, 2026:

 

Name

 

Fees Earned or Paid in Cash
($)

 

Option Awards
($)(1)

 

All Other Compensation
($)

 

Total
($)

Peter Oliver

 

$40,000

 

$164,400

 

$—

 

$204,400

Nilsa Guerrero-Mahon

 

40,000

 

150,700

 

—

 

190,700

David C. Beling (2)

 

35,000

 

137,000

 

—

 

172,000

Dean C. Kehler

 

35,000

 

137,000

 

—

 

172,000

Michael G. Maselli

 

35,000

 

137,000

 

—

 

172,000

Anthony W. Fulton (3)

 

—

 

137,000

 

—

 

137,000

Michael J. Morris (4)

 

—

 

—

 

—

 

—

 

(1)
Reflects the grant date fair value of Options granted during the 2026 fiscal year, consisting of 60,000 Options for Mr. Oliver, 55,000 Options for Ms. Guerrero-Mahon, and 50,000 Options each for Messrs. Beling, Kehler, Maselli, and Fulton, in each case at an exercise price of $4.35 per share, computed in accordance with FASB ASC Topic 718. Assumptions used in the calculation of these amounts are described in Note 9b in the Company’s consolidated financial statements included in this Annual Report on Form 10-K. These Options were vested 34% on the grant date (August 18, 2025) and an additional 33% of the Options will vest on each of the first two anniversaries of the grant date. These Options generally remain exercisable until the fifth anniversary of the grant date. The narrative below discloses the number of stock awards and option awards held by each of the directors listed in the table as of the end of fiscal year 2026.
(2)
Mr. Beling did not stand for re-election at our annual general meeting of shareholders held on April 6, 2026.
(3)
Mr. Fulton was appointed to the Board on August 9, 2025.

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(4)
Mr. Morris served on the Board until his death on July 20, 2025.

In the past, the non-employee directors of the Company have had no standard compensation arrangements, or any other arrangements, with the Company, except as herein disclosed. Option grants were determined by the Board or Compensation Committee on a discretionary basis each year, and the non-employee directors did not receive any cash fees for serving on the Board. In fiscal 2026, however, each non-employee director serving on August 13, 2025, was granted a modest cash award in recognition of their service, the value of which is reflected in the "Fiscal 2026 Director Compensation" table above.

Commencing with the 2027 fiscal year, non-employee directors are eligible for a more standardized compensation structure that includes equity awards, base annual cash retainers, and additional cash retainers for committee service. We expect to provide more information regarding such compensation structure in future fiscal years.

Executive officers of the Company who also act as directors of the Company do not receive any additional compensation for services rendered in such capacity. See “Fiscal 2026 Summary Compensation Table” above.

The aggregate number of Option awards outstanding at the end of fiscal year 2026 for each non-employee director who served during fiscal 2026 was as follows: Mr. Oliver, 160,000 Options; Ms. Guerrero-Mahon, 205,000 Options; Mr. Kehler, 150,000 Options; Mr. Maselli, 150,000 Options; and Mr. Fulton, 50,000 Options. As of June 30, 2026, 76% of the above Options were fully vested. Mr. Beling and Mr. Morris did not hold any outstanding Option awards at the end of fiscal year 2026.

Description of the 2017 Amended Long-Term Incentive Plan

On April 6, 2026, NioCorp’s shareholders approved the adoption of the 2017 Amended Long-Term Incentive Plan. Under the 2017 Amended Long-Term Incentive Plan, the Board may in its discretion from time-to-time grant Options, share units (in the form of restricted share units (“RSUs”) and performance share units (“PSUs”)) and dividend equivalents to non-employee directors, employees and certain other service providers (as further described in the 2017 Amended Long-Term Incentive Plan) of the Company and affiliated entities selected by the Board. Subject to adjustment as described in the 2017 Amended Long-Term Incentive Plan, and subject to the plan's share counting rules, the aggregate number of Common Shares available for awards under the 2017 Amended Long-Term Incentive Plan may not exceed 11,300,000 Common Shares, minus, as of April 6, 2026, one Common Share for every one Common Share subject to an award granted under the 2017 Amended Long-Term Incentive Plan after February 9, 2026 and before April 6, 2026. The 2017 Amended Long-Term Incentive Plan also limits the maximum annual compensation that may be granted to our non-employee directors for service on the Board to $750,000 (measured as described in the plan document), subject to exceptions for distributions of previously deferred compensation, compensation for services as an executive officer or employee, and non-preferential dividends or dividend equivalents.

The following table presents the burn rates for the 2017 Amended Long-Term Incentive Plan for the three most recent fiscal years:

 

Fiscal Year
Ending June 30

 

Number of awards
granted

 

Weighted average number of Common
Shares outstanding

 

Burn rate

2026

 

2,282,500

 

117,214,449

 

2.0%

2025

 

945,000

 

45,072,895

 

2.1%

2024

 

1,625,000

 

34,320,024

 

4.7%

 

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ITEM 12. SECURITY OWNERSHIP OF CERTAIN BENEFICIAL OWNERS AND MANAGEMENT AND RELATED STOCKHOLDER MATTERS

The following table sets forth the beneficial ownership of Common Shares of NioCorp as of September 25, 2026 (except where otherwise indicated), for the following: (1) each person who is known by NioCorp to beneficially own more than 5% of the outstanding shares of NioCorp’s Common Shares; (2) each of the named executive officers (as defined in the “Fiscal 2026 Summary Compensation Table,” above); (3) each of NioCorp’s directors; and (4) all directors and executive officers of NioCorp as a group.

Beneficial ownership of Common Shares in the table below is determined in accordance with the rules of the SEC and includes voting or investment power with respect to the Common Shares. Common Shares that may be acquired by an individual or group within 60 days of September 25, 2026, pursuant to the exercise of Options, the exercise of Warrants, or the exchange of shares of Class B common stock of ECRC (formerly known as GXII), are deemed to be outstanding for the purpose of computing the percentage ownership of such individual or group but are not deemed to be outstanding for the purpose of computing the percentage ownership of any other person shown in the table. Percentage of ownership is based on 145,849,630 Common Shares outstanding as of September 25, 2026. Unless otherwise noted in the table below, Options vested at the grant date.

Except as indicated in footnotes to this table, we believe that the shareholders named in this table have sole voting and investment power with respect to all Common Shares shown to be beneficially owned by them, based on information provided to us by such shareholders. Unless otherwise indicated, the address for each director and executive officer listed is: c/o NioCorp Developments Ltd., 7000 South Yosemite Street, Suite 115, Centennial, CO 80112.

 

Name and Address of
Beneficial Owner

 

Position

 

Amount and Nature of Beneficial Ownership
(1) (2)

 

 

 

 

Percent of Common Shares

 

Mark A. Smith, PE, Esq.
Highlands Ranch, Colorado, USA

 

Chief Executive Officer, President, Executive Chairman and Director

 

 

3,469,876

 

 

(3)

 

 

2.36

%

Neal Shah
Superior, Colorado, USA

 

Chief Financial Officer and Corporate Secretary

 

 

631,294

 

 

(4)

 

*

 

Scott Honan
Centennial, Colorado, USA

 

Chief Operating Officer

 

 

628,636

 

 

(5)

 

*

 

Anthony W. Fulton
Lincoln, Nebraska, USA

 

Director

 

 

267,709

 

 

(6)

 

*

 

Nilsa Guerrero-Mahon
Brighton, Colorado, USA

 

Director

 

 

232,918

 

 

(7)

 

*

 

Dean Kehler
New York, New York, USA

 

Director

 

 

3,725,311

 

 

(8)

 

 

2.49

%

Michael Maselli
Pelham, New York, USA

 

Director

 

 

671,735

 

 

(9)

 

*

 

Peter Oliver
Bunbury, Western Australia, Australia

 

Lead Director

 

 

140,200

 

 

(10)

 

*

 

All current directors, executive officers and named executive officers as a group (10 persons)

 

 

 

 

10,476,557

 

 

 

 

 

6.84

%

BlackRock, Inc.

 

 

 

 

9,013,741

 

 

(11)

 

 

6.18

%

* Represents ownership of less than 1%.

(1)
Calculated in accordance with Rule 13d-3 of the Exchange Act.
(2)
On March 17, 2023, NioCorp effected a 1-to-10 reverse stock split (the “Reverse Stock Split”) of the Common Shares, with any fractional shares resulting from the Reverse Stock Split rounded down to the nearest whole share. All Options and Warrants outstanding as of March 17, 2023, were adjusted to reflect the Reverse Stock Split. Such Options and Warrants initially covered a number of shares equal to the amount reported herein times 10 (and at an exercise price equal to the amount reported herein divided by 10). Class B common stock of ECRC, which may be exchanged for Common Shares upon certain conditions, were issued on a post-Reverse Stock Split basis.
(3)
Mr. Smith beneficially owns 2,318,819 outstanding Common Shares. In addition, he beneficially owns 275,133 Common Shares issuable upon exercise of: (i) 183,422 Warrants each exercisable for one Common Share at a price of $1.75 until November 13, 2026; and (ii) 91,711 Warrants each exercisable for one Common Share at a price of $2.07 until November 13, 2029. He also beneficially owns 875,924 Common Shares issuable upon exercise of vested Options each exercisable for one Common Share. The total does not include 317,236 Common Shares that may be issuable upon exercise of unvested Options.
(4)
Mr. Shah beneficially owns 75,032 outstanding Common Shares. In addition, he beneficially owns 556,262 Common Shares issuable upon exercise of vested Options each exercisable for one Common Share. The total does not include 157,745 Common Shares that may be issuable upon exercise of unvested Options.

100


 

(5)
Mr. Honan beneficially owns 55,762 outstanding Common Shares. In addition, he beneficially owns 572,874 Common Shares issuable upon exercise of vested Options each exercisable for one Common Share. The total does not include 189,992 Common Shares that may be issuable upon exercise of unvested Options.
(6)
Mr. Fulton beneficially owns 179,350 outstanding Common Shares. He shares both voting and investment power with respect to 2,276 of such Common Shares with members of his family. In addition, he beneficially owns 54,859 Common Shares issuable upon exercise of 49,058 Warrants assumed by NioCorp in connection with its business combination with GXII (“NioCorp Assumed Warrants”) each exercisable for 1.11829212 Common Shares at a price of $11.50 until March 17, 2028. He shares both voting and investment power with respect to 12,335 Common Shares issuable upon exercise of 11,032 of such NioCorp Assumed Warrants with members of his family. He also beneficially owns 33,500 Common Shares issuable upon exercise of vested Options each exercisable for one Common Share. The total does not include 16,500 Common Shares that may be issuable upon exercise of unvested Options.
(7)
Ms. Guerrero-Mahon beneficially owns 46,068 outstanding Common Shares. In addition, she beneficially owns 186,850 Common Shares issuable upon exercise of vested Options each exercisable for one Common Share. The total does not include 18,150 Common Shares that may be issuable upon exercise of unvested Options.
(8)
Mr. Kehler beneficially owns 212,583 outstanding Common Shares, and 1,441,290 Common Shares issuable upon the exchange of Vested Shares (as defined herein). He shares both voting and investment power with respect to 318,470 of such Vested Shares with U.S. Trust Company of Delaware, as co-trustee of the Elizabeth Kehler 2012 Family Trust under Declaration of Trust dated December 12, 2012 (the “Elizabeth Kehler Trust”). In addition, he beneficially owns 1,937,938 Common Shares issuable upon exercise of the following: (i) 1,657,057 NioCorp Assumed Warrants exercisable for an aggregate of up to 1,853,073 Common Shares held by Mr. Kehler; (ii) 56,577 Warrants each exercisable for one Common Share at a price of $1.75 until November 13, 2026; and (iii) 28,288 Warrants each exercisable for one Common Share at a price of $2.07 until November 13, 2029. He also beneficially owns 133,500 Common Shares issuable upon exercise of vested Options each exercisable for one Common Share. The total does not include 16,500 Common Shares that may be issuable upon exercise of unvested Options. The total does not include Common Shares that may be issuable upon exchange of the following: (i) 417,030 that are not exchangeable until the volume-weighted average price of the Common Shares on the principal securities exchange for the Common Shares as reported by Bloomberg (“VWAP”) equals or exceeds approximately $12.00 per share for 20 of any 30 consecutive trading days during the period from the closing of the business combination with GXII on March 17, 2023 through, and including, the tenth anniversary of such date (such period, the “Earnout Share Period”) on any stock exchange on which the Common Shares are then trading (“Tranche I Earnout Shares”) held by Mr. Kehler; (ii) 417,030 that are not exchangeable until the VWAP of the Common Shares equals or exceeds approximately $15.00 per share for 20 of any 30 consecutive trading days during the Earnout Share Period on any stock exchange on which the Common Shares are then trading (“Tranche II Earnout Shares”) held by Mr. Kehler; (iii) 118,284 Tranche I Earnout Shares held by the Elizabeth Kehler Trust; and (iv) 118,284 Tranche II Earnout Shares held by the Elizabeth Kehler Trust.
(9)
Mr. Maselli beneficially owns 323,085 outstanding Common Shares. In addition, Mr. Maselli beneficially owns 215,150 Common Shares issuable upon exercise of 192,392 NioCorp Assumed Warrants held by Mr. Maselli. He also beneficially owns 133,500 Common Shares issuable upon exercise of vested Options each exercisable for one Common Share. The total does not include 16,500 Common Shares that may be issuable upon exercise of unvested Options. The total does not include Common Shares that may be issuable upon exchange of the following: (i) 119,998 Tranche I Earnout Shares held by Mr. Maselli; and (ii) 119,998 Tranche II Earnout Shares held by Mr. Maselli.
(10)
Mr. Oliver beneficially owns 140,200 Common Shares issuable upon exercise of vested Options each exercisable for one Common Share. The total does not include 19,800 Common Shares that may be issuable upon exercise of unvested Options.
(11)
Based on a Schedule 13G/A filed on July 29, 2026 by BlackRock, Inc. ("BlackRock") with respect to the Common Shares owned by BlackRock. BlackRock reported sole voting power over 8,796,392 Common Shares and sole dispositive power over 9,013,741 Common Shares. BlackRock's address is 50 Hudson Yards, New York, NY 10001.

EQUITY COMPENSATION PLANS

The Company has maintained equity compensation plans under which Options have been granted. Option grants have been determined by the Company’s directors and are only provided in compliance with applicable laws and regulatory policy. The following information is provided with respect to compensation plans (including individual compensation arrangements) under which equity securities were authorized for issuance as of June 30, 2026.

 

Equity Compensation Plan Information

Plan Category

 

Number of Securities
to be Issued Upon
Exercise of
Outstanding Options,
Warrants, and Rights

 

Weighted-Average Exercise Price of Outstanding
Options, Warrants,
and Rights

 

Number of Securities Remaining
Available for Future Issuance Under
Equity Compensation Plans
(Excluding Securities Reflected
in Second Column)

Equity Compensation Plans Approved by Security Holders (1)

 

4,147,500

 

 

$3.42

 

 

11,300,000

 

 

Equity Compensation Plans Not Approved by Security Holders

 

—

 

 

—

 

 

—

 

 

Total(2)

 

4,147,500

 

 

$3.42

 

 

11,300,000

 

 

 

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(1)
Represents Options granted pursuant to the 2017 Amended Long-Term Incentive Plan.
(2)
As of June 30, 2026, there were: (i) 4,147,500 outstanding securities awarded under the 2017 Amended Long-Term Incentive Plan representing 2.84% of the Company’s currently issued and outstanding Common Shares; and (ii) 11,300,000 remaining securities available for grant representing 7.75% of the Company’s currently issued and outstanding Common Shares.

Performance Graph

The following graph compares total cumulative shareholder return for $100 invested in Common Shares from July 1, 2021, to June 30, 2026, with cumulative total returns for the Russell 2000 Index and the VanEck Rare Earth & Strategic Metals ETF (REMX).

Beginning with fiscal year 2026, the Company changed the indices used in this comparison. The broad equity market index is now the Russell 2000 Index, replacing the S&P/TSX Composite Index. The Company's Common Shares have traded principally on the Nasdaq Stock Market since March 2023, and the Russell 2000 comprises United States issuers of market capitalization comparable to the Company's, making it a more representative broad market comparison than a Canadian composite index.

The industry comparison index is now the MVIS Global Rare Earth/Strategic Metals Index, replacing the S&P/TSX Global Mining Index. The Company believes the MVIS index more closely reflects the Company's focus on critical minerals and rare earth elements than a diversified global mining index. Index performance is presented using the VanEck Rare Earth and Strategic Metals ETF (REMX), which tracks that index, as a proxy for total shareholder return.

Consistent with Item 201(e) of Regulation S-K, the graph presents the Company's cumulative total return against both the newly selected indices and the indices used for the immediately preceding fiscal year.

 

img85804497_3.gif

Overall, the Company’s cumulative return for the five-year period ended below the range of returns for the selected index. As an exploration stage company, the Compensation Committee and the Board have not historically adjusted executive officer compensation to reflect share performance trends. Compensation to executive officers remained flat from 2013 through February 2023, except for increases supported by additional job responsibilities and/or job promotions. Effective April 1, 2023, the Compensation Committee approved a base rate average increase of 12% for all NioCorp employees. There were no salary increases granted during fiscal years 2024 or 2025. In fiscal year 2026, the Compensation Committee approved a base rate average increase of 8% for all NioCorp employees.

ITEM 13. CERTAIN RELATIONSHIPS AND RELATED TRANSACTIONS, AND DIRECTOR INDEPENDENCE

The following sets forth certain information regarding transactions between the Company (and its subsidiaries) and its officers, directors, and significant shareholders. There have been no other transactions since the end of the Company’s most

102


 

recently completed fiscal year and there are no currently proposed transactions in which the Company was or is to be a participant and the amount involved exceeds $120,000, and in which any related person (for purposes of Item 404 of Regulation S-K) had or will have a direct or indirect material interest.

Loan Transactions:

Mr. Smith is our Chief Executive Officer, President, Executive Chairman, and Director. On September 11, 2024, the Company and Mr. Smith entered into the Smith Loan Agreement pursuant to which Mr. Smith agreed to make available to the Company a non-revolving, multiple draw credit facility of up to $2,000,000. The Smith Loan expired on June 30, 2025, was non-revolving, and amounts paid back under the terms of the Smith Loan Agreement did not again become available for drawdowns at the request of the Company.

The Company paid interest to Mr. Smith on amounts outstanding under the Smith Loan at a rate equal to 10% per annum, calculated monthly in arrears, through to the date of repayment of the Loan. Mr. Smith also received an establishment fee equal to 2.5% of the amount of each drawdown payable at the time of the drawdown as consideration of the advancement of such drawdown. Any outstanding balance on the Loan, including accrued interest, were immediately due and payable by the Company on the earlier of the date of expiration of the Smith Loan Agreement and the occurrence of an event of default thereunder (the “Due Date”). The Company could repay the Smith Loan at any time without notice and without penalty, but any amount of principal or interest repaid by the Company prior to the Due Date will be subject to an early payment fee of 2.5% of the value of any such payment. Amounts outstanding under the Smith Loan Agreement were secured by all of the Company’s assets pursuant to a general security agreement between the Company and Mr. Smith, dated September 11, 2024.

Through October 30, 2024, the Company borrowed a total of $504,000 under the Smith Loan and the largest aggregate amount of principal outstanding under the Smith Loan Agreement during the period ended June 30, 2025, was $504,000. The Company subsequently repaid $508,200, representing the balance of the principal outstanding under the Smith Loan plus accrued interest, and also repaid $40,850 related to loan origination fees payable. As of June 30, 2026, there was no principal amount or accounts payable outstanding under the Smith Loan.

November 2024 Private Offering

On November 13, 2024, the Company closed a non-brokered private placement (the “November 2024 Private Offering”) and issued an aggregate of 2,199,602 units of the Company (the “November 2024 Units”). Each November 2024 Unit consists of one Common Share, one Warrant (collectively, the “Series A Private Warrants”) to purchase one Common Share and one-half of one Warrant to purchase one-half of one Common Share (the “Series B Private Warrants” and, together with the Series A Private Warrants, the “November 2024 Private Warrants”). Each Series A Private Warrant is exercisable into one Common Share (a “Series A Warrant Share”) at an exercise price of $1.75 per Series A Warrant Share at any time on or after the date of issuance until November 13, 2026. Each Series B Private Warrant is exercisable into one Common Share (a “Series B Warrant Share”) at an exercise price of $2.07 per Series B Warrant Share at any time beginning six months and one day from the date of issuance until November 13, 2029. Messrs. Kehler and Smith subscribed to purchase an aggregate of 239,999 November 2024 Units in the November 2024 Private Offering and paid a purchase price of $1.7675 per November 2024 Unit (the “November 2024 Insider Unit Price”) upon the closing of the November 2024 Private Offering. The November 2024 Insider Unit Price included $0.125 per November 2024 Private Warrant underlying each November 2024 Unit purchased by directors of the Company. Messrs. Kehler and Smith purchased 56,577 November 2024 Units and 183,422 November 2024 Units, respectively, for aggregate purchase prices of approximately $100,000 and $324,198, respectively. The remaining investors in the November 2024 Private Offering, who are not affiliated with the Company but with whom the Company had a pre-existing relationship, subscribed to purchase an aggregate of 1,959,603 November 2024 Units at a purchase price per November 2024 Unit of $1.57. Gross proceeds to the Company from the November 2024 Private Offering were approximately $3.5 million.

Review, Approval or Ratification of Related Person Transactions

Other than as described below, the Company does not currently have in place any specific policy or procedure in respect of the review, approval or ratification of any transaction required to be reported under Item 404(a) of Regulation S-K. Sections 147-153 of the BCBCA set out rules and procedures applicable to all British Columbia corporations, pursuant to which a director presented with a resolution in respect of any matter (including an equity issuance) in respect of which he/she has an interest must disclose that interest in writing to the corporation’s board of directors prior to the approval of such matter. This procedure ensures that each equity issuance to a director or officer of the Company is approved by all directors of the Company not involved in such sale. All loan transactions from directors and officers are typically subject to review and approval by the Board prior to acceptance and are documented in the meeting minutes or resolutions related to same. Under its charter, the Audit Committee is responsible for reviewing and approving any related party transaction in advance of such transaction, unless the Chief Financial Officer or General Counsel determines that it is not practicable to wait until the next Audit Committee meeting,

103


 

in which case the related party transaction will be submitted to the Chair of the Audit Committee, who will have delegated authority to act between Audit Committee meetings.

Director Independence

The Company’s Board consists of Messrs. Smith, Fulton, Oliver, Kehler, and Maselli and Ms. Guerrero-Mahon. The Company utilizes the definition of “independent” as it is set forth in Nasdaq Listing Rule 5605(a)(2) (“Rule 5605(a)(2)”) and National Instrument 52-110 Audit Committees (“NI 52-110”). Further, the Board considers all relevant facts and circumstances in its determination of independence of all members of the Board (including any relationships). Currently, Messrs. Fulton, Oliver, Kehler, and Maselli and Ms. Guerrero-Mahon are considered independent directors. Michael J. Morris and David C. Beling, who served as directors of the Company during fiscal 2026, were previously determined by the Board to be independent directors.

ITEM 14. PRINCIPAL ACCOUNTANT FEES AND SERVICES

The following table presents fees for professional services rendered by Deloitte & Touche LLP for the fiscal years ended June 30, 2026 and June 30, 2025, for the audit of the Company’s annual consolidated financial statements and review of consolidated financial statements included in the Company’s filings and fees billed for other services rendered by the firms during those periods (Dollar amounts in the following table are presented in whole dollars).

 

Fiscal Year Ending June 30,

 

Audit Fees(1) ($)

 

 

Audit-Related
Fees
(2) ($)

 

 

Tax Fees(3) ($)

 

 

All Other
Fees
(4) ($)

2026

 

$

545,100

 

 

$

1,212,703

 

 

$

56,840

 

 

$

—

 

 

2025

 

 

662,712

 

 

 

601,309

 

 

 

94,016

 

 

 

—

 

 

 

(1)
“Audit Fees” consist of fees billed, or to be billed, for professional services rendered for the audit of our annual consolidated financial statements and reviews of our interim financial statements included in quarterly reports and services normally provided by our independent registered public accounting firm in connection with statutory filings.
(2)
“Audit-Related Fees” consist of fees billed, or to be billed, related to agreed-upon procedures and services, including for comfort letters, normally provided by our independent registered public accounting firm in connection with debt offerings or regulatory filings.
(3)
“Tax Fees” include fees for all tax services other than those included in “Audit Fees” and “Audit-Related Fees.” This category includes fees for tax compliance, tax planning, and tax advice. Tax planning and tax advice include assistance with tax audits and appeals, tax advice related to mergers and acquisitions, and requests for rulings or technical advice from tax authorities. For the financial year ended June 30, 2026, these tax services included the preparation of Canadian and U.S. federal and state tax returns and tax planning and tax advice services.
(4)
“All Other Fees” includes all other non-audit services.

Pre-approval Policies

The policy of the Audit Committee has been to pre-approve all audit, audit-related and non-audit services performed by our independent auditors and to subsequently review the actual fees and expenses paid to our independent auditors. Accordingly, the Audit Committee pre-approved all audit, audit-related and non-audit services performed by Deloitte & Touche LLP and subsequently reviewed the actual fees and expenses paid for these services. The Audit Committee has determined that the fees paid to Deloitte & Touche LLP for services are compatible with maintaining Deloitte & Touche LLP’s independence as our auditor. All of the services provided during the years ended June 30, 2026 and 2025, were approved by the Audit Committee pursuant to paragraph (c)(7)(i)(C) of Rule 2-01 of Regulation S-X.

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PART IV

ITEM 15. EXHIBITS AND FINANCIAL STATEMENT SCHEDULES

The following documents are filed as a part of this report:

Financial Statements

(1)
The Consolidated Financial Statements, together with the report thereon of Deloitte & Touche LLP, dated September 25, 2026, are included as part of Item 8, “Financial Statements and Supplementary Data,” commencing on page 53 above.

 

 

 

 

Page

Report of Independent Registered Public Accounting Firms
(
Deloitte & Touche LLP; Denver, Colorado; PCAOB ID#34)

 

53

 

Consolidated Balance Sheets

 

55

 

Consolidated Statements of Operations and Comprehensive Loss

 

56

 

Consolidated Statements of Cash Flows

 

57

 

Consolidated Statements of Shareholders’ Equity and Redeemable Noncontrolling Interest

 

58

 

Notes to Consolidated Financial Statements

 

59

 

 

105


 

(a)
Exhibits

 

Exhibit No.

 

Title

 

 

 

2.1(1)**

 

Business Combination Agreement, dated September 25, 2022, by and among NioCorp Developments Ltd., GX Acquisition Corp. II and Big Red Merger Sub Ltd

2.2(2)

 

Asset Purchase Agreement, dated as of December 4, 2025, by and among NioCorp Advanced Metals and

Alloys, LLC, FEA Materials LLC and each member of FEA Materials LLC party thereto

3.1(3)

 

Notice of Articles of NioCorp Developments Ltd., dated April 5, 2016

3.2(3)

 

Articles of NioCorp Developments Ltd., as amended, effective as of January 27, 2015

3.3(4)

 

Amendment to Articles, effective March 17, 2023

4.1(5)

 

Convertible Security Funding Agreement, dated February 16, 2021, between the Company and Lind Global Asset Management III, LLC

4.2(6)

 

Amendment #1 to Convertible Security Funding Agreement, dated December 2, 2021, between the Company and Lind Global Asset Management III, LLC

4.3(7)

 

Waiver and Consent Agreement, dated September 25, 2022, between NioCorp Developments Ltd. and Lind Global Asset Management III, LLC

4.4(8)

 

Form of Lind Contingent Consent Warrants

4.5(1)

 

Sponsor Support Agreement, dated as of September 25, 2022, by and among GX Acquisition Corp. II, NioCorp Developments Ltd., GX Sponsor II LLC, in its capacity as a shareholder of GX Acquisition Corp. II, and certain other shareholders of GX Acquisition Corp. II

4.6(9)

 

Joinder to Sponsor Support Agreement, dated as of March 17, 2023, by and among NioCorp Developments Ltd. and each of the Holders party thereto

4.7(4)

 

Amended and Restated Registration Rights Agreement, dated as of March 17, 2023, by and among NioCorp Developments Ltd., GX Acquisition Corp. II, GX Sponsor II LLC, certain holders of the common shares of the NioCorp Developments Ltd. listed on Schedule 1 thereto, certain current and former stockholders of GX Acquisition Corp. II, and other persons and entities listed on Schedule 2 thereto

4.8(4)

 

Registration Rights Agreement Joinder, dated as of March 17, 2023, by and among NioCorp Developments Ltd. and each of the parties listed on Schedule A thereto

4.9(4)

 

Exchange Agreement, dated as of March 17, 2023, by and among NioCorp Developments Ltd., GX Acquisition Corp. II and GX Sponsor II LLC

4.10(9)

 

Joinder to Exchange Agreement, dated as of March 17, 2023, by and among NioCorp Developments Ltd., Elk Creek Resources Corp (f/k/a GX Acquisition Corp. II) and each of the Holders party thereto

4.11(10)

 

Warrant Agreement, dated March 17, 2021, by and between GX Acquisition Corp. II and Continental Stock Transfer & Trust Company

4.12(4)

 

Assignment, Assumption and Amendment Agreement, dated as of March 17, 2023, by and among GX Acquisition Corp. II, NioCorp Developments Ltd., Continental Stock Transfer & Trust Company, as the existing Warrant Agent, and Computershare Inc. and its affiliate Computershare Trust Company, N.A., as the successor Warrant Agent

4.13(4)

 

Form of Warrant (included in Exhibit 4.12)

4.14(11)

 

Underwriting Agreement, dated as of November 3, 2024, by and between NioCorp Developments Ltd. and Maxim Group LLC

4.15(11)

 

Warrant Agency Agreement, dated as of November 5, 2024, by and between NioCorp Developments Ltd., Computershare Inc. and Computershare Trust Company, N.A.

4.16(11)

 

Form of November 2024 Series A Public Warrant

4.17(11)

 

Form of November 2024 Series B Public Warrant

4.18(12)

 

Form of Subscription Agreement in respect of units issued in November 2024

4.19(12)

 

Form of November 2024 Series A Private Warrant

4.20(12)

 

Form of November 2024 Series B Private Warrant

4.21(13)

 

Placement Agency Agreement, dated as of September 26, 2025, by and between NioCorp Developments Ltd. and Maxim Group LLC

4.22(13)

 

Form of September Pre-Funded Warrant (included in Exhibit 4.21)

4.23(14)

 

Placement Agency Agreement, dated as of October 13, 2025, by and between NioCorp Developments Ltd. and Maxim Group LLC

4.24(14)

 

Form of October Pre-Funded Warrant (included in Exhibit 4.23)

4.25(15)

 

Shareholder Rights Plan Agreement, dated as of November 21, 2025, between NioCorp Developments Ltd. and Computershare Investor Services Inc.

4.26(16)

 

Amended and Restated Shareholder Rights Plan Agreement, dated as of April 6, 2026, by and between NioCorp Developments Ltd. and Computershare Investor Services Inc. as rights agent (or any successor rights agent)

4.27(17)

 

Placement Agency Agreement, dated as of February 24, 2026, by and between NioCorp Developments Ltd. and Maxim Group LLC

4.28(17)

 

Form of February Pre-Funded Warrant (included in Exhibit 4.27)

4.29

 

Description of Securities

10.1(3)#

 

Consulting Agreement, dated May 13, 2014, between the Company and KMSmith, LLC

10.2(18)#

 

Amendment to Contract, dated September 1, 2019, between the Company and KMSmith, LLC

106


 

10.3(18)#

 

Contract Assignment and Novation Agreement, dated as of August 31, 2020, among the Company, KMSmith, LLC and 76 Resources, Inc.

10.4(19)#

 

Contract Assignment and Novation Agreement, dated as of August 1, 2021, among the Company, 76 Resources, Inc. and 76 Resources, LLC

10.5(20)#

 

Amendment to Contract, dated April 1, 2023, between the Company and 76 Resources, LLC

10.6(21)#

 

Amendment to Contract, dated August 18, 2025, between the Company and 76 Resources, LLC

10.7(22)*

 

Offtake agreement, dated June 13, 2016, between the Company and CMC Cometals, a division of Commercial Metals Company

10.8(23)

 

Amendment No. 1 to Offtake Agreement, dated April 13, 2020, between the Company and Traxys North America LLC, as assignee

10.9(24)

 

Offtake agreement with ThyssenKrupp Metallurgical Products GmbH

10.10(4)#

 

Form of Director and Officer Indemnification Agreement

10.11(1)#

 

Employment Agreement, dated as of September 25, 2022, by and between Elk Creek Resources Corporation and Neal Shah

10.12(1)#

 

Employment Agreement, dated as of September 25, 2022, by and between Elk Creek Resources Corporation and Scott Honan

10.13(1)#

 

Employment Agreement, dated as of September 25, 2022, by and between Elk Creek Resources Corporation and Jim Sims

10.14#

 

Employment Agreement, dated as of July 1, 2026, by and between Elk Creek Resources Corporation and Ernest Cleave

10.15(1)#

 

Form of Restrictive Covenant Agreement

10.16(16)#

 

NioCorp Developments Ltd. Long-Term Incentive Plan, as amended through April 6, 2026

10.17#

 

Form of Option Certificate

10.18(25)

 

Loan Agreement, dated as of September 11, 2024, between the Company and Mark Smith

10.19(25)

 

Security Agreement, dated as of September 11, 2024, between the Company and Mark Smith

10.20(21)

 

Defense Industrial Base Consortium Base Agreement, dated as of July 22, 2025, between Elk Creek Resources Corp. and Advanced Technology International.

10.21(21)

 

Project Sub Agreement, dated as of August 4, 2025, by and between Elk Creek Resources Corp. and Advanced Technology International

19.1(8)

 

NioCorp Developments Ltd. Insider Trading Policy

21.1

 

Subsidiaries of NioCorp Developments Ltd.

23.1

 

Consent of Deloitte & Touche LLP

23.2

 

Consent of Dahrouge Geological Consulting USA Ltd.

23.3

 

Consent of SMH Process Innovation

23.4

 

Consent of Dumas Contracting USA Inc.

23.5

 

Consent of Amplify Mine Planning LLC

23.6

 

Consent of BBA Consultants International LP

23.7

 

Consent of Olsson

23.8

 

Consent of Adrian Brown Consultants Inc.

23.9

 

Consent of Andrieux & Associates Geomechanics Consulting, L.P.

23.10

 

Consent of Tetra Tech

23.11

 

Consent of T Engineering

23.12

 

Consent of Magemi Mining Inc.

23.13

 

Consent of Metallurgy Concept Solutions

23.14

 

Consent of Scott Honan, M.Sc., SME-RM

31.1

 

Certification of the Chief Executive Officer pursuant to Exchange Act Rules 13a-14(a) and 15d-14(a), as adopted pursuant to Section 302 of the Sarbanes-Oxley Act of 2002

31.2

 

Certification of the Chief Financial Officer pursuant to Exchange Act Rules 13a-14(a) and 15d-14(a), as adopted pursuant to Section 302 of the Sarbanes-Oxley Act of 2002

32.1

 

Certification of the Chief Executive Officer pursuant to 18 U.S.C. Section 1350, as adopted pursuant to Section 906 of the Sarbanes-Oxley Act of 2002

32.2

 

Certification of the Chief Financial Officer pursuant to 18 U.S.C. Section 1350, as adopted pursuant to Section 906 of the Sarbanes-Oxley Act of 2002

95.1

 

Mine Safety Disclosure

96.1

 

2026 S-K 1300 Elk Creek Technical Report Summary

97.1(8)

 

Compensation Clawback Policy

101.INS(26)

 

XBRL Instance Document

101.SCH(26)

 

XBRL Taxonomy Extension – Schema

101.CAL(26)

 

XBRL Taxonomy Extension – Calculations

101.DEF(26)

 

XBRL Taxonomy Extension – Definitions

101.LAB(26)

 

XBRL Taxonomy Extension – Labels

101.PRE(26)

 

XBRL Taxonomy Extension – Presentations

104

 

Cover Page Interactive Data File (formatted as Inline XBRL and contained in Exhibit 101)

# Management compensation plan, arrangement or agreement.

* Portions of this exhibit have been omitted pursuant to Item 601(b)(10)(iv) of Regulation S-K, which portions will be furnished to the Securities and Exchange Commission upon request.

107


 

** Certain exhibits to this agreement have been omitted pursuant to Item 601(a)(5) of Regulation S-K. A copy of any omitted exhibit will be furnished to the Securities and Exchange Commission upon request.

(1)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 000-55710) filed with the SEC on September 29, 2022 and incorporated herein by reference.
(2)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 001-41655) filed with the SEC on December 4, 2025, and incorporated herein by reference.
(3)
Previously filed as an exhibit to the Company’s Draft Registration Statement on Form S-1 (Registration No. 377-01354) submitted to the SEC on July 26, 2016 and incorporated herein by reference.
(4)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 001-41655) filed with the SEC on March 17, 2023 and incorporated herein by reference.
(5)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 000-55710) filed with the SEC on February 17, 2021 and incorporated herein by reference.
(6)
Previously filed as an exhibit to the Company’s Quarterly Report on Form 10-Q (File No. 000-55710) filed with the SEC on February 4, 2022 and incorporated herein by reference.
(7)
Previously filed as an exhibit to the Company’s Registration Statement on Form S-4 (Registration No. 333-268227) filed with the SEC on November 7, 2022 and incorporated herein by reference.
(8)
Previously filed as an exhibit to the Company’s Annual Report on Form 10-K (File No. 001-41655) filed with the SEC on September 23, 2024 and incorporated herein by reference.
(9)
Previously filed as an exhibit to the Company’s Registration Statement on Form S-3 (File No. 333-271268) filed with the SEC on April 14, 2023 and incorporated herein by reference.
(10)
Previously filed as an exhibit to Elk Creek Resources Corp.’s (f/k/a GX Acquisition Corp. II) Current Report on Form 8-K (File No. 001-40226) filed with the SEC on March 22, 2021 and incorporated herein by reference.
(11)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 001-41655) filed with the SEC on November 5, 2024 and incorporated herein by reference.
(12)
Previously filed as an exhibit to the Company’s Quarterly Report on Form 10-Q (File No. 001-41655) filed with the SEC on November 13, 2024 and incorporated herein by reference.
(13)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 001-41655) filed with the SEC on September 29, 2025 and incorporated herein by reference.
(14)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 001-41655) filed with the SEC on October 15, 2025 and incorporated herein by reference.
(15)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 001-41655) filed with the SEC on November 21, 2025 and incorporated herein by reference.
(16)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 001-41655) filed with the SEC on April 6, 2026 and incorporated herein by reference
(17)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 001-41655) filed with the SEC on February 25, 2026 and incorporated herein by reference
(18)
Previously filed as an exhibit to the Company’s Annual Report on Form 10-K (File No. 000-55710) filed with the SEC on September 16, 2020 and incorporated herein by reference.
(19)
Previously filed as an exhibit to the Company’s Annual Report on Form 10-K (File No. 000-55710) filed with the SEC on September 8, 2021 and incorporated herein by reference.
(20)
Previously filed as an exhibit to the Company’s Post-Effective Amendment No. 1 to the Registration Statement on Form S-3 on Form S-1 (File No. 333-271268) filed with the SEC on August 22, 2023 and incorporated herein by reference.
(21)
Previously filed as an exhibit to the Company’s Quarterly Report on Form 10-Q (File No. 001-41655) filed with the SEC on November 13, 2025 and incorporated herein by reference.
(22)
Previously filed as an exhibit to the Company’s Registration Statement on Form S-1 (Registration No. 333-213451) filed with the SEC on September 2, 2016 and incorporated herein by reference.
(23)
Previously filed as an exhibit to Amendment No. 1 to the Company’s Annual Report on Form 10-K/A (File No. 000-55710) filed with the SEC on October 31, 2022 and incorporated herein by reference.
(24)
Previously filed as an exhibit to the Company’s Annual Report on Form 10-K (File No. 000-55710) filed with the SEC on August 29, 2017 and incorporated herein by reference.

108


 

(25)
Previously filed as an exhibit to the Company’s Current Report on Form 8-K (File No. 001-41655) filed with the SEC on September 11, 2024 and incorporated herein by reference.
(26)
Submitted Electronically Herewith. Attached as Exhibit 101 to this report are the following formatted in XBRL (Extensible Business Reporting Language): (i) the Consolidated Balance Sheets at June 30, 2026 and June 30, 2025, (ii) the Consolidated Statements of Operations and Comprehensive Loss for the years ended June 30, 2026 and 2025, (iii) the Consolidated Statements of Cash Flows for the years ended June 30, 2026 and 2025, (iv) the Consolidated Statements of Shareholders’ Equity and Redeemable Noncontrolling Interest for the years ended June 30, 2026 and 2025, (v) the Notes to the Consolidated Financial Statements.

ITEM 16. FORM 10–K SUMMARY

None.

109


 

SIGNATURES

Pursuant to the requirements of Section 13 or 15(d) of the Securities Exchange Act of 1934, the registrant has duly caused this report to be signed on its behalf by the undersigned, thereunto duly authorized.

 

 

NIOCORP DEVELOPMENTS LTD.

 

 

 

 

By:

/s/ Neal Shah

 

 

Neal Shah

Chief Financial Officer

 

September 25, 2026

Pursuant to the requirements of the Securities Exchange Act of 1934, this report has been signed below by the following persons on behalf of the registrant and in the capacities indicated on September 25, 2026.

 

Signature

 

Title

/s/ Mark A. Smith

 

President, Chief Executive Officer (Principal

Mark A. Smith

 

Executive Officer and Authorized U.S. Representative)

 

and Chairman of the Board of Directors

 

 

 

/s/ Neal Shah

 

Chief Financial Officer (Principal Financial and

Neal Shah

 

Accounting Officer)

 

 

 

/s/ Anthony W. Fulton

 

Director

Anthony W. Fulton

 

 

 

 

/s/ Nilsa Guerrero-Mahon

 

Director

Nilsa Guerrero-Mahon

 

 

 

 

 

/s/ Dean C. Kehler

 

Director

Dean C. Kehler

 

 

 

 

 

/s/ Michael G. Maselli

 

Director

Michael G. Maselli

 

 

 

 

 

/s/ Peter Oliver

 

Director

Peter Oliver

 

 

 

110


EX-4.29 2 nb-ex4_29.htm EX-4.29 EX-4.29

Exhibit 4.29

 

DESCRIPTION OF SECURITIES

 

Common Shares

The authorized capital of NioCorp Developments Ltd., a British Columbia corporation (the “Company”), consists of an unlimited number of common shares, without par value, of the Company (the “Common Shares”). The holders of Common Shares are entitled to receive notice of and attend all meetings of shareholders, with each Common Share held entitling the holder to one (1) vote on any resolution to be passed at such shareholder meetings. The holders of Common Shares are entitled to dividends if, as and when declared by the Company’s Board of Directors (the “Board”). The Common Shares are entitled, upon liquidation, dissolution, or winding up of the Company, to receive the remaining assets of the Company available for distribution to shareholders. There are no pre-emptive, conversion, or redemption rights attached to the Common Shares.

Exchange Controls

There are no governmental laws, decrees, or regulations in Canada that restrict the export or import of capital, including foreign exchange controls, or that affect the remittance of dividends, interest or other payments to non-resident holders of the securities of the Company, other than as discussed below and Canadian withholding tax. See “—Certain Canadian Federal Income Tax Considerations for U.S. Residents” below.

Competition Act

Limitations on the ability to acquire and hold Common Shares may be imposed by the Competition Act (Canada). This legislation permits the Commissioner of Competition of Canada (the “Commissioner”) to review any acquisition of a significant interest in the Company. This legislation grants the Commissioner jurisdiction to challenge such an acquisition before the Canadian Competition Tribunal if the Commissioner believes that it would, or would be likely to, result in a substantial lessening or prevention of competition in any market in Canada.

Investment Canada Act

The Investment Canada Act subjects an acquisition of control of a Canadian business by a non-Canadian to government notification or review depending on whether the relevant financial threshold (based on enterprise value or asset value of the company), as calculated pursuant to the legislation, is exceeded. A reviewable acquisition may not proceed unless the relevant minister is satisfied that the investment is likely to result in a net benefit to Canada. Under the national-security-review regime in the Investment Canada Act, review on a discretionary basis may also be undertaken by the federal government in respect of a broad range of investments by a non-Canadian. No financial threshold applies to a national security review. The relevant test is whether such investment by a non-Canadian could be “injurious to national security.”

Certain Canadian Federal Income Tax Considerations for U.S. Residents

The following generally summarizes certain Canadian federal income tax consequences generally applicable under the Income Tax Act (Canada) and the regulations enacted thereunder (collectively, the “Canadian Tax Act”) and the Canada-United States Tax Convention (1980) (the “Convention”) to the holding and disposition of Common Shares.

Comment is restricted to holders of Common Shares each of whom, at all material times for the purposes of the Canadian Tax Act and the Convention, (i) is resident solely in the U.S. for tax purposes, (ii) is a “qualifying person” under and entitled to the benefits of the Convention, (iii) holds all Common Shares as capital property, (iv) deals at arm’s length with and is not affiliated with the Company, (v) does not and is not deemed to use or hold any Common Shares in a business carried on in Canada (including an adventure or concern in the nature of trade), (vi) is not an insurer that carries on business in Canada and elsewhere, (vii) is not an “authorized foreign bank” (as defined in the Canadian Tax Act), (viii) has not entered into a “derivative forward agreement”, “synthetic equity arrangement” or

 


 

“synthetic disposition arrangement” (each as defined in the Canadian Tax Act) with respect to the Common Shares, and (ix) does not have and has not had, at any time, a “permanent establishment” (as defined in the Convention) of any kind in Canada (each such holder, a “U.S. Resident Holder”).

Certain U.S.-resident entities that are fiscally transparent for U.S. federal income tax purposes (including limited liability companies) may not in all circumstances be entitled to the benefits of the Convention. Members of or holders of an interest in such an entity that holds Common Shares should consult their own tax advisers regarding the extent, if any, to which the benefits of the Convention will apply to the entity in respect of its Common Shares.

Generally, a U.S. Resident Holder’s Common Shares will be considered to be capital property of such holder provided that the U.S. Resident Holder is not a trader or dealer in securities, did not acquire, hold, or dispose of the Common Shares in one or more transactions considered to be an adventure or concern in the nature of trade (i.e. speculation), and does not hold the Common Shares in the course of carrying on a business.

This summary is based on the current provisions of the Canadian Tax Act and the Convention in effect as of the date prior to the date hereof, all specific proposals to amend the Canadian Tax Act and the Convention publicly and officially announced by or on behalf of the Minister of Finance (Canada) prior to the date hereof (the “Tax Proposals”), and the current administrative policies and assessing practices of the Canada Revenue Agency (the “CRA”) published in writing and made publicly available by the CRA prior to the date hereof. This summary assumes that the Tax Proposals will be enacted as currently proposed, and that there will be no other material change to any applicable law or administrative policy or assessing practice, whether by way of judicial, legislative or governmental decision or action, although no assurance can be given in these respects. Except as otherwise expressly provided, this summary does not take into account any provincial, territorial, or foreign tax considerations, which may differ materially from those set out herein.

This summary is of a general nature only, is not exhaustive of all possible Canadian federal income tax considerations and is not intended to be and should not be construed as legal or tax advice to any particular U.S. Resident Holder, and no representations with respect to the tax consequences to any U.S. Resident Holder are made herein. The tax consequences of holding and disposing of Common Shares will vary according to the U.S. Resident Holder’s particular circumstances. U.S. Resident Holders are urged to consult their own tax advisers for advice with respect to their particular circumstances. The discussion below is qualified accordingly.

In general, for purposes of the Canadian Tax Act, all amounts relating to the holding or disposition of Common Shares must be converted into Canadian dollars based on the relevant exchange rate as determined in accordance with the Canadian Tax Act.

A U.S. Resident Holder generally will not be subject to tax under the Canadian Tax Act in respect of a capital gain realized on the disposition or deemed disposition of one or more Common Shares, nor will a capital loss arising therefrom be recognized under the Canadian Tax Act, unless such Common Shares constitute “taxable Canadian property” (as defined in the Canadian Tax Act) of the U.S. Resident Holder at the time of disposition and the U.S. Resident Holder is not entitled to relief under the Convention.

Generally, a U.S. Resident Holder’s Common Shares will not constitute “taxable Canadian property” of such holder at a particular time at which the Common Shares are listed on a “designated stock exchange” (which currently includes Nasdaq) unless at any time during the 60-month period that ends at the particular time both of the following conditions are concurrently met:

1.
25% or more of the issued shares of any class of the capital stock of the Company were owned by or belonged to one or any combination of:
(a)
the U.S. Resident Holder,
(b)
persons with whom the U.S. Resident Holder did not deal at arm’s length, and

 


 

(c)
partnerships in which the U.S. Resident Holder or a person referred to in clause (b) holds a membership interest directly or indirectly through one or more partnerships, and
2.
more than 50% of the fair market value of the Common Shares was derived directly or indirectly from, one or any combination of, real or immovable property situated in Canada, “Canadian resource properties” (as defined in the Canadian Tax Act), “timber resource properties” (as defined in the Canadian Tax Act), or options in respect of, or interests in, or for civil law rights in, any of the foregoing, whether or not the property exists.

Pursuant to Tax Proposals released by the Department of Finance (Canada) on July 23, 2026 (the “TCP Proposals”), shares that are listed on a designated stock exchange would be deemed to include an option, an interest or a right in such shares, whether or not such shares exist, such that any such options, interests or rights held by a U.S. Resident Holder would be included in determining whether such U.S. Resident Holder exceeds the 25% threshold described in (1) above. The TCP Proposals are proposed to come into force on Royal Assent.

Notwithstanding the foregoing, Common Shares may also be deemed to be “taxable Canadian property” in certain circumstances set out in the Canadian Tax Act.

U.S. Resident Holders whose Common Shares are or may be “taxable Canadian property” should consult their own tax advisors with respect to the tax and compliance considerations that may be relevant to them, including with respect to any potential relief under the Convention.

A U.S. Resident Holder to whom the Company pays or credits or is deemed to pay or credit a dividend on such holder’s Common Shares will be subject to Canadian withholding tax, and the Company will be required to withhold the tax from the dividend and remit it to the CRA for the holder’s account. The rate of withholding tax under the Canadian Tax Act is 25% of the gross amount of the dividend, but should generally be reduced under the Convention to 15% (or, if the U.S. Resident Holder is a company which is the beneficial owner of at least 10% of the voting stock of the Company, 5%) of the gross amount of the dividend. For this purpose, a company that is a resident of the U.S. for purposes of the Canadian Tax Act and the Convention and is entitled to the benefits of the Convention shall be considered to own the voting stock of the Company owned by an entity that is considered fiscally transparent under the laws of the U.S. and that is not a resident of Canada, in proportion to such company’s ownership interest in that entity.

Shareholder Rights Plan

On November 21, 2025, the Board approved the Company’s limited-duration shareholder rights plan (the “Rights Plan”) as set forth in the Shareholder Rights Plan Agreement, dated as of November 21, 2025 (the “Original Rights Plan Agreement”), by and between the Company and Computershare Investor Services Inc., as rights agent (or any successor rights agent) (the “Rights Agent”). The Board adopted the Rights Plan to help ensure that all shareholders of the Company are treated equally and fairly in the event of any unsolicited take-over bid or other attempt to acquire control of the Company (including by way of a “creeping take-over bid”). On April 6, 2026, following approval by the Company’s shareholders at the Company’s Annual Meeting of Shareholders, the Company entered into an Amended and Restated Shareholder Rights Plan Agreement (the “Amended Rights Plan Agreement”), by and between the Company and the Rights Agent, which amends and restates the Original Shareholder Rights Plan Agreement in its entirety.

Effective Date and Term

The Rights Plan originally became effective on November 21, 2025, after approval by the Board on November 21, 2025. As amended pursuant to the Amended Rights Plan Agreement, the Rights Plan will expire at 5:00 p.m. (Toronto time) on the date of the Company’s annual general meeting of shareholders held in 2027, or earlier upon the redemption of the Rights (as defined below), or provided that a Flip-in Event (as defined below) has not occurred, at such date or time as the Board may determine in its sole discretion (the “Expiration Time”).

 


 

Issue of Rights

At the close of business on December 4, 2025 (the “Record Time”), one right (a “Right”) was issued and attached to each Common Share outstanding as at the Record Time. Thereafter, one Right will attach to each Common Share issued after the Record Time and prior to the earlier of the Separation Time (as defined below) and the Expiration Time.

Rights Exercise Privilege

The Rights are not exercisable initially. The Rights generally separate from the Common Shares and become exercisable (A) ten trading days after the earlier of (i) the first date of public announcement or disclosure by the Company or an Acquiring Person (as defined in the Amended Rights Plan Agreement) of facts indicating that a person has become an Acquiring Person (such date being the “Stock Acquisition Date”), (ii) the date of the commencement of or first public announcement or disclosure of the current intention of any person (other than the Company or any of its subsidiaries) to commence a take-over bid which would result in such person becoming the Beneficial Owner (as defined in the Amended Rights Plan Agreement) of 20% or more of the outstanding Common Shares and any other shares in the capital of the Company entitled to vote generally in the election of directors (collectively, “Voting Shares”), other than pursuant to a Permitted Bid or a Competing Permitted Bid (each as defined below), and (iii) the date on which a Permitted Bid or a Competing Permitted Bid ceases to qualify as such, or (B) such later time as may be determined by the Board (in any such case, the “Separation Time”). From and after the Separation Time and prior to the Expiration Time, each Right will entitle the holder thereof to purchase one Common Share for the Exercise Price (as defined in the Amended Rights Plan Agreement) as at the business day immediately preceding the Separation Time, subject to certain adjustments, including in connection with a Flip-in Event, as described below. The transaction or event in or pursuant to which any Acquiring Person becomes the Beneficial Owner of 20% of the outstanding Voting Shares, other than by way of a Permitted Bid or a transaction otherwise permitted by the Rights Plan, is referred to as a “Flip-in Event.”

Any Rights held by an Acquiring Person (or any Affiliate or Associate (as each such term is defined in the Amended Rights Plan Agreement) of an Acquiring Person or any other person acting jointly or in concert with an Acquiring Person or any Affiliate or Associate of such other person) will become null and void upon the occurrence of a Flip-in Event. Ten trading days after the Stock Acquisition Date, each Right (excluding Rights held by an Acquiring Person (or any Affiliate or Associate of an Acquiring Person or any other person acting jointly or in concert with an Acquiring Person or any Affiliate or Associate of such other person or certain transferees) which have become void) will permit the purchase of that number of Common Shares having an aggregate Market Price (as defined in the Amended Rights Plan Agreement) on the date of consummation or occurrence of such Flip-in Event equal to twice the Exercise Price for an amount in cash equal to the Exercise Price. The “Exercise Price” is defined, for the period from and after the Separation Time, as an amount equal to three (3) times the Market Price per Common Share determined as at the Separation Time. For instance, if the Market Price at the Separation Time is $10 per share, the Exercise Price would be $30 and each Right would entitle the holder to acquire Common Shares having an aggregate Market Price on the date of consummation or occurrence of a Flip-in Event of $60 (i.e., twice the Exercise Price [2 x $30]) in exchange for cash consideration equal to the Exercise Price. In effect, each shareholder (other than an Acquiring Person (or any Affiliate or Associate of an Acquiring Person or any other person acting jointly or in concert with an Acquiring Person or any Affiliate or Associate of such other person or certain transferees)) will have the right, upon the occurrence of a Flip-in Event, to acquire six (6) Common Shares at a price equal to $30 (or 50% of the Market Price, as determined for the purposes of the Rights Plan), assuming the Market Price per Common Share on the date of consummation or occurrence of a Flip-in Event is $10.

The Amended Rights Plan Agreement provides for certain adjustments to the Exercise Price and the number of Rights outstanding upon the occurrence of certain events, including, without limitation, the declaration or payment of a stock dividend on the Common Shares, the subdivision or consolidation of the outstanding Common Shares, and the fixing of a record date for distributions to all holders of Common Shares.

Trading of Rights

Until the Separation Time, the Rights will be evidenced by the certificates or book entries representing the associated Common Shares and will be transferable only together with the associated Common Shares. Promptly

 


 

following the Separation Time, the Company will determine whether it wishes to issue separate certificates evidencing the Rights (“Rights Certificates”) or whether it will maintain the Rights in book entry form. If the Company decides to maintain Rights in book entry form, it will put in place such alternative procedures as are determined necessary in consultation with the Rights Agent for the Rights to be maintained in book entry form. In the event that the Company determines to issue Rights Certificates, then promptly following the Separation Time, Rights Certificates will be sent to holders of record of Common Shares (other than an Acquiring Person or certain transferees) as of the Separation Time. Rights Certificates will also be issued for Rights in respect of Common Shares issued after the Separation Time and before the Expiration Time, to each holder (other than an Acquiring Person or certain transferees) converting securities that are exchangeable for Common Shares after the Separation Time. Rights will trade separately from the Common Shares after the Separation Time.

Permitted Lock-up Agreements

A bidder may enter into lock-up agreements (a “Permitted Lock-Up Agreement”) with shareholders whereby such shareholders agree to deposit or tender their Voting Shares and/or Convertible Securities (as defined in the Amended Rights Plan Agreement) to a take-over bid (the “Lock-Up Bid”) without a Flip-in Event occurring, because such Voting Shares and/or Convertible Securities will not be deemed to be beneficially owned by the bidder for purposes of the Amended Rights Plan Agreement.

Such Permitted Lock-Up Agreement must be publicly disclosed and permit the shareholder to terminate its obligation to deposit or tender Voting Shares and/or Convertible Securities or not to withdraw its securities from the Permitted Lock-Up Agreement in order to deposit or tender the Voting Shares and/or Convertible Securities to another take-over bid or support another transaction that in either case (A)(i) will provide a greater price or value to the shareholder than the Lock-Up Bid or (ii) contains an offer price or value for each Voting Share or Convertible Security that exceeds by as much as or more than a specified amount, which specified amount may not be greater than 7% of the price or value to the shareholder of the Lock-Up Bid, and (B) if the number of Voting Shares or Convertible Securities to be purchased under the Lock-Up Bid is less than 100% of the Voting Shares or Convertible Securities held by Independent Shareholders (as defined below), the number of Voting Shares or Convertible Securities to be purchased under such other take-over bid or transaction at a price or value that is not less than the Lock-Up Bid (i) will be greater than the number of Voting Shares or Convertible Securities offered to be purchased under the Lock-Up Bid or (ii) exceeds the number of Voting Shares or Convertible Securities offered to be purchased under the Lock-Up Bid by as much or more than a specified amount, which specified amount may not be greater than 7% of the number of Voting Shares or Convertible Securities offered to be purchased under the Lock-Up Bid.

In addition, such Permitted Lock-Up Agreement must provide that no “break-up” fees, “top-up” fees, penalties, expenses or other amounts that exceed, in the aggregate, the greater of (i) the cash equivalent of 2.5% of the price or value of the consideration payable under the Lock-Up Bid to such shareholder and (ii) 50% of the increase in the consideration received under another take-over bid or transaction shall be payable by the shareholder if the shareholder fails to deposit or tender its securities to the Lock-Up Bid, withdraws Voting Shares and/or Convertible Securities previously deposited or tendered thereto or supports another transaction.

Permitted Bid Requirements

A “Permitted Bid” is a take-over bid, made by an Offeror (as defined below) by way of take-over bid circular, which also complies with the following additional provisions:

•
the take-over bid is made to all holders of Voting Shares on the books of the Company, other than the Offeror;
•
the take-over bid contains an irrevocable and unqualified provision that no Voting Shares and/or Convertible Securities will be taken up or paid for pursuant to the take-over bid unless more than 50% of the Voting Shares held by Independent Shareholders (i) shall have been deposited or tendered pursuant to the take-over bid and not withdrawn and (ii) have previously been or are taken up at the same time;
•
the take-over bid contains, and the take-up and payment for securities tendered or deposited is subject to, an irrevocable and unqualified provision that no Voting Shares and/or Convertible Securities will be taken up or paid for pursuant to the take-over bid prior to the close of business on the date that is not less than (i) 105

 


 

days following the date of the take-over bid or (ii) the last day of such shorter minimum deposit period for which a take-over bid (that is not exempt from any requirements of Division 5 (Bid Mechanics) of National Instrument 62-104 – Take-Over Bids and Issuer Bids (“NI 62-104”)) must remain open for deposits of securities, in the applicable circumstances at such time, pursuant to section 2.28.2 or section 2.28.3 of NI 62-104;
•
the take-over bid contains an irrevocable and unqualified provision that unless the take-over bid is withdrawn, Voting Shares and/or Convertible Securities may be deposited or tendered pursuant to such take-over bid at any time during the period of time between the date of the take-over bid and the date on which Voting Shares may be taken up and paid for and that any Voting Shares deposited pursuant to the take-over bid may be withdrawn until taken up and paid for; and
•
the take-over bid contains an irrevocable and unqualified provision that if, on the date on which Voting Shares may be taken up and paid for under the take-over bid, more than 50% of the Voting Shares held by Independent Shareholders have been deposited or tendered pursuant to the take-over bid and not withdrawn, the Offeror will make a public announcement of that fact and the take-over bid will remain open for deposits and tenders of Voting Shares and/or Convertible Securities for not less than ten days from the date of such public announcement.

For purposes of the Amended Rights Plan Agreement, (i) should a take-over bid which qualified as a Permitted Bid cease to be a Permitted Bid because it ceases to meet any or all of the requirements mentioned above prior to the time it expires (after giving effect to any extension) or is withdrawn, any acquisition of Voting Shares and/or Convertible Securities made pursuant to such take-over bid shall not be a Permitted Bid Acquisition (as defined in the Amended Rights Plan Agreement) and (ii) the term “Permitted Bid” shall include a Competing Permitted Bid.

“Independent Shareholders” is defined in the Amended Rights Plan Agreement as holders of outstanding Voting Shares, other than any Acquiring Person, any person that is making or has announced a current intention to make a take-over bid but only so long as the take-over bid so announced or made has not been withdrawn or terminated or has not expired (an “Offeror”) (other than a person who by virtue of the exception for investment advisors described below is not deemed to beneficially own the Voting Shares held by such person for purposes of the Amended Rights Plan Agreement), Affiliates or Associates of an Acquiring Person or Offeror, any person acting jointly or in concert with such Acquiring Person or Offeror (which excludes customary agreements with and between underwriters and/or banking group members and/or selling group members with respect to a distribution of securities of the Company, pledges of securities in the ordinary course of business and Permitted Lock-Up Agreements) and any employee benefit, deferred profit sharing plan, stock participation plan and any other similar plan or trust for the benefit of employees of the Company or a subsidiary, unless the beneficiaries of the plan or trust direct the manner in which the Voting Shares are to be voted or withheld from voting or direct whether the Voting Shares are to be deposited or tendered to a take-over bid.

The Rights Plan allows for a Competing Permitted Bid to be made while a Permitted Bid is in existence. A “Competing Permitted Bid” is a take-over bid that:

•
is made after a Permitted Bid or another Competing Permitted Bid has been made and prior to the expiry, termination or withdrawal of such Permitted Bid or Competing Permitted Bid;
•
complies with all of the provisions of a Permitted Bid other than the condition set forth in the third bullet of the definition of a Permitted Bid above; and
•
contains, and the take-up and payment for securities tendered or deposited is subject to, an irrevocable and unqualified provision that no Voting Shares will be taken up or paid for pursuant to the take-over bid prior to the close of business on the date that is no earlier than the date on which Voting Shares may be taken up under any Permitted Bid (determined as of the date of making the take-over bid, assuming no amendment or variation to the terms and satisfaction of all conditions to the completion of the Permitted Bid) that preceded the Competing Permitted Bid;

 


 

provided that, should a Competing Permitted Bid cease to be a Competing Permitted Bid because it ceases to meet any or all of the requirements mentioned above prior to the time it expires (after giving effect to any extension) or is withdrawn, then any acquisition of Voting Shares made pursuant to such Competing Permitted Bid, including any acquisition of Voting Shares made prior to such time, shall not be a Permitted Bid Acquisition.

Waiver

The Board, acting in good faith, may, until the occurrence of a Flip-in Event, waive the application of the Rights Plan to a particular Flip-in Event where it would occur by reason of a take-over bid which is made by a take-over bid circular sent to all holders of Voting Shares.

Where the Board exercises such waiver power for a particular Flip-in Event, the Board shall be deemed to have exercised such waiver power to any other Flip-in Events subsequently occurring by reason of a take-over bid which is made by means of a take-over bid circular to all holders of Voting Shares prior to the expiry of any other bid for which the Rights Plan is, or is deemed to have been, waived.

The Board may, in respect of any Flip-in Event, waive the application of the Rights Plan to a particular Flip-in Event where the Board has determined within ten trading days following a Stock Acquisition Date that the Acquiring Person became an Acquiring Person by inadvertence and without any intent or knowledge that it would become an Acquiring Person and such person has reduced its beneficial ownership within fourteen days after the foregoing determination by the Board such that it is no longer an Acquiring Person.

The Board, acting in good faith, may, with the approval of a majority of votes cast by the Independent Shareholders voting in person or by proxy at a meeting duly called for that purpose, determine, at any time prior to the occurrence of a Flip-in Event, to waive the application of the Rights Plan for any Flip-in Event.

Redemption

The Board, with prior approval of the holders of Voting Shares or the holders of Rights, at any time prior to the occurrence of a Flip-in Event, may redeem all of the then outstanding Rights at a price of $0.00001 each, subject to adjustment.

Amendment

The Board may amend the Amended Rights Plan Agreement with the prior approval of the holders of Voting Shares (or holders of Rights if the Separation Time has occurred).

The Board, without such approval, may make amendments to the Amended Rights Plan Agreement to correct any clerical or typographical error, which are required to maintain the validity of the Amended Rights Plan Agreement as a result of any change in any applicable legislation or regulations or rules thereunder, or to cure any ambiguity, to correct or supplement any provision therein which may be defective or inconsistent with any other provision therein, or to make any other provisions with respect to matters or questions arising thereunder, provided that such action shall not adversely affect the interests of the holders of Voting Shares or Rights in any material respect.

Exception for Investment Advisors

Investment managers (for client accounts), trust companies (acting in their capacity as trustees or administrators or in a similar capacity), statutory bodies managing investment funds (for employee benefit plans, pension plans, insurance plans or various public bodies) and registered pension funds or plans and their administrators or trustees who become the Beneficial Owner of 20% or more of the outstanding Voting Shares are exempted from triggering a Flip-in Event, provided that they are not making and have not announced an intention to make, a take-over bid, alone or by acting jointly or in concert with any other person.

 


 

Warrants

From time to time, the Company has outstanding Common Share purchase warrants (“Warrants”), with each Warrant exercisable for one Common Share. Except with respect to pre-funded Warrants, the exercise price per Common Share and the number of Common Shares issuable upon exercise of Warrants is subject to adjustment upon the occurrence of certain events, including, but not limited to, the following:

•
the subdivision or re-division of the outstanding Common Shares into a greater number of Common Shares;
•
the reduction, combination or consolidation of the outstanding Common Shares into a lesser number of Common Shares;
•
the issuance of Common Shares or securities exchangeable for, or convertible into, Common Shares to all or substantially all of the holders of Common Shares by way of stock dividend or other distribution (other than a distribution of Common Shares upon the exercise of Warrants or any outstanding options);
•
the reorganization of the Company or the consolidation or merger or amalgamation of the Company with or into another corporate body; and
•
a reclassification or other similar change to the outstanding Common Shares.

The Company generally will issue the Common Shares issuable upon exercise of Warrants within five business days following its receipt of notice of exercise and payment of the exercise price, subject to surrender of the Warrants. Prior to the exercise of any Warrants, holders of the Warrants will not have any of the rights of holders of the Common Shares issuable upon exercise, including the right to vote or to receive any payments of dividends on the Common Shares issuable upon exercise.

NioCorp Assumed Warrants

On March 17, 2023, the Company closed a series of transactions (the “GXII Transaction”) pursuant to the Business Combination Agreement, dated as of September 25, 2022 (the “Business Combination Agreement”), by and among the Company, GX Acquisition Corp. II, a Delaware corporation (“GXII”), and Big Red Merger Sub Ltd., a Delaware corporation and a direct, wholly owned subsidiary of the Company. In connection with the closing of the GXII Transaction (the “GXII Closing”), pursuant to the Business Combination Agreement, the Company assumed GXII’s obligations under the Warrant Agreement, dated March 17, 2021 (the “GXII Warrant Agreement”), by and between GXII and Continental Stock Transfer & Trust Company (“CST”), as warrant agent, and each share purchase warrant of GXII thereunder (the “GXII Warrants”) that was issued and outstanding immediately prior to the March 17, 2023 was converted into one Warrant (the “NioCorp Assumed Warrants”) pursuant to the GXII Warrant Agreement, as amended by an Assignment, Assumption and Amendment Agreement, dated the March 17, 2023 (the GXII Warrant Agreement, as so amended, the “NioCorp Assumed Warrant Agreement”), among the Company, GXII, CST, as existing warrant agent, and Computershare Inc. and its affiliate Computershare Trust Company, N.A, together as successor warrant agent (the “NioCorp Assumed Warrant Agent”). In connection with the GXII Closing, NioCorp issued (a) 9,999,959 public NioCorp Assumed Warrants in respect of the GXII Warrants that were publicly traded prior to the GXII Closing and (b) 5,666,667 NioCorp Assumed Warrants to GX Sponsor II LLC (the “Sponsor”) in respect of the GXII Warrants that it held prior to the GXII Closing, which NioCorp Assumed Warrants were subsequently distributed by the Sponsor to its members in connection with the GXII Closing.

Both the public NioCorp Assumed Warrants and the NioCorp Assumed Warrants issued to the Sponsor are subject to the terms of the NioCorp Assumed Warrant Agreement and are identical, with certain exceptions applicable to the NioCorp Assumed Warrants issued to the Sponsor for so long as such NioCorp Assumed Warrants are held by the Sponsor, its members, or their respective affiliates and other permitted transferees. In accordance with the NioCorp Assumed Warrant Agreement, any NioCorp Assumed Warrants issued to the Sponsor that are held by someone other than the Sponsor, its members, or their respective affiliates and other permitted transferees, are treated as public NioCorp Assumed Warrants.

 


 

Each NioCorp Assumed Warrant is exercisable on and after April 16, 2023, until its expiration for 1.11829212 Common Shares at a price of $11.50 per 1.11829212 Common Shares (subject to adjustments for stock splits, stock dividends, reorganizations, recapitalizations and the like). Under the terms of NioCorp Assumed Warrant Agreement, for so long as the NioCorp Assumed Warrants issued to the Sponsor are held by the Sponsor, its members, or their respective affiliates and other permitted transferees, such holders have the right to elect to exercise those NioCorp Assumed Warrants on a cashless basis. For such NioCorp Assumed Warrants exercised on a cashless basis after the GXII Closing, the holder will be entitled to pay the exercise price for those NioCorp Assumed Warrants by surrendering all or portion of the cash and/or Common Shares (valued at their fair market value) into which those NioCorp Assumed Warrants are exercisable as shall be elected by the holder. For this purpose, Common Shares so surrendered will be deemed to have a “fair market value” equal to the average reported last sale price of the Common Shares for the 10 trading days ending on the third trading day prior to the date of exercise of the applicable NioCorp Assumed Warrants.

The NioCorp Assumed Warrants will expire at 5:00 p.m., New York City time, on March 17, 2028, or earlier upon redemption or liquidation.

The Company will not be obligated to deliver any Common Shares pursuant to the exercise of a NioCorp Assumed Warrant and will have no obligation to settle such exercise unless a registration statement under the Securities Act with respect to the Common Shares underlying the NioCorp Assumed Warrants is then effective and a prospectus relating thereto is current, subject to the Company satisfying its obligations described below with respect to registration. No NioCorp Assumed Warrant will be exercisable and the Company will not be obligated to issue Common Shares upon exercise of a NioCorp Assumed Warrant unless Common Shares issuable upon such exercise have been registered, qualified or deemed to be exempt under the securities laws of the state of residence of the registered holder of the NioCorp Assumed Warrants. In the event that the conditions in the two immediately preceding sentences are not satisfied with respect to a NioCorp Assumed Warrant, the holder of such NioCorp Assumed Warrant will not be entitled to exercise such NioCorp Assumed Warrant and such NioCorp Assumed Warrant may have no value and expire worthless. In no event will the Company be required to net cash settle any NioCorp Assumed Warrant.

The NioCorp Assumed Warrants, and the underlying Common Shares issuable upon the exercise thereof, were registered under the Securities Act pursuant to the Company’s registration statement on Form S-4, originally filed on November 7, 2022, as subsequently amended, which was declared effective by the SEC on February 8, 2023. The ongoing registered offering of the Common Shares underlying the NioCorp Assumed Warrants is being conducted pursuant to the Company’s registration statement on Form S-3, originally filed on April 14, 2023, as subsequently post-effectively amended to convert such registration statement to Form S-1, which was declared effective on October 30, 2023.

The Company will have the right to call the public NioCorp Assumed Warrants for redemption at any time following the March 17, 2023:

•
in whole and not in part;
•
at a price of $0.01 per NioCorp Assumed Warrant;
•
upon not less than 30 days’ prior written notice of redemption (the “30-day redemption period”) to each public NioCorp Assumed Warrant holder;
•
if, and only if, the reported last sale price of the Common Shares equals or exceeds approximately $16.10 per share (subject to certain adjustments) for any 20 trading days within a 30-trading day period commencing once the NioCorp Assumed Warrants become exercisable and ending three business days before the Company sends the notice of redemption to the public NioCorp Assumed Warrant holders; and
•
if there is an effective registration statement covering the Common Shares issuable upon exercise of the NioCorp Assumed Warrants, and a current prospectus relating thereto, available throughout the 30-day redemption period.

 


 

The NioCorp Assumed Warrants issued to the Sponsor are not redeemable by the Company for so long as such NioCorp Assumed Warrants are held by the Sponsor, its members, or their respective affiliates or other permitted transferees. In addition, the Company may not exercise its redemption right if the issuance of Common Shares upon exercise of the NioCorp Assumed Warrants is not exempt from registration or qualification under applicable state blue sky laws or the Company is unable to effect such registration or qualification.

If the Company calls the public NioCorp Assumed Warrants for redemption as described above, the Company will have the option to require any holder that wishes to exercise its public NioCorp Assumed Warrant to do so on a “cashless basis.” In determining whether to require all holders to exercise their public NioCorp Assumed Warrants on a “cashless basis,” the Company will consider, among other factors, its cash position, the number of NioCorp Assumed Warrants that are outstanding and the dilutive effect on the Company’s shareholders of issuing the maximum number of Common Shares issuable upon the exercise of the NioCorp Assumed Warrants. If the Company takes advantage of this option, all holders of public NioCorp Assumed Warrants would pay the exercise price by surrendering their NioCorp Assumed Warrants for that number of Common Shares equal to the quotient obtained by dividing (x) the product of the number of Common Shares underlying the public NioCorp Assumed Warrants, multiplied by the difference between the exercise price of the NioCorp Assumed Warrants and the “fair market value” (defined below) by (y) the fair market value. The “fair market value” shall mean the average reported last sale price of the Common Shares for the 10 trading days ending on the third trading day prior to the date on which the notice of redemption is sent to the holders of public NioCorp Assumed Warrants. If the Company takes advantage of this option, the notice of redemption will contain the information necessary to calculate the number of Common Shares to be received upon exercise of the NioCorp Assumed Warrants, including the “fair market value” in such case. Requiring a cashless exercise in this manner will reduce the number of Common Shares to be issued and thereby lessen the dilutive effect of a redemption of the public NioCorp Assumed Warrants. If the Company calls the public NioCorp Assumed Warrants for redemption and does not take advantage of this option, the Sponsor, its members, and their respective affiliates and other permitted transferees would still be entitled to exercise their NioCorp Assumed Warrants for cash or on a cashless basis using the same formula described above that other NioCorp Assumed Warrant holders would have been required to use had all NioCorp Assumed Warrant holders been required to exercise their NioCorp Assumed Warrants on a cashless basis, as described in more detail below.

A holder of a NioCorp Assumed Warrant may notify the Company in writing in the event it elects to be subject to a requirement that such holder will not have the right to exercise such NioCorp Assumed Warrant, to the extent that after giving effect to such exercise, such holder (together with such holder’s affiliates), to the NioCorp Assumed Warrant Agent’s actual knowledge, would beneficially own in excess of 4.9% or 9.8% (or such other amount as a holder may specify) of the Common Shares outstanding immediately after giving effect to such exercise.

The NioCorp Assumed Warrants have certain anti-dilution and adjustments rights upon certain events.

The NioCorp Assumed Warrants may be exercised upon surrender of the certificate representing such NioCorp Assumed Warrants on or prior to the expiration date at the offices of the NioCorp Assumed Warrant Agent, with the exercise form on the reverse side of such certificate completed and executed as indicated, accompanied by full payment of the exercise price (or on a cashless basis, if applicable), by certified or official bank check payable to the order of the NioCorp Assumed Warrant Agent or by wire transfer, for the number of NioCorp Assumed Warrants being exercised. The NioCorp Assumed Warrant holders will not have the rights or privileges of holders of Common Shares or any attendant voting rights until they exercise their NioCorp Assumed Warrants and receive Common Shares. After the issuance of Common Shares upon exercise of the NioCorp Assumed Warrants, each holder will be entitled to one (1) vote for each Common Share held of record on all matters to be voted on by NioCorp shareholders.

If, upon exercise of the NioCorp Assumed Warrants, a holder would be entitled to receive a fractional interest in a share, the Company will, upon exercise, round down to the nearest whole number of Common Shares to be issued to the NioCorp Assumed Warrant holder.

The NioCorp Assumed Warrants were issued in registered form under the NioCorp Assumed Warrant Agreement. The NioCorp Assumed Warrant Agreement may be amended by the parties thereto without the consent of any registered holder (i) for the purpose of curing any ambiguity, or curing, correcting or supplementing any mistake, or adding or changing any other provisions with respect to matters or questions arising under NioCorp Assumed Warrant Agreement as the parties may deem necessary or desirable and that the parties deem shall not adversely affect the

 


 

interest of the registered holders of the NioCorp Assumed Warrants, and (ii) to provide for the delivery of such kind and amount of Common Shares or other securities or property (including cash) receivable upon a reclassification, reorganization, merger or consolidation, or upon a dissolution following any such sale or transfer, that the holder of NioCorp Assumed Warrants would have received if such holder had exercised his, her or its NioCorp Assumed Warrants immediately prior to such event. All other modifications or amendments, including any amendment to increase the warrant price or shorten the exercise period, shall require the vote or written consent of the registered holders of a majority of the then outstanding public NioCorp Assumed Warrants. Any amendment solely to the NioCorp Assumed Warrants issued to the Sponsor and that are held by the Sponsor, its members, or their respective affiliates or other permitted transferees, shall require the vote or written consent of a majority of the holders of the then outstanding NioCorp Assumed Warrants issued to the Sponsor.

 

 


EX-10.14 3 nb-ex10_14.htm EX-10.14 EX-10.14

 

 

 

EXHIBIT 10.14

 

EXECUTION VERSION

 

EMPLOYMENT AGREEMENT

 

THIS EMPLOYMENT AGREEMENT, by and between Elk Creek Resources Corporation, a corporation, with its principal place of business located at 386 Broadway,

P.O. Box 506, Tecumseh, NE 68450, and any successor entity thereto (the “Company”), and Ernest Cleave (“Executive”), is dated as of the 1st day of July, 2026 (the “Agreement”).

WHEREAS, the Company wishes to continue to employ Executive on the terms and conditions, and for the consideration, hereinafter set forth, and Executive desires to continue to be employed by the Company on such terms and conditions and for such consideration; and

WHEREAS, concurrently with this Agreement, Executive is receiving a copy of the Restrictive Covenant Agreement attached hereto as Exhibit A (the “Restrictive Covenant Agreement”) which includes a covenant not to compete that could restrict Executive’s options with respect to subsequent employment following the termination of Executive’s employment from the Company (or an affiliate thereof); and

WHEREAS, Executive shall have a period of fifteen (15) days from the date of this Agreement to review and execute the Restrictive Covenant Agreement.

NOW THEREFORE, in consideration of the promises provided for in this Agreement, the Company and Executive agree as follows:

1.
Employment Period. Subject to Executive’s execution of the Restrictive Covenant Agreement prior to the Effective Date (as defined below), this Agreement shall become effective upon execution. Except as otherwise provided in Section 3 of this Agreement, the Company hereby agrees to continue to employ Executive, and Executive hereby agrees to continue to be employed by the Company, on an at-will basis on the terms and conditions set forth herein for the period commencing on the Effective Date and ending on Executive’s Date of Termination (as defined in Section 3(f)) (the “Employment Period”).
2.
Terms of Employment.
(a)
Position and Duties.
(i)
During the Employment Period, Executive shall (A) serve as the Senior Vice President Business Development of NioCorp with such duties and responsibilities as are customarily commensurate with or incident to such positions for entities similar in size to, and in a business similar to that of, NioCorp and the Company, respectively, (B) report to the Chief Executive Officer of NioCorp, and (C) perform Executive’s services at the Company’s principal place of business in Centennial, Colorado (subject to reasonable travel requirements commensurate with Executive’s position).

 


 

 

 

 

 

(ii)
During the Employment Period, and excluding any periods of vacation and sick leave to which Executive is entitled, Executive agrees to devote Executive’s full business time and attention to the business and affairs of the Company. During the Employment Period, it will not be a violation of this Agreement for Executive to (A) serve on civic or charitable boards or committees, (B) deliver lectures, fulfill speaking engagements or teach at educational institutions and (C) manage personal investments, so long as such activities described in clauses (A), (B) and (C) do not significantly interfere with the performance of Executive’s responsibilities as an employee of the Company in accordance with this Agreement. Executive shall not during the Employment Period serve as a director or executive of another corporation without the prior written approval of the Chief Executive Officer of NioCorp.
(b)
Compensation.
(i)
Base Salary. During the Employment Period, Executive shall receive an annual base salary (“Annual Base Salary”) of $275,000 paid in accordance with the normal payroll practices of the Company as may be in effect from time to time, which Annual Base Salary shall be reviewed for increase at least annually.
(ii)
Employee Benefits. During the Employment Period, Executive shall be eligible to participate in the employee benefit plans, programs, and policies, as may be in effect from time to time, for senior executives of the Company generally, including, but not limited to, any annual cash bonus plan and/or any annual long-term incentive compensation program as may be established by the Company.
(iii)
Expenses. During the Employment Period, Executive shall be entitled to receive prompt reimbursement for all reasonable expenses incurred by Executive in accordance with the performance of Executive’s duties under this Agreement and in accordance with the Company’s business expense reimbursement policy.
3.
Termination of Employment.
(a)
Death or Disability. Executive’s employment shall terminate automatically if Executive dies during the Employment Period. If the Company determines in good faith that the Disability (as defined herein) of Executive has occurred during the Employment Period (pursuant to the definition of “Disability” set forth below), it may give to Executive written notice in accordance with Section 13(b) of its intention to terminate Executive’s employment. In such event, Executive’s employment with the Company shall terminate effective on the thirtieth (30th) day after receipt of such notice by Executive (the “Disability Effective Date”), provided that, within the thirty (30) days after such receipt, Executive shall not have returned to full-time performance of Executive’s duties. “Disability” means the absence of Executive from Executive’s duties with the Company on a full-time basis

 


 

 

 

 

 

for ninety (90) consecutive business days, or ninety (90) business days during any period of one hundred and twenty (120) consecutive business days, as a result of incapacity due to mental or physical illness that is determined to be total and permanent by a physician selected by the Company or its insurers and acceptable to Executive or Executive’s legal representative (such agreement as to acceptability not to be unreasonably withheld).
(b)
By the Company. The Company may terminate Executive’s employment during the Employment Period for any, or no reason, with or without Cause. For purposes of this Agreement, “Cause” will be deemed to exist upon:
(i)
any use or misappropriation by Executive of the funds, assets or property of the Company, its parent, an affiliate or a subsidiary for any personal or other improper purpose;
(ii)
any act of moral turpitude, dishonesty, fraud by or felony conviction of Executive whether or not such acts were committed in connection with the business of the Company, an affiliate or a subsidiary;
(iii)
any failure by Executive substantially to perform the lawful instructions of the person(s) to whom Executive reports (other than as a result of total or partial incapacity due to physical or mental illness) following written notice by the Company to Executive of such failure and fifteen (15) days within which to cure such failure;
(iv)
any willful or gross misconduct by Executive in connection with Executive’s duties to the Company which, in the reasonable good faith judgment of the Board of Directors of NioCorp, could reasonably be expected to be materially injurious to the financial condition or business reputation of the Company, its subsidiaries or affiliates;
(v)
any failure by Executive to follow a material Company policy;
(vi)
any material breach by Executive of this Agreement; or
(vii)
any breach by Executive of the Restrictive Covenant Agreement.
(c)
By Executive. Executive’s employment may be terminated during the Employment Period by Executive for any reason.
(d)
Notice of Termination. Any termination of employment by the Company for Cause shall be communicated by Notice of Termination to Executive given in accordance with Section 13(b) of this Agreement. “Notice of Termination” means a written notice that (i) indicates the specific termination provision in this Agreement relied upon, (ii) to the extent applicable, sets forth in reasonable detail the facts and circumstances claimed to provide a basis for termination of Executive’s employment under the provision so indicated, and (iii) if the Date of Termination (as defined herein) is other than the date of

 


 

 

 

 

 

receipt of such notice, specifies the Date of Termination (which Date of Termination shall be not more than thirty (30) days after the giving of such notice). The failure by the Company to set forth in the Notice of Termination any fact or circumstance that contributes to a showing of Cause shall not waive any right the Company hereunder or preclude the Company from asserting such fact or circumstance in enforcing the Company’s rights hereunder.
(e)
Resignation. Upon any termination of Executive’s employment with the Company for any reason, Executive agrees to resign, as of the date of such termination and to the extent applicable, as an officer of the Company and/or any of the Company’s subsidiaries and other affiliates.

 

(f)
Date of Termination. “Date of Termination” means: (i) if Executive’s employment is terminated by the Company for Cause, the date of receipt of the Notice of Termination or such later date specified in the Notice of Termination, as the case may be, (ii) if Executive’s employment is terminated by the Company other than for Cause or Disability, the date on which the Company notifies Executive of such termination, (iii) if Executive resigns, the date on which Executive notifies the Company of such termination, and (iv) if Executive’s employment is terminated by reason of death or Disability, the date of Executive’s death or the Disability Effective Date, as the case may be. Notwithstanding the foregoing, in no event shall the Date of Termination occur until Executive experiences a “separation from service” within the meaning of Section 409A of the Internal Revenue Code of 1986, as amended (the “Code”), and the date on which such separation from service takes place shall be the “Date of Termination.”
4.
Obligations of the Company upon Termination.
(a)
By the Company other than for Cause, Death or Disability. If, during the Employment Period, the Company terminates Executive’s employment without Cause (other than due to death or Disability), and Section 4(b) does not apply:
(i)
The Company shall pay to Executive, in a lump sum in cash within thirty (30) days after the Date of Termination (or earlier, if required by applicable law), the aggregate of the following amounts: the sum of: (A) Executive’s Annual Base Salary through the Date of Termination to the extent not theretofore paid; (B) Executive’s business expenses that are reimbursable pursuant to Section 2(b)(iii) of this Agreement but have not been reimbursed by the Company as of the Date of Termination; and (C) any accrued and unused vacation pay or paid time off to the extent not theretofore paid (the sum of the amounts described in subclauses (A), (B), and (C), the “Accrued Obligations”);
(ii)
Subject to Section 4(e) and Section 10(b), the Company shall continue to pay Executive the Annual Base Salary as in effect at the time of such termination for a period of twelve (12) months following such termination in

 


 

 

 

 

 

accordance with the Company’s normal payroll practices; and
(iii)
To the extent not theretofore paid or provided, the Company shall timely pay or provide to Executive any Other Benefits (as defined in Section 5) in accordance with the terms of the underlying plans or agreements.

Other than as set forth in this Section 4(a), in the event of a termination of Executive’s employment by the Company without Cause (other than due to death or Disability) and Section 4(b) does not apply, the Company shall have no further obligation to Executive under this Agreement.

 

(b)
Termination in Connection With a Change in Control. If, during the Employment Period, the Company terminates Executive’s employment without Cause (other than due to death or Disability) or Executive terminates employment for Good Reason (as defined below), in each case, within a period of two years after a Change in Control (as defined below) (such termination hereinafter referred to as a “Change in Control Termination”):
(i)
The Company shall pay to Executive, in a lump sum in cash within thirty (30) days after the Date of Termination, subject to Section 10(b), the Accrued Obligations;
(ii)
Subject to Section 10(b), on the sixty-first (61st) day after the Date of Termination, the Company shall, subject to Section 4(e), pay to Executive a lump sum cash amount equal to two (2) times Executive’s Annual Base Salary as in effect at the time of such termination (without regard to any reduction thereto); and
(iii)
To the extent not theretofore paid or provided, the Company shall timely pay or provide to Executive any Other Benefits (as defined in Section 5) in accordance with the terms of the underlying plans or agreements.

Other than as set forth in this Section 4(b), in the event of a termination of Executive’s employment by the Company without Cause (other than due to death or Disability) (and Section 4(a) does not apply) or by Executive for Good Reason, in each case, within a period of two (2) years after a Change in Control, the Company shall have no further obligation to Executive under this Agreement.

 

(c)
Death or Disability. If Executive’s employment is terminated by reason of Executive’s death or Disability during the Employment Period, the Company shall provide Executive or, in the event of death, Executive’s estate or beneficiaries, with the Accrued Obligations and the timely payment or delivery of the Other Benefits in accordance with the terms of the underlying plans or agreements, and shall have no further obligations under this Agreement. The Accrued Obligations shall be paid to Executive or, in the event of death, Executive’s estate or beneficiaries, in a lump sum in cash within thirty (30) days of the applicable Date of Termination.
(d)
Cause; Other than for Good Reason Following a Change in Control. If Executive’s employment is terminated for Cause during the Employment Period, the Company shall provide

 


 

 

 

 

 

Executive with Executive’s Annual Base Salary through the Date of Termination, and the timely payment or delivery of the Other Benefits in accordance with the terms of the underlying plans or agreements, and shall have no further obligations under this Agreement. If Executive voluntarily terminates employment for any reason (other than for Good Reason within two (2) years after a Change in Control as provided in Section 4(b)) during the Employment Period, the Company shall provide to Executive the Accrued Obligations and the timely payment or delivery of the Other Benefits in accordance with the terms of the underlying plans or agreements, and shall have no further obligations under this Agreement. In such case, all the Accrued Obligations shall be paid to Executive in a lump sum in cash within thirty (30) days of the Date of Termination.
(e)
Release. Notwithstanding anything herein to the contrary, the Company shall not be obligated to make any payment under Sections 4(a)(ii) or 4(b)(ii) of this Agreement unless (i) prior to the sixtieth (60th) day following the Date of Termination, Executive executes a release of claims against the Company and its affiliates in a form provided by the Company (the “Release”), and (ii) any applicable revocation period has expired during such sixty (60)-day period without Executive revoking such Release.

 

(f)
Definition of Change in Control. For purposes of this Agreement, a “Change in Control” will be deemed to have occurred upon the occurrence (after the Effective Date) of any transaction that constitutes a “change in ownership,” a “change in effective control,” or a “change in the ownership of a substantial portion of the assets” of the Company under Section 409A(a)(2)(A)(v) of the Code.
(g)
Definition of Good Reason. For purposes of this Agreement, “Good Reason” shall mean, in the absence of the prior written consent of Executive:
(i)
a material reduction of Executive’s Annual Base Salary;
(ii)
relocation of Executive’s primary workplace, as assigned to Executive by the Company in accordance with Section 2(a)(i)(C) beyond a 50 mile radius from such workplace; or
(iii)
any other material breach by the Company of this Agreement;

provided, however, that Executive’s termination of employment shall not be deemed to be for Good Reason unless (A) Executive has notified the Company in writing describing the occurrence of one or more Good Reason events within ninety (90) days of such occurrence, (B) the Company fails to cure such Good Reason event within thirty (30) days after its receipt of such written notice and (C) the termination of employment occurs within one hundred and eighty (180) days after the occurrence of the applicable Good Reason event.

 

5.
Non-Exclusivity of Rights. Amounts that Executive is otherwise entitled to receive under any plan, policy, practice or program of or any other contract or agreement with the

 


 

 

 

 

 

Company at or subsequent to the Date of Termination (“Other Benefits”) shall be payable in accordance with such plan, policy, practice or program or contract or agreement, except as explicitly modified by this Agreement. Notwithstanding the foregoing, Executive shall not be eligible to participate in any other severance plan, program or policy of the Company.
6.
Set-off; No Mitigation. The Company’s obligation to make the payments provided for in this Agreement and otherwise to perform its obligations hereunder shall be subject to set- off, counterclaim, recoupment, defense, or other claim, right or action that the Company may have against Executive to the extent such set-off or other action does not violate Section 409A of the Code. In no event shall Executive be obligated to seek other employment or take any other action by way of mitigation of the amounts payable to Executive under any of the provisions of this Agreement; provided, however, that it is expressly understood that the Company’s payment obligations under Sections 4(a)(ii) and 4(b)(ii) of this Agreement shall cease in the event Executive breaches any of the terms contained in the Restrictive Covenant Agreement.
7.
Limitations on Payments Under Certain Circumstances. Notwithstanding any provision of any other plan, program, arrangement or agreement to the contrary, in the event that it shall be determined that any payment or benefit to be provided by the Company to Executive pursuant to the terms of this Agreement or any other payments or benefits received or to be received by Executive (a “Payment”) in connection with or as a result of any event which is deemed by the U.S. Internal Revenue Service or any other taxing authority to constitute a change in the ownership or effective control of the Company, or in the ownership of a substantial portion of the assets of the Company and subject to the tax (the “Excise Tax”) imposed by Section 4999 (or any successor section) of the Code, the Payments, whether under this Agreement or otherwise, shall be reduced so that the Payment, in the aggregate, is reduced to the greatest amount that could be paid to Executive without giving rise to any Excise Tax; provided that in the event that Executive would be placed in a better after-tax position after receiving all Payments and not having any reduction of Payments as provided hereunder, Executive shall, notwithstanding the provisions of any other plan, program, arrangement or agreement to the contrary, receive all Payments and pay any applicable Excise Tax. All determinations under this Section 7 shall be made by a nationally recognized accounting firm selected by the Company (the “Accounting Firm”). Without limiting the generality of the foregoing, any determination by the Accounting Firm under this Section 7 shall take into account the value of any reasonable compensation for services to be rendered by Executive (or for holding oneself out as available to perform services and refraining from performing services (such as under a covenant not to compete)). If the Payments are to be reduced pursuant to this Section 7, the Payments shall be reduced in the following order: (a) Payments which do not constitute “nonqualified deferred compensation” subject to Section 409A of the Code shall be reduced first; and (b) all other Payments shall then be reduced, in each case as follows: (i) cash payments shall be reduced before non-cash payments and (ii) payments to be made on a later payment date shall be reduced before payments to be made on an earlier payment date.

 

8.
Successors.

 


 

 

 

 

 

(a)
This Agreement is personal to Executive and without the prior written consent of the Company shall not be assignable by Executive otherwise than by will or the laws of descent and distribution. This Agreement shall inure to the benefit of, and be enforceable by, Executive’s legal representatives.
(b)
This Agreement shall inure to the benefit of and be binding upon the Company and its successors and assigns. As set forth in the preamble, as used in this Agreement, “Company” shall mean the Company as hereinbefore defined and any successor to its business and/or assets as aforesaid which assumes and agrees to perform this Agreement by operation of law, or otherwise.
9.
Indemnification. The Company shall indemnify Executive to the maximum extent permitted under applicable law for acts taken within the scope of Executive’s employment and Executive’s service as an officer or director of the Company or any of its subsidiaries or affiliates. To the extent that the Company obtains coverage under a director and officer indemnification policy, Executive will be entitled to such coverage on a basis that is no less favorable than the coverage provided to any other officer or director of the Company.
10.
Section 409A of the Code.
(a)
The intent of the parties is that payments and benefits under this Agreement comply with, or be exempt from, Section 409A of the Code and the regulations and guidance promulgated thereunder (collectively “Section 409A”) and, accordingly, to the maximum extent permitted, this Agreement shall be interpreted to be in compliance therewith.
(b)
Notwithstanding any provision of this Agreement to the contrary, in the event that Executive is a “specified employee” within the meaning of Section 409A (as determined in accordance with the methodology established by the Company as in effect on the Date of Termination) (a “Specified Employee”), any payments or benefits that are considered non- qualified deferred compensation under Section 409A payable under this Agreement on account of a “separation from service” during the six-month period immediately following the Date of Termination shall, to the extent necessary to comply with Section 409A, instead be paid, or provided, as the case may be, on the first business day after the date that is six months following Executive’s “separation from service” within the meaning of Section 409A. For purposes of Section 409A, Executive’s right to receive any installment payments pursuant to this Agreement shall be treated as a right to receive a series of separate and distinct payments. In no event may Executive, directly or indirectly, designate the calendar year of any payment to be made under this Agreement that is considered nonqualified deferred compensation, subject to Section 409A.
(c)
With regard to any provision herein that provides for reimbursement of costs and expenses or in-kind benefits that are deferred compensation subject to Section 409A, (i) the right to reimbursement or in-kind benefits shall not be subject to liquidation or exchange for another benefit, (ii) the amount of expenses eligible for reimbursement, or in-kind benefits, provided during any taxable year shall not affect the expenses eligible for reimbursement, or in-kind benefits to be provided, in any other taxable year and (iii) such payments shall be made on or before the last day of Executive’s taxable year following the taxable year in which the expense occurred.

 


 

 

 

 

 

11.
Compensation Recovery Policy. Notwithstanding anything in this Agreement to the contrary, Executive acknowledges and agrees that this Agreement and any compensation described herein are subject to the terms and conditions of the Company’s clawback policy (if any) as may be in effect from time to time, including specifically to implement Section 10D of the Securities Exchange Act of 1934, as amended, and any applicable rules or regulations promulgated thereunder (including applicable rules and regulations of any national securities exchange on which the shares of the Company’s common stock may be traded) (the “Compensation Recovery Policy”), and that applicable sections of this Agreement and any related documents shall be deemed superseded by and subject to the terms and conditions of the Compensation Recovery Policy from and after the effective date thereof.
12.
Complete Agreement. This Agreement sets forth the entire agreement of the parties hereto in respect of the subject matter contained herein, and supersedes all prior agreements, promises, covenants, arrangements, communications, representations or warranties, whether oral or written, by any officer, employee or representative of any party hereto in respect of the subject matter contained herein.
13.
Miscellaneous.
(a)
This Agreement shall be governed by and construed in accordance with the laws of the State of Colorado, without reference to principles of conflict of laws. Executive agrees that the state and federal courts located in the State of Colorado shall have jurisdiction in any action, suit or proceeding against Executive based on or arising out of this Agreement and Executive hereby:

(i) submits to the personal jurisdiction of such courts; (ii) consents to service of process in connection with any action, suit or proceeding against Executive; and (iii) waives any other requirement (whether imposed by statute, rule of court or otherwise) with respect to personal jurisdiction, venue or service of process. The captions of this Agreement are not part of the provisions hereof and shall have no force or effect. This Agreement may not be amended or modified otherwise than by a written agreement executed by the parties hereto or their respective successors and legal representatives.

(b)
All notices and other communications hereunder shall be in writing and shall be given by hand delivery to the other party or by registered or certified mail, return receipt requested, or nationally-recognized overnight courier service, postage prepaid, addressed as follows:

If to Executive: At the most recent address on file at the Company.

If to the Company: 7000 South Yosemite Street, Suite 115

Centennial, CO 80112

 

or such other address as either party shall have furnished to the other in writing in accordance herewith (including via electronic mail). Notice and communications shall be effective when actually received by the addressee.

(c)
The invalidity or unenforceability of any provision of this Agreement shall not

 


 

 

 

 

 

affect the validity or enforceability of any other provision of this Agreement.
(d)
The Company, its subsidiaries and affiliates may withhold from any amounts payable under this Agreement such Federal, state, local or foreign taxes or social security charges as shall be required to be withheld pursuant to any applicable law or regulation. None of the Company, its subsidiaries or affiliates guarantees any tax result with respect to payments or benefits provided hereunder. Executive is responsible for all taxes owed with respect to all such payments and benefits.
(e)
Subject to any limits on applicability contained therein, the Restrictive Covenant Agreement shall survive and continue in full force in accordance with its terms notwithstanding any termination or expiration of the Employment Period.
(f)
During Executive’s employment with the Company and thereafter, Executive will provide reasonable assistance to the Company in litigation and regulatory matters that relate to events that occurred during Executive’s period of employment with the Company and its predecessors, and will provide reasonable assistance to the Company with matters relating to its corporate history from the period of Executive’s employment with it or its predecessors. Executive will be entitled to reimbursement of reasonable out-of-pocket travel or related costs and expenses relating to any such cooperation or assistance that occurs following the Date of Termination.
(g)
This Agreement may be executed in several counterparts, each of which shall be deemed to be an original but all of which together will constitute one and the same instrument.
(h)
Executive’s or the Company’s failure to insist upon strict compliance with any provision of this Agreement or the failure to assert any right Executive or the Company may have hereunder shall not be deemed to be a waiver of such provision or right or any other provision or right of this Agreement.
(i)
With respect to any controversy or claim arising out of or relating to or concerning injunctive relief for Executive’s breach or purported breach of the Restrictive Covenant Agreement, the Company shall have the right, in addition to any other remedies it may have, to seek specific performance and injunctive relief with a court of competent jurisdiction, without the need to post a bond or other security.
14.
Other Acknowledgements. Nothing in this Agreement prevents Executive from providing, without prior notice to the Company, information to governmental authorities regarding possible legal violations or otherwise testifying or participating in any investigation or proceeding by any governmental authorities regarding possible legal violations.

[Remainder of page intentionally left blank]

 


 

 

 

 

 

IN WITNESS WHEREOF, Executive and the Company have executed this Agreement on the date first above written.

EXECUTIVE

 

/s/ Ernest Cleave

Ernest Cleave

 

 

ELK CREEK RESOURCES CORPORATION

 

 

By /s/ Mark Smith

Name: Mark Smith

Title: Chief Executive Officer

 


 

 

 

 

 

Exhibit A

Restrictive Covenant Agreement (See attached.)

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 


 

 

 

 

 

RESTRICTIVE COVENANT AGREEMENT

 

THIS RESTRICTIVE COVENANT AGREEMENT (this “Agreement”) is made and entered into as of July 1, 2026 by and between Elk Creek Resources Corporation, a Delaware corporation, with its principal place of business located at 386 Broadway, P.O. Box 506, Tecumseh, NE 68450, and any successor entity thereto (the “Company”), and Ernest Cleave (“Executive”). This Agreement shall become effective upon execution.

In consideration of the mutual covenants contained herein and other good and valuable consideration (including as set forth in the Employment Agreement between the Company and Executive dated as of July 1, 2026 (the “Employment Agreement”)), the receipt and sufficiency of which are hereby acknowledged, the parties hereto agree as follows:

1.
Competitive Activity; Confidentiality; Nonsolicitation.
(a)
Acknowledgements and Agreements. Executive hereby acknowledges and agrees that in the performance of Executive’s duties to the Company during the Employment Period (as defined in the Employment Agreement), Executive shall be brought into frequent contact with existing and potential customers of the Company throughout the world. Executive also agrees that trade secrets and confidential information of the Company, more fully described in Section 1(h) gained by Executive during Executive’s association with the Company, have been developed by the Company through substantial expenditures of time, effort and money and constitute valuable and unique property of the Company. Executive further understands and agrees that the foregoing makes it necessary for the protection of the Company’s business that Executive not compete with the Company during Executive’s employment with the Company and not compete with the Company for a reasonable period thereafter, as further provided in the following sections.
(b)
Covenants.
(i)
Covenants During Employment. Except for permitted activities expressly approved by the Board, while employed by the Company, Executive will not compete with the Company anywhere in the world. In accordance with this restriction, but without limiting its terms, while employed by the Company, Executive will not:
(A)
enter into or engage in any business which competes with the Company’s business;

 

(B)
solicit customers, business, patronage or orders for, or sell, any products or services in competition with, or for any business that competes with, the Company’s business; divert, entice or otherwise take away any customers, business, patronage or orders of the Company or attempt to do so; or
(C)
promote or assist, financially or otherwise, any person, firm, association, partnership, corporation or other entity engaged in any business which competes with the Company’s business.

 

 

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(ii)
Covenants Following Termination. For a period of (x) one (1) year following the date of termination of Executive’s employment with the Company for any reason other than a Change in Control Termination (as such term is defined in the Employment Agreement) or (y) two (2) years following the date of termination of Executive’s employment with the Company in the event of a Change in Control Termination (such period of time, the “Post-Termination Restricted Period”), Executive will not:

 

(A)
enter into or engage in any business which competes with the Company’s Business within the Restricted Territory (as hereinafter defined);

 

(B)
solicit customers, business, patronage or orders for, or sell, any products or services in competition with, or for any business, wherever located, that competes with, the Company’s Business within the Restricted Territory;

 

(C)
divert, entice or otherwise take away any customers, business, patronage or orders of the Company within the Restricted Territory, or attempt to do so; or
(D)
promote or assist, financially or otherwise, any person, firm, association, partnership, corporation or other entity engaged in any business which competes with the Company’s Business within the Restricted Territory.

 

(iii)
Indirect Competition. For the purposes of Sections 1(a) and (b) above, inclusive, but without limitation thereof, Executive will be in violation thereof if Executive engages in any or all of the activities set forth therein directly as an individual on Executive’s own account, or indirectly as a partner, joint venturer, employee, agent, salesperson, consultant, officer and/or director of any firm, association, partnership, corporation or other entity, or as a stockholder of any corporation in which Executive or Executive’s spouse, child or parent owns, directly or indirectly, individually or in the aggregate, more than 5% of the outstanding stock.

 

(c)
The “Company.” For purposes of this Section 1, the “Company” shall include any and all direct and indirect subsidiaries, parents, and affiliated, or related companies of the Company for which Executive worked or had responsibility, or with respect to which Executive had access to trade secrets or confidential information at the time of termination of Executive’s employment and at any time during the two (2) year period prior to such termination.
(d)
The Company’s “Business.” For the purposes of this Section 1, the Company’s “Business” is defined to be the acquisition, exploration, and development of mineral properties, as further described in any and all manufacturing, marketing and sales manuals and materials of the Company as the same may be altered, amended, supplemented or otherwise changed from time to

 

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time, or of any other products or services substantially similar to or readily substitutable for any such described products and services.
(e)
“Restricted Territory.” For purposes of Section 1, the Restricted Territory shall be defined as and limited to:
(i)
the geographic area(s) within a 100 mile radius of any and all of the Company’s location(s) in, to, or for which Executive worked, to which Executive was assigned or had any responsibility (either direct or supervisory) at the time of termination of Executive’s employment and at any time during the two-year period prior to such termination;

 

(ii)
the United States; and

 

(iii)
all of the specific customer accounts, whether within or outside of the geographic area described in (i) and (ii) above, with which Executive had any contact or for which Executive had any responsibility (either direct or supervisory) at the time of termination of Executive’s employment and at any time during the two-year period prior to such termination.

 

(f)
Extension. If it shall be judicially determined that Executive has violated any of Executive’s obligations under Section 1(b), then the period applicable to each obligation that Executive shall have been determined to have violated shall automatically be extended by a period of time equal in length to the period during which such violation(s) occurred.
(g)
Non-Solicitation. Executive will not directly or indirectly at any time during the period of Executive’s employment or thereafter, attempt to disrupt, damage, impair or interfere with the Company’s business by raiding any of the Company’s employees or soliciting any of them to resign from their employment with the Company, or by disrupting the relationship between the Company and any of its consultants, agents or representatives. Executive acknowledges that this covenant is necessary to enable the Company to maintain a stable workforce and remain in business.
(h)
Further Covenants.
(i)
Executive will keep in strict confidence and shall not, directly or indirectly, at any time during or after Executive’s employment with the Company, disclose, furnish, disseminate, make available or, except in the course of performing Executive’s duties of employment, use any trade secrets or confidential business and technical information of the Company or its customers or vendors, without limitation as to when or how Executive may have acquired such information. Such confidential information shall include, without limitation, the Company’s unique selling, manufacturing and servicing methods and business techniques, training, service and business manuals, promotional materials, training courses and other training and instructional materials, vendor and product information, customer and prospective customer lists, other customer and prospective customer information, employee evaluation and employee performance information, and other business information. Executive specifically acknowledges that all such confidential information, whether reduced to writing,

 

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maintained on any form of electronic media, or maintained in Executive’s mind or memory and whether compiled by the Company, and/or Executive, derives independent economic value from not being readily known to or ascertainable by proper means by others who can obtain economic value from its disclosure or use, that reasonable efforts have been made by the Company to maintain the secrecy of such information, that such information is the sole property of the Company and that any retention and use of such information by Executive during Executive’s employment with the Company (except in the course of performing Executive’s duties and obligations to the Company) or after the termination of Executive’s employment shall constitute a misappropriation of the Company’s trade secrets. The restrictions set forth in this Section 1(h) shall be perpetual for all confidential information that is a trade secret, or for so long as the information remains a trade secret under applicable law. The restrictions set forth in this Section 1(h) shall last for ten (10) years after termination, for all other forms of confidential information.
(ii)
Executive agrees that upon termination of Executive’s employment with the Company for any reason, Executive shall return to the Company, in good condition, all property of the Company, including without limitation, the originals and all copies of any materials which contain, reflect, summarize, describe, analyze or refer or relate to any items of information listed in this Section 1(h) of this Agreement. In the event that such items are not so returned, the Company will have the right to charge Executive for all reasonable damages, costs, attorneys’ fees and other expenses incurred in searching for, taking, removing and/or recovering such property.

 

(iii)
The U.S. Defend Trade Secrets Act of 2016 (“DTSA”) provides that an individual shall not be held criminally or civilly liable under any federal or state trade secret law for the disclosure of a trade secret that (A) is made in confidence to a federal, state or local government official, either directly or indirectly, or to an attorney, and solely for the purpose of reporting or investigating a suspected violation of law; or (B) is made in a complaint or other document filed in a lawsuit or other proceeding, if such filing is made under seal. In addition, the DTSA provides that an individual who files a lawsuit for retaliation by an employer for reporting a suspected violation of law may disclose the trade secret to the attorney of the individual and use the trade secret information in the court proceeding, if the individual files any document containing the trade secret under seal and does not disclose the trade secret, except pursuant to court order.

 

(i)
Discoveries and Inventions; Work Made for Hire.
(i)
During the period of Executive’s employment Executive agrees that upon conception and/or development of any idea, discovery, invention, improvement, software, writing or other material or design that (A) relates to the business of the Company, or (B) relates to the Company’s actual or demonstrably anticipated research or development, or (C) results from any work performed by Executive for the Company, Executive hereby assigns to the Company the entire right, title and interest in and to any such idea,

 

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discovery, invention, improvement, software, writing or other material or design. Executive has no obligation to assign any idea, discovery, invention, improvement, software, writing or other material or design that Executive conceives and/or develops entirely on Executive’s own time without using the Company’s equipment, supplies, facilities, or trade secret information unless the idea, discovery, invention, improvement, software, writing or other material or design either: (x) relates to the business of the Company, or (y) relates to the Company’s actual or demonstrably anticipated research or development, or (z) results from any work performed by Executive for the Company. Executive agrees that any idea, discovery, invention, improvement, software, writing or other material or design that relates to the business of the Company or relates to the Company’s actual or demonstrably anticipated research or development which is conceived or suggested by Executive, either solely or jointly with others, within one (1) year following termination of Executive’s employment shall be presumed to have been so made, conceived or suggested in the course of such employment with the use of the Company’s equipment, supplies, facilities, and/or trade secrets.
(ii)
In order to determine the rights of Executive and the Company in any idea, discovery, invention, improvement, software, writing or other material, and to insure the protection of the same, Executive agrees that during Executive’s employment, and for one (1) year after termination of Executive’s employment Executive will disclose immediately and fully to the Company any idea, discovery, invention, improvement, software, writing or other material or design conceived, made or developed by Executive solely or jointly with others. The Company agrees to keep any such disclosures confidential. Executive also agrees to record descriptions of all work in the manner directed by the Company and agrees that all such records and copies, samples and experimental materials will be the exclusive property of the Company. Executive agrees that at the request of and without charge to the Company, but at the Company’s expense, Executive will execute a written assignment of the idea, discovery, invention, improvement, software, writing or other material or design to the Company and will assign to the Company any application for letters patent or for trademark registration made thereon, and to any common-law or statutory copyright therein; and that Executive will do whatever may be necessary or desirable to enable the Company to secure any patent, trademark, copyright, or other property right therein in the United States and in any foreign country, and any division, renewal, continuation, or continuation in part thereof, or for any reissue of any patent issued thereon. In the event the Company is unable, after reasonable effort, and in any event after ten (10) business days, to secure Executive’s signature on a written assignment to the Company of any application for letters patent or to any common-law or statutory copyright or other property right therein, whether because of Executive’s physical or mental incapacity or for any other reason whatsoever, Executive irrevocably designates and appoints the Corporate Secretary of the Company as Executive’s attorney-in-fact to act on Executive’s behalf to execute and file any such application and to do all other lawfully permitted acts to further the prosecution and issuance of such letters

 

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patent, copyright or trademark.

 

 

(iii)
Executive acknowledges that, to the extent permitted by law, all work papers, reports, documentation, drawings, photographs, negatives, tapes and masters therefor, prototypes and other materials (hereinafter, “items”), including without limitation, any and all such items generated and maintained on any form of electronic media, generated by Executive during Executive’s employment with the Company will be considered a “work made for hire” and that ownership of any and all copyrights in any and all such items will belong to the Company. The item shall recognize the Company as the copyright owner, will contain all proper copyright notices, e.g., “(creation date) NioCorp Developments Ltd., All Rights Reserved,” and shall be in condition to be registered or otherwise placed in compliance with registration or other statutory requirements throughout the world.
(j)
Non-Disparagement.
(i)
Throughout Executive’s employment with the Company and during the Post-Termination Restricted Period, outside the ordinary course of business on behalf of the Company, Executive will not make or issue, or procure any person, firm, or entity to make or issue, any statement in any form, including written, oral and electronic communications of any kind, which conveys negative or adverse information concerning the Company or its subsidiaries or affiliates, or any of their legal predecessors, successors, assigns, parents, subsidiaries, divisions or other affiliates, or any of the foregoing’s respective past, present or future directors, officers, employees or representatives (collectively, the “Non-Disparagement Parties”), or any Non-Disparagement Party’s business, or its actions, to any person or entity, regardless of the truth or falsity of such statement. Throughout Executive’s employment with the Company and during the Post-Termination Restricted Period, the Company will reasonably direct the executive officers and directors of the Company not make or issue, or procure any person, firm, or entity to make or issue, any statement in any form, including written, oral and electronic communications of any kind, which conveys negative or adverse information concerning Executive or any of Executive’s legal successors, assigns, or other affiliates, or any of the foregoing’s respective past, present or future directors, officers, employees or representatives (collectively, the “Executive Non-Disparagement Parties”), or any Executive Non-Disparagement Party’s business, or its actions, to any person or entity, regardless of the truth or falsity of such statement.
(ii)
This Section 1(j) does not apply to truthful testimony or disclosure compelled or required by applicable law or legal process. Notwithstanding anything in this Agreement to the contrary, Executive is not prohibited from providing information voluntarily to the Securities and Exchange Commission pursuant to Section 21F of the Securities Exchange Act of 1934, as amended.
(k)
Communication of Contents of Agreement. While employed by the Company and for two (2) years thereafter, Executive will communicate the contents of Section 1 of this Agreement to any person, firm, association, partnership, corporation or other entity that Executive intends to be employed by, associated with, or represent.

 

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(l)
Confidentiality Agreements. Executive agrees that Executive shall not disclose to the Company or induce the Company to use any secret or confidential information belonging to Executive’s former employers. Executive warrants that Executive is not bound by the terms of a confidentiality agreement or other agreement with a third party that would preclude or limit Executive’s right to work for the Company and/or to disclose to the Company any ideas, inventions, discoveries, improvements or designs or other information that may be conceived during employment with the Company. Executive agrees to provide the Company with a copy of any and all agreements with a third party that preclude or limit Executive’s right to make disclosures or to engage in any other activities contemplated by Executive’s employment with the Company.
(m)
Remedies. The parties acknowledge and agree that any breach by Executive of the terms of this Agreement may cause the Company irreparable harm and injury for which money damages would be inadequate. Accordingly, the Company, in addition to any other remedies available at law or equity, shall be entitled, as a matter of right, to injunctive relief in any court of competent jurisdiction. The parties agree that such injunctive relief may be granted without the necessity of proving actual damages. Nothing in this Agreement shall limit the Company’s remedies under state for federal law or elsewhere.
(n)
Reasonableness. Executive acknowledges and agrees that Executive received the notice required by Colo. Rev. Stat. Ann. § 8-2-113. Executive acknowledges that Executive’s obligations under this Section 1 are reasonable in the context of the nature of the Company’s business and the competitive injuries likely to be sustained by the Company if Executive were to violate such obligations and that these obligations do not place an undue burden on Executive. Executive further acknowledges that this Agreement is made in consideration of, and is adequately supported by the agreement of the Company to perform its obligations under this Agreement and by other consideration, including Executive’s continued employment with the Company, which Executive acknowledges constitutes good, valuable and sufficient consideration. It is the desire and intent of the parties hereto that the provisions of this Agreement shall be enforced to the fullest extent legally-permissible. Accordingly, if any particular provision(s) of this Agreement shall be adjudicated to be invalid or unenforceable, the court may modify or sever such provision(s), such modification or deletion to apply only with respect to the operation of such provision(s) in the particular jurisdiction in which such adjudication is made. In addition, if any one or more of the provisions contained in this Agreement shall for any reason be held to be excessively broad as to duration, geographical scope, activity or subject, it shall be construed by limiting and reducing it, so as to be enforceable to the extent compatible with the applicable law as it shall then appear. The remaining provisions of this Agreement shall remain in full force and effect.
2.
Choice of Law. This Agreement shall be governed by, and construed in accordance with, the internal, substantive laws of the State of Colorado. Executive agrees that the state and federal courts located in the State of Colorado shall have jurisdiction in any action, suit or proceeding against Executive based on or arising out of this Agreement and Executive hereby:

(a) submits to the personal jurisdiction of such courts; (b) consents to service of process in connection with any action, suit or proceeding against Executive; and (c) waives any other requirement (whether imposed by statute, rule of court or otherwise) with respect to personal jurisdiction, venue or service of process.

3.
Notices. Any notice provided to the Company provided for in this Agreement shall be in writing to the Company, marked Attention: Corporate Secretary, and any notice to Executive shall be addressed to said Executive at Executive’s address on file with the Company.

 

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Except as otherwise provided herein, any written notice shall be deemed to be duly given if and when delivered personally or deposited in the United States mail, first class registered mail, postage and fees prepaid, and addressed as aforesaid. Any party may change the address to which notices are to be given hereunder by written notice to the other party as herein specified (provided that for this purpose any mailed notice shall be deemed given on the third business day following deposit of the same in the United States mail).
4.
Headings. The headings herein have been inserted for convenience only and shall not be deemed to limit or otherwise affect any of the provisions of this Agreement.
5.
Counterparts; Effectiveness. This Agreement may be executed in one or more counterparts (including counterparts transmitted by facsimile or Adobe PDF attached to an email), each of which shall be deemed an original and all of which shall constitute one and the same agreement. The exchange of copies of this Agreement and executed signature pages hereto by facsimile or in Adobe PDF attached to an email shall constitute effective execution and delivery of this Agreement and may be used in lieu of the original Agreement for all purposes.
6.
Amendment and Waiver. The provisions of this Agreement may be amended or waived only with the prior written consent of the Company and Executive, and no course of conduct or failure or delay in enforcing the provisions of this Agreement shall affect the validity, binding effect or enforceability of this Agreement.
7.
Complete Agreement. This Agreement and the Employment Agreement embody the complete agreement and understanding between the parties with respect to the subject matter hereof and shall supersede all other agreements or arrangements between the parties with regard to the subject matter hereof and effective as of their dates supersede and preempt any prior understandings, agreements or representations by or between the parties, written or oral, which may have related to the subject matter hereof in any way. Notwithstanding the foregoing, this Agreement does not supersede or in any way limit or otherwise affect any restrictive covenants to which Executive may be bound, pursuant to another agreement or otherwise. Those restrictive covenants would be enforceable separately in accordance with their terms.
8.
Prevailing Party’s Litigation Expenses. In the event of litigation between the Company and Executive related to this Agreement, the non-prevailing party shall reimburse the prevailing party for any costs and expenses (including, without limitation, attorneys’ fees) reasonably incurred by the prevailing party in connection therewith.
9.
Successors and Assigns. This Agreement shall bind and inure to the benefit of and be enforceable by Executive, the Company and their respective heirs, executors, personal representatives, successors and assigns by merger or consolidation, except that Executive may not assign any rights or delegate any obligations hereunder without the prior written consent of the Company. As set forth in the preamble, as used in this Agreement, “Company” shall mean the Company as hereinbefore defined and any successor to the Company by merger or consolidation or purchase of all or substantially all of the Company’s assets which assumes the liabilities of the Company hereunder. Executive hereby consents to the assignment by the Company of all of its rights and obligations hereunder to any successor to the Company by merger or consolidation or purchase of all or substantially all of the Company’s assets, provided such transferee or successor assumes the liabilities of the Company hereunder.

 

20


 

 

 

 

 

 

 

10.
Severability. Whenever possible, each provision of this Agreement shall be interpreted in such manner as to be effective and valid under applicable law, but if any provision of this Agreement is held to be invalid or unenforceable in any respect under any applicable law, such invalidity or unenforceability shall not affect any other provision, but this Agreement shall be reformed, construed and enforced as if such invalid or unenforceable provision had never been contained herein.
11.
Other Acknowledgements. Nothing in this Agreement prevents Executive from providing, without prior notice to the Company, information to governmental authorities regarding possible legal violations or otherwise testifying or participating in any investigation or proceeding by any governmental authorities regarding possible legal violations.

[Remainder of page intentionally left blank]

 

21


 

 

 

 

 

IN WITNESS WHEREOF, Executive and the Company have executed this Agreement on the date first above written.

EXECUTIVE

 

/s/ Ernest Cleave

Ernest Cleave

 

 

ELK CREEK RESOURCES CORPORATION

 

 

By /s/ Mark Smith

Name: Mark Smith

Title: Chief Executive Officer

 


EX-10.17 4 nb-ex10_17.htm EX-10.17 EX-10.17

 

EXHIBIT 10.17

NIOCORP DEVELOPMENTS LTD.
Long Term Incentive Plan

Option Certificate

This Certificate is issued pursuant to the provisions of the NioCorp Developments Ltd. (the “Issuer”) Long Term Incentive Plan (the “Plan”) and evidences that [NAME] is the holder (the “Option Holder”) of an option (the “Option”) to purchase up to [# Options] Common shares (the “Shares”) in the capital stock of the Issuer at a purchase price of US$[0.00] per Share. Subject to the provisions of the Plan:

(a)
the Award Date of this Option is [DATE];
(b)
the Expiry Date of this Option is [DATE];
(c)
this Option vests upon the following schedule
(i)
(ii)
(iii)
(d)
this is an [ Incentive Stock Options (ISO) / Non-Qualified Option (NQO) ]; and
(e)
this Option terminates 90 days after the Option Holder ceases to be an eligible person to receive Options under the Plan.

This Option may be exercised at any time and from time to time from and including the Award Date through to and including up to 4:30 local time in Denver, Colorado on the Expiry Date by delivery to the Administrator of the Plan an Exercise Notice, in the form provided in the Plan, together with this Certificate and a certified cheque or bank draft payable to “NioCorp Developments Ltd.” in an amount equal to the aggregate of the Exercise Price of the Shares in respect of which this Option is being exercised.

This Certificate and the Option evidenced hereby is not assignable, transferable or negotiable and is subject to the detailed terms and conditions contained in the Plan, the terms and conditions of which the Option Holder hereby expressly agrees with the Issuer to be bound by. This Certificate is issued for convenience only and in the case of any dispute with regard to any matter in respect hereof, the provisions of the Plan and the records of the Issuer shall prevail.

The foregoing Option has been awarded this [X] day of [MONTH YEAR].

NIOCORP DEVELOPMENTS LTD.

 

Per: _____________
Administrator, Stock Option Plan
NioCorp Developments Ltd.

 

 


EX-21.1 5 nb-ex21_1.htm EX-21.1 EX-21.1

 

Exhibit 21.1

List of Subsidiaries of NioCorp Developments Ltd. (the “Company”)

Name

State/Province of
Formation

Ownership

0896800 B.C. Ltd. (“0896800”)

British Columbia

100%

Elk Creek Resources Corp.

Delaware

81.33%(1)

NioCorp Advanced Metals and Alloys, LLC

 

Delaware

 

100%

NioCorp Technologies Limited

United Kingdom

100%

 

(1)

 Represents 100% of Class A common stock owned by 0896800, and 3,516,140 Vested Shares and 3,391,596 Earnout Shares (each as defined in the Company’s Annual Report on Form 10-K for the year ended June 30, 2026) held by third parties, and outstanding as of June 30, 2026.


EX-23.1 6 nb-ex23_1.htm EX-23.1 EX-23.1

 

EXHIBIT 23.1

 

CONSENT OF INDEPENDENT REGISTERED PUBLIC ACCOUNTING FIRM

We consent to the incorporation by reference in Registration Statement Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541, and 333-271266 on Form S-1, Nos. 333-280176 and 333-290837 on Form S-3 and Nos. 333-290671 and 333-222313 on Form S-8 of our report dated September 25, 2026, relating to the financial statements of NioCorp Developments Ltd. appearing in this Annual Report on Form 10-K for the year ended June 30, 2026.

/s/ DELOITTE & TOUCHE LLP

Denver, Colorado

September 25, 2026


EX-23.2 7 nb-ex23_2.htm EX-23.2 EX-23.2

EXHIBIT 23.2

img73087251_0.jpg

 

 

CONSENT OF QUALIFIED PERSON

 

Dahrouge Geological Consulting USA Ltd. hereby consents to the public filing of Sections 1.1 to 1.5, 1.7, 1.12, 1.17, 2, 3, 4, 5, 6, 7, 8, 9, 11, 16, 20, 22.1, 22.7, 23.1, 23.9, 24 and 25 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

Dahrouge Geological Consulting USA Ltd. also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

Dahrouge Geological Consulting USA Ltd. also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

Dahrouge Geological Consulting USA Ltd. also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

Dahrouge Geological Consulting USA Ltd. certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 

 


 

Signed and dated this 25th day of September, 2026 at Centennial, Colorado.

/s/Trevor Mills
Trevor Mills, P.G., SME-RM
Principal Geologist / US Operations Manager
Dahrouge Geological Consulting USA Ltd.

 


EX-23.3 8 nb-ex23_3.htm EX-23.3 EX-23.3

img74010772_0.jpg EXHIBIT 23.3

 

 

CONSENT OF QUALIFIED PERSON

 

SMH Process Innovation hereby consents to the public filing of Sections 1.6, 1.6.2, 1.10, 10, 10.1, 10.3, 14.1, 14.2, 14.2.2, 14.3, 14.3.2, 14.4, 14.4.2, 14.5, 14.5.2, 14.6, 14.6.2, 22.3, 22.4, 23.2 and 23.6 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

SMH Process Innovation also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

SMH Process Innovation also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

SMH Process Innovation also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

SMH Process Innovation certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 


 

Signed and dated this 25th day of September, 2026 at Salt Lake City, Utah.

/s/Eric Larochelle
Eric Larochelle, B. Eng.
Owner

SMH Process Innovation

 


EX-23.4 9 nb-ex23_4.htm EX-23.4 EX-23.4

EXHIBIT 23.4

img74934293_0.jpg

CONSENT OF QUALIFIED PERSON

Dumas Contracting USA Inc. hereby consents to the public filing of Sections 13.4.5, 13.5.2, 13.7, 13.8, 13.9, 15.2.3, 15.2.4 and 15.6.1 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

Dumas Contracting USA Inc. also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

Dumas Contracting USA Inc. also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

Dumas Contracting USA Inc. also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

Dumas Contracting USA Inc. certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 

 


 

Signed and dated this 25th day of September, 2026 at Timmins, Ontario, Canada.

/s/Tony Linton
Tony Linton, FEC, P.Eng.
Director, Engineering & Technical Services
Dumas Contracting USA Inc.

 


EX-23.5 10 nb-ex23_5.htm EX-23.5 EX-23.5

img75857814_0.jpg EXHIBIT 23.5

 

 

CONSENT OF QUALIFIED PERSON

 

Amplify Mine Planning LLC hereby consents to the public filing of Sections 1.8, 1.9, 12, 13.1, 13.4, 13.4.1, 13.4.2, 13.4.3, 13.4.4, 13.5, 13.5.1, 13.5.3, 13.5.4, 13.6, 13.6.1, 13.6.2, 13.6.3, 13.6.6, 22.2 and 23.4 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

Amplify Mine Planning LLC also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

Amplify Mine Planning LLC also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

Amplify Mine Planning LLC also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

Amplify Mine Planning LLC certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 


 

Signed and dated this 25th day of September, 2026 at Centennial, Colorado.

/s/Scott Britton
Scott Britton, P.E.
Principal Consulting Engineer
Amplify Mine Planning LLC

 


EX-23.6 11 nb-ex23_6.htm EX-23.6 EX-23.6

img76781335_0.gif EXHIBIT 23.6

 

CONSENT OF QUALIFIED PERSON

 

BBA Consultants International LP hereby consents to the public filing of Sections 1.11.1, 15.8, 15.9, 15.10, 15.11, 15.12, and 22.5.1 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

BBA Consultants International LP also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

BBA Consultants International LP also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

BBA Consultants International LP also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

BBA Consultants International LP certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 


 

Signed and dated this 25th day of September, 2026 at Lakewood, Colorado.

/s/Troy Meyer
Troy Meyer, P.E.
Chief Geotechnical Quality Engineer

BBA Consultants International LP

 


EX-23.7 12 nb-ex23_7.htm EX-23.7 EX-23.7

EXHIBIT 23.7

img77704856_0.jpg

CONSENT OF QUALIFIED PERSON

Olsson hereby consents to the public filing of Sections 1.13, 17, 22.6 and 23.8 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

Olsson also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

Olsson also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

Olsson also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

Olsson certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 


 

Signed and dated this 25th day of September, 2026 at Omaha, Nebraska.

/s/Brian Osborn
Brian Osborn, BSc
Environmental Technical Expert
Olsson

 


EX-23.8 13 nb-ex23_8.htm EX-23.8 EX-23.8

EXHIBIT 23.8

img78628377_0.jpg

 

CONSENT OF QUALIFIED PERSON

Adrian Brown Consultants Inc. hereby consents to the public filing of Section 13.3 (the “Covered Section”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

Adrian Brown Consultants Inc. also consents to the incorporation by reference of the Covered Section in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

Adrian Brown Consultants Inc. also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

Adrian Brown Consultants Inc. also consents to any extracts from or a summary of the Covered Section in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

Adrian Brown Consultants Inc. certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Section.

***SIGNATURE PAGE FOLLOWS***

 

 


 

Signed and dated this 25th day of September, 2026 at Denver, Colorado, USA.

/s/Adrian Brown
Adrian Brown, P.G., PE
Principal Engineer
Adrian Brown Consultants Inc.

 


EX-23.9 14 nb-ex23_9.htm EX-23.9 EX-23.9

EXHIBIT 23.9

img79551898_0.jpg

CONSENT OF QUALIFIED PERSON

Andrieux & Associates Geomechanics Consulting, L.P. hereby consents to the public filing of Sections 13.2, 13.6.5 and 23.3 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

Andrieux & Associates Geomechanics Consulting, L.P. also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

Andrieux & Associates Geomechanics Consulting, L.P. also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

Andrieux & Associates Geomechanics Consulting, L.P. also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

Andrieux & Associates Geomechanics Consulting, L.P. certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 


 

Signed and dated this 25th day of September, 2026 in Montreal, Quebec, Canada.

/s/Patrick Andrieux
Patrick Andrieux, Ph.D., P.Eng., Eng.
Principal Engineer
Andrieux & Associates Geomechanics Consulting, L.P.

 


EX-23.10 15 nb-ex23_10.htm EX-23.10 EX-23.10

EXHIBIT 23.10

img89699940_0.jpg

CONSENT OF QUALIFIED PERSON

Tetra Tech hereby consents to the public filing of Sections 1.11, 14.7, 15.1, 15.2, 15.2.1, 15.2.2, 15.3, 15.4, 15.5, 15.6, 15.6.2, 15.7, 22.5 and 23.7 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

Tetra Tech also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

Tetra Tech also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

Tetra Tech also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

Tetra Tech certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 


 

Signed and dated this 25th day of September, 2026 at Salt Lake City, Utah.

/s/David Winters
David Winters, SE, PE
Project Manager and Senior Principal Engineer
Tetra Tech

 


EX-23.11 16 nb-ex23_11.htm EX-23.11 EX-23.11

img90623461_0.jpg EXHIBIT 23.11

 

CONSENT OF QUALIFIED PERSON

 

T Engineering hereby consents to the public filing of Sections 13.6.4 and 15.13 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

T Engineering also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

T Engineering also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

T Engineering also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

T Engineering certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

 

***SIGNATURE PAGE FOLLOWS***

 


 

Signed and dated this 25th day of September, 2026 at Oakville, Ontario.

/s/Bernie Ting
Yen Jui (Bernie) Ting, P. Eng., MASc.
Principal, SME and Lead Engineer
T Engineering

 


EX-23.12 17 nb-ex23_12.htm EX-23.12 EX-23.12

EXHIBIT 23.12

img91546982_0.jpg

CONSENT OF QUALIFIED PERSON

Magemi Mining Inc. hereby consents to the public filing of Sections 1.6.1, 10.2, 14.2.1, 14.3.1, 14.4.1, 14.5.1 and 14.6.1 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

Magemi Mining Inc. also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

Magemi Mining Inc. also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

Magemi Mining Inc. also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

Magemi Mining Inc. certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 


 

Signed and dated this 25th day of September, 2026 at North York, Ontario, Canada.

/s/Georgi Doundarov
Georgi Doundarov, M.SC, P.Eng., PMP, CCP
CEO
Magemi Mining Inc.

 


EX-23.13 18 nb-ex23_13.htm EX-23.13 EX-23.13

EXHIBIT 23.13

img92470503_0.jpg

CONSENT OF QUALIFIED PERSON

Metallurgy Concept Solutions hereby consents to the public filing of Sections 1.6.3, 10.4, 14.2.3, 14.3.3, 14.4.3, 14.5.3, 14.6.3 and 23.5 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

Metallurgy Concept Solutions also consents to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

Metallurgy Concept Solutions also consents to the use of and references to our name, including our status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

Metallurgy Concept Solutions also consents to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

Metallurgy Concept Solutions certifies that we have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***

 


 

Signed and dated this 25th day of September, 2026 at Valleyfield, QC, Canada.

/s/Sylvain Harton
Sylvain Harton, P. Eng.

President & Owner

Metallurgy Concept Solutions

 


EX-23.14 19 nb-ex23_14.htm EX-23.14 EX-23.14

img93394024_0.jpg EXHIBIT 23.14

 

CONSENT OF QUALIFIED PERSON

I, Scott Honan, M.Sc., SME-RM, consent to the public filing of Sections 1.14, 1.15, 1.16, 18, 19, 21 and 22.8 (the “Covered Sections”) of the Technical Report Summary titled “Technical Report Summary, Elk Creek Project, Nebraska” with an Effective Date of June 30, 2026 (the “Technical Report Summary”) as an exhibit to the Annual Report on Form 10-K for the fiscal year ended June 30, 2026 (the “Form 10-K”) of NioCorp Developments Ltd. (the “Company”).

I also consent to the incorporation by reference of the Covered Sections in the Company’s Registration Statements on Form S-1 (Registration Nos. 333-285066, 333-279429, 333-271268, 333-254511, 333-270541 and 333-271266), Registration Statements on Form S-3 (Registration Nos. 333-280176 and 333-290837) and Registration Statements on Form S-8 (Registration Nos. 333-290671 and 333-222313) (collectively, the “Registration Statements”).

I also consent to the use of and references to my name, including my status as an expert or “qualified person” (as defined in Subpart 1300 of Regulation S-K promulgated by the U.S. Securities and Exchange Commission), in connection with the Form 10-K, the Registration Statements and the Technical Report Summary.

I also consent to any extracts from or a summary of the Covered Sections in the Form 10-K and incorporated by reference in the Registration Statements (the “Disclosure”).

I certify that I have read the Disclosure being filed by the Company and that it fairly and accurately represents the information in the Covered Sections.

***SIGNATURE PAGE FOLLOWS***


 

Signed and dated this 25th day of September, 2026 at Centennial, Colorado, USA.

/s/Scott Honan
Scott Honan, M.Sc., SME-RM
Chief Operating Officer
NioCorp Developments Ltd.

 


EX-31.1 20 nb-ex31_1.htm EX-31.1 EX-31.1

 

EXHIBIT 31.1

CERTIFICATION

I, Mark A. Smith, certify that:

1. I have reviewed this Annual Report on Form 10-K of NioCorp Developments Ltd.;

2. Based on my knowledge, this report does not contain any untrue statement of a material fact or omit to state a material fact necessary to make the statements made, in light of the circumstances under which such statements were made, not misleading with respect to the period covered by this report;

3. Based on my knowledge, the financial statements, and other financial information included in this report, fairly present in all material respects the financial condition, results of operations and cash flows of the registrant as of, and for, the periods presented in this report;

4. The registrant's other certifying officer(s) and I are responsible for establishing and maintaining disclosure controls and procedures (as defined in Exchange Act Rules 13a-15(e) and 15d-15(e)) and internal control over financial reporting (as defined in Exchange Act Rules 13a-15(f) and 15d-15(f)) for the registrant and have:

(a) Designed such disclosure controls and procedures, or caused such disclosure controls and procedures to be designed under our supervision, to ensure that material information relating to the registrant, including its consolidated subsidiaries, is made known to us by others within those entities, particularly during the period in which this report is being prepared;

(b) Designed such internal control over financial reporting, or caused such internal control over financial reporting to be designed under our supervision, to provide reasonable assurance regarding the reliability of financial reporting and the preparation of financial statements for external purposes in accordance with generally accepted accounting principles;

(c) Evaluated the effectiveness of the registrant's disclosure controls and procedures and presented in this report our conclusions about the effectiveness of the disclosure controls and procedures, as of the end of the period covered by this report based on such evaluation; and

(d) Disclosed in this report any change in the registrant's internal control over financial reporting that occurred during the registrant's most recent fiscal quarter (the registrant's fourth fiscal quarter in the case of an annual report) that has materially affected, or is reasonably likely to materially affect, the registrant's internal control over financial reporting; and

5. The registrant's other certifying officer(s) and I have disclosed, based on our most recent evaluation of internal control over financial reporting, to the registrant's auditors and the audit committee of the registrant's board of directors (or persons performing the equivalent functions):

(a) All significant deficiencies and material weaknesses in the design or operation of internal control over financial reporting which are reasonably likely to adversely affect the registrant's ability to record, process, summarize and report financial information; and

(b) Any fraud, whether or not material, that involves management or other employees who have a significant role in the registrant's internal control over financial reporting.

 

Date: September 25, 2026

By:

/s/ Mark A. Smith

 

 

Mark A. Smith

 

 

Chief Executive Officer

 

 

(Principal Executive Officer)

 

 


EX-31.2 21 nb-ex31_2.htm EX-31.2 EX-31.2

 

EXHIBIT 31.2

CERTIFICATION

I, Neal Shah, certify that:

1. I have reviewed this Annual Report on Form 10-K of NioCorp Developments Ltd.;

2. Based on my knowledge, this report does not contain any untrue statement of a material fact or omit to state a material fact necessary to make the statements made, in light of the circumstances under which such statements were made, not misleading with respect to the period covered by this report;

3. Based on my knowledge, the financial statements, and other financial information included in this report, fairly present in all material respects the financial condition, results of operations and cash flows of the registrant as of, and for, the periods presented in this report;

4. The registrant's other certifying officer(s) and I are responsible for establishing and maintaining disclosure controls and procedures (as defined in Exchange Act Rules 13a-15(e) and 15d-15(e)) and internal control over financial reporting (as defined in Exchange Act Rules 13a-15(f) and 15d-15(f)) for the registrant and have:

(a) Designed such disclosure controls and procedures, or caused such disclosure controls and procedures to be designed under our supervision, to ensure that material information relating to the registrant, including its consolidated subsidiaries, is made known to us by others within those entities, particularly during the period in which this report is being prepared;

(b) Designed such internal control over financial reporting, or caused such internal control over financial reporting to be designed under our supervision, to provide reasonable assurance regarding the reliability of financial reporting and the preparation of financial statements for external purposes in accordance with generally accepted accounting principles;

(c) Evaluated the effectiveness of the registrant's disclosure controls and procedures and presented in this report our conclusions about the effectiveness of the disclosure controls and procedures, as of the end of the period covered by this report based on such evaluation; and

(d) Disclosed in this report any change in the registrant's internal control over financial reporting that occurred during the registrant's most recent fiscal quarter (the registrant's fourth fiscal quarter in the case of an annual report) that has materially affected, or is reasonably likely to materially affect, the registrant's internal control over financial reporting; and

5. The registrant's other certifying officer(s) and I have disclosed, based on our most recent evaluation of internal control over financial reporting, to the registrant's auditors and the audit committee of the registrant's board of directors (or persons performing the equivalent functions):

(a) All significant deficiencies and material weaknesses in the design or operation of internal control over financial reporting which are reasonably likely to adversely affect the registrant's ability to record, process, summarize and report financial information; and

(b) Any fraud, whether or not material, that involves management or other employees who have a significant role in the registrant's internal control over financial reporting.

 

Date: September 25, 2026

By:

/s/ Neal Shah

 

 

Neal Shah

 

 

Chief Financial Officer

 

 

(Principal Financial and Accounting Officer)

 

 


EX-32.1 22 nb-ex32_1.htm EX-32.1 EX-32.1

EXHIBIT 32.1

CERTIFICATION PURSUANT TO 18 U.S.C. SECTION 1350

AS ADOPTED PURSUANT TO

SECTION 906 OF THE SARBANES-OXLEY ACT OF 2002

In connection with the Annual Report on Form 10-K of NioCorp Developments Ltd. (the "Company"), for the year ended June 30, 2026, as filed with the Securities and Exchange Commission on the date hereof (the "Report"), I, Mark A. Smith, Chief Executive Officer of the Company, hereby certify pursuant to 18 U.S.C. Section 1350, as adopted pursuant to Section 906 of the Sarbanes-Oxley Act of 2002, that, to my knowledge:

1. The Report fully complies with the requirements of Section 13(a) or 15(d) of the Securities Exchange Act of 1934; and

2. The information contained in the Report fairly presents, in all material respects, the financial condition and results of operations of the Company.

 

Date: September 25, 2026

By:

/s/ Mark A. Smith

 

 

Mark A. Smith

 

 

Chief Executive Officer

(Principal Executive Officer)

 


EX-32.2 23 nb-ex32_2.htm EX-32.2 EX-32.2

 

EXHIBIT 32.2

CERTIFICATION PURSUANT TO 18 U.S.C. SECTION 1350

AS ADOPTED PURSUANT TO

SECTION 906 OF THE SARBANES-OXLEY ACT OF 2002

In connection with the Annual Report on Form 10-K of NioCorp Developments Ltd. (the "Company"), for the year ended June 30, 2026, as filed with the Securities and Exchange Commission on the date hereof (the "Report"), I, Neal Shah, Chief Financial Officer of the Company, hereby certify pursuant to 18 U.S.C. Section 1350, as adopted pursuant to Section 906 of the Sarbanes-Oxley Act of 2002, that, to my knowledge:

1. The Report fully complies with the requirements of Section 13(a) or 15(d) of the Securities Exchange Act of 1934; and

2. The information contained in the Report fairly presents, in all material respects, the financial condition and results of operations of the Company.

 

Date: September 25, 2026

By:

/s/ Neal Shah

 

 

Neal Shah

 

 

Chief Financial Officer

(Principal Financial and Accounting Officer)

 

 


EX-95.1 24 nb-ex95_1.htm EX-95.1 EX-95.1

EXHIBIT 95.1

MINE SAFETY DISCLOSURES

The following disclosure is provided pursuant to Section 1503 of the Dodd-Frank Wall Street Reform and Consumer Protection Act (the "Dodd-Frank Act"), Section 13(a) of the Securities Exchange Act of 1934, as amended, and Item 104 of Regulation S-K (17 C.F.R. § 229.104), in respect of each coal or other mine of NioCorp Developments Ltd. (the "Company") or any of its subsidiaries that was subject to the jurisdiction of the U.S. Department of Labor, Mine Safety and Health Administration ("MSHA") under the Federal Mine Safety and Health Act of 1977, as amended (the "Mine Act"), at any time during the three months ended June 30, 2026.

The Elk Creek Critical Minerals Project in Johnson County, Nebraska (the "Elk Creek Project"), operated by Elk Creek Resources Corp. ("ECRC"), an indirect majority-owned subsidiary of the Company, is subject to the jurisdiction of MSHA under the Mine Act. The MSHA Mine Identification Number for the Elk Creek Project is 25-01332. No other properties of the Company or its subsidiaries were subject to MSHA jurisdiction during the quarter. Other than as set forth below, no events required to be disclosed under Item 104 of Regulation S-K occurred at the Elk Creek Project, or at any other property of the Company or its subsidiaries, during the three months ended June 30, 2026.

Citations, Orders, Assessments and Fatalities

Mine or Operating Name / MSHA ID

Section 104 S&S Citations (1)

Section 104(b) Orders (2)

Section 104(d) Citations and Orders (3)

Section 110(b)(2) Violations (4)

Section 107(a) Orders (5)

Total Dollar Value of Proposed MSHA Assessments ($) (6)

Mining-Related Fatalities

 

Elk Creek Critical Minerals Project (MSHA ID: 25-01332)

1

0

0

0

0

$151

0

 

Pattern of Violations Notices and Legal Actions

Mine or Operating Name / MSHA ID

Pattern of Violations Notice Under Section 104(e)

(7)

Potential Pattern Notice Under Section 104(e)

(7)

Legal Actions Pending as of Last Day of Period

(8)

Legal Actions Initiated During Period (8)

Legal Actions Resolved During Period

 (8)

Elk Creek Critical Minerals Project (MSHA ID: 25-01332)

No

No

0

0

0

Notes to the Foregoing Tables:

(1) Citations issued under Section 104 of the Mine Act, 30 U.S.C. § 814, for violations that could significantly and substantially contribute to the cause and effect of a mine safety or health hazard (“S&S” citations).

(2) Orders issued under Section 104(b) of the Mine Act for failure to abate a cited violation within the period specified in the citation.

(3) Citations and orders issued under Section 104(d) of the Mine Act for unwarrantable failure to comply with mandatory health or safety standards.


(4) Flagrant violations issued under Section 110(b)(2) of the Mine Act, 30 U.S.C. § 820(b)(2).

(5) Orders issued under Section 107(a) of the Mine Act, 30 U.S.C. § 817(a), for the existence of an imminent danger.

(6) Proposed assessments received from MSHA during the period under 30 C.F.R. Part 100. Amounts shown reflect proposed assessments received during the period and do not reflect any subsequent settlement, adjustment, or final determination.

(7) Written notices received from MSHA under Section 104(e) of the Mine Act, 30 U.S.C. § 814(e), of a pattern of violations, or of the potential to have such a pattern.

(8) Legal actions before the Federal Mine Safety and Health Review Commission (the “FMSHRC”), including contests of citations, orders, and proposed penalties; complaints for compensation under Section 111 of the Mine Act; complaints of discharge, discrimination, or interference under Section 105 of the Mine Act; applications for temporary relief under Section 105(b)(2) of the Mine Act; and appeals of judges’ decisions or orders to the FMSHRC.


EX-96.1 25 nb-ex96_1.htm EX-96.1 EX-96.1

SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

 

img170397038_0.gif

 

SK-1300 Technical Report Summary

Elk Creek Project, Nebraska

 

 

 

 

Prepared For:

NioCorp Developments Ltd.

 

EFFECTIVE DAte:

June 30, 2026

 

Signature Date:

September 23, 2026

 

 

 

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Prepared and Signed by:

1.
Dahrouge Geological Consulting USA Ltd.
2.
SMH Process Innovation.
3.
Dumas Contracting USA Inc.
4.
Amplify Mine Planning LLC
5.
BBA Consultants International LP
6.
Olsson
7.
Adrian Brown Consultants Inc.
8.
Andrieux & Associates Geomechanics Consulting, L.P.
9.
Tetra Tech
10.
Metallurgy Concept Solutions
11.
Magemi Mining Inc.
12.
T Engineering
13.
Scott Honan, M.Sc., SME-RM, NioCorp Developments Ltd.

 

 

 

i | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Table of Contents

1

Executive Summary

1

1.1

Principal Outcomes

1

1.2

Property Location, Description & Ownership

1

1.3

History

2

1.4

Geological Setting & Mineralization

2

1.5

Exploration and Drilling

3

1.6

Mineral Processing & Metallurgical Testing

3

1.6.1

Mineral Processing

3

1.6.2

Hydrometallurgical Testing (Hydromet)

4

1.6.3

Pyrometallurgical Processing (Pyromet)

4

1.7

Mineral Resource Estimation

5

1.8

Mineral Reserve Estimation

6

1.9

Mining Methods

7

1.10

Recovery Methods

8

1.11

Project Infrastructure

9

1.11.1

Tailings

10

1.12

Markets and Contracts

10

1.13

Environmental Studies, Permitting & Social or Community Impact

11

1.14

Capital Cost Estimate

13

1.15

Operating Cost Estimate

14

1.16

Economic Analysis

14

1.17

Conclusions and Recommendations

16

2

Introduction

18

2.1

Registrant

18

2.2

Terms of Reference and Purpose of the Report

18

2.3

Sources of Information

19

2.4

Effective Date

19

2.5

Details of Inspection

19

2.6

Qualifications of Qualified Persons

20

2.7

Units of Measure

22

3

Property Description & Location

22

3.1

Property Location

22

3.2

Mineral Title and Land Tenure

23

3.2.1

Nature and extent of Issuer’s Interest

25

3.3

Royalties, Agreements and Encumbrances

25

3.4

Environmental Liabilities and Permitting

25

3.5

Other Significant Factors and Risks

26

4

Accessibility, Climate, Local Resources, Infrastructure and Physiography

27

4.1

Accessibility and Transportation to the Property

27

4.2

Climate and Length of Operating Season

28

4.3

Physiography

28

4.4

Infrastructure and Local Resources

28

5

History

29

5.1

Exploration History

29

5.2

Ownership History

30

5.3

Historical Mineral Resource Estimates

30

5.4

Historical Mineral Reserve Estimates

30

ii | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

5.5

Historical Production

31

6

Geological Setting, Mineralization and Deposit

32

6.1

Regional Geology

32

6.2

Property Geology

34

6.2.1

Marine Sedimentary Rocks

36

6.2.2

Elk Creek Carbonatite

37

6.2.3

Structural Geology

38

6.3

Mineralization

39

6.3.1

Niobium and Titanium Mineralization

40

6.3.2

Scandium Mineralization

42

6.3.3

Rare Earth Element Mineralization

42

6.4

Deposit Type

43

7

Exploration and Drilling

46

7.1

Exploration

46

7.2

Drilling

47

7.2.1

Project Drilling Procedures

50

7.2.1.1

Collar and Downhole Surveys

50

7.2.1.2

Geomechanical Core Logging

51

7.2.1.3

Geological Core Logging

51

8

Sample Preparation, Analyses & Security

52

8.1

Sample Preparation & Security

52

8.2

Sample Analysis Procedures

54

8.3

Quality Assurance & Quality Control (“QAQC”) Programs

55

8.3.1

Historical QAQC

55

8.3.1.1

Molycorp, 1973-1986

57

8.3.1.2

NioCorp, 2011-2014

58

8.3.1.3

Historical Re-Sampling Programs, 2010-2021

58

8.3.1.4

Quality Assurance and Quality Control

59

8.3.2

NioCorp 2025 QAQC

60

8.3.2.1

Field Quartz Blanks

60

8.3.2.2

Certified Reference Material

62

8.3.2.2.1

Nb2O5standards and Certified Reference Material

63

8.3.2.2.2

Sc standards and Certified Reference Material

64

8.3.2.2.3

TiO2 standards and Certified Reference Material

65

8.3.2.2.4

Certified Reference Material and other REE results.

65

8.3.2.3

Duplicates

67

8.3.2.4

Third Party Check Samples

74

8.4

Qualified Person’s Opinion on the Adequacy of Sample Preparation, Security & Procedures

77

9

Data Verification

78

9.1

Data Validation

78

9.1.1

Core Processing Protocols

79

9.1.2

Database Validation

79

9.1.3

NioCorp QAQC

79

9.2

Limitations

79

9.3

Qualified Person’s Opinion

80

10

Mineral Processing and Metallurgical Testing

81

10.1

Historical Test Work

81

10.2

Mineral Processing

81

iii | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

10.3

Hydrometallurgy

82

10.3.1

Mineralogy and Feed Characterization

82

10.3.2

Process Development & Flowsheet

83

10.3.2.1

Metallurgical Recoveries and Performance

83

10.3.2.1.1

Area 100 – Ore Activation

84

10.3.2.1.2

Area 200 - Ammonium Chloride Cycle

84

10.3.2.1.3

Area 300 - Hydrochloric Leach

87

10.3.2.1.4

Area 400 – Sulfuric Acid

90

10.3.2.1.5

Area 500 – Chlorination

92

10.3.2.1.6

Area 600 – Rare Earth Elements Extraction

96

10.3.2.1.7

Area 700 - Rare Earth Separation

98

10.3.2.1.8

Area 800 - Chloride Recovery

104

10.3.3

Significant Factors

107

10.4

Pyrometallurgy

108

11

Mineral Resource Estimate

112

11.1

Introduction

112

11.2

Source Database

112

11.3

Geological Domaining

113

11.4

Density Determination and Assignment

113

11.5

Exploratory Data Analysis

114

11.5.1

Distributed Analysis

114

11.5.2

Top Cut Analysis

119

11.5.3

Declustering

124

11.5.4

Correlation Analysis

125

11.6

Data Preparation

126

11.7

Variography

127

11.8

Block Model Resource Estimation

132

11.8.1

Block Model Configuration

132

11.8.2

Estimation Method

133

11.8.3

Estimation Pass Structure

133

11.9

Model Validation

135

11.10

Mineral Resource Classification

140

11.11

Reasonable Prospects of Eventual Economic Extraction

140

11.12

Cut-Off Grade

141

11.13

Mineral Resource Tabulation

141

11.14

Mineral Resource Sensitivity

142

11.15

Relevant Factors

143

12

Mineral Reserve Estimates

144

12.1

Introduction

144

12.2

Conversion, Assumptions, Parameters & Methods

146

12.2.1

Dilution

146

12.2.2

Recovery

148

12.2.3

COG / NSR Calculation

149

12.2.4

Mine Design

153

12.3

Reserves

153

12.4

Relevant Factors

156

13

Mining Methods

157

13.1

Geology Overview

157

13.2

Rock Engineering

157

iv | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

13.2.1

Geomechanical Appraisal

157

13.2.1.1

Available Geomechanical Data

157

13.2.1.2

Data Gaps

158

13.2.1.3

In-Situ Stress Conditions

159

13.2.1.4

Rock Mass Geomechanical Domains

159

13.2.1.5

Intact Rock Properties

160

13.2.1.6

Property-Scale Structures

161

13.2.1.7

Rock Mass Jointing

161

13.2.1.8

Rock Mass Classification

163

13.2.1.9

Anticipated Rock Mass Behaviour

163

13.2.2

Geomechanical Guidelines for Mine Design

165

13.2.2.1

Stope Dimensions and Dilution Estimates

165

13.2.2.2

Dimension of Pillars

166

13.2.2.3

Backfill Strength Requirement

167

13.2.2.4

Seismic Conditions

167

13.2.2.5

Infrastructure Proximity Relative to Ore Body

167

13.2.2.6

Ground Support

168

13.3

Hydrogeology Design Parameters

169

13.3.1

Conceptual Hydrogeology

170

13.3.2

Mine Inflow Control

176

13.3.2.1

Mine Inflow

176

13.3.2.2

Groutability of the Elk Creek Orebody

178

13.3.2.3

Grouting Design

181

13.3.2.4

Grout hole drilling

185

13.3.2.5

Inrush Safety

186

13.4

Mine Design

189

13.4.1

Selection of Mining Method

189

13.4.2

Stope Optimization

191

13.4.3

Stope Design

192

13.4.4

Development Design

194

13.4.5

Mine Access

198

13.4.5.1

Dual Portal Box Cut

198

13.4.5.2

Fresh Air Raise

199

13.5

Production Schedule

200

13.5.1

Productivity

200

13.5.2

Box Cut, Portal and Ramp Development

203

13.5.3

Primary Haulage Ramp & Secondary Access Ramp

205

13.5.4

Development and Production Schedule

205

13.6

Mining Operations

208

13.6.1

Production Schedule

208

13.6.2

Development

209

13.6.3

Truck and LHD Haulage

209

13.6.3.1

Development Phase Haulage

209

13.6.3.2

Transition to Railveyor Haulage

210

13.6.3.3

Production Phase Haulage

210

13.6.4

Backfilling

211

13.6.4.1

Normal Operation

211

13.6.4.1.1

Paste Backfill Quality Control

211

13.6.4.2

Upset Conditions

211

v | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

13.6.5

Ground Support

212

13.6.6

Grade Control and Reconciliation

212

13.7

Ventilation

212

13.8

Airflow Requirements

213

13.8.1

Ventilation Controls

218

13.8.1.1

Ventilation on Demand (VOD)

218

13.8.1.2

Surface Intake Fans

218

13.8.1.3

Auxiliary Fans

218

13.8.1.4

Monitoring and Control Infrastructure

219

13.8.2

Ventilation Model

219

13.8.2.1

Ventilation Numerical Modelling

219

13.8.3

Ventilation Equipment

221

13.8.3.1

Main Surface Ventilation

221

13.8.3.2

Auxiliary Ventilation

223

13.8.3.3

Development Headings

223

13.8.3.4

Crosscut (Draw Points) and Ore/Waste Pass Ventilation

223

13.8.3.5

Substations, Sumps, and Refuge Station Ventilation

223

13.8.3.6

Railveyor Loadout Ventilation

223

13.8.4

Recommended Ventilation Infrastructure

224

13.8.5

Ventilation Power Consumption

225

13.8.6

Mine Air Heating

226

13.8.6.1

Primary Equipment Heat

226

13.8.6.2

Railveyor Heat Loads

226

13.8.6.3

Sumps, Substations, Shops, and Refuge Stations

226

13.8.7

Thermal Exposure

231

13.9

Mine Infrastructure and Services

231

13.9.1

Material Handling System

231

13.9.2

Mine Dewatering System

233

13.9.3

Compressed Air System

235

13.9.4

Underground Water Supply

236

13.9.5

Underground Fuel Storage and Distribution

236

13.9.6

Workshop, Maintenance Bays, and Warehouse

237

13.9.7

Explosives Storage

238

13.9.8

Refuge Stations

239

13.9.9

Surface Electrical Distribution

240

13.9.10

Underground Electrical Distribution

241

13.9.11

Electrical Buried Services Distribution

242

13.9.12

Development Face Grouting

243

13.9.13

Dust Suppression System

244

13.9.14

Communications Systems

244

13.9.15

Safety and Health

245

13.9.16

Workforce

246

13.9.16.1

Development Phase

246

13.9.16.2

Full Production Phase

246

13.9.16.3

Direct and Indirect Designations

246

13.9.16.4

Engineering Maturity and Risk Statement

247

13.9.17

Equipment

247

13.9.17.1

Equipment Strategy and Fleet Basis

247

13.9.17.2

Underground Haulage and Material Handling

247

vi | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

13.9.17.2.1

Load-Haul-Dump Equipment

248

13.9.17.2.2

Engineering Maturity and Implementation

248

13.9.17.2.3

Equipment Table

248

14

Process and Recovery Methods

251

14.1

Overview

251

14.2

Process Plant Design Criteria

252

14.2.1

Surface Crushing, Ore Storage & Mineral Processing

252

14.2.2

Hydrometallurgical Plant

254

14.2.3

Pyrometallurgical Plant

277

14.3

Flowsheets and Process Description

279

14.3.1

Surface Crushing, Ore Storage & Mineral Processing Plant

279

14.3.2

Hydrometallurgical Plant

281

14.3.3

Pyrometallurgical Plant

299

14.3.3.1

Furnace Feed System

301

14.3.3.2

Furnace Operation

302

14.3.3.3

Design of the Induction Furnace

302

14.3.3.3.1

Tapping Schedule — Design Basis

302

14.4

Mass Balances

303

14.4.1

Surface Crushing, Ore Storage & Mineral Processing Plant

303

14.4.2

Hydrometallurgical Plant

304

14.4.3

Pyrometallurgical Plant

310

14.5

Process Equipment

312

14.5.1

Surface Crushing, Ore Storage & Mineral Processing Plant

312

14.5.2

Hydrometallurgical Plant

313

14.5.3

Pyrometallurgical Plant

340

14.6

Power Requirements

341

14.6.1

Surface Crushing, Ore Storage & Mineral Processing Plant

341

14.6.2

Hydrometallurgical Plant

341

14.6.3

Pyrometallurgical Plant

342

14.7

Plant Layout

342

14.7.1

General

342

14.7.2

Mineral Processing Plant, Surface Crushing and Ore Storage

343

14.7.3

Hydrometallurgical Plant

344

14.7.4

Pyrometallurgical Plant

344

15

Project Infrastructure

349

15.1

General Information Site Layout

349

15.2

Electrical Power

350

15.2.1

Microgrid

350

15.2.2

Electrical Power Distribution - Plant and Facilities

350

15.2.3

Electrical Power Distribution – Underground

350

15.2.4

Emergency Power Generation

350

15.3

Control & Communications

351

15.3.1

Process Control System

351

15.3.2

Site Communications

351

15.3.3

Access and Security System

351

15.4

Natural Gas

351

15.4.1

Natural Gas Pipeline to Site

351

15.4.2

Natural Gas Distribution on Site

351

15.5

Plant Water

351

vii | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

15.5.1

Water Treatment Plant

351

15.5.1.1

Flow Equalization

353

15.5.1.2

Softening Clarification

353

15.5.1.3

Multimedia Filtration

353

15.5.1.4

Reverse Osmosis (RO) System

354

15.5.1.5

Sludge Handling

354

15.5.1.6

Evaporation and Crystallization System

355

15.5.2

Process Water

357

15.5.3

Fire Water

357

15.5.4

Potable Water

358

15.6

Auxiliary Buildings and Facilities

358

15.6.1

Mining Infrastructure

358

15.6.2

Supporting Infrastructure

360

15.7

Roads

362

15.7.1

Main Access Road to Site

362

15.7.2

Secondary Site Access Roads

362

15.7.3

Secondary Site Roads

362

15.8

Carbonatite Rock Stockpile

362

15.9

Surface Water Management for TSF and Temporary Stockpile Areas

364

15.9.1

Stockpile

364

15.9.2

Tailings Storage Facility (“TSF”)

364

15.10

Tailings Surface Logistics

367

15.11

Tailings Storage and Associated Facilities

367

15.11.1

Overview and Capacity

367

15.11.2

Design Basis

368

15.11.3

Embankment Configuration

368

15.11.4

Liner System

369

15.11.5

Instrumentation

369

15.11.6

Conceptual Closure

370

15.12

Salt Management Cells

370

15.12.1

Mine Water Holding Function

370

15.12.2

Wastewater Treatment Solids Disposal

371

15.13

Paste Backfill System and Underground Distribution

372

15.13.1

Paste Backfill Plant

372

15.13.1.1

Basis of Design

372

15.13.1.2

Key Design Parameters

373

15.13.1.3

Process Description

374

15.13.1.4

Paste Backfill Plant Design

376

15.13.1.5

Power Requirements

379

15.13.2

Paste Distribution System

379

15.13.2.1

Throughput

379

15.13.2.2

Hydraulic Modelling

379

15.13.2.3

Paste Distribution System Process Description

380

15.13.3

Paste Backfill Test Work

380

15.13.3.1

Characterization

381

15.13.3.2

Paste Mix Design

381

16

Market Studies

382

16.1

Market Studies

382

16.1.1

Niobium Market Overview

382

viii | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

16.1.2

Titanium Tetrachloride (TiCl4) Market Overview

384

16.1.3

Scandium Trioxide Market Overview

388

16.1.3.1

Scandium Trioxide Market Supply

389

16.1.3.2

Scandium Trioxide Market Demands

390

16.1.3.3

Scandium Trioxide Pricing

394

16.1.4

Rare Earth Market Overview

396

16.1.4.1

Market Demand

398

16.1.4.2

Pricing

400

16.2

Contracts and Status

403

16.2.1

Ferroniobium Offtake Agreement with Thyssen Krupp Metallurgical Products GmbH

403

16.2.2

Definitive Offtake Agreement with Traxys North America LLC

404

16.3

Market Dynamics

406

16.3.1

Scandium

406

16.3.2

Dysprosium and Terbium

410

16.3.3

Economic Model Pricing

411

17

Environmental Studies, Permitting & Plans, Negotiations, or Agreements with Local Individuals or Groups

413

17.1

Environmental Studies

413

17.1.1

Soils

413

17.1.2

Climate/Meteorology/Air Quality

413

17.1.3

Cultural and Archaeological Resources

413

17.1.4

Vegetation

413

17.1.5

Wildlife

414

17.1.6

Threatened, Endangered, and Special Status Species

414

17.1.7

Land Use

415

17.1.8

Hydrogeology (Groundwater)

415

17.1.9

Hydrology (Surface Water)

416

17.1.10

Environmental Geochemistry

416

17.1.11

Known Environmental Issues

419

17.2

Waste Management & Disposal

419

17.2.1

Mine Overburden

419

17.2.2

Tailings/Waste Rock/Process Waste (Onsite)

419

17.2.3

Project Waste Disposal (Offsite)

419

17.2.4

Site Monitoring

420

17.2.5

Water Management

420

17.2.6

Chemical and Reagents Handling

420

17.3

Project Permitting Requirements

421

17.3.1

Nebraska Underground Injection Control

426

17.3.2

DHHS Radioactive Materials Program and Licensing

426

17.3.3

Nebraska Air Quality Permitting

426

17.3.4

Nebraska Dam Permitting

427

17.3.5

Permitting Status

428

17.3.6

Post-Performance and Reclamation Bonding

429

17.4

Community Relations and Social Responsibilities

430

17.4.1

Safety and Health

430

17.5

Reclamation & Closure

430

17.5.1

Surface Disturbance

430

17.5.2

Buildings and Equipment

431

17.5.3

Tailings Disposal Facility

431

ix | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

17.5.4

Closure Cost Estimate

431

17.6

International Standards & Guidelines

432

18

Capital and Operating Costs

433

18.1

Capital Cost Estimate

433

18.1.1

Basis of Estimate

433

18.1.1.1

Mining, Process, and Infrastructure Capital Cost

433

18.1.1.2

Tailings and Tailings Water Management Capital Costs

433

18.2

Capital Cost Summary

433

18.2.1

Capitalized Pre-production Costs

434

18.2.2

Mining Capital Costs

434

18.2.3

Processing Plant Capital Costs

435

18.2.3.1

Processing Indirects

436

18.2.3.2

Process Commissioning

436

18.2.4

Tailings, Stockpile, Salt Management and Paste Tailings Costs

436

18.2.5

Water Management and Infrastructure

437

18.2.6

Site Preparation and Infrastructure Capital Costs

437

18.2.7

Owner’s Costs

437

18.2.8

Closure and Reclamation

438

18.2.9

Sustaining Capital Costs

439

18.2.10

Contingency

439

18.3

Operating Costs

439

18.3.1

Basis of Estimate (BoE)

439

18.3.1.1

Mining Operating Costs BoE

439

18.3.1.2

Process Plant Operating Costs BoE

440

18.3.1.3

Tailings Management Costs

441

18.3.1.4

General and Administrative (G&A) Costs BoE

441

18.3.1.5

Water Supply Operating Costs BoE

441

18.3.1.6

Closure and Reclamation

441

18.3.2

Operating Cost Summary

442

18.3.2.1

Mining Operating Costs

442

18.3.2.2

Process Plants Operating Costs

443

18.3.2.3

Tailings and Salt Management Operating Costs

446

18.3.2.4

Site G&A Operating Costs

446

18.3.3

Mine Operating Costs

448

19

Economic Analysis

450

19.1

Cautionary Statement

450

19.2

Methodology Used

450

19.3

Financial Model Parameters and Assumptions

451

19.3.1

Physicals

452

19.3.2

Revenue

453

19.3.3

Operating

456

19.3.4

Capital Costs

456

19.4

Cashflow Forecasts & Annual Production Forecasts

457

19.5

Taxes, Royalties & Other Interests

458

19.6

Sensitivity Analysis

459

20

Adjacent Properties

465

21

Other Relevant Data and Information

466

21.1

Project Implementation Plan

466

21.1.1

Project Cost Objectives

466

x | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

21.1.2

Project Schedule Objectives

466

21.1.3

Early Works

467

21.1.4

Project Team

467

21.1.5

Project and Document Control

467

21.1.6

Engineering

468

21.1.7

Supply Chain and Procurement

468

21.1.8

Construction Management

468

21.1.9

Commissioning, Operational Readiness, and Early Operations

469

21.2

Risk Assessment

470

21.2.1

2022 Risk and Current Status

470

22

Interpretations and Conclusions

476

22.1

Geology & Mineral Resource

476

22.2

Mining & Mineral Reserve

477

22.3

Recovery Methods

477

22.4

Processing & Metallurgical Testing

478

22.5

Infrastructure

479

22.5.1

Tailings Storage Facility

480

22.6

Environmental, Permitting & Social or Community Considerations

480

22.7

Market Studies & Contracts

481

22.8

Projected Economic Outcomes

482

23

Recommendations

483

23.1

Geology and Resources

483

23.2

Hydrometallurgical Plant

483

23.3

Geomechnical

484

23.4

Mining & Reserves

484

23.5

Pyrometallurgical Plant

485

23.6

Recovery Methods

485

23.7

Infrastructure

485

23.8

Environmental & Social

486

23.9

Summary of Costs for Recommended Work

487

24

References

488

24.1

Definition of Terms

493

24.2

Abbreviations

495

25

Reliance on Information Provided By the Registrant

499

26

Signature Page

500

 

 

xi | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

List of Figures

Figure 3-1:

Project Location Map

23

Figure 3-2:

Project Tenure Map

24

Figure 3-3:

Net Smelter Return (“NSR”) Map

25

Figure 4-1:

Project Access

27

Figure 6-1:

Regional Geology

33

Figure 6-2:

Merged Aeromagnetic Anomaly Map of Nebraska, Kansas and Oklahoma showing Midcontinental Rift and Nemaha Uplift

34

Figure 6-3

Generalized Stratigraphy of the Elk Creek Area

35

Figure 6-4:

(Left) Drill core illustrating the transition from eroded paleosurface of the Elk Creek Carbonatite Complex to the “Limestone Breccia”. (Right) Photographs of microstructures in the drill core.

36

Figure 6-5:

Plan view of the location of the mineralized carbonatite (outlined in red) with underground development projected to surface

40

Figure 6-6:

Plan and Cross -Sections of Geologic Model Hanging Wall Boundary and Mineralized Domain

40

Figure 6-7:

Basic Statistics of Nb2O5Mineralization

41

Figure 6-8:

Correlation Statistics of Nb2O5 and TiO2 and Fe2O3

42

Figure 6-9:

Basic Statistics of Sc Mineralization

42

Figure 6-10:

Schematic Diagram of St. Honoré Carbonatite

45

Figure 7-1:

Geology of the Elk Creek Carbonatite as expressed in drill holes at an elevation of 394 ft (120 m) AMSL (approximately 755 ft or 230 m BGS)

46

Figure 7-2:

All drilling completed within the area of the Elk Creek Carbonatite Complex

48

Figure 7-3:

2025 Drillhole locations on the Project

49

Figure 8-1:

Sample Process Flow Chart (2014 - 2025 drill programs)

53

Figure 8-2:

NioCorp Technicians cutting core at the project site.

53

Figure 8-3:

Secure storage of the NioCorp Drill holes and pulps.

54

Figure 8-4:

Summary of Blank Control Charts for Nb2O5, Sc, TiO2 Submission SGS for the 2025 Drill Program

62

Figure 8-5:

Summary of Blank Control Charts for Nd, Pr, Dy and Tb Submissions to SGS

62

Figure 8-6:

OREAS465 and OREAS464 Results for Nb2O5

64

Figure 8-7:

OREAS465 and OREAS464 Results for Sc

64

Figure 8-8:

OREAS465 and OREAS464 Results for TiO2

65

Figure 8-9:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Pulp Duplicate) Core Duplicate Analysis for Analytes Nb2O5 and Sc

67

Figure 8-10:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Pulp Duplicate) Core Duplicate Analysis for Analytes TiO2, Nd, Pr, Dy and Tb

68

Figure 8-11:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Nb2O5, Sc and TiO2

69

Figure 8-12:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Nd and Pr.

70

Figure 8-13:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Dy and Tb.

71

Figure 8-14:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Nb2O5, Sc and TiO2

72

xii | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Figure 8-15:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Nd and Pr

73

Figure 8-16:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Dy and Tb

74

Figure 8-17:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (External Lab Duplicate) Core Duplicate Analysis for Analytes Nb2O5, Sc and TiO2

75

Figure 8-18:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (External Lab Duplicate) Core Duplicate Analysis for Analytes Nd and Pr

76

Figure 8-19:

Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (External Lab Duplicate) Core Duplicate Analysis for Analytes Dy and Tb.

77

Figure 10-1:

Calcium (top) and Magnesium (bottom) concentration over time and moving average trendline.

86

Figure 10-2:

Ammonium chloride leach performance for Ca and Mg.

87

Figure 10-3:

Ca and Mg leaching performance per countercurrent leach stage.

87

Figure 10-4:

(a) Ca and Mg distribution in the precipitate from the Ca Precipitation (CaP) and the Magnesium Precipitation (MgP). (b) The aqueous concentration in grams per liter of Ca and Mg after the precipitation process.

87

Figure 10-5:

Leach efficiencies for leach 1 and leach 2 in the counter current leach process.

90

Figure 10-6:

Ti and Nb water leaching efficiency of acid baked material over various tests.

91

Figure 10-7:

Aqueous concentration in gram per liter throughout the hydrolysis procedure for Ti and Nb. (a) NCPn-16, (b) NCPn-17, (c) NCPn-18.

92

Figure 10-8:

L3 2026

93

Figure 10-9:

Phase II Chlorination Equipment Design

95

Figure 10-10:

Concentration of elements over time in the Extraction stage of the solvent extraction system.

99

Figure 10-11:

Concentration of elements over time in the Scrub stage of the solvent extraction system.

99

Figure 10-12:

Concentration of elements over time in the Strip 1 stage of the solvent extraction system.

100

Figure 10-13:

Concentration of elements over time in the Strip 2 and Strip 3 stages of the solvent extraction system.

101

Figure 10-14:

Distribution of the LREEs throughout the circuit.

102

Figure 10-15:

Distribution of the SEG REEs throughout the circuit.

103

Figure 10-16:

Distribution of the Tb, Dy, and Y throughout the circuit.

104

Figure 10-17:

Distribution of the HREEs throughout the circuit.

104

Figure 10-18:

Demonstration Ferric Chloride Pyro-Hydrolysis Reactor Unit Photo

105

Figure 10-19:

Demonstration Ferric Chloride Pyro-Hydrolysis Reactor Unit Schematic

106

Figure 10-20:

Iron Oxide Residue

107

Figure 10-21:

Pyrohydrolysis residue elemental distribution.

107

Figure 10-22:

Chemical analysis results for the 400 g sample supplied by L3 Process Development

110

Figure 11-1:

Nb2O5Grade distribution by domain

115

Figure 11-2:

TiO2 Grade distribution by domain

116

Figure 11-3:

Sc Grade distribution by domain

117

Figure 11-4:

TREO Grade distribution by domain

118

Figure 11-5:

Nb2O5Log Probability Plot

121

Figure 11-6:

TiO2 Log Probability Plot

121

xiii | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Figure 11-7:

Sc Log Probability Plot

122

Figure 11-8:

TREO Log Probability Plot

123

Figure 11-9:

Nb2O5 Ortho Directional Variogram for MCarb Domain.

128

Figure 11-10:

Sc Omni Directional Variogram for MCarb Domain

129

Figure 11-11:

TiO2 Omni Directional Variogram for MCarb Domain

130

Figure 11-12:

TREO Omni Directional Variogram for MCarb Domain.

131

Figure 11-13:

Swath Plot Nb2O5for the MCarb Domain

137

Figure 11-14:

Swath Plot Sc for the MCarb Domain

137

Figure 11-15:

Swath Plot TiO2for the MCarb Domain

138

Figure 11-16:

Swath Plot TREO for the MCarb Domain

139

Figure 12-1:

2026 Elk Creek Study Mine Design

145

Figure 12-2:

Sources of Mining Dilution for Typical Stope Layout (Not to scale).

147

Figure 12-3:

NioCorp Grade (Nb2O5)-Tonne Curves Based on NSR Cut-Off

150

Figure 12-4:

NioCorp Grade/Tonne Curves Based on NSR Cut-Off (TiO2)

151

Figure 12-5:

NioCorp Grade (Sc ppm) – Grade Tonne Curves Based on NSR Cut-Off

151

Figure 12-6:

NioCorp Grade (TREO %) – Grade Tonne Curves Based on NSR Cut-Off

152

Figure 12-7:

Current Mine Design

153

Figure 13-1:

Lower hemisphere equal angle plots showing the structural data and joint sets interpretation per structural domain

163

Figure 13-2:

Regional Hydrogeology

172

Figure 13-3:

Hydrogeology of the Elk Creek Mine – view looking northeast

173

Figure 13-4:

Hydraulic Conductivity of Geologic Materials at the Elk Creek Mine

175

Figure 13-5:

Mine inflow with no controls — Schematic

177

Figure 13-6:

Mine inflow with grout control — Schematic

178

Figure 13-7:

Geophysical tests showing widely spaced high permeability flow zones (left panel) and corresponding widely-spaced large aperture voids (right panel)

180

Figure 13-8:

Grout hole location plan, showing grouting boreholes, development drifts, mining stopes and sections.

182

Figure 13-9:

Section A-A' looking northeast, showing geology, grouting boreholes, development drifts, and mining stopes

183

Figure 13-10:

Section B-B looking northwest, showing geology, grouting boreholes, development drifts, and mining stopes

184

Figure 13-11:

Example of a mobile concrete batch plant (Photo courtesy of Techwill Inc.)

186

Figure 13-12:

Stability of grouted stope outer pillar against water drive — Force diagram

187

Figure 13-13:

Vertical stress in 65.6 foot- (20 meter) thick and 131.2 foot- (40 meter) high grouted stope outer pillar located 3,280 feet (1,000 meters) below ground surface with 10 MPa (1,450 psi) water drive applied to outer edge of terminal pillar (blue arrows). All stresses reported in MPa, mesh blocks are 3.28-foot (1-meter) cubes.

188

Figure 13-14:

2026 Current Design

190

Figure 13-15:

Undiluted Stope Optimization Results for Varying NSR Cut-Offs

192

Figure 13-16:

Stopes and Crosscut Accesses (Cross Section View)

193

Figure 13-17:

Level Layout with Stopes and Footwall Accesses (Rotated View Looking North)

194

Figure 13-18:

Completed Mine Design (Plan View)

195

Figure 13-19:

Completed Mine Design (Cross Sectional View)

195

Figure 13-20:

Completed Mine Design - Main Infrastructure (Looking South)

196

Figure 13-21:

Mine Design Coloured by Nb2O5Grade.

196

Figure 13-22:

Mine Design Coloured by NSR ($/t)

197

Figure 13-23:

Box Cut Design Dimensions – Plan View Looking Northeast

203

Figure 13-24:

GSI Proposal for Slope Stability

204

xiv | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Figure 13-25:

Initial Ramp Development – Isometric View Looking North

205

Figure 13-26:

Mine Production Schedule - Colored by Year

208

Figure 13-27:

Current Overall Mine Ventilation Layout

213

Figure 13-28:

Stage 1 Development to 210 Level

220

Figure 13-29:

Life-of-Mine (LoM) Stage

221

Figure 13-30:

Main Fan Configuration

222

Figure 13-31:

Railveyor System Schematic

233

Figure 14-1:

Overall Crushing Conceptual Block Flow Diagram

281

Figure 14-2:

Area 100 – Ore Activation Block Flow Diagram

281

Figure 14-3:

Area 200 – Ammonium Chloride Cycle Block Flow Diagram

282

Figure 14-4:

Area 300 – Hydrochloric Acid Leach Block Flow Diagram

284

Figure 14-5:

Area 400 – Sulfuric Acid Block Flow Diagram

286

Figure 14-6:

Area 500 – Chlorination Block Flow Diagram

288

Figure 14-7:

Area 600 - REE Recovery Block Flow Diagram

292

Figure 14-8:

Area 700 – Rare Earth Separation Block Flow Diagram

294

Figure 14-9:

Area 800 – Chloride Recovery Block Flow Diagram

298

Figure 14-10:

Area 900 – Sulfate Effluent Block Flow Diagram

299

Figure 14-11:

Pyrometallurgical Processing Simplified Flowsheet

301

Figure 14-12:

Product Summary Block Flow Diagram

304

Figure 14-13:

Summary of the pyrometallurgical plant

312

Figure 14-14:

Process Plant Layout

343

Figure 14-15:

Hydromet Plant

344

Figure 14-16:

Pyromet Building Southeast View

345

Figure 14-17:

Bulk Feed and Storage

345

Figure 14-18:

FeNb Furnace Feed System

346

Figure 14-19:

FeNb Furnace, Pelletization Basin, Dryer and Packaging Equipment

346

Figure 14-20:

Office and Control Room

347

Figure 14-21:

Pyromet Building Northwest View

348

Figure 14-22:

Dust Collection and Cooling Systems

348

Figure 15-1:

Elk Creek Project Site Plan Layout

349

Figure 15-2:

Process Water Treatment Plant Block Flow Diagram

356

Figure 15-3:

Overall Water Balance

357

Figure 15-4:

Building 31 A – General Mine Admin, First Aid, Dry, and Underground Central Control

359

Figure 15-5:

Building 31C - Shop and Battery Charging

360

Figure 15-6:

Carbonatite Stockpile Layout

363

Figure 15-7:

TSF West Cells Water Management

366

Figure 15-8:

TSF East Cells Water Management

366

Figure 15-9:

TSF General Arrangement

368

Figure 15-10:

Process Flow Diagram of Paste Backfill Plant - Page 1

375

Figure 15-11:

Process Flow Diagram of Paste Backfill Plant - Page 2

376

Figure 15-12:

Plan View of the Paste Backfill Plant and SSF

377

Figure 15-13:

Elevation View of the Paste Backfill Plant and SS

378

Figure 15-14:

Paths of the Paste Distribution System Modelled

380

Figure 16-1:

Ferroniobium Demand 2025-2035 (kt Nb)

384

Figure 16-2:

Ferroniobium Price Forecast 2025-2035 (US$/kg)

384

Figure 16-3:

Chinese Indicative TiCl4Pricing

386

Figure 16-4:

Historical and Forecast TiCl4 Pricing

388

Figure 16-5:

Sc2O3tonnes Supply and Demand; Established Demand Segments Only

393

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Figure 16-6:

Projected Sc2O3Price per Kg through 2035

395

Figure 16-7:

Lanthanide Series for REE's modified after Van Gosen 2014.

397

Figure 16-8:

Historical global consumption and forecasted demand for NdFeB magnets by end-use category

399

Figure 16-9:

Forecasted China domestic price of dysprosium oxide

401

Figure 16-10:

Forecasted China domestic price of terbium oxide

402

Figure 16-11:

Forecasted China price of neodymium oxide, praseodymium oxide and didymium oxide.

402

Figure 18-1:

Reagent Consumption Percentages for the Hydrometallurgical facility

445

Figure 18-2:

Natural Gas Consumption per Process area in Hydrometallurgy

446

Figure 19-1:

Pre-Tax NPV Sensitivity Analysis

460

Figure 19-2:

Pre-Tax IRR Sensitivity Analysis

460

Figure 19-3:

After-Tax NPV Sensitivity Analysis

460

Figure 19-4:

After-Tax IRR Sensitivity Analysis

461

Figure 19-5:

Pre-Tax NPV Sensitivity to Grade and Recovery

461

Figure 19-6:

After Tax NPV Sensitivity to Grade and Recovery

462

Figure 19-7:

Pre-Tax IRR Sensitivity to Grade and Recovery

462

Figure 19-8:

After Tax IRR Sensitivity to Grade and Recovery

463

Figure 19-9:

Before-Tax NPV Profile

463

Figure 19-10:

After-Tax NPV Profile

464

Figure 20-1:

Adjacent Properties

465

Figure 21-1:

Likelihood and Consequence Matrix

470

 

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

 

List of Tables

Table 1-1:

Elk Creek Mineral Resource Estimate by Classification Inclusive of Reserves

5

Table 1-2:

Elk Creek Mineral Resource Estimate by Classification Exclusive of Reserves

5

Table 1-3

Elk Creek Mineral Reserves

6

Table 1-4:

Capital Costs Summary (US$ 000’s)

13

Table 1-5:

Operating Cost Summary

14

Table 1-6:

Indicative Economic Results

15

Table 2-1:

A summary of the site visit inspections by the QP consultants

19

Table 2-2:

List of Qualified Persons responsible for sections of this Report

21

Table 3-1:

Active Option to Purchase Agreements Covering the Project

24

Table 5-1:

Historical Exploration Summary

30

Table 6-1:

Project rock types as defined by Molycorp and DGC

37

Table 6-2:

List of Elements & Oxides Associated with REE Mineralization

43

Table 7-1:

Drilling Completed within the Carbonatite Complex

47

Table 7-2:

2025 Drill Hole Summary

49

Table 8-1:

Analytical methods used for sample assay.

54

Table 8-2:

Summary of Historical Sample Preparation, Analysis, and QA/QC Programs — Elk Creek Project

56

Table 8-3:

Summary of Field Quartz Blank Performance — 2011 and 2014 Drill Programs (Nb₂O₅)

59

Table 8-4:

Summary of designed level of insertion of QC submissions in the 2025 drill program.

60

Table 8-5:

Summary of 2025 Drill Program Field Blank Insertion

61

Table 8-6:

Summary of the CRM used for the 2025 Program

62

Table 8-7:

Summary of the Nb2O5Results per CRM (SGS)

63

Table 8-8:

Summary of the Sc Results per CRM (SGS)

64

Table 8-9:

Summary of the TiO2Results per CRM (SGS)

65

Table 8-10:

REE performance on CRM's OREAS 465, ORES463, GRE-11 and GRE-08

66

Table 9-1:

Summary of QP Site Visits

78

Table 10-1:

Summary of Historical Technical Reports

81

Table 10-2:

Ore Feed Characterization Summary

83

Table 10-3:

Product Recoveries per area

83

Table 10-4:

Ammonium chloride test conditions and associated recoveries for select tests.

84

Table 10-5:

HCl-PLS composition of for high and low density scenarios.

88

Table 10-6:

Test conditions and leach efficiencies for select HCl leaching tests.

89

Table 10-7:

Experiment test conditions and results for select acid bake-water leach tests.

90

Table 10-8:

Experiment test conditions and results for select hydrolysis tests.

91

Table 10-9:

Phase I Experimental Conditions

93

Table 10-10:

Phase I Results

93

Table 10-11:

Phase II Experimental Conditions

95

Table 10-12:

Phase II Results

96

Table 10-13:

Extraction PLS Description

96

Table 10-14:

Experiment test conditions and results for select DGA-6 extraction tests

96

Table 10-15:

Experiment test conditions and results for select DGA-6 scrub tests

97

Table 10-16:

REE solvent extraction operational parameters.

98

Table 11-1:

Bulk density by estimation domain

114

Table 11-2:

Top Cut Summary by Domain and Analyte

124

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Table 11-3:

Optimum cell size ranges used for cell declustering by domain and analyte.

125

Table 11-4:

Pearson Correlation Matrix (Capped Composite Grades by Domain)

126

Table 11-5:

Variogram Model Parameters: All Domains and Analytes

127

Table 11-6:

Block Model Configuration Parameters

132

Table 11-7:

Bulk Density Summary by Geologic Domain

133

Table 11-8:

Multi-Pass Estimation Parameters

134

Table 11-9:

Mineral Resource Classification Material

140

Table 11-10:

NSR Conversion, Recoveries and Pricing

141

Table 11-11:

Elk Creek Mineral Resource Estimate Inclusive of Reserve - Effective June 30, 2026

141

Table 11-12:

Elk Creek Mineral Resource Estimate Exclusive of Reserve – Effective June 30, 2026

142

Table 11-13:

Elk Creek Mineral Resource Sensitivity

142

Table 12-1:

Mineral reserves as of June 30, 2026 and stated in this report

144

Table 12-2:

Potential sources of mining dilution by stope type (primary and secondary) for a typical stope geometry and standard mining practices in the ground conditions expected at Elk Creek.

148

Table 12-3:

Example of an NSR Block Calculation

149

Table 12-4:

Operating Costs Used for Mine Design NSR Cut-off

152

Table 12-5:

In-situ Underground Mineral Reserves Estimate for Elk Creek, Effective Date June 30, 2026

154

Table 13-1:

Summary of available geomechanical data from drill holes for the Elk Creek Project

157

Table 13-2:

In-situ stress conditions considered for the Elk Creek Project

159

Table 13-3:

Number of valid intact rock strength laboratory tests per geomechanical domain used to establish intact rock strength envelopes.

160

Table 13-4:

Summary of intact rock mechanical properties per geomechanical domain.

160

Table 13-5:

Summary of mean joint set orientations per structural domain

162

Table 13-6:

Summary of rock mass classification per geomechanical domain

163

Table 13-7:

Undiluted Stope Optimization Results for Varying NSR Cut-offs

192

Table 13-8:

Mine Design Summary - by Activity Type

197

Table 13-9:

Productivity Rates

200

Table 13-10:

Dimensions by Heading Types

201

Table 13-11:

Workforce Schedule Parameters for Underground

202

Table 13-12:

Cut Design Dimensions

203

Table 13-13:

Mine Production Schedule

206

Table 13-14:

Airflow Determination

215

Table 13-15:

Ventilation Infrastructure Matrix

224

Table 13-16:

Equipment Heat

228

Table 13-17:

Underground Equipment

249

Table 14-1:

Process Design Criteria

252

Table 14-2:

Plant Design Criteria

255

Table 14-3:

Area 100 – Ore Activation Process Design Criteria

255

Table 14-4:

Area 200 – Ammonium Chloride Cycle Process Design Criteria

255

Table 14-5:

Area 300 – Hydrochloric Acid Leach Process Design Criteria

257

Table 14-6:

Area 400 – Sulfuric Acid Process Design Criteria

258

Table 14-7:

Area 500 – Chlorination Process Design Criteria

260

Table 14-8:

Area 600 – Solvent Extraction Process Design Criteria

264

Table 14-9:

Area 700 – Rare Earth Separation

266

Table 14-10:

Area 800 – Chloride Recovery Process Design Criteria

275

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Table 14-11:

Area 900 – Sulfate Effluent Treatment Process Design Criteria

276

Table 14-12:

Pyrometallurgical process design criteria.

277

Table 14-13:

Comminution Circuit Material Balance

303

Table 14-14:

Recovery of Saleable Products

304

Table 14-15:

Area 100 / 200 Summary Mass Balance Table

306

Table 14-16:

Area 300 / 400 Summary Mass Balance Table

307

Table 14-17:

Area 500 Summary Mass Balance Table

308

Table 14-18:

Area 600 / 700 Summary Mass Balance Table

308

Table 14-19:

Area 700 Summary Mass Balance Table

309

Table 14-20:

Area 800 Summary Mass Balance Table

309

Table 14-21:

Reagent and approximate feed rate (t/d).

311

Table 14-22:

FeNb Furnace Partition Coefficients

311

Table 14-23:

Primary Equipment List

312

Table 14-24:

Ancillary Equipment List

313

Table 14-25:

Area 100 – Ore Activation Summary Equipment List

314

Table 14-26:

Area 200 – Ammonium Chloride Cycle Summary Equipment List

315

Table 14-27:

Area 300 - Hydrochloric Acid Leach Summary Equipment List

319

Table 14-28:

Area 400 – Sulfuric Acid Summary Equipment List

321

Table 14-29:

Area 500 – Chlorination Summary Equipment List

324

Table 14-30:

Area 600 – Solvent Extraction Summary Equipment List

328

Table 14-31:

Area 700 – Rare Earth Separation Summary Equipment List

330

Table 14-32:

Area 800 – Chloride Recovery Summary Equipment List

338

Table 14-33:

Area 900 – Sulfate Effluent Summary Equipment List

340

Table 14-34:

Pyrometallurgical processing major equipment list.

341

Table 14-35:

Installed power breakdown

342

Table 14-36:

FeNb Furnace Power Requirements

342

Table 15-1:

Design Requirements

352

Table 15-2:

TSF Infrastructure Description

364

Table 15-3:

TSF Capacity Summary

367

Table 15-4:

Expected Quality of Formation Water to WWT

370

Table 15-5:

Primary Expected Solid Flows to Salt Cell from Process Water Treatment

371

Table 15-6:

Paste Backfill System Key Design Parameters

373

Table 15-7:

Backfill Throughput Rates

379

Table 16-1:

Niobium Producers

383

Table 16-2:

North American TiCl₄ Producers (2024)

385

Table 16-3:

TiCl4 Demand by End-Use Application (Excl. TiO2 Pigment)

386

Table 16-4:

Indicative TiCl4Production Cost Breakdown (TZMI Model)

388

Table 16-5:

Known Scandium Oxide Producers, Feedstock and Status

389

Table 16-6:

Scandium Oxide Supply vs. Demand by Year

393

Table 16-7:

Price Forecast by Region 2025 through 2035

395

Table 16-8:

Comparison of NioCorp Pricing to publicly available information.

402

Table 16-9:

Price projections, current US$, scandium oxide per Kg by source, 2025-35.

408

Table 16-10:

Revised Price projections, current US$, scandium oxide per Kg by source, 2025-36

409

Table 16-11:

Argus Non-Ferrous Market Pricing for Dy and Tb

410

Table 16-12:

Pricing Comparison – Resource/Reserve versus Economic Model

412

Table 17-1:

Project Permits

421

Table 18-1:

Capital Costs Summary (US$ 000’s)

434

Table 18-2:

Mine Direct Initial Capital Cost Breakdown

435

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Table 18-3:

Mine Indirect Capital Cost Breakdown

435

Table 18-4:

Process Plant Costs Summary

435

Table 18-5:

Processing Indirects Cost Summary

436

Table 18-6:

Pre-production Facilities

436

Table 18-7:

Owner’s Costs

437

Table 18-8:

LOM Operating Cost Unit Rate Summary

442

Table 18-9:

Steady State Mining Operating Unit Cost

443

Table 18-10:

ROM Processing Operating Cost Unit Rate Breakdown

444

Table 18-11:

Support Roles for Facility Operations

447

Table 18-12:

Steady State Mining Operating Unit Cost

448

Table 19-1:

General Assumptions

451

Table 19-2:

Mining Physicals

452

Table 19-3:

Processing Physicals

453

Table 19-4:

Pricing Assumptions

453

Table 19-5:

Scandium Trioxide Pricing Assumptions

454

Table 19-6:

TREO Pricing Assumptions

454

Table 19-7:

Operating Cost Summary

456

Table 19-8:

Capital Cost Summary (US$ 000’s)

456

Table 19-9:

Initial Capital Costs Summary (US$ 000’s)

457

Table 19-10:

Indicative Economic Results (US$ 000’s)

457

Table 22-1:

Hydromet Elemental Recovery Summary

478

Table 24-1:

Summary of general mining terms potentially used in this Technical Report Summary.

493

Table 25-1:

Information supplied by Registrant

499

 

 

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

1 Executive Summary

NioCorp Developments Ltd. (“NioCorp” or the “Company”) is a U.S.-based mineral development company focused on developing several critical minerals from the proposed Elk Creek, Nebraska Critical Minerals Mine (the “Elk Creek Mine,” the “Elk Creek Project” or the “Project”). NioCorp plans to produce eight commercial mineral products — ferroniobium, scandium oxide, titanium tetrachloride, NdPr oxide, Tb oxide, Dy oxide, SEG carbonate and heavies carbonate from a single underground orebody. All of the Elk Creek Project’s products have been designated as “Critical Minerals” by the U.S. Government, as have the rare earth elements. NioCorp is a publicly traded company that is listed on the NASDAQ under the ticker symbol “NB”.

This Technical Report Summary ( this “Technical Report Summary,” “TRS” or “Report”) for the Elk Creek Project (“the Project”) located in southeast Nebraska was prepared for NioCorp in accordance with Item 601(b)(96) and subpart 1300 of Regulation S-K (“Regulation S-K 1300”) promulgated by the United States Securities and Exchange Commission (“SEC”) by Dahrouge Geological Consulting USA Ltd. (“DGC”), SMH Process Innovation (“SMH”), Amplify Mine Planning LLC (“Amplify”), Adrian Brown Consultants, Inc. (“ABC”), BBA Consultants International LP, formerly Tierra Group International, Ltd. (“Tierra Group/BBA”), Olsson, Andrieux & Associates Geomechanics Consulting, L.P. (“A2GC”), Magemi Mining Inc. (“Magemi”), Dumas Contracting USA Inc. (“Dumas”), T Engineering (“T Eng”), Tetra Tech, Metallurgy Concept Solutions (“MCS”), and Scott Honan, M.Sc., SME-RM, NioCorp (collectively, the “Qualified Persons” or “QPs”).

This Technical Report Summary summarizes the results of a pre-feasibility study (as that term is defined under Regulation S-K 1300) (the “2026 Elk Creek Study”) prepared by the Qualified Persons. The reason that the 2026 Elk Creek Study does not qualify as feasibility study under Regulation S-K 1300 is because additional work with respect to the engineering of and procurement for the planned surface plant is required to allow the Qualified Person to reduce the overall contingency range attributed to the initial capital expenditure estimate for the Elk Creek Project from the current 14% to less than or equal to 10%.

1.1 Principal Outcomes

This Technical Report Summary is based on processing of 45,929,462 tons of ore over a 40-year operational life to produce 205,464 tons of Nb in the form of ferroniobium, 4,585 tons of scandium oxide, 2,341,367 tons of TiCl4, 25,923 tons of NdPr oxide, 690 tons of Tb oxide, 2,649 tons of Dy oxide, 13,886 tons of SEG carbonate and 10,161 tons of heavies carbonate.

This has been estimated using a cut-off of US$218/ton.

The initial capital cost is US$ 1,849 million. The total capital cost is US$ 4,019 million including sustaining and closure/reclamation capital. The overall contingency on initial capital is 14%.

Based on current assumptions and design listed in this report, the project returns a pre-tax NPV 8% of US$ 4,111 million and an IRR of 24.0% along with an after-tax NPV 8% of US$ 3,441 million and IRR of 22.8%.

1.2 Property Location, Description & Ownership

The Project is located in southeast Nebraska, USA. It is located approximately 47 miles southeast of Lincoln, Nebraska (the state capital), and 68 miles south of Omaha, Nebraska. The Property is located

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

within the U.S. Geological Survey Tecumseh Quadrangle Nebraska SE (7.5-minute series) mapsheet in Sections 1-6, 9-11; Township 3N; Range 11 and Sections 19-23, 25-36; Township 4N, Range 11. The area is well developed with direct access to roads, rail, supply and distribution companies, and a local workforce including heavy equipment operators.

The Project consists of one 709.93-acre parcel of land 100% owned by the Company along with six option-to purchase agreements covering approximately 1,010.96 acres. Option agreements are between NioCorp's wholly owned subsidiary Elk Creek Resources Corp. (“ECRC”) and the individual landowners. The parcel owned by the Company contains most of the Mineral Resources and Mineral Reserves associated with the project. NioCorp retains 100% of the mineral rights to the Property and is the operator. The option agreements are in the form of pre-paid Exploration Lease Agreements (ELA), with an Option to Purchase (OTP) the mineral rights and/or the surface rights at any time during the term of the agreement. The individual landowners have title to the surface and subsurface rights, and the agreements are primarily concerned with only the mineral and surface interest of each property. The agreements convey to the Company adequate surface rights to access the land and to complete mineral exploration work. The option agreements that the Company currently holds include all the Mineral Resources and Mineral Reserves described in this report.

Except for a 2% NSR royalty attached to the parcel owned by NioCorp and the OTPs that include the mineral rights, the Property has no other outstanding royalties, agreements, or encumbrances.

1.3 History

Exploration activities on the Property prior to NioCorp ownership were conducted by the University of Nebraska – Lincoln, Nebraska Conservation and Survey Division, United States Geological Survey (“USGS”), Cominco American Inc. (“Cominco American”), Molybdenum Corporation of America and later Molycorp Inc. (“Molycorp”). These activities consisted of airborne magnetic and gravity surveys, geochemical sampling and core drilling.

Since 2011, NioCorp has completed extensive project development work on its Elk Creek Project, including Reverse Circulation (RC) drilling, core drilling, metallurgical testing, multiple Mineral Resource Estimates and Mineral Resource updates, two Preliminary Economic Assessments completed in 2015, and feasibility studies completed in, 2017, 2019 and 2022.

1.4 Geological Setting & Mineralization

The Project includes the Elk Creek Carbonatite (“the Carbonatite”) that intruded older Precambrian granitic and low to medium grade metamorphic basement rocks. Both the Carbonatite and Precambrian rocks are interpreted to be unconformably overlain by approximately 650 ft of Paleozoic marine sedimentary rocks of Pennsylvanian age. As a result of this thick cover, there is no surface outcrop within the Property area of the Carbonatite, which was identified and targeted through magnetic surveys and confirmed through subsequent drilling. The available magnetic data indicates dominant northeast, west-northwest striking lineaments, and secondary northwest and north-oriented features that mimic the position of regional faults parallel and/or perpendicular to the Nemaha Uplift.

The Carbonatite hosts significant niobium (reported as Nb2O5), titanium (reported as TiO2) and scandium (reported as Sc) and is composed predominantly of dolomite, calcite and ankerite, with lesser chlorite, barite, phlogopite, pyrochlore, serpentine, fluorite, sulphides and quartz. Niobium is

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

contained primarily within the mineral pyrochlore, and rare earth element (REE) mineralization is reported to occur as bastnäsite, parisite, synchysite and monazite.

The Elk Creek Deposit (“the Deposit”), as defined in the Mineral Resource Estimate, consists of niobium, titanium, scandium and rare earth mineralization that is chiefly hosted within a magnetite (hematite) dolomite carbonatite.

1.5 Exploration and Drilling

Multiple drilling programs have been completed on the Project. The first were conducted by Molycorp during the 1970s and 1980s, followed by a second program by Quantum Rare Earth Development Corp. (predecessor to NioCorp) in 2011 and another three programs by NioCorp in 2014, 2015 and 2025. The 2014 program included nineteen holes drilled for resource estimation, totalling 52,389 ft. The 2015 program included five holes, totaling 11,000 ft drilled for hydrogeological and geotechnical studies and were not used for resource estimation. To date, a total of 160 drillholes have been completed within the Carbonatite complex totalling 269,905 ft (82,267 m), with 79 drillholes completed on the Property totalling 178,602 ft (54,438 m).

The 2025 drilling program was specifically designed to target gaps within the current Mineral Resource in support of converting a portion of the Resource from Indicated and Inferred to Measured, Indicated and Inferred. The drilling for the 2025 program was completed by Boart Longyear Company – Western Coring, 7013 West Augusta Ave, Glendale, Arizona 85303. Drilling was initiated on April 29, 2025, and was completed on October 3, 2025. During this campaign a total of 16 HQ diameter drillholes were completed totalling 37,861 ft (11,540 m) utilizing 2 (two) LF-160 drill rigs, one track mounted and one truck mounted core drill. All drilling was completed using diamond coring methods (Table 7‑2). Overburden was cased using HWT casing, and the remainder of the drillholes were completed using HQ thereafter.

1.6 Mineral Processing & Metallurgical Testing

1.6.1 Mineral Processing

The comminution test work was completed in two stages at SGS Canada Inc. (“SGS”) in Lakefield, Ontario in 2016. The primary stage test work (SGS Canada Inc., 2016a) was conducted on six composite samples and 13 variability samples and included:

•
Bond Rod Mill Work Index (Rwi) testing.
•
Bond Ball Mill Work Index (Bwi) testing.
•
Bond Abrasion Index (Ai) testing.
•
Bond Low-energy Impact (Cwi) testing.
•
JK Drop Weight (JKDW) testing.
•
Semi-autogenous grinding (SAG) Mill Comminution (SMC) testing.

The second stage of comminution test work (SGS Canada Inc., 2016b) was conducted on a single composite sample, using a LABWAL high-pressure grinding roll (HPGR) semi-pilot scale test work program.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

The test work results indicate that the Project ore is categorized as soft to moderately hard in terms of ore hardness, and amenable to standard grinding as well as an HPGR operation.

A bulk representative sample (approximately 3,000 kg) of ore was subjected to locked cycle pilot scale testing at NRRI-Coleraine in Minnesota. The ore tested indicates that it is amenable to processing via the HPGR. Autogenous layer buildup and flake generation were both acceptable, and there was, on average, 40% < 1 mm product generated from the HPGR when in steady state.

The most notable observations from the testing are:

(1)
Final product particle size is largely independent of press force and moisture.
(2)
Specific energy increases as both moisture and press force increase.
(3)
There is a decrease in specific throughput as the press force increases.
(4)
There is a decrease in specific throughput as the feed moisture increases.

Based on the results as indicated above, it would be recommended to run an installed HPGR at lower pressures, i.e. 3.0 N/mm2 or less, and to remove as much free water from the circuit as possible. This will have the effect of reducing power requirements with limited to no impacts on size reduction.

The data as collected to date is suitable for full HPGR scale up and process guarantees around envisioned plant operation conditions.

1.6.2 Hydrometallurgical Testing (Hydromet)

Metallurgical test work was conducted at L3 Process Development between 2021 and 2026, with post-FS optimization test work on-going. The test work campaigns were used to develop and optimize the flowsheet and process units to extract and purify a crude niobium oxide product suitable for further treatment into ferroniobium (FeNb) as well as marketable products of titanium chloride, scandium trioxide, dydimium oxide (Nd(Pr) oxide), terbium oxide and dysprosium oxide from Elk Creek Ore.

Test work consisted of multiple bench and pilot scale hydrometallurgical test programs followed by the operation of an integrated demonstration scale circuit aimed at further refining the final flowsheet using different reagents and technologies. The operation of the demonstration plant showed that high recovery rates of the niobium, scandium, rare earths and titanium could be achieved, and that recycling and regeneration of reagents was also possible; thus, minimizing fresh reagent input and waste generation. Recoveries of 84.7% Nb, 80.5% Ti, 94.3% Sc, 88.7-94.4% NdPr, 94.4% Tb, and 94.6% Dy have been demonstrated.

1.6.3 Pyrometallurgical Processing (Pyromet)

The initial KPM test work completed in 2016 established the basis for the Pyromet process, with niobium recovery estimated at 96%. Building on this work, XPS testing conducted in September 2025 successfully demonstrated the production of ferroniobium alloy from the sodium-bearing Hydromet feed. Further evaluation completed in April 2026 confirmed the technical viability of the process and established that titanium must be removed from the Hydromet feed. The remaining development priorities include achieving consistent Hydromet feed composition, improving slag fluidity and metal–slag separation, selecting an appropriate refractory, implementing effective phosphorus control, and conducting additional representative-scale testing to confirm the achievable niobium recovery.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

1.7 Mineral Resource Estimation

The Mineral Resource Estimate for the Elk Creek Carbonatite Project has been prepared by Dahrouge Geological Consulting USA Ltd. (DGC) and has an effective date of June 30, 2026. The estimate is reported in accordance with Regulation S-K 1300.

The resource is estimated within three geological domains (MCARB, DOL_CARB, and LAMP) utilizing hard boundaries and modeled in Leapfrog GeoTM. All domains are defined from lithological logging of 65 diamond core drill holes of HQ size. Grade estimation is completed in Maptek VulcanTM using Ordinary Kriging informed by a domain specific variogram model, applied to a database of 39,098 composites. Top cutting is applied selectively by domain and analyte to manage high grade outliers, and cell declustering is applied throughout to correct for clustered drill spacing. The resulting block model is validated through global mean comparison, swath plot analysis, and grade tonnage curve comparison, and is considered unbiased and geologically reasonable. Mineral Resources are reported in-situ and effective as of June 30, 2026.

Mineral resources are classified as Measured, Indicated or Inferred based on estimation pass number and slope of regression, and are reported at a cut-off of NSR > US$218/ton, reflecting updated operating cost assumptions from the 2026 Elk Creek Study (Table 1‑1).

Table 1‑1: Elk Creek Mineral Resource Estimate by Classification Inclusive of Reserves

Classification

Cut-off NSR (US$/ton)

Tonnage (Mtons)

Nb₂O₅ (%)

TiO₂ (%)

Sc (ppm)

TREO (%)

Measured

218

21.7

0.61

2.46

69.1

0.35

Indicated

218

187.4

0.5

2.36

59.85

0.36

Measured + Indicated

218

209.1

0.51

2.38

60.81

0.36

Inferred

218

169.2

0.38

2.14

51.02

0.39

 

Table 1‑2: Elk Creek Mineral Resource Estimate by Classification Exclusive of Reserves

Classification

Cut-off NSR (US$/ton)

Tonnage (Mtons)

Nb₂O₅ (%)

TiO₂ (%)

Sc (ppm)

TREO (%)

Measured

218

14.1

0.53

2.05

47.6

0.39

Indicated

218

149.0

0.43

1.70

42.5

0.39

Measured + Indicated

218

163.1

0.44

1.89

45.3

0.39

Inferred

218

169.2

0.38

2.14

51.02

0.39

Source: Dahrouge 2026

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

(1)
Mineral Resources are not Mineral Reserves and do not have demonstrated economic viability. There is no certainty that all or any part of the Mineral Resource will be converted to Mineral Reserves.
(2)
Mineral Reserves are reported separately in Section 12 of this report.
(3)
Prepared in accordance with Regulation S-K 1300
(4)
NSR cut-off of US$218/ton (US$240/tonne) based on longhole stoping underground mining; incorporates metallurgical recoveries of Nb 86.72%, TiO₂ 83.65%, Sc 92.00%, and REE by-products 92.00%, at metal prices of US$52.00/kg Nb, US$2,000.00/kg Sc, US$1.86/kg TCl4, US$1,845.00/kg Tb₂O₃, US$125.00/kg NdPr, and US$8.97/kg SEG carbonate.
(5)
TREO = LREO + HREO expressed as a percentage (TREO% = TREO ppm ÷ 10,000)
(6)
Tonnages in millions of short tons (Mtons). Grades rounded to reflect the approximate nature of resource estimates.
(7)
Totals may not sum due to rounding.

 

This estimate supersedes the 2022 Mineral Resource Estimate and reflects the introduction of a Measured category, revised Inferred tonnage in the DOL_CARB domain, and an increased NSR cut-off. Full detail on the estimation methodology, parameters, and classification criteria is provided in Section 11 of this report.

1.8 Mineral Reserve Estimation

The Project has advanced from late-stage exploration into initial development, with underground long hole stoping identified as the preferred mining method based on the Deposit geometry and available geotechnical information. The mine plan incorporates paste backfill to improve recovery, enable adjacent stope extraction, and reduce the need for rib pillars. Mineral Reserves were defined by applying appropriate modifying factors to Measured and Indicated Mineral Resources in accordance with Regulation S-K 1300.

As of June 30, 2026, the Elk Creek underground Mineral Reserve Estimate totals 45.93 million tons, comprising 7.57 million tons Proven and 38.36 million tons Probable reserves at an NSR cut-off of US$218/ton. The total reserve grades average 0.759% Nb₂O₅, 2.68% TiO₂, 69.3 ppm Sc, and 0.34% TREO. The reserve supports a 43-year life of mine (3 years development, 40 years operating), with a design strategy targeting an average cut-off grade of 0.650% Nb₂O5 and a life-of-mine average NSR of US$590.84/ton. Mineral Reserves are represented as in-situ, as of June 30, 2026.

Table 1‑3 Elk Creek Mineral Reserves

2026 Reserve

Mineral Reserve Classification

Cut-off NSR

Tonnage

Grade

Grade

Grade

Grade

(US$/ton)

(ton)

(Nb2O5%)

(TiO2%)

(Sc ppm)

(TREO %)

Proven

218

       7,570,098

0.760

2.70

71.5

0.32

Probable

218

    38,359,365

0.759

2.67

68.8

0.35

Total

218

    45,929,462

0.759

2.68

69.3

0.34

 

Classification

Tonnage (ton)

Nb2O5 Grade (%)

FeNb (ton)

Payable Nb (ton)

TiO2 Grade (%)

Payable TiCl4 (ton)

Sc Grade (ppm)

Payable Sc2O3 (ton)

TREO Grade (ppm)

Payable TREO (ton)

Proven

  7,570,098

  0.76

 53,651

  34,873

2.70

405,938

71.5

 762

3,232

22,509

Probable

38,359,365

  0.76

271,386

176,401

2.67

2,036,334

68.8

 3,717

3,489

123,115

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Total

45,929,462

  0.76

325,038

211,274

2.68

2,442,272

69.3

 4,479

 3,446

145,625

Source: Amplify Mine Planning LLC, 2026.

Notes:

(1)
All figures are rounded to reflect the accuracy of the estimates. Totals may not sum due to rounding.
(2)
The Qualified Person for the Mineral Reserve estimate is Amplify Mine Planning LLC. The estimate has an effective date of June 30, 2026.
(3)
The Mineral Reserve is based on the mine design and mine plan, utilizing an average cut-off grade of 0.650% Nb2O5 with an NSR of US$ 218/ton.
(4)
The estimate of Mineral Reserves may be materially affected by metal prices, environmental, permitting, legal, title, taxation, socio-political, marketing, infrastructure development, or other relevant issues.

 

The underground mine design uses primary and secondary stoping within three mining horizons separated by partially recoverable sill pillars. Standard stope dimensions are planned at approximately 49 ft wide, with variable stope lengths of 33 ft to 49 ft and 131 ft level spacing. Primary and secondary stopes are expected to achieve 95% recovery, while sill pillar stopes are assigned 62.5% recovery. Mining dilution averages approximately 6%, derived from 3% dilution for primary stopes, 9% for secondary stopes, and 5% for ore development.

Access to the deposit will be provided by two spiral ramps driven from a surface box cut: a primary access ramp for personnel, equipment, services, intake ventilation, and logistics; and a secondary haulage ramp serving as exhaust ventilation, a secondary escapeway, and the route for a Railveyor® ore haulage system. The haulage ramp has been extended deeper than prior feasibility study designs to reflect the increased Mineral Reserve base and to improve access to higher-grade ore zones. The Railveyor® system is sized to support the planned daily mine and mill production requirements.

Ore will be mined using underground LHDs, trucks, ore passes, conveyors, and the Railveyor® system for transport to surface stockpiles. Mine access, underground infrastructure, surface infrastructure, ventilation, tailings, and material handling systems have been designed to align with production requirements and the selected mining method. Based on the information presented, no known environmental, permitting, legal, socio-economic, marketing, political, or other factors are currently identified that would materially affect the underground Mineral Reserve Estimate.

1.9 Mining Methods

Geomechanical investigations included core logging, televiewer surveys, laboratory rock strength testing, and numerical modelling. Geomechanical analyses supported the selected mining method, stope dimensions, dilution assumptions, ground support requirements, and backfill strength criteria.

The selected mining method for the deposit is underground longhole stoping with cemented paste backfill, chosen to balance economic viability, geotechnical suitability, orebody geometry, and the need for selective extraction of higher-grade Nb₂O₅ mineralization. While bulk mining methods such as block or sub-level caving may be technically and economically feasible, they were not preferred due to limited grade selectivity under the 3,047 tpd milling constraint. The mine plan is organized into three resource blocks mined generally together using a declining-grade strategy, with bottom-up sequencing, primary/secondary stoping, and partial sill pillar recovery. Stope designs use 49 ft widths, 33–49 ft panel lengths, and 131 ft level spacing, with dilution of approximately 6% and 95% ore recovery applied. The resulting design supports approximately 45.93 million ore tons at 0.759% Nb₂O₅, producing an estimated 316,099 tons of ferroniobium over a mine life of about 43 years,

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

including 40 years at full production. The schedule targets steady-state production of 3,047 tpd and approximately 8,282 t/y ferroniobium, with production beginning 16 months after ramp development starts and ramping up over the following six months.

1.10 Recovery Methods

The recovery process is an integrated multi-stage hydrometallurgical flowsheet designed to extract and separate the following products: niobium, titanium, scandium, and four magnetic rare earth elements (Pr, Nd, Tb and Dy) from the Elk Creek Ore. All major unit operations are commercially demonstrated technologies. The overall circuit has been engineered to achieve commercially relevant specification for all products while minimizing tailings.

The principal commercial products are niobium oxide intended for conversion into ferroniobium, titanium tetrachloride (TiCl₄), high-purity oxides of didymium (NdPr), terbium, dysprosium and scandium. Mixed SEG (Sm, Eu, Gd) and HREY (Ho, Er, Tm, Yb, Lu, Y) carbonate concentrates are produced as secondary products.

Process sequence:

• Area 100 – Ore Activation: Indirect-fired calcination converts carbonate minerals to oxides and recovers CO₂ for reuse.

• Area 200 – Ammonium Chloride Cycle: Two-stage counter-current ammonium chloride leaching selectively removes calcium and magnesium from the ore. Both are mineralized as carbonates, fully regenerating the ammonium chloride solution; a portion of the carbonates is used in the process for neutralization purposes while the excess reports to paste backfill.

• Area 300 – Hydrochloric Acid Leach: Two-stage counter-current HCl leaching dissolves the rare earth elements (including scandium) and associated impurities, generating a pregnant leach solution for solvent extraction and a niobium-titanium residue.

• Area 400 – Sulfuric Acid Treatment: Acid baking, water leaching, hydrolysis and calcination convert the niobium-titanium residue into a chlorination feed.

• Area 500 – Chlorination: Fluid-bed chlorination followed by staged condensation and purification produces commercial-grade TiCl₄. Niobium and iron are recovered as a mixed chloride that is hydrolyzed and calcined to an oxide intermediate feed to pyrometallurgy for ferroniobium production.

• Area 600 – Rare Earth Element Recovery: Diglycolamide solvent extraction recovers scandium and the rare earths from the HCl pregnant leach solution.

• Area 700 – Rare Earth Separation: A multi-circuit solvent extraction unit using Cyanex 801 and Cyanex 572 extractants separates the mixed rare-earth solution into high-purity didymium, terbium, dysprosium and scandium oxides, together with the two mixed carbonate by-products.

• Area 800 – Chloride Recovery: Pyro-hydrolysis of the chloride waste streams regenerates hydrochloric acid and recovers metal oxides for disposal into paste backfill.

• Area 900 – Sulfate Effluent Management: Neutralization and dewatering of sulfate streams produce solids suitable for paste backfill, with treated water returned to the process.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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The flowsheet is deliberately sequenced to first remove acid-consuming calcium and magnesium, then extract the rare earths and scandium together with the majority of the base metals, followed by treatment of the refractory niobium-titanium minerals, and finally recovery and recycle of the principal reagents (ammonium chloride, hydrochloric acid, and carbon dioxide). This design supports efficient production of multiple critical minerals while minimizing consumable requirements and environmental discharges.

1.11 Project Infrastructure

There are several local communities near the Project, including Elk Creek, Tecumseh, Pawnee City and Syracuse that are intended to provide local housing for the Project construction and operating staff. There are several other communities within driving distance, and the large cities of Lincoln and Omaha are within reasonable driving distance. Both cities have substantial regional airports.

Presently, the site has no existing infrastructure except for access via the Nebraska State Highway 50 and County Road 721. The Project will be accessed from the North from County Road 721 through a guarded gate house into the Project property. A secondary access point is available on the east side of the project from Highway 50.

The Project will incorporate surface and underground infrastructure, as well as surface tailings and salt storage facilities. The offsite infrastructure includes a water supply pipeline from the City of Tecumseh along with temporary and permanent natural gas pipelines.

On-site power will be provided by a third party microgrid based off modular 2.5 MW natural gas fired generators, rated at approximately 50 MW. A small amount of grid power (200 kW) will also be used. Telecommunications service will be provided by the local telecom supplier with on-site telecommunications distribution consisting of a combination of hardwire and fiber optics systems.

The on-site surface infrastructure will include:

•
the microgrid generation system, including switchgear, transformer and a power distribution system;
•
on-site telecommunications;
•
fuel storage and dispensing system for above ground vehicles;
•
temporary fuel storage and dispensing system for the underground mine during mine construction;
•
truck scale;
•
process water treatment center;
•
potable water/fire water system including tankage, distribution and hydrants;
•
sanitary wastewater collection system with lift stations pumping to an on-site sewage lagoon
•
natural gas distribution to site loads; and
•
access roads to the site with parking, fencing and security.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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Infrastructure building facilities will have an administration building and security gate house, assay laboratory, combination warehouse and maintenance shop, modular warehouse/maintenance shop offices, process water treatment plant building, and the mine change building.

The mining related facilities will include a lined mine waste rock and ore storage area, surface water control facilities, and the tailings and salt impoundments. The mine surface facilities include the mine portal, surface Railveyor installation and Railveyor maintenance facility, mine control room, mine substations, paste backfill plant, the mine ventilation system and the mine dry.

The underground facilities will include shop / warehouse areas, offices, explosives storage areas, electrical distribution system, water pumping and discharge system, process water distribution, ventilation infrastructure, compressed air distribution, and the backfill distribution system. The underground material handling system includes three loadout facilities equipped with grizzlies to load the Railveyor system, which will transport ore and waste to surface.

A modular grout plant will be constructed near injection well NEC15-003 at the approximate geographic center of the resource. The grout plant will provide grout for the underground grouting program in the first year of construction, as well as shotcrete for underground use. The modular grout plant will then be relocated adjacent to the mine portal and will continue to supply shotcrete for mine use.

1.11.1 Tailings

The tailings storage facilities (“TSFs”) are designed for storage of paste tailings solids in lined facilities permitted under State of Nebraska Industrial Solid Waste regulations. Based on the parameters and assumptions outlined in Section 18.11, the TSFs have been designed with adequate containment and capacity to manage the planned production of waste streams over the life of the mine.

1.12 Markets and Contracts

Market studies for niobium, titanium dioxide and scandium trioxide are an important part of the proposed Elk Creek Mine. These products, especially niobium and scandium trioxide (scandium), are thinly traded without an established publicly available price discovery mechanism. Marketing studies and product price assumptions are based on research, and forecasts and NioCorp management’s knowledge of the markets for the following products:

•
Niobium: CMP Group Market Report, 2025
•
Scandium: OnG Market Reports, 2025 and 2026
•
Titanium: TZMI Market Report and Pricing Estimate, 2025
•
Magnetic Rare Earths: Adamas Intelligence Q2/25 outlook, base case
•
SEG and Heavy Rare Earths: Adamas forecast 2025, base case

NioCorp is considering selling ferroniobium, scandium trioxide and titanium dioxide products from the Project through all avenues, which include entering into long-term offtake contracts and Letters of Intent with buyers.

Niobium, titanium, scandium and rare earth elements (“REEs”) comprise the mineral reserve reported in this Technical Report Summary, as well as the mineral resource. The rare earth elements (lanthanides plus yttrium), comprise a wide variety of markets, some more thinly traded and opaque

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

than others. However, the "magnetic” rare earths (neodymium, praseodymium, terbium, and dysprosium) which are used to manufacture rare earth permanent magnets are more widely traded and are the primary REEs of interest for the Project. The Company has utilized market studies and forecasts from Adamas Intelligence (Adamas Intelligence, 2019 and 2022) to support inclusion of the REEs into the mineral resource.

At the time of this report, NioCorp had entered into two off-take agreements covering 75% of the

ferroniobium and an MOU for the balance of production.

It is assumed that product not covered by an offtake agreement will be sold on a spot price, ex-mine gate basis.

1.13 Environmental Studies, Permitting & Social or Community Impact

NioCorp has developed information and conducted the following environmental studies for baseline site characterization:

•
Soils
•
Climate/meteorology/air quality
•
Cultural and archeological resources
•
Vegetation
•
Wildlife
•
Threatened, endangered, and special status species
•
Land use
•
Hydrogeology (groundwater)
•
Hydrology (surface water)
•
Wetlands/riparian zones
•
Geochemistry (Section 17.1.10)

There are low levels of naturally occurring radioactive materials (NORMs) in this ore body. Therefore, waste materials (e.g., RO treatment salts and process waste/tailings), water sourced from the carbonatite and wastewater have the potential for low radioactivity levels. Gross alpha, gross beta, and radioactivity of nine isotopes analyzed in process tailings indicated that fugitive dust and external radiation exposure are potential concerns for this setting. Three parameters (gross alpha, Ra-226, and Ra-228) exceeded the screening level but were below respective MCLs. Results indicate that the site materials are non-hazardous and will be permitted/managed as non-hazardous.

Confirmation testing will be performed as the mine processes are developing and as permitting processes proceed. These waste materials will be landfilled in the on-site solid waste disposal units and closed according to those permits.

Dewatering will be required during excavation of the mine portal. A construction dewatering permit has been secured from the Nebraska Department of Water, Energy, and Environment (DWEE) and NioCorp will maintain compliance with conditions of this permit. Dewatered groundwater from the portal excavation will be directed to a stormwater detention pond which will gradually discharge to an intermittent tributary to Elk Creek.

Demonstration process plant residuals (water leach residue, Fe-oxide, and Mg/Ca Carbonate) were analyzed with a comprehensive suite of static tests. Tailings were also characterized using the Toxicity Characteristic Leaching Procedure (“TCLP”), including the eight inorganic substances

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

expected to be present in the material (organic parameters are not expected to be present in the material). This set of results has no parameters exceeding regulatory action levels. Details can be found in Section 17.1.10.

Detailed geochemical results from the demonstration process plant indicated, in sum, that while some waste material contained acidic characteristics, treatment and disposal facilities planned for the site would be sufficiently protective of the environment. Acid-base accounting results indicate that water leach would not have persistent acid-containing potential.

Excavated portal material/uncontaminated overburden consists of marine sediments and will be crushed and used as construction fill/material.

The permitted solid waste disposal units will receive waste from the surface production plant and from the mining operation. These waste sources include waste rock, tailings, process wastes, and slag. Waste rock sourced from the carbonatite will be placed in a lined impoundment on the surface or co-disposed with the tailings in lined impoundments. Plant waste streams will be combined with water, cement, and fly ash and either pumped underground as structural fill in the underground mine or pumped to engineered and lined surface disposal impoundments. Pyrometallurgical slag will be hauled to the same engineered and lined surface disposal impoundments.

Once the mine is in operation, it is expected up to 200 gpm of mine groundwater will be pumped and treated through an RO treatment system. This clean water will be used in the process plant, and the RO reject will be evaporated and crystallized and disposed of in the onsite Salt Management Cell.

Stakeholder engagement has been previously completed for the Project, including town halls (Most recently in December 2025) and individual meetings with pertinent stakeholders. NioCorp met with Johnson, Pawnee, Nemaha, and Richardson County representatives as well as representatives from the Southeast Nebraska Development District (Batty et al. 2022). No additional stakeholder engagement has been identified for the Project at this stage, as the community at large remains supportive of the Project.

The mineral exploration process is permitted through Nebraska’s Mineral Exploration Permit. Nebraska does not have a specific permit for operating mines but has a comprehensive permitting process that applies to any industrial undertaking. This permitting process includes mining plans, mining reclamation and bonding/financial assurance. While the formal operational permitting program for the Project is dependent upon the completion of the mine plan, preliminary permitting and consultation as necessary to initiate portal excavation and construction has been completed. These permits and authorizations have allowed for the commencement of mine portal excavation and construction, and other construction and operations permits as needed have been scheduled for initiation as needed to support the remaining stages of construction and commencement of operation.

The Project has or will provide these items including financial surety for proper closure and reclamation of the site; the estimated direct cost for closure and reclamation, is US$106 million using a 2026 cost basis.

Engagement of local and state regulators is currently in progress. At this time, NioCorp has completed the following:

(1)
Nebraska Department of Water, Energy, and Environment (DWEE) Mineral Exploration Permit for exploration drilling;

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

(2)
DWEE air quality construction permit;
(3)
DWEE authorization for Class V underground injection well for the hydrogeological portion of the exploration drilling;
(4)
Johnson County road use and maintenance agreement;
(5)
Johnson County special use permit;
(6)
DWEE construction stormwater permit;
(7)
DWEE construction dewatering discharge permit;
(8)
notification of Commencement of Operations with the Mine Safety and Health Administration (MHSA); and
(9)
Johnson County floodplain development permit.

At this time, there are no known environmental concerns that would materially impact NioCorp’s ability to extract the mineral reserves at the Elk Creek Project. Environmental permitting timelines at the state level require up to six months for processing of most individual permits, with roughly 18 months needed for solid waste permitting for tailings impoundments. Broadly speaking, general permits can be active within seven to 10 days of providing a full and complete application package.

1.14 Capital Cost Estimate

Table 1‑4 shows the breakout in initial and sustaining capital estimates. An overall 14% contingency factor has been applied to the initial capital estimate. The pre-production period is defined as the first 35 months, after which the mine and plant are operating at nameplate capacity.

Table 1‑4: Capital Costs Summary (US$ 000’s)

Description

Initial

Sustaining

Total

Capitalized Preproduction Expenses

$2,506

 

$2,506

Site Preparation and Infrastructure

$24,722

$42,032

$66,754

Processing Plant

$870,468

$309,322

$1,179,790

Water Management & Treatment

$13,000

 

$13,000

Mining Infrastructure

$144,938

$382,347

$527,285

Tailings Management

$56,874

$168,930

$225,804

Site Wide Indirects

$3,894

 

$3,894

Processing Indirects

$33,620

 

$33,620

Mining Indirects

$169,167

$999,917

$1,169,084

Owner's Costs Indirects

$296,437

$2,522

$298,959

Closure and Reclamation

$0

$95,930

$95,930

Contingency

$233,409

$169,168

$402,577

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Description

Initial

Sustaining

Total

Total Capital Costs

$1,849,036

$2,170,168

$4,019,204

Source: NioCorp 2026

1.15 Operating Cost Estimate

Operating cost estimates were developed to show monthly and annual costs for production. All unit costs are expressed as US$/ton processed and are based on Q2 2026 US$. Operating cost metrics in the technical economic model are developed on a unit rate basis and applied to the 40-year operating period of the project, from the end of construction to the end of the mine life.

The total operating cost unit rate of US$ 268.78/st processed is summarized in Table 1‑5.

Table 1‑5: Operating Cost Summary

Description

LOM
$/st ore

Hydromet

128.01

Mining

71.34

Pyromet

17.69

Water Management

14.44

Site G&A

13.26

Infrastructure

8.60

Paste Plant

7.34

Mineral Processing

7.12

Product Packaging

0.97

Total

268.78

Source: NioCorp 2026

 

1.16 Economic Analysis

The results of the economic analysis represent forward-looking information that is subject to a number of known and unknown risks, uncertainties and other factors that may cause actual results to differ materially from those presented here. Forward-looking statements in this Report include, but are not limited to, statements with respect to future niobium, scandium, titanium and rare earth prices, the estimation of Mineral Resources and Mineral Reserves, the estimated mine production and niobium, scandium, titanium, and rare earths recovered, the estimated capital and operating costs, and the estimated cash flows generated from the planned mine production.

Actual results may be affected by:

•
Differences in estimated initial capital costs and development time from what has been assumed in this Technical Report Summary.

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•
Unexpected variations in the quantity of ore, grade or recovery rates, or presence of deleterious elements that would affect the process plant or waste disposal.
•
Unexpected geotechnical and hydrogeological conditions from what was assumed in the mine designs, including water management during construction, mine operations, and post mine closure.
•
Differences in the timing and amount of estimated production, costs of future production, sustaining capital requirements, future operating costs, assumed currency exchange rate, requirements for additional capital, and unexpected failure of plant, equipment or processes not operating as anticipated.
•
Changes in government regulation of mining operations, environment, and taxes.
•
Unexpected social risks, higher closure costs and unanticipated closure requirements, and mineral title disputes.

The production schedules and financial analysis annualized cash flow tables are presented with conceptual years shown. Years shown in these tables are for illustrative purposes only. If additional mining, technical, and engineering studies are conducted, these may alter the Project assumptions as discussed in this Report and may result in changes to the calendar timelines presented and the information and statements contained in this Report.

The technical economic model metrics are prepared on an annual pre-tax and after-tax basis, the results of which are summarized in Table 1‑6. Based on current assumptions and design listed in this Report, the project returns a pre-tax NPV 8% of US$ 4,111 million and an IRR of 24.0% along with an after-tax NPV 8% of US$ 3,441 million and IRR of 22.8%.

Table 1‑6: Indicative Economic Results

Pre-Tax NPV8% ($M)

$4,111

Pre-Tax IRR

24.0%

After-Tax NPV8% ($M)

$3,441

After-Tax IRR

22.8%

After-Tax Payback Period (years)

2.93

Total Upfront CAPEX ($M)

$1,849

Mine Life (years)

40

LoM Gross Revenue ($M)

$37,435

Niobium ($M)

$9,781

Scandium ($M)

$14,331

Titanium ($M)

$3,946

Rare Earths ($M)

$9,378

NdPr Oxide ($M)

$3,255

Dy Oxide ($M)

$3,137

Tb Oxide ($M)

$2,827

SEG Carbonate ($M)

$113

Heavy Rare Earth Carbonate ($M)

$46

Average Annual EBITDA ($M)

$608

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Average EBITDA Margin1 over LoM (EBITDA as % of total revenue)

67%

Average Annual Operating Cash Flow over LoM ($M)

$519

Revenue Per Ton, (US$/ton)

$815

Annual Operating Cost (OPEX) (US$/ton)

($255)

Effective Tax Rate

14.3%

Development Timeline (months)

35

Source: NioCorp 2026

1.17 Conclusions and Recommendations

Based on the data available and the analyses described in this Technical Report Summary, the Project has a valid Mineral Resource and Mineral Reserve. The Elk Creek deposit is a carbonatite-hosted, multi-element system defined by drilling and geophysics across three estimation domains (MCARB, DOL_CARB, LAMP); the Mineral Resource Estimate, effective June 30, 2026 and prepared in accordance with Regulation S-K 1300 which totals 209.1 Mt Measured + Indicated and 169.2 Mt Inferred at a US$218/ton NSR cut-off, and is considered unbiased and geologically reasonable based on domain-specific variography, Ordinary Kriging, and validation against the declustered composite mean. DGC is not aware of any drilling, sampling, or QA/QC factors that would materially affect the reliability of the resource database. Key uncertainties are geological confidence at depth and along the peripheral DOL_CARB domain margins, the relatively large Inferred tonnage compared to Measured and Indicated, and the sensitivity of the NSR cut-off to metallurgical recovery and commodity prices across seven analytes, particularly niobium and scandium. Long-hole open stoping, with a primary/secondary paste-backfill sequence, is confirmed as the appropriate mining method based on geotechnical characterization, and the mine design, production schedule (3,047 tons/d steady state), and grouting-based hydrogeological control plan are considered technically sound.

Metallurgical testing indicates the ore is amenable to standard grinding or HPGR comminution, and demonstration-plant operation of the hydrometallurgical circuit has achieved high recoveries of niobium, scandium, rare earths, and titanium (84.7% Nb, 80.5% Ti, 94.3% Sc, 88.7-94.4% NdPr, 94.4% Tb, 94.6% Dy), supported by a flowsheet update that reduced acid consumption, reagent use, and process complexity while adding rare earth products. The Pyromet program has established the technical feasibility of producing ferroniobium alloy from Hydromet feed via aluminothermic reduction; SMH, MCS, and Magemi Mining are confident the design will yield the expected product suite, though further development work is required to confirm slag behavior, feed consistency, and refractory selection at commercial scale. Project infrastructure, including power, water, and site facilities, is expected to meet the Project's needs based on current design assumptions, and six tailings storage facilities have been designed with adequate capacity for the mine plan. It is recommended that hydrometallurgical optimization continue, focused on the ammonium chloride and chloride pyrohydrolysis circuits and on larger-scale piloting of the chlorination and rare earth separation units to reduce capital cost and finalize process calibration; that a larger-scale Pyromet test program be conducted using representative Hydromet feed to confirm design parameters, refractory compatibility, and phosphorus control at commercial scale; and that a comprehensive paste backfill testing and heat-integration (Pinch Analysis) program be undertaken to address the identified impact of carbonate content on backfill strength and to optimize energy recovery in the Hydromet flowsheet.

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No known environmental factors are expected to materially affect the Project's ability to extract its mineral reserves, and NioCorp has obtained the permits needed to commence mine portal excavation and construction, with a current closure and reclamation cost estimate of US$106 million; risks remain in the permitting process given the limited precedent for this type of mining in Nebraska. Market studies support the marketability of the Project's product suite notwithstanding thinly traded pricing, with offtake and marketing agreements in place for a substantial portion of planned production. Total life-of-mine capital costs are estimated at US$4,019 million (including initial capital of US$1,849 million over a 35-month construction period), and total operating costs are estimated at US$268.78 per ton processed; on this basis, the Project is expected to generate a pre-tax NPV (8% discount) of US$4,111 million and an IRR of 24.0%, and a post-tax NPV of US$3,441 million and an IRR of 22.8%, over a 40-year mine life. Olsson recommends continued, transparent engagement with identified stakeholders and with state and local regulators throughout construction and operation, to maintain a shared, current understanding of the mine plan and to keep permitting timelines predictable as the Project advances toward construction.

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2 Introduction

2.1 Registrant

This Technical Report Summary (this “Technical Report Summary,” “TRS” or “Report”) was prepared in accordance with Item 601(b)(96) and subpart 1300 of Regulation S-K (“Regulation S-K 1300”) promulgated by the United States Securities and Exchange Commission (“SEC”) for NioCorp Developments Ltd (“NioCorp” or “the Company”).

The TRS was prepared by Qualified Persons listed in Section 1 for the proposed Elk Creek, Nebraska Critical Minerals Mine (the “Elk Creek Mine,” the “Elk Creek Project” or the “Project”), located in southeastern Nebraska.

NioCorp is a publicly held company with its corporate office located at:

7000 S. Yosemite Street, Suite 115

Centennial, Colorado 80112 USA

 

This Technical Report Summary summarizes the results of a pre-feasibility study (as that term is defined under Regulation S-K 1300) (the “2026 Elk Creek Study”) prepared by the Qualified Persons. The reason that the 2026 Elk Creek Study does not qualify as feasibility study under Regulation S-K 1300 is because additional work with respect to the engineering of and procurement for the planned surface plant is required to allow the Qualified Person to reduce the overall contingency range attributed to the initial capital expenditure estimate for the Elk Creek Project from the current 14% to less than or equal to 10%.

2.2 Terms of Reference and Purpose of the Report

This Technical Report Summary has been prepared for NioCorp in accordance with the requirements of Regulation S-K 1300. The purpose of the TRS is to provide a technical summary of the Elk Creek Project.

The Elk Creek Project is an existing project for which previous exploration, drilling, geological interpretation, metallurgical testwork, engineering studies, and other technical evaluations have been completed. The current study incorporates the available historical information together with subsequent technical work and updated project assumptions considered appropriate as of the effective date of this TRS.

The scope of the 2026 Elk Creek Study includes, as applicable, an update, review and evaluation of the geological database, data verification and quality assurance/quality control procedures, update of the Mineral Resource estimation and Mineral Reserve estimation, geotechnical and hydrogeological considerations, mining methods, metallurgical testwork, mineral processing and recovery methods, infrastructure requirements, environmental and permitting considerations, market assumptions, capital and operating cost estimates, and economic analysis.

The conclusions and estimates presented in this TRS are based on information available to the Qualified Persons as of the effective date of June 30, 2026. The Qualified Persons have reviewed the information relevant to their respective areas of responsibility and consider the data and supporting technical studies adequate for the purposes of the disclosures presented in this TRS.

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2.3 Sources of Information

The parties responsible for generating this TRS are listed on Page i.

The sources of information provided by NioCorp and utilized in the preparation of this Report include:

•
Information on land ownership and land agreements in the Project Area
•
Information on permitting requirements for the Project and the status of the Company’s permitting efforts
•
Information related to NioCorp’s relationships with local community and community groups
•
Market reports and market data related to niobium, scandium, titanium and rare earth elements

The Qualified Persons relied on certain information provided by the following persons in preparation of portions of this Technical Report Summary. The Qualified Persons responsible for the sections of this Technical Report Summary indicated below have reviewed and adopted such information and do not disclaim responsibility therefor.

•
Dr. Andrew Matheson, OnG Commodities – Sections 16.1.3 and 16.3.1 (Scandium Market)
•
Cari Anderson, SRK Consulting – Section 17.5 (Reclamation and Closure)
•
Mark Willow, SRK – Section 17.5 (Reclamation and Closure)
•
David Bird, M.Sc, PG, Consulting Hydrogeochemist, Section 17.2 (Waste Management and Disposal)

External sources of information used to prepare the TRS are listed in Section 24 (References).

2.4 Effective Date

The overall effective date of this Technical Report Summary is June 30, 2026.

2.5 Details of Inspection

A summary of the Qualified Persons that completed a site visit are summarized below in Table 2‑1.

Table 2‑1: A summary of the site visit inspections by the QP consultants

QP

Company

Expertise

Date(s) of Visit

Details of Inspection

Anthony (Tony) Linton

Dumas Contracting USA Inc.

Mine Engineering

March 10 to 11, 2026

View ongoing Portal Excavation

Trevor Mills

Dahrouge Geological Consulting USA Ltd.

Geology

Multiple times from April 24, 2025 through November 17, 2025

Review of drill core, review, verification of the geological setting / environment, logging, sampling, analytical, QA/QC, site facilities.

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QP

Company

Expertise

Date(s) of Visit

Details of Inspection

Jacob Andersdon

Dahrouge Geological Consulting USA Ltd.

Geology Resources

September 8 to 10, 2025

Review of drill core, review, verification of the geological setting / environment, logging, sampling, analytical, QA/QC, site facilities, drill collar locations

Janine Brown

Dahrouge Geological Consulting USA Ltd.

Geology

May 10 to 16, 2025

Review of drill core, review, verification of the geological setting / environment, logging, sampling, analytical, QA/QC, site facilities.

Amélie C. Ouellet

Andrieux & Associates Geomechanics Consulting

Rock Mechanics

May 13-14, 2025

Review of drilling operations and drill core logging

Scott Britton

 

Amplify Mine Planning

Reserves/Mining

March 30 to 31, 2026

Review of field operations, resource and reserve locations, property position

Adrian Brown

Adrian Brown Consultants Inc

Hydrogeology

July 25 to August 12, 2025;

September 23 to September 25, 2025

Oversight of drilling operations related to hydrogeologic investigations and grouting test program.

Troy Meyer

Tierra Group/BBA

Tailings

January 22, 2026

Review of field operations, resource and reserve locations, property position

Eric Larochelle

SMH Process Innovation

Hydrometallurgy & Process Engineering

March 12, 2026

Review of field operations, resource and reserve locations, property position

 

2.6 Qualifications of Qualified Persons

The Qualified Persons preparing this Report are specialists in the fields of geology, exploration, Mineral Resource and Mineral Reserve estimation and classifications, underground mining, mining backfill, geotechnical, environmental, permitting, metallurgical testing, mineral processing, processing design, pipeline design, capital and operating cost estimation, and mineral economics.

None of the Qualified Persons, nor any associates involved in the preparation of this Technical Report Summary, holds any beneficial interest in NioCorp. The Qualified Persons are not insiders, associates, or affiliates of NioCorp. The conclusions and results presented in this Technical Report Summary are independent and are not influenced by any prior agreements regarding the outcomes to be reached, nor are there any undisclosed arrangements concerning future business dealings between NioCorp and the Qualified Persons. The Qualified Persons have been compensated for their services in accordance with standard professional consulting practices.

Technical expertise and specialist services used in the preparation of this Technical Report Summary were provided by the Qualified Persons identified in Table 2-2. The areas of contribution included geology, exploration, Mineral Resource and Mineral Reserve estimation, mining, geotechnical

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engineering, environmental studies and permitting, metallurgy and mineral processing, infrastructure design, cost estimation, and mineral economics.

The Qualified Persons, along with the sections of this Technical Report Summary for which they are responsible, are identified in Table 2‑2.

Table 2‑2: List of Qualified Persons responsible for sections of this Report

Qualified Person

Sections

Dahrouge Geological Consulting USA Ltd.

1.1 to 1.5, 1.7, 1.12, 1.17, 2, 3, 4, 5, 6, 7, 8, 9, 11, 16, 20, 22.1, 22.7, 23.1, 23.9, 24, and 25

SMH Process Innovation

1.6, 1.6.2, 1.10, 10, 10.1, 10.3, 14.1, 14.2, 14.2.2, 14.3, 14.3.2, 14.4, 14.4.2, 14.5, 14.5.2, 14.6, 14.6.2, 22.3, 22.4, 23.2, and 23.6

Dumas Contracting USA Inc.

13.4.5, 13.5.2, 13.7, 13.8, 13.9, 15.2.3, 15.2.4, and 15.6.1

Amplify Mine Planning LLC

1.8, 1.9, 12, 13.1, 13.4, 13.4.1, 13.4.2, 13.4.3, 13.4.4, 13.5, 13.5.1, 13.5.3, 13.5.4, 13.6, 13.6.1, 13.6.2, 13.6.3, 13.6.6 22.2 and 23.4

Tierra Group/BBA

1.11.1, 15.8, 15.9, 15.10, 15.11, 15.12, and 22.5.1,

Olsson

1.13, 17, 22.6, and 23.8

Adrian Brown Consultants Inc.

13.3

Andrieux & Associates Geomechanics Consulting, L.P.

13.2, 13.6.5, and 23.3

Tetra Tech

1.11, 14.7, 15.1, 15.2, 15.2.1, 15.2.2, 15.3, 15.4, 15.5, 15.6, 15.6.2, 15.7, 22.5, and 23.7

T Engineering

13.6.4 and 15.13

Magemi Mining Inc.

1.6.1, 10.2, 14.2.1, 14.3.1, 14.4.1, 14.5.1, and 14.6.1

Metallurgy Concept Solutions

1.6.3, 10.4, 14.2.3, 14.3.3, 14.4.3, 14.5.3, 14.6.3, and 23.5

Scott Honan, M.Sc., SME-RM, NioCorp

1.14 to 1.16, 18, 19, 21, and 22.8

 

As described in Section 2.3, the Qualified Persons reviewed and incorporated into their opinions and conclusions contained herein certain information that was provided to the Qualified Persons by NioCorp and others throughout the course of the investigations.

The Qualified Persons used their experience to determine if the information from previous reports was suitable for inclusion in this Technical Report Summary and adjusted information that required amending. This report includes technical information, which required subsequent calculations to derive subtotals, totals and weighted averages. Such calculations inherently involve a degree of rounding and consequently introduce a margin of error. Where these occur, the Qualified Persons do not consider them to be material.

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Except as specifically disclosed herein, the Qualified Persons have not independently verified legal, commercial, financial, taxation, permitting, or other non-technical information relied upon in this Technical Report Summary, nor have the Qualified Persons sought independent legal opinions regarding such matters.

2.7 Units of Measure

Unless otherwise noted, the following measurement units, formats and systems are used throughout this Report:

•
All references to measurement units use the Imperial System for measurement unless otherwise noted.
•
All references to orientation and coordinates in this Report are presented as UTM.
•
Currencies outline in this Report are stated in U.S. dollars (US$) unless otherwise noted.
•
Symbols and abbreviations used in this Report are outline in Section 24.2

3 Property Description & Location

3.1 Property Location

The Property is located in southeastern Nebraska, USA (Figure 3‑1M). The Property is situated within the United States Geological Survey (“USGS”) Tecumseh SE Quadrangle (7.5-minute series) mapsheet and encompasses Sections 1–6 and 9–11, Township 3 North, Range 11 East, as well as Sections 19–23 and 25–36, Township 4 North, Range 11 East. The approximate center of the Project is located at UTM coordinates 739240 E and 4461282 N (NAD83, Zone 14N). The Project is located approximately 47 miles southeast of Lincoln, the state capital of Nebraska, and 68 miles south of Omaha, Nebraska. The nearest municipalities are Elk Creek, located approximately 3 miles east-northeast of the Property, and Tecumseh, located approximately 7 miles north of the Project.

The mineralized body is located within Johnson County, Nebraska; however, NioCorp land ownership extends across both Johnson and Pawnee counties.

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img170397038_1.jpg

Source: DGC, 2026

Figure 3‑1: Project Location Map

 

3.2 Mineral Title and Land Tenure

The Property consists of a 709.93-acre (287.30 ha) parcel of land owned by the Company along with six option-to-purchase agreements covering approximately 1010.96 acres (463.72 ha). Option agreements are between NioCorp's subsidiary Elk Creek Resources Corp. (“ECRC”) and the individual landowners (Figure 3‑2). The surface and mineral rights owned by the Company were purchased in a series of transactions with landowners between 2021 and 2025. The parcel owned by the Company contains the Mineral Resources and Mineral Reserves associated with the Project. ECRC is a Nebraska-based wholly owned subsidiary of NioCorp. NioCorp retains 100% of the mineral rights to the Project and is the operator. The option agreements are in the form of pre-paid Exploration Lease Agreements (ELA), with an Option to Purchase (“OTP”) the mineral rights and/or the surface rights at any time during the term of the agreement. The individual landowners have title to the surface and subsurface rights, and the agreements are primarily concerned with only the mineral and surface interest of each property. The agreements convey to the Company adequate surface rights to access the land and to complete mineral exploration work. The parcels ECRC 5 and ECRC 1, of which the Company owns all surface and mineral rights, include all the Mineral Resources and Mineral Reserves described in this report. Active OTP agreements are listed in Table 3‑1.

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img170397038_2.jpg

Source: DGC 2026

Figure 3‑2: Project Tenure Map

 

Table 3‑1: Active Option to Purchase Agreements Covering the Project

Agreement Identifier

Hectares

Acres

Agreement Expiry

Beethe007

66.27

163.75

20-Jan-31

Heidemann005

79.55

196.57

16-Mar-30

Nielsen001

100.91

249.32

25-Jun-30

Woltemath002

152.49

376.81

4-Dec-29

Krueger001

32.78

63.79

12-Nov-30

Shuey001

32.37

80

27-May-40

Source: NioCorp 2026

The majority of the Mineral Resource is located on Company-owned parcels, and additional surface rights have been secured through OTP agreements as required. The Company’s land package provides sufficient area for mine waste and tailings disposal, a processing plant, and related infrastructure.

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3.2.1 Nature and extent of Issuer’s Interest

The Company has secured surface rights under the exploration OTP agreements, allowing access for drilling and related exploration activities. Certain agreements also include mineral rights subject to a 2% NSR royalty, with options to acquire the surface rights, mineral rights, or both during the agreement term.

3.3 Royalties, Agreements and Encumbrances

The leases covering the Property are 100% owned by NioCorp. Except for a 2% NSR royalty attached to the land owned by NioCorp and the OTPs that include the mineral rights, there are no other outstanding royalties, agreements, or encumbrances affecting the Property (Figure 3‑3).

img170397038_3.jpg

Source: DGC 2026

Figure 3‑3: Net Smelter Return (“NSR”) Map

3.4 Environmental Liabilities and Permitting

At this time, there are no known environmental concerns that would materially impact NioCorp’s ability to extract the mineral reserves or mineral resources near Elk Creek. Environmental permitting timelines at the state level require up to six months for processing of most individual permits, with roughly 18 months needed for solid waste permitting for tailings impoundments. Broadly speaking,

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general permits can be active within seven to 10 days of providing a full and complete application package

Exploration work conducted to date on the Project has been completed under Exploration Permit NE0211001 issued by the Nebraska Department of Environment and Energy (“NDEE”). The permit provides the Company with the right to have ten open boreholes active at the Project at any given time.

The Project will require various federal, state, and local permits for operations. Most permits are routine and involve standard applications and fees. Certain Nebraska permits, including a Solid Waste Permit and Air Operating Permit, are discretionary and require state approval. While the risk involved in such permits is low, such discretionary permits require more processing time by the state and do require the state agency to make a decision in favor of issuance of the permit.

Permit costs and timelines are included in the Project execution plan. The Company has already received a Construction Air Permit from the State of Nebraska and a Special Use Permit from Johnson County, Nebraska. Details on the project’s permitting requirements can be found in Section 0 of this report.

3.5 Other Significant Factors and Risks

There are no known other significant factors or risks which could have a material impact on the ability to affect access, titles, or the right to perform exploration and development work on the Project.

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4 Accessibility, Climate, Local Resources, Infrastructure and Physiography

4.1 Accessibility and Transportation to the Property

The Project is easily accessible year-round as it is situated approximately 47 miles southeast of Lincoln (State Capital), Nebraska and approximately 68 miles south of Omaha, Nebraska. Access to the site can be achieved via interstates and state highways from one of the regional airports. There are several regular scheduled flights to both Lincoln and Omaha (Figure 4‑1), with Omaha providing more regularly commercially serviced options.

From Eppley Airfield in Omaha, Nebraska, the Project is accessed via paved roads by the following:

•
Abbott drive to Interstate I-480 for approximately 3.4 miles until exit 425C to merge onto Interstate I-80W towards Lincoln, Nebraska;
•
Then continue west on interstate I-80 for approximately 15 miles until exit 440 for state highway NE-50.
•
Then head south on State Highway NE-50 for approximately 62 miles through Tecumseh, Nebraska to the Project entrance.

img170397038_4.jpg

Source: DGC 2026

Figure 4‑1: Project Access

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4.2 Climate and Length of Operating Season

Southeast Nebraska is situated in a Humid Continental Climate (Dfa) under the Köppen climate classification system. This climate is generally characterized by hot, humid summers and cold winters. Based on 1991–2020 climate normals for Tecumseh, Nebraska, average winter (January) temperatures are approximately 13°F to 35°F, while average summer (July) temperatures are approximately 65°F to 88°F.

Average monthly precipitation (rain and liquid-equivalent snowfall) at the Tecumseh 1S station ranges from approximately 0.8 inches to 5.3 inches, with a mean annual total of approximately 32.3 inches (30-year “Normal”). Average annual snowfall in Tecumseh is approximately 22 inches. Exploration and mining-related activities may be conducted year-round, although severe winter weather and spring/early-summer thunderstorm activity can periodically affect operations.

Nebraska is located within a region of the central United States that experiences severe thunderstorms and tornadoes, with peak tornado occurrence generally during May through July, although events can occur outside this period.

4.3 Physiography

The local topography of eastern Nebraska is relatively low relief with shallow rolling hills intersected by shallow river valleys. Elevation varies from 1,066 ft to 1,276 ft (325 to 390 m) above mean sea level. Bedrock outcrop exposure is nonexistent in the Project area.

Much of the Project area is used for cultivation of corn and soybeans, along with use as grazing land. Native vegetation typical of eastern Nebraska is upland tall-grass, prairie, and upland deciduous forests.

4.4 Infrastructure and Local Resources

Technical and trades personnel can be sourced from local colleges and universities. An underground-experienced mining-related workforce can be found around Weeping Water, Nebraska as well as in neighboring states such as Salt Lake City, Utah, South Dakota and Denver, Colorado (eight hours drive west of the Project).

Additional detailed information regarding specific infrastructure required for the Project can be found in Section 15.

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5 History

5.1 Exploration History

Regional airborne magnetic surveys were completed between November 1963 and January 1964 which identified regional features within southeast Nebraska. Further investigation of the Project was not completed until 1970 when a gravity survey was conducted by the Conservation and Survey Division (CS) of the University of Nebraska-Lincoln (“UNL”). Coinciding independent work was also being completed by the UNL geology department mapping the magnetic expression of the Nemaha Arch and Humbolt Fault systems. The comparison of the two surveys results identified a positive of the two geophysical survey results showed positive correlations between the magnetic and gravity anomalies which is now defined as the Elk Creek gravity anomaly (Anzman, 1976). The gravity survey outlined a near-circular anomaly, along with a concurrent magnetic anomaly, approximately 4.35 miles (7 km) in diameter. Analysis of the geophysical data provided a model of a cylindrical mass with of indefinite length with a radius of 5,500 ft (1,676 m) (Carlson & Treves, 2005).

This early work resulted in early drilling by the Nebraska Geological Survey and the United States Bureau of Mines. In 1971, test hole 2-B-71 intersected carbonatite with pyrochlore mineralization and elevated niobium and rare earth elements, confirming the source of the anomaly.

A private mineral leasing and exploration phase began in the early 1970s. Cominco American Inc. acquired mineral rights in 1973 and undertook exploration work, after which the rights were acquired by Molycorp in 1974. Molycorp completed detailed aeromagnetic surveying in 1973 and, in 1980, carried out a regional exploration program including gravity work, magnetic surveying, geologic mapping, surface sampling, and drilling. Between 1973 and 1986, Molycorp completed a regional drill program over an approximately 4.3 mi × 4.3 mi (7 km × 7 km) gravity anomaly, totaling 114 drill holes for approximately 157,992 ft (48,156 m). Within the Elk Creek Deposit area, 27 holes totaling 52,848 ft (16,108 m) were drilled during the 1970–1980 period, forming the foundation of the historical drilling database.

The TRS notes that no known exploration was completed on the Property between 1986 and 2011. In 2010–2011, Quantum initiated verification and modernization of the historical dataset through DGC, compiling and checking historical drilling, lithology, and assay information, and completing resampling of historical material to assess comparability with historical results. Quantum then completed a 2011 diamond drilling program consisting of five inclined holes totaling 11,220 ft (3,420 m) of HQ core; three holes 7,605 ft (2,318 m) targeted the Elk Creek Deposit and two holes tested regional REE targets (not used in the Mineral Resource Estimate).

Following acquisition, NioCorp advanced the project through additional diamond drilling programs to improve confidence and support updated technical studies. Between 2014 and 2015 NioCorp drilled a total of 24 holes within the Elk Creek Deposit totaling 63,389 ft (19,321 m). The program included data validation, metallurgical and mineralogical studies, geotechnical and hydrogeological studies all in support of resource estimation. Details of the program are provided in previous technical studies (Batty et al., 2022; Nordmin, 2019; SRK, 2014, 2015, 2017; Tetra Tech Wardrop, 2012).

Table 5‑1: Historical Exploration Summary

Year

Company

Exploration Work

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1963-1964

US Geological Survey

Regional Airborne Survey

1970

UNL

Airborne Gravity & Magnetic Surveys

1971

Nebraska Geological Survey and the United States Bureau of Mines

1 Drill hole 2-B-71 (NN-1)

1973

Cominco American

 4 Drill holes within the Carbonatite Complex

1973-1986

Molycorp

114 Drill holes within the Carbonatite Complex

2010-2011

Quantum

Historical Data Verification; 5 Drill holes within Carbonatite Complex

2014-2015

NioCorp

24 Drill holes

Source: Dahrouge 2026

5.2 Ownership History

Details of the original ownership of the complete Project area remain unclear; however, previous reports note that the initial land packages over the Project were controlled by Cominco American Inc. (“Cominco American”) and Molycorp Inc. (“Molycorp”) during the early 1970’s. Much of the historical exploration work completed over the Project area was done by Molycorp before 1984. On May 4, 2010, Quantum Rare Earth Developments Corp. (“Quantum”) announced the acquisition of the mineral rights to the Project and on March 3, 2013, Quantum announced an official name change to NioCorp Developments Ltd. (“NioCorp”).

5.3 Historical Mineral Resource Estimates

Multiple historical resource estimates have been completed on the project and are detailed in the reports listed below. The previous resource estimate was completed by Understood Mineral Resources Ltd. in 2022.

•
Internal Molycorp Memo (Cook & Shearer, 1986)
•
Elk Creek NB Project, Nebraska, US Resource Estimate Update Tetra Tech Wardrop Estimate April 23, 2012 (Tetra Tech Wardrop, 2012)
•
NI 43-101 Technical Report on Resources Elk Creek Niobium Project, Nebraska (SRK, 2014)
•
NI 43-101 Technical Report Updated Preliminary Economic Assessment, Elk Creek Niobium Project, Nebraska (SRK, 2015)
•
NI 43-101 Technical Report Feasibility Study Elk Creek Niobium Project Nebraska NI 43-101 Technical Report Feasibility Study, Elk Creek, Superalloy Materials Project, Nebraska Nordmin Engineering April 16, 2019 (Nordmin, 2019)

5.4 Historical Mineral Reserve Estimates

There is no historical reserve estimate on the Project.

 

5.5 Historical Production

There has been no historical production at the Project.

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6 Geological Setting, Mineralization and Deposit

6.1 Regional Geology

The Nebraska Precambrian basement is comprised mainly of granite, diorite, basalt, anorthosite, gneiss, schist and clastic sediments. A series of island arcs sutured onto the Archean continent created the basic framework of the area. This suture left a north-trending intervening boundary zone ancestral to the Nemaha Uplift, providing a pre-existing tectonic framework which controlled the trend of the later Midcontinent Rift System (1.0 to 1.2 Ga) (Carlson & Treves, 2005). The Elk Creek Carbonatite is located at the northeast extremity of the Nemaha Uplift.

The Midcontinent Rift System, or Keweenawan Rift, comprises mafic igneous rocks and forms a belt over 1,242 mi (2,000 km) long and 34 mi (55 km) wide that is exposed at the surface in the Lake Superior Region and extends southwards through the states of Michigan, Wisconsin, Minnesota, Iowa, Nebraska and into Kansas (Carlson, 1992). Both basalt and associated red clastic sedimentary rocks are found in the Precambrian basement of southeastern Nebraska. These rocks are very similar to those found in the Lake Superior region and are thus considered to be a product of the Keweenawan rifting (Burchett & Reed, 1967; Treves & Low, 1983). Figure 6‑1 illustrates the major rock types of the Midcontinental Rift system.

The Nemaha Uplift (300 Ma) extends southward as a narrow belt from around Omaha, Nebraska across Kansas to around Oklahoma City, along the midcontinent rift system (King, 1969) (Figure 6‑1 and Figure 6‑2). Along the northern and eastern margins are complex fault zones and steeply dipping units. Regional north-northeast to northeast striking faults are locally transected by northwest trending ones, including the Central Plains mega-shear (Central Missouri Fault) to the north and the Oklahoma mega shear to the south (McBee, 2003). The Elk Creek Carbonatite body intruded near to the axis of the Nemaha uplift and has similar age dates to a cluster of carbonatites north of Lake Superior that are in the range of 560 to 580 Ma. (Erdosh, 1979; Woolley, 1989). Temporally, the carbonatite occurs near the boundary between the Penokean Orogen (approximately 1,840 Ma) and the Dawes terrane (1,780 Ma) of the Central Plains Orogen (Carlson & Treves, 2005).

Regional geophysical data and drilling have confirmed the presence of kimberlitic intrusive bodies in northern Kansas to the southwest of the Elk Creek Carbonatite. These kimberlites were emplaced along the rift system during the Cretaceous time (Berendsen, P. & Weis, 2001).

The eastern portion of Nebraska was glaciated several times throughout the early Pleistocene (Wayne, 1981), resulting in the deposition of up to 164 ft of unconsolidated till.

Figure 6‑2 shows a merged airborne magnetic anomaly map of Nebraska, Kansas, and Oklahoma states (Sweeney & Hill, 2005) showing the Midcontinent Rift and Nemaha Uplift systems.

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_5.gif

Source: Modified from (Palacas et al., 1990)

Figure 6‑1: Regional Geology

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_6.gif

Source: Modified from Sweeney and Hill, 2005

Figure 6‑2: Merged Aeromagnetic Anomaly Map of Nebraska, Kansas and Oklahoma showing Midcontinental Rift and Nemaha Uplift

6.2 Property Geology

The Property includes the carbonatite that has intruded older Precambrian granitic and low- to medium-grade metamorphic basement rocks. The carbonatite and Precambrian rocks are unconformably overlain by approximately 656 ft (200 m) of Paleozoic marine sedimentary rocks of Pennsylvanian age ranging from ca. 299 to 318 Ma.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_7.jpg

Source: Modified from KGS O-F Report 91-52

Figure 6‑3 Generalized Stratigraphy of the Elk Creek Area

As a result of this thick cover, there is no surface outcrop within the Project area of the carbonatite, which was identified and targeted through magnetic surveys and confirmed through subsequent drilling. The available magnetic data indicates dominant northeast, west-northwest striking lineaments and secondary northwest and north-oriented features that mimic the position of regional faults parallel and/or perpendicular to the Nemaha Uplift (Figure 6‑2).

Previous technical report summaries interpreted the contact between the Elk Creek carbonatite and the Pennsylvanian sedimentary sequence as a sheared and oxidized contact zone, suggesting an intrusive relationship between the carbonatite and the Pennsylvanian strata, and described associated brittle to brittle-ductile deformation features (tension veins, sheared veins, and slickensided fault planes) affecting both units (Batty et al., 2022). Based on subsequent review of drill core and the sub-horizontal, planar geometry of the broken rubble zone at the contact, the current interpretation is the Pennsylvanian–carbonatite boundary is an erosional unconformity rather than a shear-generated contact. This revised interpretation is consistent with the regional framework described by Carlson and Treves (2005), who concluded that uplift on the Nemaha Uplift was followed by significant erosion that likely truncated (beveled) the top of the carbonatite body, prior to reburial beneath Upper Pennsylvanian marine sediments. Under the revised model, the “brecciated limestone” immediately above the carbonatite is interpreted as a basal Pennsylvanian

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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unit formed by transgressive–regressive reworking and erosion during early Pennsylvanian deposition, rather than as a product of shearing along the contact (Figure 6‑4). Brittle faults, veins, and related deformation features described previously remain recognized in core (Figure 6‑4); however, they are interpreted as superimposed structural features that may locally modify the contact zone but are not considered the primary process responsible for formation of the unconformity.

 

img170397038_8.gif img170397038_9.jpg

Source: NioCorp 2025; SRK 2014

Figure 6‑4: (Left) Drill core illustrating the transition from eroded paleosurface of the Elk Creek Carbonatite Complex to the “Limestone Breccia”. (Right) Photographs of microstructures in the drill core.

6.2.1 Marine Sedimentary Rocks

The state-wide Nebraska test hole database contains information for about 5,500 test holes drilled since 1930 by the CSD (Conservation and Survey Division of the University of Nebraska-Lincoln (UNL), School of Natural resources (SNR), (UNL-CSD/SNR), and cooperating agencies. Test hole

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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location data, as well as lithological descriptions, stratigraphic interpretations, and geophysical log records, are included in the database. In addition, UNL-CSD/SNR maintains an extensive collection of geologic samples obtained from the drilling process (UNL-CSD/SNR website).

There are active limestone quarries, and underground mines within approximately 43 miles of the Project site that create road materials, lime, fill, and construction materials. These quarries are actively mining approximately 2.2 million tons/year from within the Pennsylvanian limestone units. The Pennsylvanian limestone unit is the same as is currently located above the carbonatite unit at the Project site.

6.2.2 Elk Creek Carbonatite

The Elk Creek Carbonatite Complex is an elliptical magmatic body with a northwest-trending long axis perpendicular to the strike of the 1.1 Ga Midcontinent Rift System (Figure 6‑1 and Figure 6‑2), near the northern part of the Nemaha uplift (Burchett, 1982; Carlson, 1992). The definitive confirmation of carbonatite was completed using Rare Earth Element (REE), P2O5 and Sr87/Sr86 isotope analysis (Brookins et al., 1975). The carbonatite has also been compared to the Iron Hill carbonatite stock in Gunnison County, Colorado, based on similar mineralogy (Xu, 1996).

The lithological units present in the carbonatite complex were originally defined by Molycorp during their drill programs, additional studies by Xu in 1996 based on select drillholes (2-B-71 (also known as "NN-1"), EC-40, EC-42, EC-50, EC-70, and EC- 82) and were further simplified by DGC for interpretation purposes during each stage of the Project (2011, 2014, 2025). The carbonatite phase was classified into two main units (defined by texture, massive or brecciated) and several sub-units including a massive carbonatite (dolomite carbonatite, apatite bearing dolomite carbonatite and pyrochlore-bearing Carbonatite, apatite dolomite carbonatite, hematite dolomite carbonatite and magnetite dolomite carbonatite) and brecciated carbonatite. Xu (1996) also classified several silicate units including an altered basalt, altered lamprophyre and altered syenite.

During the 2014, 2015 and 2025 drilling campaigns, DGC geologists split the dolomite carbonatite (“dolCarb”) units down into a number of key units using the information of the different phases of carbonatite. The main carbonatite lithologies used for geologic interpretation are:

•
Dolomite Carbonatite – dolCarb
•
Dolomite Carbonatite Breccia – dolCarbBc
•
Hematite Dolomite Carbonatite – hemdolCarb
•
Magnetite Dolomite Carbonatite – mdolCarb
•
Magnetite Dolomite Carbonatite Breccia – mdolCarbBc

DGC considers the more detailed split of the carbonatite units for geologic interpretation to be relevant to determining the distribution of different grade populations as supported by statistics (discussed in Section 8.3). The most significant difference is the change in the logging codes between dolCarb and mdolCarb, in terms of the major rock types.

Summarized below in Table 6‑1 are the lithological units captured from compiled drillhole logs and corresponding geology reports, and the nomenclature applied by DGC.

Table 6‑1: Project rock types as defined by Molycorp and DGC

Unit Name (Molycorp)

Code

Unit Name (DGC)

Code

Overlying Lithologies

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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Unit Name (Molycorp)

Code

Unit Name (DGC)

Code

Quaternary sediments

 Qt

Overburden (~165 ft)

Ovb

Pennsylvanian Sediments

 Pu

Pennsylvanian Sediments (~656 ft thick)

sed

  Elk Creek Complex

Younger Mafic Rock

 ym

Mafic Breccia

mafBc

Barite Beforsite III

 bb III

Barite Dolomite Carbonatite

dolCarb

Barite Beforsite II

 bb II

Beforsite Breccia

 bbx

Dolomite Carbonatite Breccia

dolCarbBc

Barite Beforsite I

 bb I

Barite Dolomite Carbonatite

dolCarb

Apatite Beforsite II

 ab II

Apatite Dolomite Carbonatite Breccia

dolCarb

Apatite Beforsite I

 ab I

Older Mafic Rock

 om

Mafic dyke, vein or fragment

maf

Lamprophyre

Lamp

Magnetite Beforsite

 mb

Magnetite Dolomite Carbonatite

mdolCarb

Syenite II

 sy II

Syenite

sy

Syenite I

 sy I

  Host Rocks

Granite/Gneiss

 pCgg

Granite/Gneiss

gn

Amphibole Biotite — Gneiss

 pCbg

Amphibole Biotite — Gneiss

gn

Source: DGC 2026

Limited age dating of the Elk Creek Carbonatite has been carried out with recent U-Pb zircon dates from the carbonatite ranging from 480 ±20 to Ma 540 ±14 (Farmer et al., 2013). The carbonatite consists predominantly of dolomite, calcite and ankerite, with lesser chlorite, barite, phlogopite, pyrochlore, serpentine, fluorite, sulphides and quartz (Xu, 1996). The stratigraphic reconstruction based on drill core observation in the area suggests that the carbonatite is unconformably overlain by approximately 656 feet (200 meters) of essentially flat-lying Palaeozoic marine sedimentary rocks, including carbonates, sandstones, and shales of Pennsylvanian age (ca. 299 to 318 Ma).

6.2.3 Structural Geology

Based on data provided to carry out the structural study, the Project contains five main sets of brittle faults variably cutting through the Pennsylvanian rocks and the carbonatite boundary which appears to be tectonic. The orientations of the faults were determined by comparing Acoustic Televiewer (“ATV”) logs with specific customized structural core logging data, and by undertaking a preliminary interpretation of the provided geophysics images.

This data has been used to model the fault pattern in 3D for use in further resource estimation and geotechnical studies. The overall fault model included approximately 28 structures with the vicinity

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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of the Project with varying levels of confidence. Based on a review within the mineralization, at least three key northeast-trending faults have been identified and used during the geological modeling process.

The joints and veins define orientation sets comparable to the fault trends. Hematite veins, which may be up to 3.28 feet (one meter) thick, represent the weakest fault- and joint-infilling material which may be problematic for mining and should, therefore, be given more attention during any future geotechnical studies.

6.3 Mineralization

The Property hosts niobium, titanium, and scandium mineralization as well as REE and barium mineralization that occur within the Elk Creek Carbonatite. In this TRS, niobium, titanium, scandium, and rare earth elements are considered the main elements of interest.

The current extent of modelled mineralization is 3,937 ft (1,200 m) along strike, 1,640 ft (500 m) wide, and 2,461 ft (750 m) in dip extent below the unconformity. Previous reports found that that the mineralization is open in all directions. The recent drilling reported in this report indicates that there is a hanging wall contact between the Nb-Ti-Sc rich magnetite-dolomite-carbonatite lithology and the surrounding dolomite carbonatite to the south of the deposit, demonstrated in Figure 6‑5 and Figure 6‑6.

img170397038_10.gif

Source: DGC 2026

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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Figure 6‑5: Plan view of the location of the mineralized carbonatite (outlined in red) with underground development projected to surface

 

img170397038_11.jpg

Source: DGC 2026

Figure 6‑6: Plan and Cross -Sections of Geologic Model Hanging Wall Boundary and Mineralized Domain

6.3.1 Niobium and Titanium Mineralization

The deposit contains significant concentrations of niobium. Based on the metallurgical test work completed to date at several laboratories using QEMSCAN® analysis, the niobium mineralization is known to be fine-grained, and that 77% of the niobium occurs in the mineral pyrochlore, while the balance occurs in an iron-titanium-niobium oxide mineral of varying composition. Distribution and

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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statistical review of Nb2O5 within the mineralized carbonatite, are shown in Figure 6‑7 and discussed in Section 6.4 and Section 11.

Figure 6‑8 demonstrates that there is a fairly high correlation between increasing Nb2O5 grade and Fe2O3 and TiO2 grades.

img170397038_12.jpg

Source: DGC 2026

Figure 6‑7: Basic Statistics of Nb2O5 Mineralization

img170397038_13.jpg

Source: DGC 2026

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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Figure 6‑8: Correlation Statistics of Nb2O5 and TiO2 and Fe2O3

6.3.2 Scandium Mineralization

Within the Elk Creek Carbonatite, a host of other elements exist with varying degrees of concentration. The Company has completed both whole rock analysis and multi-element analysis on all samples for the 2014 program, plus re-sampling programs of selected historical core and/or pulps between 2011 and 2021.

As the metallurgical test work advanced during 2014 and 2015, the ability to obtain a titanium dioxide (TiO2) and scandium (Sc) product became apparent. TiO2 is strongly and positively correlated with niobium grades, whereas the scandium mineralization is spatially related to niobium and titanium mineralization, but with lesser degree of correlation. Basic statistics for Sc mineralization are shown in Figure 6‑9. Detailed discussion is presented in Section 14.

img170397038_14.jpg

Source: DGC 2026

Figure 6‑9: Basic Statistics of Sc Mineralization

6.3.3 Rare Earth Element Mineralization

Within the Elk Creek Carbonatite complex, there are several occurrences of REE mineralization, including the Project area. REE mineralization is associated with a barite dolomite carbonatite and occurs within the following minerals:

•
Bastnäsite ([Ce,La,Y]CO3F)
•
Parisite (Ca[Ce,La]2[CO3]3F2)
•
Synchysite (Ca[Ce,La][CO3]F)
•
Monazite ([Ce,La]PO4)

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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Based on an excerpt from Molycorp’s drill logs: “Lanthanide minerals occur as radial patches and random aggregates of needles, irregular patches and vein-like aggregates. The aggregates occur with and without quartz. The aggregates appear as light-gray patches in reddish-brown, hematite-altered beforsite. Although individual lanthanide mineral grains are in the micrometer size range, aggregates of lanthanide minerals range from 0.23 to 8 mm. in maximum dimension. Monazite and bastnäsite have been identified in the aggregates, and EDX spectra show Ce > La."

Present day nomenclature for REE is shown in Table 6‑2. Promethium (Pm) is not included as it is very rare in nature. The division into light and heavy rare-earth elements made below is based on differences in processing. Elsewhere in literature, the division has been made between gadolinium and terbium (atomic number 64 and 65) based on the lack of paired electrons in the inner incomplete subshell (4f) (Van Gosen et al., 2017).

Statistical analysis of distribution and correlation of REEs within the deposit are presented in Section 11.

Table 6‑2: List of Elements & Oxides Associated with REE Mineralization

Element

Element Acronym

Compound

Associated Elements and Oxides

Nb

Nb2O5

Niobium

Light Rare Earth Metals and Oxides (LREO)

Lanthanum

La

La203

Cerium

Ce

Ce203

Praseodymium

Pr

Pr203

Neodymium

Nd

Nd203

Heavy Rare Earth Metals and Oxides (HREO)

 

Samarium

 Sm

Sm2O3

Europium

Eu

Eu203

Gadolinium

Gd

Gd203

Terbium

Tb

Tb203

Dysprosium

Dy

Dy203

Holmium

Ho

Ho203

Erbium

Er

Er203

Thulium

Tm

Tm203

Ytterbium

Yb

Yb203

Lutetium

Lu

Lu203

Yttrium

Y

Y203

Source: DGC 2026

6.4 Deposit Type

The Project is hosted within the Elk Creek Carbonatite. By definition, a carbonatite is an igneous rock body with greater than 50% modal carbonate minerals, mainly in the form of calcite, dolomite, ankerite, or sodium- and potassium-bearing carbonates. Carbonatites commonly occur as intrusive bodies, such as isolated sills, dykes, or plugs, although they can rarely occur as extrusive rocks (Oldoinyo Lengai, Tanzania). Many carbonatites are associated with alkalic silicate complexes which include syenite, nepheline syenite, ijolite, urtite, and pyroxenite. Carbonatites are generally related to large-scale, intra-plate fractures, grabens, or rifts that correlate with periods of extension, and

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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range from Precambrian to recent in age. They are usually surrounded by an aureole of metasomatically altered rocks called fenites. Carbonatite-associated deposits can be classified as magmatic or metasomatic types (Richardson & Birkett, 1996).

Carbonatites have been classified based on chemical classification into four classes (Woolley and Kempe, 1989; Wyllie and Lee, 1998), and further subdivided based on mineralogical and textural characteristics:

•
Calcio-carbonatite coarse-grained: sövite, and finer-grained: alvikite
•
Magnesio-carbonatite dolomite-rich: beforsite, and ankerite-rich: rauhaugite
•
Ferro-carbonatite (iron-rich carbonates)
•
Natro-carbonatite (sodium-potassium-calcium carbonates)

The use of a chemical classification of carbonatites should be used with caution when replacement, or metasomatic, processes have altered the primary composition of the carbonatite rock (Mitchell, 2005).

The majority of carbonatite deposits are located within stable, intra-plate crustal units, although some are linked with orogenic activity or plate separation. It is also important to note that carbonatites tend to occur in clusters, and in many places, there has been a repetition of intrusive activity over time (Woolley, 1989).

Carbonatite-hosted deposits occur almost exclusively in intrusive carbonatite and may be subdivided into magmatic, replacement/veins, and residual sub-types. The Elk Creek Carbonatite can be classified as a magmatic sub-type, similar to the St-Honoré deposit in Quebec, Canada (Niobec niobium mine, Iamgold – Figure 6‑10), the Mountain Pass Deposit in California, U.S.A. (REE), and the Palabora Deposit in South Africa (apatite).

The pipe-like carbonatites typically occur as sub-circular or elliptical shapes and can be up to 1.9-2.5 mi (3-4 km) in diameter. Magmatic mineralization within pipe-like carbonatites is commonly found in crescent shaped, steeply dipping zones. As carbonatite magma is typically volatile rich with low viscosity, it may ascend rapidly through the mantle, fracturing the crust on impact, causing a characteristic alternating ring (crescent) structure of carbonatite and wall rock to be formed. Metasomatic mineralization occurs as irregular forms, breccias, or veins. Carbonatites typically consist of multiple phases of intrusion with different mineralogical and textural characteristics. Early phases tend to consist mainly of calcite with later phases mainly consisting of dolomite, ankerite, or siderite. The later phases are typically more enriched in niobium or tantalum with the latest phases more enriched in rare earth minerals. In general, geochemical zonation of phases begin with calcio-carbonatite intrusion, followed by magnesio-carbonatite and finally ferro-carbonatite. Fenitization (alkali metasomatism) is common around many carbonatite intrusions.

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img170397038_15.jpg

Source: Jaroslav 2025 (Modified after Valliéres et al. (2013))

Figure 6‑10: Schematic Diagram of St. Honoré Carbonatite

The major mineral constituents are calcite, dolomite, siderite, ferroan calcite, ankerite as carbonates, and hematite, biotite, titanite, olivine, and quartz. Economic minerals include fluorite (F), apatite (P), pyrochlore (Nb), anatase (Ti), columbite (Nb-Ta), monazite (REE), bastnaesite (REE), parasite (REE), zircon (Zr), and magnesite (Mg), among others. Mineralization within carbonatites is typically syn- to post-intrusion. The mineralization is controlled primarily by fractional crystallization within the intrusion, with tectonic and local structures influencing the form of metasomatic mineralization (Birkett & Simandl, 1999; Richardson & Birkett, 1996; Woolley & Kempe, 1989).

Worldwide, carbonatite deposits are mined for niobium, REE, iron, copper, phosphate (apatite), vermiculite and fluorite; with barite, zircon/baddeleyite, tantalum and uranium as common by-products (Richardson & Birkett, 1996).

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

7 Exploration and Drilling

7.1 Exploration

Regional airborne magnetic surveys in 1963–64 first identified geophysical features in southeast Nebraska, followed by a 1970 gravity survey by UNL's Conservation and Survey Division that, combined with concurrent UNL mapping of the Nemaha Arch and Humboldt Fault systems, revealed a positive correlation between magnetic and gravity anomalies now known as the Elk Creek gravity anomaly. This anomaly was modeled as a near-circular feature roughly 4.35 miles (7 km) in diameter, corresponding to a cylindrical mass of indefinite length with a 5,500 ft (1,676 m) radius. This work prompted early drilling by the Nebraska Geological Survey and U.S. Bureau of Mines, and in 1971 test hole 2-B-71 intersected carbonatite with pyrochlore mineralization and elevated niobium and rare earth elements, confirming the anomaly's source.

The carbonatite complex is a 3.7-4.9 mi (6–8 km) diameter alkaline intrusive body buried beneath roughly 656 ft (200 m) of Pennsylvanian marine sedimentary rocks with no surface expression, meaning exploration has relied entirely on geophysics and drilling. It comprises several lithologies dominated volumetrically by apatite dolomite, with the magnetite dolomite unit — though volumetrically minor — serving as the primary host of niobium mineralization (Figure 7‑1).

img170397038_16.jpg

Source: Drenth 2014

Note:

(1)
The term beforsite used in this figure has been superseded by the terms magnesio-carbonatite or dolomite carbonatite. Other rock-type names have been modified subsequently (see Table 6‑1).

 

Figure 7‑1: Geology of the Elk Creek Carbonatite as expressed in drill holes at an elevation of 394 ft (120 m) AMSL (approximately 755 ft or 230 m BGS)

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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There is no other relevant exploration work outside of drilling completed on the Property on behalf of current and previous owners.

Detailed descriptions of the geotechnical data, testing and analysis are included in Section 13.2. Descriptions, characterization and analysis of hydrogeology are included in Section 13.3.

7.2 Drilling

Mineral Resource definition drilling on the Project has been conducted in four phases:

•
Phase I: Drilling Campaigns completed during the 1970s and 1980s by MolyCorp.
•
Phase II: Initial Restart Drilling completed in 2011 by Quantum (NioCorp’s predecessor).
•
Phase III: Focused Resource Drilling completed in 2014 & 2015 by NioCorp.
•
Phase IV: Focused Resource Drilling completed in 2025 by Niocorp.

To date, 94 drill holes have been completed on the Project for a total of 196,114 ft (59,775 m) (Figure 7‑2; Table 7‑1), including 16 drill holes totaling 37,861 ft (11,540 m) completed in 2025. A further five holes totaling 11,598 ft (3,353.1 m) were drilled in 2015 for hydrogeological and geotechnical studies but were not used for resource estimation. All drilling has been completed using a combination of tricone, reverse circulation (RC) or diamond drilling (DDH) core in the upper portion of the hole within the Pennsylvanian sediments. A portion of the 2014 drill holes used RC drilling within the Pennsylvanian sediments to increase drilling efficiency through cover material within areas of strong geological confidence. All drilling within carbonatite has been completed using diamond coring methods.

To date, local labor has been used by drilling contractors when preparing the drill hole pads. All drilling has been completed using standardized procedures which are in line with international standards of best practice. The drilling by Molycorp was completed using company-owned equipment and sampling procedures. The drilling companies used by the Company between 2011 and 2015 programs are detailed below:

•
2011: Black Rock Drilling, LLC (BRD Personnel and Leasing Corp.), 17525 E Euclid Ave, Spokane Valley, WA 99216
•
2014: Envirotech Drilling LLC, 900 East 4th Street, Winnemucca, NV 89445
•
2014: West-Core Drilling, LLC, 561 W Main Elko, NV 89801 USA; and
•
2014: Idea Drilling, 1997 9th Avenue North, Virginia, MN 55792
•
2015: Idea Drilling, LLC, 1997 9th Avenue North, Virginia, MN 55792
•
2015: Envirotech Drilling LLC, 900 East 4th Street, Winnemucca, NV 89445

Table 7‑1: Drilling Completed within the Carbonatite Complex

Year

Company

Number of Holes in Carbonatite Complex

Number of holes on Project

Project Hole Average Depth (m)

Project Hole Average Depth (ft)

Total Length (ft) Drillholes on Project

Total Length (m) Drillholes on Project

1971-1986

Molycorp

114

49

530

1,738

85,171

25,960

2011

Quantum

5

4

739

2,423

9,692

2,954

2014-2015

NioCorp

24

24

805

2,641

63,390

19,321

2025

NioCorp

17

17

679

2,227

37,861

11,540

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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Subtotal:

160

94

688

2,257

196,114

59,775

 

Source: DGC 2026

 

img170397038_17.jpg

Source: DGC 2026

Figure 7‑2: All drilling completed within the area of the Elk Creek Carbonatite Complex

During 2015 five holes (NEC15-001 to NEC15-005) were completed totalling 11,001 ft (3,353.1 m) for hydrogeological and geotechnical studies. The drilling was carried out by Idea Drilling and Envirotech Drilling LLC with Envirotech Drilling LLC as subcontractor.

Not all the drill holes within the Project were used in the 2026 Mineral Resource Estimation, as many do not intersect the Nb2O5 anomaly and are located a significant distance away from the Deposit (Figure 7‑2). A total of 79 drill holes has been drilled within the Project, of these 65 drill holes were used to inform the Elk Creek Deposit Mineral Resource Estimation (Figure 7‑3). Note that there are more holes within the Project area, but some holes were excluded from the Mineral Resource as they were drilled for other purposes (geotechnical, hydrogeology) and were not sampled. A summary of the drilling in the Project area can be seen in Figure 7‑2.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_18.jpg

Source: DGC 2026

Figure 7‑3: 2025 Drillhole locations on the Project

The 2025 drilling program was specifically designed to target gaps within the current Mineral Resource in support of converting a portion of the Resource from Indicated and Inferred to Measured, Indicated and Inferred. The drilling for the 2025 program was completed by Boart Longyear Company – Western Coring, 7013 West Augusta Ave, Glendale, Arizona 85303. Drilling was initiated on April 29, 2025, and was completed on October 3, 2025. During this campaign a total of 16 HQ diameter drillholes were completed totalling 37,861 ft (11,540 m) utilizing 2 (two) LF-160 drill rigs, one track mounted and one truck mounted core drill. All drilling was completed using diamond coring methods (Figure 7‑2). Overburden was cased using HWT casing, and the remainder of the drillholes were completed using HQ thereafter.

Table 7‑2: 2025 Drill Hole Summary

Drill hole ID

Easting

Northing

Elevation (m)

Length

Azimuth

Inclination

Comments

NEC25-024

739068.9

4461370.1

350.7

740.7

118

-81

NEC25-025

739201.9

4461347

354.9

935.6

300

-85

NEC25-026

739002.9

4461298.9

349.8

920.8

30

-80

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Drill hole ID

Easting

Northing

Elevation (m)

Length

Azimuth

Inclination

Comments

NEC25-027

739217.1

4461460

353.5

859.8

182

-83

NEC25-028

739000.9

4461296.2

349.8

229.1

30

-63

Lost hole.

NEC25-028a

739000.6

4461295.6

349.8

410.6

30

-63

Re-drill of NEC25-028

NEC25-029

739182

4461456.5

355.4

850.7

205

-80

NEC25-030

739478.9

4461193

345.5

768.7

280

-75

NEC25-031

739074.8

4461223.2

347.9

292.1

20

-65

NEC25-031a

739074.8

4461223.2

347.9

545.9

20

-65

Wedge: NEC25-031.

NEC25-032

739309.6

4461173.3

344.5

801.6

25

-85

NEC25-033

739448.9

4461218.6

347.8

900.7

290

-68

NEC25-034

739444.9

4461139.4

341.7

451.4

30

-75

NEC25-035

739494.9

4461120.7

340.8

431.3

30

-80

NEC25-036

739524.2

4461088.2

340.6

451.5

30

-75

NEC25-037

739489.6

4460945.9

340.5

1,000.10

295

-65

NEC25-038

739075.6

4461210.1

347.5

949.4

320

-80

Source: DGC 2026

7.2.1 Project Drilling Procedures

Historical Molycorp drilling (1970s–80s) was never reviewed by DGC, though presumed to reflect era-appropriate industry practice, while the 2011 Quantum program and all NioCorp drilling since 2014 were managed under consistent DGC/SRK quality control protocols. Drill collars were staked and oriented using GPS, compass, and Azimuth Pointing System equipment, with core drilled by West-Core, Idea Drilling, and Boart Longyear and transitioned from PQ to HQ size beneath the Pennsylvanian-carbonatite contact; completed holes were either piezometer-equipped or grouted and abandoned per standard procedure.

Eight of the 2014 drill holes were completed with piezometers using locking steel casing, cement pads, and identification nameplates, while the remaining holes were marked with steel posts and nameplates noting hole number, depth, and orientation. All non-piezometer holes were abandoned with grout from total depth to the Pennsylvanian contact and cemented to surface, while piezometer holes were grouted from total depth to the base of the piezometer.

7.2.1.1 Collar and Downhole Surveys

Drill collar locations were surveyed by ESP, Inc., Jorgensen Surveying, and CES Group using GPS/RTK equipment with horizontal accuracies of approximately 10–11 mm, referenced to NAD83(2011)/NAVD88, with historical Molycorp and 2011 collars re-excavated and re-surveyed as needed. Downhole survey methods evolved from compass readings historically, to Devico DeviFlex

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

surveys in 2011, to Reflex GYRO surveys in 2014 (chosen to avoid magnetic interference from deposit mineralogy), to TruGyro gyrocompass surveys in 2025 at 50–100 ft intervals, all using non-magnetic tools appropriate to hole lengths exceeding 2,300 ft (700 m).

7.2.1.2 Geomechanical Core Logging

Geomechanical logging was performed by DGC personnel under direction of A2GC, following a project-specific manual and on-site training in May 2025, using the Q-system (Barton, 1974) to assess rock mass quality. Recorded parameters included RQD, joint characteristics, fracture data, and lithological/alteration data, entered into a customized MX Deposit database. Additionally, geomechancial core logging data was also collected in 2014 and 2015 under the supervision of SRK.

7.2.1.3 Geological Core Logging

The Qualified Person has reviewed the drilling, surveying, and core-logging procedures used across the 2011, 2014, and 2025 programs and considers them adequate and consistent with industry-standard practice to support Mineral Resource estimation, including collar and downhole survey methods, geomechanical logging, and geological logging and sample QAQC procedures. Historical Molycorp drilling and survey data (1970s–80s) have not been independently verified by the QP unless otherwise discussed in Section 8 and are relied upon with correspondingly reduced confidence due to their age, wider measurement spacing, and use of older equipment. The QP considers the sampling, security, and data verification methods described in this section adequate to support the reliability of the analytical results used in Mineral Resource estimation, consistent with the internal controls disclosure required under § 229.1305.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

8 Sample Preparation, Analyses & Security

8.1 Sample Preparation & Security

In 2025, drill core was transported daily to the Project core processing facility in the core boxes for logging, photographing, sampling, and storage. Diamond drilling was monitored by DGC geologists and trained geological staff, with professional oversight provided by DGC.

Standardized logging codes and lithological descriptions, developed from historical procedures, were used to maintain consistency between logging geologists. Geological observations, including lithology, texture, structure, mineralization, alteration, and color, were recorded by sample interval in the MX Deposits database. Drill core was digitally photographed at high resolution before cutting.

Sample intervals were generally 3.28 ft (1 m) long and were assigned unique sample numbers. Specific gravity measurements were collected at approximately 19.67 ft (6 m) intervals. HQ core was split in half along orientation marks using water-cooled diamond saws. Broken or soft intervals were split as evenly as practicable. Split core was cleaned before bagging, and cutting equipment was routinely cleaned between samples.

Samples were placed in labelled, barcoded sample bags containing backup sample tags. Original samples and field-inserted control samples were scanned, secured in five-gallon shipping pails, and accompanied by hard-copy and digital shipping records and laboratory preparation instructions. Samples were transported to the analytical laboratory by bonded carrier. The remaining half-core was retained in labelled core boxes and securely stored at the Project site for reference and potential future sampling.

Sample security measures included redundant sample identification, secure bag closures, controlled storage, and shipment in sealed pails. The authors consider these procedures consistent with industry practice for a project of this scale.

The sampling, preparation, and shipment procedures were standardized and monitored to minimize sample identification and handling errors. The on-site geologist managed the QA/QC program, which included certified reference materials, quartz blanks, field duplicates, coarse-reject duplicates, pulp duplicates, and external check analyses. Samples were prepared and analyzed at SGS and Activation Laboratories, with selected samples submitted for secondary check analysis.

The data collection from the processed drill core is outlined in Figure 8‑1 process flow.

 

 

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_19.gif

Source: DGC 2014

Figure 8‑1: Sample Process Flow Chart (2014 - 2025 drill programs)

 

img170397038_20.jpg

Source: NioCorp 2026

Figure 8‑2: NioCorp Technicians cutting core at the project site.

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_21.jpg

Source: NioCorp 2026

Figure 8‑3: Secure storage of the NioCorp Drill holes and pulps.

8.2 Sample Analysis Procedures

Analytical methods used during the program included fusion XRF, fusion ICP-MS, and sodium peroxide fusion ICP-MS/ICP-OES methods available from SGS and Act labs. The recommended methodologies each have differences in the sample decomposition technique, analytical finish, and intended concentration range, and are applicable to the mineralization. The results generated by different laboratories and methods were compared with consideration of method-specific digestion efficiency, detection limits, upper reporting limits, and the mineralogical deportment of the elements of interest.

Table 8‑1: Analytical methods used for sample assay.

Company

Method

Decomposition

Finish

Use

Act labs

FUS-XRF

Lithium borate fusion

XRF

Whole rock / major oxides

Act labs

FUS-MS

Lithium borate fusion

ICP-MS

Trace elements / REE / HFSE

SGS

GC_XRF72MET

Borate fusion

XRF

Metallurgical / concentrate-grade material

SGS

GC_XRF76V

Borate fusion

XRF

Ore-grade / overlimit XRF

SGS

GE_IMS91A50

Sodium peroxide fusion

ICP-MS

Trace-level refractory elements

SGS

GE_ICP91A50

Sodium peroxide fusion

ICP-OES / ICP-AES

Higher concentration multi-element work

Source: DGC 2026

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

 

The selected analytical methods are considered appropriate for the sample material and elements reported. The method-specific detection limits, overlimit procedures, and QAQC performance are reviewed accordingly.

Overall, the analytical methods reviewed are considered appropriate for the elements and sample types reported; however, comparisons between laboratories should be assessed with reference to the specific decomposition method, analytical finish, reporting limits, and QAQC performance for each dataset.

8.3 Quality Assurance & Quality Control (“QAQC”) Programs

Quality Control (QC) measures are typically set in place to ensure the reliability and trustworthiness of exploration data. Appropriate documentation of quality control measures and regular analysis of quality control data are essential as a safeguard for project data and form the basis for the Quality Assurance (QA) program implemented during exploration.

Analytical QC measures typically involve internal and external laboratory procedures implemented to monitor the precision and accuracy of the sample preparation and assay data. They are also important to identify potential sample sequencing errors and to monitor for contamination of samples.

Sampling and analytical QA/QC protocols typically involve taking duplicate samples and inserting quality control samples (CRMs and blanks) to monitor the reliability of the assay results throughout the drill program. Umpire check assays are typically performed to evaluate the primary lab for bias and involve re-assaying a set proportion of sample rejects and pulps at a secondary umpire laboratory

8.3.1 Historical QAQC

The following section summarizes the historical sampling methodologies, analytical procedures, and quality assurance and quality control (QAQC) programs applied to the Elk Creek Project from the original Molycorp drilling campaigns (1973–1986) through to NioCorp's 2021 re-sampling program. Detailed descriptions of all procedures, QAQC results, and the Qualified Person's (QP's) opinion are provided for in the 2022, S-K 1300 Elk Creek Technical Report Summary. Sampling at the Elk Creek Project spans five decades and multiple operators. Table 8‑2 summarizes the key attributes of each program era, including core size, laboratory, analytical methods, and QA/QC controls employed

Table 8‑2: Summary of Historical Sample Preparation, Analysis, and QA/QC Programs — Elk Creek Project

Program Era

Period

Core Size

Laboratory

Primary Analytical Methods

QA/QC Controls Employed

Molycorp (Historical)

1973–1986

NQ / BQ

Molycorp Louviers Lab (CO); occasional Bondar-Clegg

WD-XRF on pressed powder pellets (pulverized to -325 mesh); Nb₂O₅ and LnO (total lanthanides) reported; individual REEs not reported

Internal Elk Creek standards; instrumentation changed (Philips PW1212 → PW1400, 1981); limited external checks

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Program Era

Period

Core Size

Laboratory

Primary Analytical Methods

QA/QC Controls Employed

Quantum / NioCorp Re-Sampling

2010

NQ / HQ pulps

ALS Chemex, Reno NV (prep); ALS North Vancouver BC (analysis)

XRF (ME-XRF10): pulverized to 90% passing -70 μm, Li-borate flux fusion; Nb₂O₅ reported; Sc and TiO₂ not included

SRM SX18-01 & SX18-05 (Dillinger Hütte); field pulp duplicates; quartz blanks; subset checked at Hazen (Golden, CO)

NioCorp Drilling (2011 Program)

2011

HQ core (half)

Actlabs, Ancaster, ON (primary); Inspectorate (external check)

XRF (Panalytical Axios-mAX, Li-metaborate/ tetraborate fusion, 2 g): Nb₂O₅ and Ta₂O₅. ICP/MS (Perkin Elmer Sciex, Li-borate fusion): 43 major/trace elements including REEs. Preparation: crush 90% <2 mm, riffle split 250 g, pulverize 95% <75 μm (Actlabs RX1)

SRM SX18-01, SX18-04, SX18-05 (Dillinger Hütte); CRM AMIS0185; field quartz blanks (5%); 1/4-core field duplicates (5%); coarse-reject and pulp duplicates; Inspectorate external pulp check (~5%)

NioCorp Drilling (2014 Program)

2014

HQ / PQ core (half / quarter)

Actlabs, Ancaster, ON (primary); SGS Lakefield, ON (secondary check)

Same as 2011 program. Additional fluoride analysis (4F-F method) for NEC14-006/007/008. SGS secondary: XRF (GO_XRF76V) for Nb₂O₅ and 13 major oxides; Sc by GE_JCP90A (ICP-MS, 5 ppm DL)

SRM SX18-01, -02, -04, -05; field quartz blanks (5%); 1/4-core duplicates (~4.3%); coarse-reject duplicates (~2.7%); pulp duplicates (~4.9%); SGS external check pulps (~5%)

Re-Sampling: Sc Infill

2014–2015

Molycorp pulps / coarse splits

SGS Lakefield, ON

Sc analysis only (GE_JCP90A); 1,410 samples from 2010 ALS program lacking Sc values

CRM GRE-04 (Geostats; Nb₂O₅, Sc, TiO₂, REE); pulp duplicates (0.6%); insertion rate ~4.8% CRM

Re-Sampling: Multi-Element Infill

2016

Molycorp pulps / fine crush

Actlabs, Ancaster, ON

Full multi-element ICP/MS and XRF (Code 8-Nb₂O₅, WRA4B2); 667 samples targeting missing TiO₂, Sc, and REE results from 2015 MRE

CRM GRE-03 and GRE-04 (Geostats); SRM SX18-01; pulp duplicates (6.6%); insertion rate ~6.2% total standards

Re-Sampling: REE / Sc Infill

2021

Molycorp pulps / coarse / chip splits

Actlabs, Ancaster, ON

Full multi-element ICP/MS and XRF (same as 2011/2014 programs); 1,094 interval samples targeting REE and Sc gaps in outer resource

CRM GRE-03 (Geostats), Oreas 460 and 464, AMIS0185; insertion rate ~7% total control samples

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Program Era

Period

Core Size

Laboratory

Primary Analytical Methods

QA/QC Controls Employed

 

 

 

 

boundaries across 19 historical drillholes

 

Source: DGC 2022

8.3.1.1 Molycorp, 1973-1986

Detailed documentation of Molycorp's sampling procedures was not formally preserved, and the QPs did not directly review primary source records. Based on a review of previous technical reports and discussions with a former Molycorp sampling technician, the following procedures were reconstructed:

•
Drill core was photographed at the time of drilling.
•
Samples were derived from 5 ft (1.52 m) or 10 ft (3.05 m) intervals of hydraulically split, predominantly NQ diameter core, with minor BQ diameter material. Core was crushed on site prior to dispatch.
•
The on-site crusher was cleaned between samples using limestone blank material.
•
Core samples were shipped to Molycorp's exploration laboratory at Louviers, Colorado, for niobium (Nb₂O₅) and total lanthanide oxide (LnO) analysis by wavelength-dispersive XRF on pressed powder pellets, following pulverization to -325 mesh. Individual REE values were not reported.
•
Molycorp employed internal Elk Creek samples as standards. Over the project duration, the number and identification of these standards changed several times. In 1981, the primary instrument was upgraded from a Philips PW1212 to a PW1400. A limited number of samples from holes EC-27 and EC-30 were checked against an external commercial laboratory (possibly Bondar-Clegg), which used a single standard from hole EC-11 compared to 19 standards used by Louviers.
•
Sample homogenization methods were not clearly defined in historical records, and photographs of core were not included with available historic records.

Historical drill core, coarse-reject splits, and pulverized material were donated to and are currently stored at a facility managed by the University of Nebraska-Lincoln (UNL), located approximately 5.2 mi (8.5 km) south of Mead, Nebraska. NioCorp and DGC have completed multiple site visits to confirm the condition and organization of stored material. The facility is secured and maintained by UNL. Select Molycorp samples were subsequently re-assayed in 2010, 2014, 2016, and 2021 to expand the analytical suite and apply modern QA/QC protocols.

8.3.1.2 NioCorp, 2011-2014

Re-sampling programs of historical Molycorp core and pulps were conducted between 2010 and 2014 to verify results and QA/QC procedures. In 2015 a re-assay program was conducted on pulps to add scandium and titanium analysis. Further re-sampling was conducted between 2016 and 2021.

NioCorp implemented a detailed core processing and sampling program commencing with the 2011 drilling program, with continuous improvements applied through the 2014 program. Diamond drilling utilized HQ core as the standard size, with minor PQ intervals. Core was boxed at the drill site daily and transported to the on-site processing facility, where it was photographed, logged, and split.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Professional oversight was provided by geologists and engineers from DGC, SRK Consulting, and NioCorp.

Core logging used standardized codes entered the Datamine Fusion drillhole database. The full carbonatite intersection was sampled at approximately 3.28 ft (1 m) intervals. Core was halved using electric, water-cooled diamond-bladed core saws (BD 3003E). Sampled intervals were placed in barcoded sample bags, secured in five-gallon plastic pails, and shipped via bonded trucking company to Activation Laboratories Ltd. (Actlabs), Ancaster, Ontario. Redundant barcode identification was applied both inside and outside each sample bag to ensure accurate chain of custody. Half-core not used for analysis was retained in labelled core boxes at the secured on-site facility.

At Actlabs, samples were prepared using the RX1 modified preparation package: dried at 140°F (60°C) for 12 hours; crushed by jaw crusher to 90% passing 2 mm (with quartz wash between samples); riffle split to 250 g; and pulverized using ring and puck ESSA pulverizers to 95% passing 75 μm (with quartz wash between each sample). Primary analysis was by XRF (Panalytical Axios-mAX, Li-metaborate/tetraborate fusion, 2 g aliquot) for Nb₂O₅ and Ta₂O₅, and by ICP/MS (Perkin Elmer Sciex, Li-borate fusion) for 43 major and trace elements including the full REE suite. Actlabs maintained ISO/IEC 17025 and ISO 9001 accreditation throughout the program periods.

SGS Lakefield, Ontario (ISO 17025 accredited) served as the secondary umpire laboratory for the 2014 program. SGS analyzed pulp splits for Nb₂O₅ and 13 major oxides by XRF (GO_XRF76V borate fusion) and Sc by ICP-MS (GE_JCP90A, 5 ppm detection limit). Fluoride analysis (method 4F-F) was additionally completed for holes NEC14-006, NEC14-007, and NEC14-008.

8.3.1.3 Historical Re-Sampling Programs, 2010-2021

NioCorp in 2010 and 2021, undertook four re-sampling programs targeting the historical Molycorp sample archive to expand analyte coverage, infill QA/QC data, and address gaps identified during successive resource estimates.

2010 Re-Sampling (Quantum/NioCorp): A total of 1,860 pulverized or coarse-split samples from Molycorp drillholes were submitted to ALS Chemex (preparation in Reno, NV; analysis in North Vancouver, BC) using method ME-XRF10 (Li-borate flux, XRF). Samples were selected based on geological interpretation and proximity to elevated Nb₂O₅ values. The program introduced NioCorp's first systematic QA/QC protocol over historical material, including SRM SX18-01 and SX18-05 (Dillinger Hütte), quartz blanks, and field pulp duplicates. A subset of results was checked at Hazen Research, Golden, Colorado. Note: Nordmin (2019) identified that SRM results ran consistently low using the ME-XRF10 methodology relative to later programs; this methodology was not used in the 2011 or 2014 drilling programs.

2014–2015 Sc Infill Re-Sampling: The 2015 Mineral Resource Estimate (SRK) identified that the 2010 ALS program did not include Sc analysis and that a portion of the database lacked TiO₂ and Sc values. A total of 1,410 pulverized Molycorp samples were submitted to SGS Lakefield for Sc-only analysis (GE_JCP90A), with CRM GRE-04 (Geostats; Nb₂O₅, Sc, TiO₂, REE certified) inserted at approximately 4.8%.

2016 Multi-Element Infill Re-Sampling: A second infill phase submitted 667 pulverized and fine-crush Molycorp samples to Actlabs for full multi-element analysis (Code 8-Nb₂O₅ XRF and WRA4B2 ICP/MS), targeting residual TiO₂, Sc, and REE gaps from the 2015 MRE. QA/QC included CRM GRE-03 and GRE-04 (Geostats), SRM SX18-01, and pulp duplicates at 6.6% insertion rate.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

2021 REE and Sc Infill Re-Sampling: An internal evaluation identified 1,095 intervals across 19 historical Molycorp drillholes that contained Nb₂O₅ results but lacked REE and Sc values within the outer resource boundaries. A total of 1,094 interval samples (1,047 pulverized splits, 24 coarse splits, and 23 chip splits) were submitted to Actlabs using the same ICP/MS and XRF methods applied in the 2011 and 2014 programs. QA/QC included CRMs GRE-03 (Geostats), Oreas 460 and 464, and AMIS0185, at a combined insertion rate of approximately 7%.

8.3.1.4 Quality Assurance and Quality Control

NioCorp integrated a systematic QA/QC program across all 2011–2021 programs. Control sample types inserted at the field stage included: optical-quality quartz blanks (5%), CRMs and SRMs (5–6%), and field quarter-core duplicates (5%). These were supplemented by laboratory-generated coarse-reject and pulp duplicates, and external umpire laboratory check analysis. Table 8‑3 summarizes blank performance across the 2011 and 2014 drill programs.

Table 8‑3: Summary of Field Quartz Blank Performance — 2011 and 2014 Drill Programs (Nb₂O₅)

Drill Program

No. of Blanks Submitted

Insertion Rate

Blank Failure Rate (Nb₂O₅)

2011

90

5.1%

39% (early program; corrected)

2014

454

4.7%

4% (following corrective measures)

Source: DGC 2022

Note: (1) Failure defined as result exceeding 2× XRF detection limit.

The elevated blank failure rate observed in the 2011 program (39%) was attributed to contamination early in the program. This was identified, reported to the laboratory, and corrective measures were implemented, resulting in a significant reduction to 4% failure in the 2014 program. Failing blanks were re-analyzed to differentiate between contamination and analytical error. The QPs concluded that blank material exhibited acceptable levels of error with no evidence of material contamination following corrective action.

CRMs and SRMs used across the programs were sourced from carbonatite-matrix certified reference materials (Dillinger Hütte SX18-series; Geostats GRE-03 and GRE-04; Oreas 460 and 464; AMIS0185), all carrying certified values for Nb₂O₅, Sc, TiO₂, and REE as appropriate to the program era. Where SRM or CRM failures were identified, ten samples on either side of the failing control were re-assayed, with the re-assay result accepted as the final value. For the 2011 program, no standards required re-assay at a level of concern.

Reject and pulp duplicate programs confirmed acceptable sampling precision throughout both drill programs, with most duplicate pairs plotting within expected variability ranges for the deposit type. Third-party external check analysis submitted to Inspectorate (2011) and SGS Lakefield (2014) confirmed the primary laboratory results were free from systematic bias.

8.3.2 NioCorp 2025 QAQC

Routine QAQC procedures throughout the sampling and analytical analysis for the 2025 drilling programs continued at the highest level of quality standard throughout the process. Insertion of duplicate samples taken from various stages of the process, insertion of known control samples

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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(SRMs, CRMs and blanks) and sending third-party pulps to the secondary lab was done similarly to previous sampling programs.

Table 8‑4: Summary of designed level of insertion of QC submissions in the 2025 drill program.

Sample Type

Sample Sub-type

Type

Number

Actual Insertion Rate

Blanks

Field Quartz Blanks

Optical Quartz

463

6%

Certified Reference Material

OREAS 465

Nb CRM

116

6%

OREAS 464

Nb CRM

95

GRE-11

Nb CRM

123

GRE-08

Nb CRM

120

Duplicates

Field quartered core

¼ HQ Core

398

6%

External Lab Checks

Coarse-Rejects

Reject split

282

4%

Pulp

Pulp split

490

6%

Source: DGC 2026

 

To meet the planned QAQC insertion rates the following guidelines were followed:

•
Field quartz blanks (1 in 20, or 5%) were inserted within or immediately after samples collected from mineralized intervals, targeting zones of elevated visual mineralization, where possible.
•
CRMs (1 in 20, or 5%) were inserted in the field with the sample sequence.
•
Field quarter-core duplicates (1 in 20, or 5%) were inserted to test mineralization and sampling variability.

The following sections provide detail on the types of samples used to validate the QA/QC results and the certain discussion around how the results were managed.

8.3.2.1 Field Quartz Blanks

The 2025 Drill program had a similar methodology utilizing coarse natural clear quartz blanks (sourced from an optical-quality quartz quarry, in Arkansas, USA) whereby the samples were inserted into the sample sequence to identify potential contamination and to confirm sample sequence consistency.

Table 8‑5: Summary of 2025 Drill Program Field Blank Insertion

Element Nb2O5

Drill Program

# of Assays sent to Lab

7,198

# of Field Quartz Blanks Sent to Lab

462

Insertion Rate of Blanks

6%

# of Blank Failure (2x XRF Detection Limit)

51

Percentage of Blank Failure Rate

11%

Source: DGC 2026

 

The TiO2 data for the blank quartz material is more variable than the Nb2O5 data. Results for Sc were 99% below the control line of 2 x XRF detection limit of 5ppm. Overall good results were returned for Nb2O5 and Sc.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

DGC considers that the blank material has acceptable levels of error and there is limited evidence of any major contamination issues at the laboratory. The laboratory utilised internally supplied blank material at the sample preparatory stage.

 

img170397038_22.jpg

Source: DGC 2026

Figure 8‑4: Summary of Blank Control Charts for Nb2O5, Sc, TiO2 Submission SGS for the 2025 Drill Program

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_23.jpg

Source: DGC 2026

Figure 8‑5: Summary of Blank Control Charts for Nd, Pr, Dy and Tb Submissions to SGS

8.3.2.2 Certified Reference Material

Certified reference material was selected for the 2025 sampling program to monitor the accuracy of the analytical methods.

Four CRMS were selected for the sampling program based on their representativity of the carbonatite matrix. The main purpose of the CRM insertion was to provided controls of Nb2O5, Sc and TiO2.

The CRM selected were OREAS464 and OREAS 465 from Ore Research & Exploration and GRE-11 and GRE-08 from Geostats. These were added as the best representation the Sc, TiO2, REE’s and the Nb2O5 ranges for the orebody.

Table 8‑6: Summary of the CRM used for the 2025 Program

Analyte

Unit

CRM - Certified Values

OREAS 465

OREAS 464

GRE-11

GRE-08

Nb2O5

%

0.67

0.272

0.875

0.148

Sc

ppm

149

141

72

91

TiO2

%

10.52

3.26

 -

 -

La

ppm

24100

12000

523

1467

Ce

ppm

39500

15300

135

5099

Pr

ppm

3772

2597

601

953

Nd

ppm

11800

9940

3574

4433

Sm

ppm

1361

1498

452

515

Eu

ppm

286

324

82.7

108.8

Gd

ppm

584

676

183

283

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Analyte

Unit

CRM - Certified Values

OREAS 465

OREAS 464

GRE-11

GRE-08

Tb

ppm

57

54

17.5

33.4

Dy

ppm

217

178

67

143

Ho

ppm

27.7

21.3

8.5

19.1

Er

ppm

50

38.2

17.1

33.8

Tm

ppm

4.52

3.56

1.9

3

Yb

ppm

19

15.7

9.9

14.6

Lu

ppm

1.72

1.69

1.2

1.8

Y

ppm

524

449

179

448

Source: DGC 2026

8.3.2.2.1 Nb2O5 standards and Certified Reference Material

The summary of the results for Nb2O5 analysis for each CRM is summarized below. The 2025 drill program performed well showing a very low failure rates, less than 2%. Bulk of the results returned were within the acceptable 3 Standard deviation limits.

Very low Bias overall was reported. With GRE11- and GRE08 reporting -4% and 2% respectively. The OREAS 464 and OREAS465 reported very low at 1% and 0%.

Table 8‑7: Summary of the Nb2O5 Results per CRM (SGS)

Standard (Nb2O5)

Count

Certified Value (%)

STD DEV (%)

Mean Assay (%)

Range (%)

Min (%)

Max (%)

N outside 3SD

OREAS 465

113

0.67

0.043

0.6691

0.43

0.27

0.7

1

1%

OREAS 464

94

0.2723

0.0115

0.2747

0.41

0.25

0.66

1

1%

GRE-11

123

0.87

0.03

0.84

0.77

0.15

0.92

2

2%

GRE-08

119

0.148

0.005

0.154

0.04

0.13

0.17

1

1%

Source: DGC 2026

The failure on OREAS464 and OREAS465 was due to a mislabelling of the CRM when sampled. The mislabelling was corrected in the database, Figure 8‑6 shows results of the original data before the correction.

The performance observed for the certified reference material and their coverage support accurate assay results received for the assay labs and the incorporation of these results in future work is recommended.

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img170397038_24.jpg

Source: DGC 2026

Figure 8‑6: OREAS465 and OREAS464 Results for Nb2O5

8.3.2.2.2 Sc standards and Certified Reference Material

The summary of the results for Sc analysis for each CRM is summarized below. The 2025 drill program showed erratic values for Sc on OREAS465. The lab was contacted and the results began to improve. Failure rates on OREAS464, GRE-11 and GRE-08 showing a failure rate below 9%. Bulk of the results returned were within the acceptable 3 Standard deviation limits.

Table 8‑8: Summary of the Sc Results per CRM (SGS)

Standard (Sc)

Count

Certified Value ppm)

STD DEV ppm)

Mean Assay ppm)

Range (ppm)

Min (ppm)

Max (ppm)

N outside 3SD

OREAS 465

113

149

9.1

156.07

69

132

201

31

27%

OREAS 464

94

141

5.8

139.9

40

123

163

8

9%

GRE-11

123

72

5

66.47

33

59

92

1

1%

GRE-08

889

91

6

83.12

17

76

93

0

0%

Source: DGC 2026

Very low Bias overall was reported. With GRE11- and GRE08 reporting very low bias at -8% and -9% respectively. The OREAS 464 and OREAS465 reported a low bias at 5% and -1% respectively.

img170397038_25.jpg

Source: DGC 2026

Figure 8‑7: OREAS465 and OREAS464 Results for Sc

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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8.3.2.2.3 TiO2 standards and Certified Reference Material

The summary of the results for TiO2 analysis for each CRM is summarized below. The 2025 drill program showed variability at the start of the program. Internal Lab issues were addressed with SGS and results started showing more consistency.

Failure rates on OREAS464 and OREAS465 showed low failure rates of 1%. GRE-08 and GRE-11 were not reported as the CRM did not have an approved methodology for reporting of the TiO2 analyte.

Overall results returned were within the acceptable 3 Standard deviation limits.

Table 8‑9: Summary of the TiO2 Results per CRM (SGS)

Standard (Ti02)

Count

Certified Value (%)

STD DEV (%)

Mean Assay (%)

Range (%)

Min (%)

Max (%)

N outside 3SD

OREAS 465

113

10.51

0.307

10.36

7.33

3.27

10.6

1

1%

OREAS 464

94

3.26

0.099

3.32

7.4

3.043

10.53

1

1%

GRE-11

123

 -

 -

0.632

0.25

0.46

0.71

not measured

GRE-08

119

 -

 -

0.458

0.04

0.43

0.48

not measured

Source: DGC 2026

 

OREAS465 and OREAS 464 reported -1 and 2% bias respectively. Differences after correction at the lab were negligible.

img170397038_26.jpg

Source: DGC 2026

Figure 8‑8: OREAS465 and OREAS464 Results for TiO2

8.3.2.2.4 Certified Reference Material and other REE results.

The CRM’s used for the 2025 Drill programs provide reference control of Nd, Pr, Dy and Tb. These CRMs performed within acceptable ranges with a low bias across all grade ranges for both Nd and Pr. Reported results for both Dy and Tb were generally close to the expected values.

There is a 1% to 8% percent sample failure rate for Nd, Dy and Tb. Pr showed a good performance on OREAS464 and OREAS465 with bias less than 1%, however on GRE08 and GRE11 result reported a positive bias between 3% to 9% resulting from several of the results falling outside the upper limits. These certified reference materials are not individually suited for REE evaluations but when considered in combination, the overall performance of REE’s across the 4 CRMS submitted to the lab is within acceptable limits. The results represent the expected levels of REE.

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Overall, the CRM’s performed well. Using this information obtained from external carbonatite projects assisted with compiling a better understanding of what is to be expected.

Table 8‑10: REE performance on CRM's OREAS 465, ORES463, GRE-11 and GRE-08

OREAS 465

Element

Count

Certified Assay Value (ppm)

STD DEV (ppm)

Mean Assay (ppm)

Range (ppm)

Min (ppm)

Max (ppm)

N outside 3 STD DEV

Nd

113

11800

500

11596

2907

9693

12600

1

1.00%

Pr

113

3772

18.13

3781

1400

2800

4200

1

1.00%

Dy

113

217

13

59

28.17

48.05

76.22

5

4.00%

Tb

113

57

3.1

226

101

180

281

9

8.00%

 

 

 

 

 

 

 

 

 

 

OREAS 464

Element

Count

Certified Assay Value (ppm)

STD DEV (ppm)

Mean Assay (ppm)

Range (ppm)

Min (ppm)

Max (ppm)

N outside 3 STD DEV

Nd

94

9940

320

9828.6

2286

9114

11400

5

5.00%

Pr

94

2597

106

2625.1

2900

1000

3900

5

5.00%

Dy

94

178

8

184.89

51

171

222

5

5.00%

Tb

94

54

2.7

54.8

14.37

49.1

63.47

4

4.00%

 

 

 

 

 

 

 

 

 

 

GRE-11

Element

Count

Certified Assay Value (ppm)

STD DEV (ppm)

Mean Assay (ppm)

Range (ppm)

Min (ppm)

Max (ppm)

N outside 3 STD DEV

Nd

123

3574

153

3514.1

1482

2926

4408

4

3.00%

Pr

123

601

22

637

475

525

1000

19

15.00%

Dy

123

67

2

67.6

89.07

56.93

146

8

7.00%

Tb

123

17.5

0.9

17.07

17.38

14.61

31.99

3

2.00%

 

 

 

 

 

 

 

 

 

GRE-08

Element

Count

Certified Assay Value (ppm)

STD DEV (ppm)

Mean Assay (ppm)

Range (ppm)

Min (ppm)

Max (ppm)

N outside 3 STD DEV

Nd

119

4433

197

4361.3

734

3996

4730

0

0.00%

Pr

119

953

36

982.7

600

700

1300

20

17.00%

Dy

119

143

6

144.64

26

132

158

0

0.00%

Tb

119

33.4

1.6

32.89

6.65

28.98

35.63

0

0.00%

Source: DGC 2026

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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8.3.2.3 Duplicates

Pulp Duplicates

The Pulp duplicates that were taken after pulverization, were sent to the lab as part of the 2025 sample submission. The 463 pairs represent approximately ~6% of total sample submissions from the 2025 drilling program. The results indicate a reasonable comparison between the original and duplicate assays (Figure 8‑9 and Figure 8‑10). All REE’s were evaluated, charted, and classified as reasonable comparisons, during this review and the targeted REE’s element charts.

img170397038_27.jpg

Source: DGC 2026

Figure 8‑9: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Pulp Duplicate) Core Duplicate Analysis for Analytes Nb2O5 and Sc

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_28.jpg

Source: DGC 2026

Figure 8‑10: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Pulp Duplicate) Core Duplicate Analysis for Analytes TiO2, Nd, Pr, Dy and Tb

Course Reject Duplicates

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

A total of 282 coarse duplicate samples, taken after crushing, were sent to the lab for analysis (blind) as part of the sample submission. This represent ~3% of the total sample submissions from the 2025 drilling program.

Upon review there was a positive mean difference trend for TiO2, Tb, Pr, Dy where Nb2O5, Sc showed a negative mean bias. Overall, the precision of the results is within the acceptable limits as no analyte fell beyond the 10% average relative difference boundary (Figure 8‑11 to Figure 8‑13).

img170397038_29.jpg

Source: DGC 2026

Figure 8‑11: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Nb2O5, Sc and TiO2

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_30.jpg

Source: DGC 2026

Figure 8‑12: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Nd and Pr.

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_31.jpg

Source: DGC 2026

Figure 8‑13: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Dy and Tb.

 

Field ¼ Core Duplicates

A total of 398 field duplicate samples comprised of ¼ core were resubmitted to the lab representing 5.5% of total sample submissions for 2025.

The results for the ¼ core duplicates were relatively good. A small positive bias was reported for TiO2, Nd, Pr, Dy and TiO2 and a slight negative bias on Nb2O5 and Sc less than 1%. Overall excellent precision reported for the samples retuned for the 2025 exploration program (Figure 8‑14 to Figure 8‑16).

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_32.jpg

Source: DGC 2026

Figure 8‑14: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Nb2O5, Sc and TiO2

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_33.jpg

Source: DGC 2026

Figure 8‑15: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Nd and Pr

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_34.jpg

Source: DGC 2026

Figure 8‑16: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (Coarse Reject Duplicate) Core Duplicate Analysis for Analytes Dy and Tb

8.3.2.4 Third Party Check Samples

For 2025, pulp duplicates of the samples that SGS labs prepared samples were submitted to Actlabs for alternative analyses. These 463 pulps represent approximately ~6% of total sample submissions from the 2025 drilling program. An additional 27 of those external duplicated were duplicated and sent to an umpire lab for testing. Overall, 490 external pulps were analysed to determine if there is any bias.

There is a slightly high bias observed from these results. A possible reason for these results could be that most duplicate samples are expected to a have a degree of variability between laboratories and analytical methods.

•
It is recommended to utilise a higher relative difference cutoff be considered when comparing third party duplicate check analysis.

The Samples for both analyses reviewed remain below an average 10% relative difference, identifying a degree of risk, but falling within accepted limits.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_35.jpg

Source: DGC 2026

Figure 8‑17: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (External Lab Duplicate) Core Duplicate Analysis for Analytes Nb2O5, Sc and TiO2

 

 

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_36.jpg

Source: DGC 2026

Figure 8‑18: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (External Lab Duplicate) Core Duplicate Analysis for Analytes Nd and Pr

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_37.jpg

Source: DGC 2026

Figure 8‑19: Paired Relative Difference and an XY Scatter Comparison of Original Versus Quarter (External Lab Duplicate) Core Duplicate Analysis for Analytes Dy and Tb.

8.4 Qualified Person’s Opinion on the Adequacy of Sample Preparation, Security & Procedures

It is the QP’s opinion that the sample preparation, security, and analytical procedures used by NioCorp are consistent with standard industry practices and that the data is suitable for the 2026 Mineral Resource Estimate. The continuation of a robust QAQC program from the 2022 work has led to the opinion that there are no material concerns with the geological or analytical procedures used or the quality of the resulting data.

The QP confirms that the Elk Creek geological database is of suitable quality to support both Mineral Resource and Mineral Reserve estimation. The QPs responsible for the preparation of this report have reviewed the historical sample preparation, analytical procedures, and QA/QC protocols and have confirmed they remain current and applicable to the geological database used in this report. No new material scientific or technical information has become available that would alter the QP's opinion on the adequacy of the historical data.

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9 Data Verification

The QPs responsible for this report have reviewed the data verification section of the 2022 Technical Report Summary and are satisfied that the procedures described therein are adequate for the purposes of this report. The QPs confirm that the geological database is of suitable quality to support the Mineral Resource and Mineral Reserve estimates disclosed herein.

9.1 Data Validation

Site visits to the Elk Creek Project between 2025 and 2026 are detailed below in Table 9‑1:

Table 9‑1: Summary of QP Site Visits

QP

Company

Expertise

Date(s) of Visit

Jacob Anderson, CPG, MAusIMM

Dahrouge Geological Consulting USA Ltd.

Mineral Resources

September 8 to 10, 2025

Janine Brown, P.Geo.

Dahrouge Geological Consulting USA Ltd.

Geology

May 10 to 16, 2025

Trevor Mills

Dahrouge Geological Consulting USA Ltd.

Geology; procedures; QAQC

Multiple times from April 24, 2025 to November 17, 2025

Amélie C. Ouellet, P.Eng

Andrieux & Associates Geomechanics Consulting

Rock Mechanics

May 13-14 2025

Scott Britton, P.E.

 

Amplify Mine Planning

Reserves/Mining

March 30 to 31, 2026

Adrian Brown, P.E.

Adrian Brown Consultants Inc

Hydrogeology

July 25 to August 12, 2025;

September 23 to September 25, 2025

Troy Meyer, P.E. P.Eng

Tierra Group/BBA

Tailings

January 22, 2026

Anthony (Tony) Linton, FEC, P.Eng., IntPE (Canada)

Dumas Contracting USA Inc.

Mine Engineering

March 10 to 11, 2026

Eric Larochelle, B.Eng

SMH Process Innovation

Hydrometallurgy & Process Engineering

March 12, 2026

 

During the site visits completed by the Qualified Persons, the following site visit included:

•
Review of current drilling, logging, sampling, analytical and QAQC procedures used during the 2025 drilling program.
•
Review and verification of the interpreted geological setting of the Project.
•
Visual confirmation of some previously completed drill hole collars.

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•
Visual confirmation of previously completed drilling in 2011 and 2014.
•
Review of overall site facilities.

9.1.1 Core Processing Protocols

Core processing was completed by DGC during the 2011 and later work programs. As such, the QPs have relied on DGC’s database to review the core logging procedures, collection of samples, and chain of custody associated with those programs. DGC provided the QPs with data exports from the project drillhole database (MX Deposit) and electronic copies of the original assay certificates and procedural documentation. The QA/QC protocols employed by DGC included the routine insertion of field duplicates, laboratory pulp duplicates, blanks, and niobium, scandium, titanium and REE certified reference standards.

No significant issues were identified during the site visit. It is DGC’s opinion that the geological data collection procedures and the chain of custody were found to be consistent with industry standards and in accordance with NioCorp’s internal procedural documentation.

9.1.2 Database Validation

Multiple database validations have been completed by SRK between 2014 and 2017, with subsequent validations completed by Nordmin in 2019, Understood and Optimize in 2022. Detailed information on database validations is described in detail in previous technical reports on the Project.

Data validation for the current report is summarized below. Validation consisted of the verification of collar locations, downhole survey data, geologic and assay data, along with checks for missing values, duplicate entries and inconsistencies among tables. Checks were applied to confirm that the aforementioned data types were accurate and fell within the appropriate thresholds. All inaccuracies that were identified were corrected before incorporating them into the final dataset.

9.1.3 NioCorp QAQC

It is the opinion of the QPs that NioCorp implemented a robust QA/QC process, as described in Section 11. Assay results were actively monitored throughout all drill programs including the 2025 drill program and QA/QC results were summarized. A number of failures for standard and blank reference materials were documented. Most of the reference materials performed as expected within tolerances of 2 to 3 standard deviations of the mean grade. The QP is satisfied that the QA/QC process is performing as designed to ensure the quality of the assay data.

9.2 Limitations

All Qualified Persons were not limited in access to any of the supporting data use for the resource estimation or describing the geology and mineralization in this report. The database verification is limited to the procedures described above. All mineral resource data relies on industry professionalism and integrity of those who collected and handled the database.

 

9.3 Qualified Person’s Opinion

It is of the opinion of the QP that all geological data collection, standard operating procedures and QA/QC procedures implemented during all programs since 2011 are of suitable quality to support the Mineral Resource and Mineral Reserve Estimates and meet industry best practice standards.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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10 Mineral Processing and Metallurgical Testing

This section describes the mineral processing and metallurgical testing conducted for the Elk Creek Niobium, Scandium, Titanium, and Rare Earth Production Facility.

The Qualified Persons (QPs) for this section have reviewed the testwork and modeling results and opine that they provide a reasonable basis for the process flowsheet, subject to the limitations noted. The process targets production of niobium, scandium, titanium tetrachloride (TiCl4), and rare earth products from the Elk Creek orebody. It is the QP’s opinion that the data generated from the testwork is adequate for the purposes of this TRS, and that the data itself was produced using conventional industry practice.

The metallurgical program for the Elk Creek Project has evolved through multiple phases, incorporating drill core analysis, mineralogical reconciliation, bench-scale tests, pilot campaigns, and demonstration plant operations. Recoveries and performance metrics presented in this section are derived from empirical data as observed by L3 Process Development during various bench scale and demonstration scale testing campaigns. L3 is independent of the Company and is not certified by any standards association. The QP (SMH) provided oversight for all of the metallurgical work conducted at L3’s facilities in Trois Rivieres, Quebec.

10.1 Historical Test Work

Historical metallurgical test work was conducted at SGS Canada Inc. (SGS), Hazen Research (Hazen) and Kingston Process Metallurgy (KPM) throughout 2014, 2015, 2016 and into 2017 to properly design the required process units for the conversion of mined ore into niobium, titanium and scandium products. The preliminary test work was performed on flotation concentrate, which has since been abandoned due to the poor recovery it offered. Test work then focused on whole ore as a feed and consisted of the extensive exploratory bench and pilot scale hydrometallurgical test programs aimed at defining and proving out a flowsheet using different reagents and technologies. The historical process flowsheet was therefore established and proven by test work and piloting performed in all the process units. Historical metallurgical test work has been previously extensively disclosed in technical reports issued during the period 2015-2022.

Table 10‑1: Summary of Historical Technical Reports

Technical Report Stage

Issue Date

Source

Preliminary Economic Assessment

2015-05-15

 (SRK, 2015)

Feasibility Study

2017-08-10

 (SRK, 2017)

Feasibility Study

2019-05-29

 (Nordmin, 2019)

Feasibility Study

2022-06-28

  (Batty et al., 2022)

10.2 Mineral Processing

The comminution test work was completed in two stages at SGS Canada Inc. (SGS) in Lakefield, Ontario in 2016. The primary stage test work (SGS 2016a) was conducted on six composite samples and 13 variability samples and included:

•
Bond Rod Mill Work Index (Rwi) testing.
•
Bond Ball Mill Work Index (Bwi) testing.
•
Bond Abrasion Index (Ai) testing.

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•
Bond Low-energy Impact (Cwi) testing.
•
JK Drop Weight (JKDW) testing.
•
Semi-autogenous grinding (SAG) Mill Comminution (SMC) testing.

The second stage of comminution test work (SGS 2016b) was conducted on a single composite sample, using a LABWAL high-pressure grinding roll (HPGR) semi-pilot scale test work program.

The test work results indicate that the Project ore is categorized as soft to moderately hard in terms of ore hardness, and amenable to standard grinding as well as an HPGR operation.

A bulk representative sample (approximately 3,000 kg) of ore was subjected to locked cycle pilot scale testing at NRRI-Coleraine in Minnesota. The ore tested indicates that it is amenable to processing via the HPGR. Autogenous layer buildup and flake generation were both acceptable, and there was, on average, 40% < 1 mm product generated from the HPGR when in steady state.

The most notable observations from the testing are:

a)
Final product particle size is largely independent of press force and moisture
b)
Specific energy increases as both moisture and press force increase
c)
There is a decrease in specific throughput as the press force increases
d)
There is a decrease in specific throughput as the feed moisture increases

Based on the results as indicated above, it would be recommended to run an installed HPGR at lower pressures, i.e. 3.0 N/mm2 or less, and to remove as much free water from the circuit as possible. This will have the effect of reducing power requirements with limited to no impacts on size reduction.

The data as collected to date is suitable for full HPGR scale up and process guarantees around envisioned plant operation conditions.

10.3 Hydrometallurgy

10.3.1 Mineralogy and Feed Characterization

The following ore samples were received by L3 Process Development and used in the execution of bench scale, pilot scale and demonstration scale underlying the flowsheet disclosed in this technical report. The material was characterized as screen undersized material from the High-Pressure Grinding Rolls (HPGR) test work performed by Weir.

The ore used in the HPGR test was obtained from assay reject samples from exploration activity, all passing 10 mesh. These samples were received from the 2014 core drilling program and were used as feed material to test the HPGR circuit. A total of ten representative samples representing different areas of the mine that could be reasonably expected during production were combined into a composite sample and used as feed to the HPGR program.

The material received at the demonstration plant was analyzed, and the results are shown in Table 10‑2.

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Table 10‑2: Ore Feed Characterization Summary

Parameter

Value/Source

Key Minerals

Carbonates (converted to oxides), MgO, CaO, REE-bearing phases

Elemental Content

Reconciled from drill core assays

Water Content

Estimated from anhydrous/hydroxide minerals

Mass Loss (Calcination)

~30% (CO2 + H2O)

10.3.2 Process Development & Flowsheet

The process flowsheet follows a sequential structure divided into areas and units. The area breakdown is as follows:

Area 100 – Ore Activation

Area 200 – Ammonium Chloride Cycle

Area 300 – Hydrochloric Acid Leach

Area 400 – Sulfuric Acid Baking and Water Leaching

Area 500 – Niobium and Titanium Recovery

Area 600 – Rare Earth Elements Extraction

Area 700 – Rare Earth Separation

Area 800 – Chloride Recovery

Area 900 – Sulfate Effluent Treatment

10.3.2.1 Metallurgical Recoveries and Performance

Table 10‑3 summarizes the product recoveries for each of the areas.

Table 10‑3: Product Recoveries per area

Element/Unit

100 / 200

300

400

500

600

700

Overall

Ti

100%

99.00%

81.20%

100%

80.50%

Nb

100%

99.70%

85.40%

99.60%

84.70%

Sc

100%

96.20%

98.10%

94.30%

Pr

100%

90.00%

100%

98.50%

88.70%

Nd

100%

94.90%

100%

99.40%

94.40%

Tb

100%

95.00%

100%

99.30%

94.40%

Dy

100%

95.00%

100%

99.50%

94.60%

 

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10.3.2.1.1 Area 100 – Ore Activation

The activation process involves the thermal decomposition of carbonates minerals to oxides in an indirect natural gas rotary calciner at 1,454°F (790°C). During this process, CO2 is released then recovered, dehydrated and used to mineralize calcium and magnesium in Area 200 - Ammonium Chloride Cycle.

Ore activation is performed using a continuous rotary kiln processing 10 kg per hour at an external tube temperature of 1,652°F (900°C) for an average of 15 minutes. In this process, calcium and magnesium carbonates are converted to their respective oxides and made available for leaching by an ammonium chloride solution. Approximately 21 wt% of the initial ore mass is lost during this stage. Between 2022 and 2023, L3 generated approximately 2,400 kg of calcined ore. As part of an on-going optimization campaign, L3 has processed an additional 1,153 kg since January 2026.

10.3.2.1.2 Area 200 - Ammonium Chloride Cycle

The ammonium chloride cycle is a closed loop process using an ammonium chloride solution to selectively leach Ca and Mg as chlorides, followed by their mineralization as carbonates, regenerating the ammonium chloride leach solution.

The demonstration unit has been operated during 11 months between 2022 and 2024 to process the 2,400 kg of calcined material. The continuous demonstration unit operation revealed that the leaching process was effective with over 80% calcium removal achieved. The complex equilibria between ammonia (a weak base) and carbonic acid (a weak acid) in combination with magnesium and calcium ions resulted in difficulty precipitating the MgCO3 from solution in initial design of the Carbonate Mineralization portion of the circuit. As a result, additional test work was performed to identify a steady-state process that would successfully mineralize MgCO3 from solution.

During the 2026 Elk Creek Study, L3 modeled the system and the speciation across the unit. The difference in behavior between calcium and magnesium allowed for a 2-stage selective precipitation of both elements in sequence and for a potential increase in calcium recovery. Since 2025, L3 has performed various optimization campaigns to support the 2026 Elk Creek Study modeling and associated recovery of calcium. Selected experiments conditions and leach efficiencies are presented as Table 10‑4. Concentration of feed and residue in the NHL leach unit is presented in Figure 10‑1.

Table 10‑4: Ammonium chloride test conditions and associated recoveries for select tests.

Experiment ID

NCPn
NHL25

NCPn
NHL28

NCPn
NHL31

NCPn
NHL33

Leaching Conditions

Concurrent

Concurrent

Countercurrent

Countercurrent

Temperature (°C)
   (Leach 1/Leach 2)

99/99

99/99

98/98

99/100

NH4Cl Conc. (gpL)

125

125

125

125

Leach pH (1/2)

7.69/8.06

7.03/6.85

7.77/7.73

7.67/7.59

% Solids

10%

10%

10%

10%

Reaction time (min)
    (Leach 1/Leach 2)

135/50

90/60

120/50

120/50

Leach Efficiency

Ca

82%

68%

79%

80%

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Mg

40%

43%

73%

66%

Fe

5%

2%

0%

0%

LREE

0%

0%

0%

0%

MREE

0%

0%

0%

0%

HREE

0%

0%

0%

0%

TREE + Y

0%

0%

0%

0%

Source: L3 2026

img170397038_38.jpg

Source: L3 2026

Figure 10‑1: Calcium (top) and Magnesium (bottom) concentration over time and moving average trendline.

Recovery of selected concurrent and counter current campaigns are presented as Figure 10‑2. A detailed look at the countercurrent leach recoveries is presented as Figure 10‑3. The demonstration

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unit was modified in March 2026 to reflect the dual precipitation process, and initial data is presented in Figure 10‑4.

img170397038_39.jpg

Source: L3 2026

Figure 10‑2: Ammonium chloride leach performance for Ca and Mg.

img170397038_40.jpg

Source: L3 2026

Figure 10‑3: Ca and Mg leaching performance per countercurrent leach stage.

 

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img170397038_41.jpg

Source: L3 2026

Figure 10‑4: (a) Ca and Mg distribution in the precipitate from the Ca Precipitation (CaP) and the Magnesium Precipitation (MgP). (b) The aqueous concentration in grams per liter of Ca and Mg after the precipitation process.

10.3.2.1.3 Area 300 - Hydrochloric Leach

The hydrochloric acid leach area employs a counter-current HCl leach circuit to solubilize metals and concentrate niobium and titanium in the residue. The following section is adapted from Larochelle et al., 2024: “A new paradigm for the recovery of rare earth elements: the high activity flowsheet as applied to the Elk Creek deposit” (Proceedings IMPC 2024: XXXI international mineral processing congress).

The initial hydrochloric acid leach unit was composed of a cascade of three 1-hour residence time agitated reactors with temperature controlled at 80 ºC. L3 operated this unit for approximately 6 months, processing ammonium chloride circuit residue. During the demonstration campaign and following the optimization of the ammonium chloride operation, it became obvious that the HCl pregnant leach solution (HCl-PLS) had too much residual acid, with molarities up to 5 M HCl, for the subsequent solvent extraction circuits. Slurry handling equipment constraints between the reactor stages at the chosen scale prevented L3 from increasing the solids content in the leach circuit. Thus, it was decided that HCl-PLS would be recycled in the leach circuit to mimic a high solids content. L3 operated the hydrochloric acid leach circuit for approximately 5 months in its initial configuration and for three months in the configuration where recycled PLS was used on fresh solids to mimic the high-density leaching operation. The circuit processed approximately 1,500 kg of ammonium chloride leach residue. The leach efficiency and HCl-PLS composition for both scenarios is presented in Table 10‑6. The typical HCl-PLS composition for each scenario is presented as Table 10‑5. The low- density leaching operation aggregates data from approximately 1-month continuous campaign while the high-density operation aggregates data from over a month of HCl-PLS fed to the solvent extraction process covering many leach campaigns. XRF assays are identified using a * and are elements that do not have a significant impact in the solvent extraction circuit. The improved process allowed for smaller and more efficient solvent extraction circuits.

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Table 10‑5: HCl-PLS composition of for high and low density scenarios.

 

 

Low Density Leaching

High Density Leaching

Element

Unit

Average

σ

Average

σ

Mg

mg/L

2,657

440

6,545

273

Ca

mg/L

7,331

2,003

36,759

2,192

Si*

mg/L

10

9

1.6

3.0

Al*

mg/L

980

423

1,607

155

Fe

mg/L

20,854

1,862

58,502

3,185

Mn*

mg/L

840

163

1,485

98

Zn*

mg/L

55

14

115.8

12.4

Ti

mg/L

266

29

97.1

9.5

Nb

mg/L

22.6

6

7.5

0.9

Sc

mg/L

10.2

2.3

24.4

2.1

TREE

mg/L

429

56

1,144

114

Th

mg/L

45.5

6.9

160.7

9.6

Source: L3 2026

 

The PLS generated during those campaigns was used to operate the solvent extraction demonstration circuit described in Section 10.3.2.1.6.

Following the initial campaign, L3 has modified the leaching unit to transition from a co-current unit toward a counter-current unit. Initial test work revealed this arrangement was more effective in leaching the rare earths and scandium. Selected experiments are presented in Table 10‑6.

 

Table 10‑6: Test conditions and leach efficiencies for select HCl leaching tests.

Experiment ID

NCPl
HCL03

NCPl
HCL04

NCPm
HCL12

NCPm
HCL13

NCPn
HCL15

NCPn
HCL16

Leaching Conditions

Temperature (°C)
  (Leach 1/Leach 2)

90/90

90/90

90/60

80/60

80/60

80/60

PLS Acid Molarity

NA

1.88

4.56

7.04

3.03

2.65

Feed Iron Mass %

27.2%

18.0%

21.3%

20.4%

20.9%

19.3%

% Solids

25%

25%

17%

17%

30%

30%

Reaction time

(min)

120

120

60

60

20

20

Leach Efficiency

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Experiment ID

NCPl
HCL03

NCPl
HCL04

NCPm
HCL12

NCPm
HCL13

NCPn
HCL15

NCPn
HCL16

Ca

98%

97%

91%

90%

91%

89%

Mg

99%

99%

97%

94%

99%

94%

Fe

97%

97%

90%

86%

89%

82%

Th

96%

73%

89%

93%

75%

67%

Nb

<1%

<1%

<1%

<1%

<1%

<1%

Ti

<1%

<1%

<1%

<1%

<1%

<1%

Sc

98%

88%

96%

98%

89%

86%

LREE

98%

89%

93%

92%

88%

84%

MREE

98%

92%

95%

95%

90%

82%

HREE

98%

87%

94%

93%

80%

59%

TREE + Y

98%

89%

94%

93%

89%

82%

Source: L3 2026

 

Two tests were performed using material optimally processed in the ammonium chloride circuit. The tests were performed using 4,500 g of ammonium chloride circuit residue and subjected to a counter current leach using 13 liters of PLS from the previous stage 2 experiment and 15 liters of 32 wt.% hydrochloric acid. Both leaches were performed at 194°F (90°C) for 120 minutes. The individual rare earth recoveries for these experiments are presented as Table 10‑3.

img170397038_42.jpg

Source: L3 2026

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Figure 10‑5: Leach efficiencies for leach 1 and leach 2 in the counter current leach process.

10.3.2.1.4 Area 400 – Sulfuric Acid

The sulfuric acid area employs a pug mill, where concentrated sulfuric acid is mixed with the residue from the Hydrochloric Acid leach circuit, and a rotary calciner to convert niobium and titanium to water-soluble sulfates. This is then followed by their dissolution and hydrolysis. Selected experiments are presented Table 10‑7. Calculated recoveries of typical experiments are presented as Source: L3 2026

Figure 10‑6. However, it should be noted that the system is designed to account for the residual concentrations following the recycling of barren solution in the water leach and hydrolysis circuit. Therefore, such concentration profiles for selected representative experiments are presented as Figure 10‑7.

Table 10‑7: Experiment test conditions and results for select acid bake-water leach tests.

Experiment ID

NCPm-ABK03

NCPm-ABK04

NCPn-ABK05

Acid Bake Conditions

Outlet Temperature °C

300

300

300

Acid/Solid Ratio (m/m)

48%

49%

36%

Cake Yield

132%

134%

81%

 

 

 

 

Experiment ID

NCPm-WTL09

NCPm-WTL10

NCPn-WTL10

Water Leach Conditions

Temperature °C

90

90

40

Reaction Time (min)

120

120

30

% Solid

23%

23%

23%

Wash Conditions

Number of Washes

3

3

3

Final Cake Humidity

30%

34%

36%

Conversion Efficiency

Fe

72%

89%

65%

Ti

86%

79%

80%

Nb

89%

85%

91%

Source: L3 2026

 

Table 10‑8: Experiment test conditions and results for select hydrolysis tests.

Experiment ID

NCPm-HYD07

NCPm-HYD08

NCPm-HYD12

NCPm-HYD15

Hydrolysis Conditions

Temperature °C

105

105

105

105

Reaction Time (min)

30

30

30

30

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Water to PLS Ratio

2

2

2

2

Residual Concentration

(g/L)

Fe

0.52

0.75

0.30

0.22

Ti

0.28

0.73

0.24

0.16

Nb

0.06

0.23

0.50

0.01

Source: L3 2026

 

img170397038_43.jpg

Source: L3 2026

Figure 10‑6: Ti and Nb water leaching efficiency of acid baked material over various tests.

 

img170397038_44.jpg

Source: L3 2026

 

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Figure 10‑7: Aqueous concentration in gram per liter throughout the hydrolysis procedure for Ti and Nb. (a) NCPn-16, (b) NCPn-17, (c) NCPn-18.

 

10.3.2.1.5 Area 500 – Chlorination

Carbo-chlorination (Chlorination) is the primary commercial process to convert titanium oxide into titanium tetrachloride, which is then purified by distillation. It has also been applied successfully to other refractory metals. The reaction involving both carbon and chlorine is presented as Eq.

MxOy + yC + yCl2 → xMCl2y/x + yCO

Chlorination test work was performed in two phases of increasing complexity. The goals of the test work campaigns were to demonstrate that the chlorination and separation of Nb from Ti from hydrolysate material could be achieved. A minimum working chlorinator and condensing train was designed, fabricated, and operated. The phase I unit is illustrated as Figure 10‑8.

.

img170397038_45.jpg

Source: L3 2026

Figure 10‑8: L3 2026

Phase I consisted of 5 experiments, involving the processing of 502g of hydrolysate material. While the technical feasibility of niobium chlorination was demonstrated, the design of the unit did not allow for the calculation of a mass balance. A summary of the test work parameters and results is presented as Table 10‑9 and Table 10‑10 respectively.

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Table 10‑9: Phase I Experimental Conditions

Test No

Hydrolysate
Mass

Graphite Feed
Ratio

Temperature

Cl2 Flow

Retention
Time

g

m/m

°C

CFH

min

1

70

0.17

900

5

60

2

120

0.67

900

5

70

3

108

0.50

900

3

120

4

108

0.50

900

3

120

5

96

0.33

900

3

120

Source: L3 2026

 

Table 10‑10: Phase I Results

Recovery

Nb/Ti Ratio (wt.%)

Test No

Mass Out

Nb

Ti

In

C1

C2

C3

2

30.1

N/A

N/A

0.31

9.32

12.69

0.03

3

N/A

N/A

N/A

0.43

3.31

0.35

0.06

4

28.49

96%

93%

0.43

17.45

10.44

0.03

5

8.26

99%

99%

0.36

10.09

28.01

0.04

Source: L3 2026

 

The first series of tests allowed the researchers to ensure the safe operation (test 1, not presented) and validate the operating procedures while starting the data collection. This first campaign demonstrated that chlorination was an effective method for recovering niobium and separating it from titanium. Recoveries are estimated from the chlorinator feed and residue and should be used as indicative only.

Phase II involved the addition of a titanium tetrachloride scrubbing loop similar to the commercial flowsheet design. The goal of phase II was to demonstrate that niobium could be recovered and separated from titanium using selective condensation and titanium vaporization with an emphasis on the composition of the niobium product. Recoveries should also be considered as indicative because the campaign did not aim at their optimization. The phase II unit is presented as Figure 10‑9.

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img170397038_46.jpg

Source: L3 2026

Figure 10‑9: Phase II Chlorination Equipment Design

 

Phase II consisted of 3 weeks of tests, involving the processing of 2,779 g of hydrolysate material. The technical feasibility of niobium separation and recovery from titanium was demonstrated with niobium samples with low titanium concentration. Summary of the test work is presented as Table 10‑11 and Table 10‑12.

 

Table 10‑11: Phase II Experimental Conditions

Week

Hydrolysate Mass

Graphite Ratio

Temperature

Cl2Flow

Retention Time

g

C:H

°C

CFH

min

1

820.8

0.21

900

3

60

2

1096.8

0.20

900

3

60

3

861.6

0.21

900

3

60

Source: L3 2026

 

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Table 10‑12: Phase II Results

Nb/Ti Ratio

Week

Residue (g)

In

Out

Nb

1

495

0.36

73.41

22.24

2

513

0.39

119.12

27.1

3

402

0.35

125.71

27.27

Source: L3 2026

 

10.3.2.1.6 Area 600 – Rare Earth Elements Extraction

The Rare Earth Elements Extraction area uses dimethyloctyl dihexyl diglycolamide (DMODHDGA, DGA-6) to selectively extract rare earths and scandium from HCl PLS at high activity. Co-extracted impurities are then scrubbed and the rare earth are stripped using a weakly acidic chloride solution. Residual iron in the strip liquor is precipitated out as iron hydroxide using ammonium hydroxide and the REE-rich strip solution is sent to Area 700 – Rare Earth Separation.

Bench scale extraction test work was performed on HCl PLS at different acidity and activity levels. Selected extraction experiments are described as Table 10‑13, with results presented as Table 10‑14. Each test was performed using a matrix approach to reproduce the effect of a 3-stage counter-current extraction circuit and derive distribution ratios from developed profiles using aqueous-based mass balance. The data presented is the 3rd stage extraction data.

Table 10‑13: Extraction PLS Description

Experiment ID (NCPt)

DG6-01

Base Case HCl PLS

DG6-02

DG6-01 PLS Neutralized to 2.11M HCl using MgCO3

DG6-03

DG6-01 PLS diluted to 1.5 M HCl using ROW

DG6-04

DG6-01 PLS Neutralized to 1.0M HCl using MgCO3

Source: L3 2026

 

Table 10‑14: Experiment test conditions and results for select DGA-6 extraction tests

Experiment ID (NCPt)

DG6-01

DG6-02

DG6-03

DG6-04

Extraction parameters

O:A

1:3

1:3

1:3

1:3

PLS Free Acid (M)

2.72

2.11

1.54

0.96

Contact Time (min)

30

30

30

30

Results

Raff. Free Acid (M)

2.63

2.27

1.17

1.09

Disengagement (sec)

30

30

15

30

Phase Separation (min)

3.5

4.0

1.3

5.0

 

 

 

 

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Experiment ID (NCPt)

DG6-01

DG6-02

DG6-03

DG6-04

Distribution Ratio*

 

Mg

0.07

0.11

0.21

0

Ca

0.62

0.57

1.37

0.55

Al

0.03

0.11

0.47

0

Fe

1.53

1.07

1.49

1.25

Ti

1.31

0.82

0.62

0.28

Nb

1.04

2.08 **

0.36

0

Sc

5.2

3.65

313

3.43

Y

4.03

3.10

11.61

3.53

La

4.24

3.08

4.91

3.31

Ce

5.95

4.25

22.99

4.36

Nd

7.46

5.33

73.71

5.88

Dy

3.86

7.61

37.05

5.23

Th

0.65

0.58

0.44

0.14

* Sc, Y and Dy had raffinate concentrations near the ICP-OES detection limit and should be considered indicative only.

** DL in organic phase assay.

Source: L3 2026

 

Bench scale scrubbing test work was performed on loaded organic at different acidity and activity levels. Selected scrub experiments are described as Table 10‑15. Each test was performed using a matrix approach to reproduce the effect of a 3-stage counter-current scrub circuit.

Table 10‑15: Experiment test conditions and results for select DGA-6 scrub tests

Experiment ID (NCPt)

DG6-01

SCB-01

DG6-01

SCB-02

DG6-08

DGB-07

Extraction parameters

O:A

1:1

1:1

3:1

Scrub Solution Free Acid (M)

0.01

0.01

0

Scrub Solution MgCl2 (M)

0.5

0.1

1.2

Contact Time (min)

15

15

15

Scrub Stage No

3

3

1

Results

SCB Liquor Free Acid (M)

0.53

0.45

0.37

Disengagement (sec)

15

15

60

Phase Separation (min)

2.0

2.0

5.0

Distribution Ratio

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Experiment ID (NCPt)

DG6-01

SCB-01

DG6-01

SCB-02

DG6-08

DGB-07

Mg

N/A

N/A

0.07

Ca

2.73

1.12

1.05

Fe

0.66

0.35

1.81

Sc

Note 1

2,724

553.9

Y

4,018

157

1,288

La

5.28

1.66

52.1

Ce

19.58

4.14

409.2

Nd

Note 1

21.47

150.8

Dy

Note 1

180.77

Note 1

Th

Note 1

4.43

N/A

Source: L3 2026

Note 1. UDL in the scrub liquor.

 

10.3.2.1.7 Area 700 - Rare Earth Separation

L3 used its predictive rare earth separation simulation software and literature extraction data to design a separation flowsheet to recover magnet rare earth elements. The first circuit in the area was assembled and operated over a 3-month period using synthetic PLS with ratios similar to the modeled REE extraction circuit strip liquor to generate calibration data for more accurate circuit modeling. The circuit was designed with 2 saponification stages, 6 extraction stages, 16 scrub stages, 24 strip 1 stages, 6 strip 2 stages and 2 strip 3 stages. The organic phase was prepared using 35 v% Cyanex 572 diluted in D80 kerosene. The circuit operated as intended and a summary of the operation, with the circuit concentration of target element across the various discharge streams is presented as Figure 10‑10 to Figure 10‑13. The relative distribution of each element across those streams is then presented as Figure 10‑14 to Figure 10‑17.

The operation parameters are presented as Table 10‑16.

 

Table 10‑16: REE solvent extraction operational parameters.

SAP

EXT

SCB

STR1

STR2

STR3

Flow Rate (mL/min)

Aqueous

9.1

100

8

6.4

4.1

3.1

Recirculation

0

0

13

16

5

20

Org

22

22

22

22

22

22

[H+]/[OH-]

0.25

0.5

1

1.5

3

Source: L3 2026

 

 

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img170397038_47.jpg

Source: L3 2026

Figure 10‑10: Concentration of elements over time in the Extraction stage of the solvent extraction system.

img170397038_48.jpg

Source: L3 2026

Figure 10‑11: Concentration of elements over time in the Scrub stage of the solvent extraction system.

 

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img170397038_49.jpg

Source: L3 2026

Figure 10‑12: Concentration of elements over time in the Strip 1 stage of the solvent extraction system.

img170397038_50.jpg

Source: L3 2026

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Figure 10‑13: Concentration of elements over time in the Strip 2 and Strip 3 stages of the solvent extraction system.

img170397038_51.jpg

Source: L3 2026

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Figure 10‑14: Distribution of the LREEs throughout the circuit.

img170397038_52.jpg

Source: L3 2026

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Figure 10‑15: Distribution of the SEG REEs throughout the circuit.

img170397038_53.jpg

Source: L3 2026

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Figure 10‑16: Distribution of the Tb, Dy, and Y throughout the circuit.

img170397038_54.jpg

Source: L3 2026

Figure 10‑17: Distribution of the HREEs throughout the circuit.

 

10.3.2.1.8 Area 800 - Chloride Recovery

The ferric chloride pyrohydrolysis demonstration unit was designed and fabricated to demonstrate the technical feasibility of using pyrohydrolysis for the recovery of hydrochloric acid from ferric chloride solutions. A photo and a schematic of the demonstration unit are presented respectively as Figure 10‑18 and Figure 10‑19.

The demonstration unit operated for 190 hours over 6 weeks and processed 122 gallons of ferric chloride produced by the iron recovery circuit.

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img170397038_55.jpg

Source: L3 2026

Figure 10‑18: Demonstration Ferric Chloride Pyro-Hydrolysis Reactor Unit Photo

 

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img170397038_56.jpg

Source: L3 2026

Figure 10‑19: Demonstration Ferric Chloride Pyro-Hydrolysis Reactor Unit Schematic

The unit was not optimized, and signs of corrosion are observable in the ferric oxide residue. This was specific to the pilot unit and is not representative of commercial operation. A typical residue produced during the operation is presented as Figure 10‑20. The distribution of elements in the residue is presented as Figure 10‑21. It should be noted that most of the base metals such as Mo, Ni and Cr assayed in the solid residue are likely corrosion products from the demonstration unit itself as they are not present in the ferric chloride liquor.

The demonstration unit is designed as a spray roaster pyrohydrolyser, operating at 0.9 gallon per hour, at a temperature of 1200°F, and using natural gas burners.

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img170397038_57.jpg

Source: L3 2026

Figure 10‑20: Iron Oxide Residue

 

img170397038_58.jpg

Source: L3 2026

Figure 10‑21: Pyrohydrolysis residue elemental distribution.

10.3.3 Significant Factors

A sufficient level of test work was conducted to support the design for the Hydrometallurgical Facility included in this Technical Report Summary and to reduce the risk of a fatal flaw in the flowsheet to a negligible level. (Here the term ‘fatal flaw’ is defined as an impairment or risk that is significant enough that if realized, would prevent the process from operating as intended, create a significant operating cost burden or result in a much lower recovery than expected for targeted metals). It’s

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important to note that optimization was not achieved in all areas, and some areas were not operated at the pilot or demonstration level. In addition, a vendor testing program is essential to the final equipment selection effort. Process optimization should continue to be explored both in preparation for and throughout detailed design.

While the current model for rare earth separation has been successfully calibrated to a level sufficient for this Technical Report Summary, L3 recommends that the full circuit be piloted and that commercial samples be produced to perform the final calibration of the model for each circuit and to optimize the circuit design and operation.

Finally, it is likely that the facility design could be optimized by increasing the project mass balance definition through process simulation of monthly elemental feed composition using the processing plant model and the compositions from the mine plan.

10.4 Pyrometallurgy

The purpose of the pyrometallurgical plant is to reduce the niobium oxide present in the Hydromet feed and convert it into a saleable ferroniobium metal. Pyrometallurgical test work has been conducted at multiple facilities, including:

•
Consulting & Testwork Services (XPS), Sudbury, Ontario, Canada (Spring 2015)
•
Kingston Process Metallurgy (KPM), Kingston, Ontario, Canada (Summer 2017)
•
Consulting & Testwork Services (XPS), Sudbury, Ontario, Canada (Fall 2025)
•
Consulting & Testwork Services (XPS), Sudbury, Ontario, Canada (ongoing, 2026)

The 2015 and 2017 test programs did not fully characterize the chemical nature of the compounds present in the Hydromet feed; however, the material was identified as being rich in titanium. Subsequent Hydromet process improvements led to a significant reduction in titanium content by 2025, shifting the focus of the pyrometallurgical process toward the treatment of niobium–sodium–oxide compounds formed following calcination. More recent 2026 testing identified the presence of titanium oxide along with phosphorus-bearing niobium oxide phases, indicating variability in feed composition. Despite these variations, the aluminothermic reaction has consistently demonstrated the capability to produce a Fe–Nb alloy, supporting the development of multiple processing options pending confirmation of the ongoing test program.

For the 2025 test campaign conducted at the Glencore XPS facility in Sudbury, Ontario, Canada, approximately 400 g of material was used for pyrometallurgical testing. The sample was supplied by L3 Process Development (Trois-Rivières, Québec, Canada), and the corresponding chemical analysis results are presented in Figure 10‑22.

Hydrometallurgical process improvements implemented between 2019 and 2023 resulted in a significant reduction in titanium content in the product stream feeding the pyrometallurgical stage. Chemical analysis indicated that titanium was present only at trace levels, thereby mitigating previous concerns related to slag handling and slag chemistry. However, the chemical analysis did not provide information regarding the specific nature of the compounds present in the hydrometallurgical precipitate. X-ray diffraction (XRD) analysis identified a polyoxoniobate compound, Na₇(H₃O)(Nb₆O₁₉)·(H₂O)₁₄, as the dominant phase.

This compound cannot be directly reduced in its existing form. Thermal decomposition at elevated temperature (approximately 1,022°F (550 °C)) results in the formation of sodium niobate (NaNbO₃),

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which can subsequently be reduced using aluminum in the presence of Fe₂O₃ to produce a ferroniobium alloy.

For the 2025 test campaign, a discrete Fe0.₈₇Nb intermetallic phase was not directly identified. However, microstructural and compositional analyses of the produced alloy indicated Fe/Nb ratios consistent with the targeted FeNb alloy composition. These results confirm that, despite the complex chemical form of niobium in the Hydromet feed, the NaNbO₃ phase obtained after calcination can be effectively reduced through the pyrometallurgical process to produce a ferroniobium alloy meeting compositional expectation.

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img170397038_59.gif

Source: L3 Process Development, 2026

Figure 10‑22: Chemical analysis results for the 400 g sample supplied by L3 Process Development

 

 

 

 

 

 

 

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While the pyrometallurgical test work successfully demonstrated the production of FeNb alloy, several aspects require further evaluation and optimization prior to advancement to detailed engineering:

•
Improved understanding and control of polyoxoniobate formation within the Hydromet circuit to ensure consistent feed chemistry
•
Larger-scale testing to optimize slag fluidity and enhance metal–slag separation
•
Optimization of flux composition to promote effective slag formation while maintaining acceptable refractory life and plant availability
•
Production of sufficient quantities of FeNb alloy to define product handling and shipping requirements
•
Evaluation of suitable crucible and refractory materials compatible with process chemistry and operating temperatures
•
Determination of the optimal Fe/Nb ratio based on both market requirements and process performance

Pyrometallurgical test work conducted at Kingston Process Metallurgy confirmed the technical viability of producing a saleable FeNb alloy through aluminothermic reduction of niobium-bearing precipitates, including under conditions of elevated TiO₂ content. The test program demonstrated niobium recovery on the order of 96% and validated the use of hematite (Fe₂O₃) as an effective iron source. Within this framework, the pyrometallurgical circuit functions both as a metal production step and as a contributing mechanism for managing residual titanium-bearing compounds.

Ongoing test work is evaluating process performance under updated feed conditions, with results pending at the time of this report. Variations in feed composition and compound speciation, particularly with respect to titanium-bearing phases, are expected to influence process behavior and phase distribution. The current program is therefore focused on confirming the applicability of earlier assumptions and refining the operating basis where required.

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11 Mineral Resource Estimate

11.1 Introduction

The Mineral Resource Estimate for the Elk Creek Carbonatite Project was prepared by Dahrouge Geological Consulting USA Ltd. and has an effective date of June 30, 2026. The Mineral Resource Estimate was reported by Dahrouge Geological Consulting USA Ltd.

The geology was modeled in Leapfrog Geo™ software, and the 3D bock model, grade estimation and classification were developed in Maptek Vulcan™ software. The resource encompasses four commodity streams niobium (Nb₂O₅), titanium (TiO₂), scandium (Sc), and total rare earth oxides (TREO) — hosted within a carbonatite intrusive complex located in Johnson County, Nebraska, USA.

The methodology followed a systematic, domain-controlled estimation workflow comprising of source database validation, geological domaining, exploratory data analysis (EDA) and compositing, variography, ordinary kriging block model estimation, model validation, and resource classification. Each phase is described in the subsections that follow.

It is of the opinion of the QP that all geological data collection, standard operating procedures and QA/QC procedures implemented during all programs since 2011 are of suitable quality to support the Mineral Resource Estimate and meet industry best practice standards. All issues relating to all relevant technical and economic factors likely to influence the prospect of economic extraction can be resolved with further work.

11.2 Source Database

The drillhole database used for resource estimation was managed in MX Deposit and transferred into Maptek Vulcan™ for compositing and estimation. The database was compiled and maintained by DGC for independent resource estimation.

The resource database comprises 65 drill holes totalling approximately 127,569 ft (38,883 m) of HQ diamond core, with individual holes ranging from surface to a maximum depth of approximately 3,280 ft (1,000 m). All mineralised intercepts are located within the carbonatite intrusive complex and were drilled using diamond core methods. The full composite dataset contains 38,876 approximately 3.28 ft (one-meter) and 336 sub 3.28 foot (one-meter) composite intervals for a total of 39,098 composite sales spanning depths of 587 ft to 3,280 ft (179 m to 1,000 m) below surface, consistent with the sub-cropping nature of the deposit beneath approximately 656 ft (200 m) of Pennsylvanian marine sediment cover.

The assay database includes determinations for the following analytes used in resource estimation: Nb₂O₅ (%), range 0.010–4.093%; TiO₂ (%), range 0.001–11.570%; Sc (ppm), range 0–306 ppm; LREO (ppm, calculated), range 0–43,642 ppm; HREO (ppm, calculated), range 0–2,480 ppm; and TREO (ppm, calculated), range 0.01–44,004 ppm.

LREO is calculated as the sum of La₂O₃, Ce₂O₃, Pr₂O₃, Nd₂O₃, and Sm₂O₃; HREO is calculated as the sum of Eu₂O₃, Gd₂O₃, Tb₂O₃, Dy₂O₃, Ho₂O₃, Er₂O₃, Tm₂O₃, Yb₂O₃, and Lu₂O₃; and TREO is the sum of LREO and HREO (14 rare earth oxides in total).

Prior to compositing, DGC carried out standard database validation procedures within MX Deposit and Maptek Vulcan™ including checks for overlapping sample intervals, missing or inconsistent collar and survey data, and interval length consistency. No material errors were identified, and no

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significant corrections were required. The database was considered suitable for resource estimation purposes.

11.3 Geological Domaining

Three estimation domains were defined by DGC for the Elk Creek resource estimate, based on the primary lithological controls on mineralisation within the carbonatite intrusive complex. Domain wireframes were constructed by DGC geologists in Leapfrog Geo™ using logged lithological contacts from all 65 drill holes in the resource database. Domain boundaries were interpreted to honour the principal lithological transitions observed in core logging and were not grade driven. All three domain boundaries were treated as hard boundaries for estimation purposes, meaning no composites from one domain were permitted to inform grade estimates in an adjacent domain. This treatment is justified by the pronounced grade contrasts between domains: Domain contacts were validated by visual inspection of drill sections and plans in Leapfrog Geo™. The three domains are described below:

(1)
MCARB – Magnetite / Dolomite Carbonatite (Primary Resource Domain)

The MCARB domain encloses the magnetite-dolomite carbonatite, which is the principal host of economic mineralisation at Elk Creek. This domain contains 18,675, 3.28-foot (one-meter) composites from 46 drill holes and represents the highest-grade, most continuous mineralised unit in the deposit. Mean grades within MCARB of 0.560% Nb₂O₅, 2.434% TiO₂, 65.7 ppm Sc, and 2,837 ppm TREO are markedly elevated relative to all other domains. Grade distributions within MCARB are comparatively well-behaved, with coefficients of variation (“CV”) of 0.74 for Nb₂O₅ and 0.53 for TiO₂, consistent with a spatially coherent, continuously mineralised carbonatite body.

(2)
DOL_CARB – Dolomite Carbonatite (Peripheral Domain)

The DOL_CARB domain is composed of dolomite carbonatite peripheral to and transitional with the MCARB unit. It contains 9,845 composites from 54 drill holes. Grades are substantially lower than MCARB across all analytes. The DOL_CARB domain is highly variable with CVs (coefficient of variation) of 1.12 for Nb₂O₅ and 1.53 for TiO₂. TREO grades in DOL_CARB are more erratic, with a high CV of 1.51 and a pronounced high-grade tail.

(3)
LAMP – Lamprophyre (Intrusive Dyke Domain)

The LAMP domain encloses lamprophyre dykes that intrude the carbonatite complex. It contains 2,858 composites from 19 drill holes, spanning depths of 623 ft (190 m) to 3,317 ft (950 m). Lamprophyre is lithologically and geochemically distinct from the carbonatite units, with moderate Nb₂O₅ grades (mean 0.149%), elevated TiO₂ relative to DOL_CARB (mean 1.782%), and subdued Sc (mean 29.7 ppm).

(4)
Non Mineralized Domain

There are 7,720 non mineralized composites in the database. These intervals are contained within the overlying Marine Sediments are were not used in the estimation.

11.4 Density Determination and Assignment

Dry bulk density values were determined from 3,382 core samples collected from diamond core during the 2025 drilling program. Density was measured by two methods: volumetric determination

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from dry weight and dimensional measurements (primary method, 2,955 measurements), and water immersion.

Domain average dry bulk density values were calculated as the arithmetic mean of valid measurements within each domain and assigned uniformly to all estimated blocks within the corresponding domain wireframe. No spatial interpolation of density applied. Density statistics by domain are summarized in Table 11‑1.

Table 11‑1: Bulk density by estimation domain

Domain

Number of Samples

Mean SG (t/m3)

Std. Dev.

MCARB

1,471

3.06

0.23

DOL_CARB

898

2.87

0.17

LAMP

784

2.86

0.19

 

The large measurement populations and low standard deviations, particularly for DOL_CARB and LAMP, support the use of domain arithmetic means as representative density values. The elevated MCARB density (3.06 t/m3) is consistent with the abundant magnetite characteristic of the magnetite-dolomite carbonatite lithology that defines this domain.

11.5 Exploratory Data Analysis

Exploratory data analysis (EDA) was carried out by DGC on the 3.28-foot (one-meter) composite database following domain assignment, conducted independently for the MCARB, DOL_CARB, and LAMP domains across Nb₂O₅, TiO₂, Sc, and TREO.

11.5.1 Distributed Analysis

Grade distributions were examined using histograms, log-probability plots, and summary statistics (Figure 11‑1 through Figure 11‑4).

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img170397038_60.jpg

Source: DGC 2026

Figure 11‑1: Nb2O5 Grade distribution by domain

 

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img170397038_61.jpg

Source: DGC 2026

Figure 11‑2: TiO2 Grade distribution by domain

 

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img170397038_62.jpg

Source: DGC 2026

Figure 11‑3: Sc Grade distribution by domain

 

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img170397038_63.jpg

Source: DGC 2026

Figure 11‑4: TREO Grade distribution by domain

 

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11.5.2 Top Cut Analysis

Top-cut values were determined using a combination of three methods:

(1)
log-probability plot disintegration;
(2)
CV stabilisation analysis; and
(3)
fixed-percentile evaluation at the 99th percentile used as a cross-check.

Top-cut decisions were made on a per-analyte, per-domain basis. Sc was not top cut by any domain. Log probability plots show the upper tail tracking the fitted lognormal reference line continuously and is consistent with well behaved distributions that do not require outliner suppression (Figure 11‑5 through Figure 11‑8).

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img170397038_64.jpg

Source: DGC 2026

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Figure 11‑5: Nb2O5 Log Probability Plot

img170397038_65.jpg

Source: DGC 2026

Figure 11‑6: TiO2 Log Probability Plot

 

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img170397038_66.jpg

Source: DGC 2026

Figure 11‑7: Sc Log Probability Plot

 

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img170397038_67.jpg

Source: DGC 2026

Figure 11‑8: TREO Log Probability Plot

 

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After analysis the results of the top cut by analyte and domain are contained in Table 11‑2.

Table 11‑2: Top Cut Summary by Domain and Analyte

Domain

Analyte

Cap Value

Composites Affected

% of Domain

Mean Before

Mean After

Change

MCARB

Nb₂O₅

3.000%

21

0.11%

0.5595%

0.5591%

−0.1%

MCARB

TiO₂

Not applied

—

—

2.434%

2.434%

—

MCARB

TREO

Not applied

—

—

2,837 ppm

2,837 ppm

—

DOL_CARB

Nb₂O₅

1.000%

84

0.85%

0.1695%

0.1654%

−2.4%

DOL_CARB

TiO₂

3.570%

172

1.75%

0.5763%

0.5611%

−2.6%

DOL_CARB

TREO

15,000 ppm

99

1.01%

2,045 ppm

1,995 ppm

−2.5%

LAMP

Nb₂O₅

1.200%

1

0.03%

0.1489%

0.1487%

−0.1%

LAMP

TiO₂

Not applied

—

—

1.782%

1.782%

—

LAMP

TREO

Not applied

—

—

2,227 ppm

2,227 ppm

—

Source: DGC 2026

11.5.3 Declustering

Cell declustering was applied independently to each analyte (Nb₂O₅, TiO₂, Sc, TREO) across all three domains using the Vulcan™ cell declustering algorithm configured to minimise the weighted average grade. Isotropic cell geometry was used throughout (Y and Z anisotropy = 1.0), with 5 offsets per cell size and 10 cell sizes tested across domain-specific ranges bracketing the representative drill spacing. The resulting declustered weight fields were passed directly to the Vulcan™ estimator as sample weighting inputs. The optimum cell sizes and resulting declustered means are presented in Table 11‑3.

In the MCARB domain, declustered means are 7–14% lower than arithmetic means across all analytes, confirming a positive clustering bias in the high-grade core where infill drilling at closer spacing has preferentially sampled higher-grade material. The optimum cell sizes of 394-886 ft (120-270 m) in MCARB are consistent with the representative drill spacing of 164-246 ft (50-75 m) for Indicated resources and confirm that the declustering correction is geologically meaningful rather than an artefact of cell size selection. The declustered MCARB Nb₂O₅ mean of 0.484% is the reference grade against which the OK block model mean was benchmarked during validation, where the volume-weighted estimated mean was confirmed within 5% of this value.

In DOL_CARB, the pattern is more variable. Nb₂O₅ and Sc show moderate negative clustering bias (−16% and −20% respectively), consistent with a peripheral domain where wider-spaced holes have sampled both higher and lower grade zones unevenly. The near-zero declustering correction for TiO₂ (+0.6%) and small positive correction for TREO (+3.0%) in DOL_CARB reflect the more erratic spatial distribution of these analytes in the peripheral carbonatite. The short optimum cell size for DOL_CARB TREO (10 m) indicates that TREO in this domain has no meaningful clustering bias at deposit scale and the arithmetic mean is effectively the declustered mean. In LAMP, declustering

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corrections are small (< 8%) across all analytes, consistent with the more uniform drill spacing in that domain.

Table 11‑3: Optimum cell size ranges used for cell declustering by domain and analyte.

Domain

Analyte

Units

Arithmetic Mean

Capped Mean

Optimum Cell Size (m)

Declustered Mean

MCARB

Nb₂O₅

%

0.5595

0.5591

120

0.4837

TiO₂

%

2.434

2.434

250

2.224

Sc

ppm

66

66

270

57

TREO

ppm

2,837

2,837

260

2,634

DOL_CARB

Nb₂O₅

%

0.1695

0.1654

290

0.1391

TiO₂

%

0.576

0.561

280

0.565

Sc

ppm

22

22

280

17

TREO

ppm

2,045

1,995

10

2,055

LAMP

Nb₂O₅

%

0.1489

0.1487

290

0.1433

TiO₂

%

1.782

1.782

280

1.718

Sc

ppm

30

30

120

28

TREO

ppm

2,227

2,227

20

2,324

Source: DGC 2026

11.5.4 Correlation Analysis

Inter-element correlations were evaluated through bivariate scatter plots and Pearson correlation matrices within each domain (Table 11‑4). Strong positive correlations exist between Nb₂O₅ and TiO₂ within the MCARB domain, consistent with co-occurrences pyrochlore, magnetite, and rutile/ilmenorutile in the magnetite-dolomite carbonatite assemblage. Sc correlates positively with both Nb₂O₅ and TiO₂ in MCARB, supporting co-product NSR modelling. TREO correlations with base metals are moderate in MCARB and weaker in DOL_CARB, reflecting more erratic REE distribution in peripheral carbonatite.

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Table 11‑4: Pearson Correlation Matrix (Capped Composite Grades by Domain)

img170397038_68.jpg

Source: DGC 2026

11.6 Data Preparation

Assay intervals were composited to a uniform 3.28 ft (1 m) downhole length using length-weighted averaging within Maptek Vulcan™. Compositing was performed independently within each estimation domain, with domain boundaries treated as hard constraints such that no composite interval spans more than one domain. At domain contacts, residual intervals shorter than the

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nominal composite length were assigned to the dominant domain by majority interval length. The resulting composite database contains 39,098 samples with a length of 3.28 ft (1 m): 18,675 samples in MCARB, 9,845 samples in DOL_CARB, 2,858 samples in LAMP and 7,720 non mineralized samples. The mean composite length across all domains is 0.994 m, confirming a highly uniform support with minimal residual interval effects. Capped composite grades were used as inputs to variography and estimation.

11.7 Variography

Experimental semivariograms were computed and modelled by DGC for each estimation analyte within each domain using capped composite grades. All variograms were standardised to a total sill of 1.0. For all other domain-analyte combinations, the nugget was determined by visual fitting to the y-intercept of the experimental variogram, as data density in those domains and directions was insufficient to compute reliable downhole variograms. All structures were fitted using spherical models. The MCARB domain Nb₂O₅ variogram was computed directionally; all other domain-analyte combinations were modelled omni-directionally due to data density constraints. The complete variogram model parameters are presented in Table 11‑5.

Table 11‑5: Variogram Model Parameters: All Domains and Analytes

Domain

Analyte

Nugget

Str.

Type

Sill (C)

Maj Range (m)

Semi (m)

Min (m)

Orientation

MCARB

Nb₂O₅

0.30

1

Sph

0.70

110

70

30

Az30°/Pl75°/Dip90°

MCARB

TiO₂

0.30

1

Sph

0.70

35.8

35.8

35.8

Omni

MCARB

Sc

0.14

1

Sph

0.86

268.6

268.6

268.6

Omni

MCARB

TREO

0.35

1

Sph

0.42

60

60

60

Omni

MCARB

TREO

—

2

Sph

0.23

319

319

319

Omni

DOL_CARB

Nb₂O₅

0.30

1

Sph

0.70

38

38

38

Omni

DOL_CARB

TiO₂

0.30

1

Sph

0.70

11.8

11.8

11.8

Omni

DOL_CARB

Sc

0.20

1

Sph

0.80

31.8

31.8

31.8

Omni

DOL_CARB

TREO

0.20

1

Sph

0.80

380

380

380

Omni

LAMP

Nb₂O₅

0.25

1

Sph

0.75

92.4

92.4

92.4

Omni

LAMP

TiO₂

0.25

1

Sph

0.75

74.2

74.2

74.2

Omni

LAMP

Sc

0.13

1

Sph

0.87

14.0

14.0

14.0

Omni

LAMP

TREO

0.30

1

Sph

0.70

191

191

191

Omni

Source: DGC 2026

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img170397038_69.jpg

Source: DGC 2026

Figure 11‑9: Nb2O5 Ortho Directional Variogram for MCarb Domain.

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img170397038_70.jpg

Source: DGC 2026

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Figure 11‑10: Sc Omni Directional Variogram for MCarb Domain

 

img170397038_71.jpg

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Source: DGC 2026

Figure 11‑11: TiO2 Omni Directional Variogram for MCarb Domain

 

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img170397038_72.gif

Source: DGC 2026

Figure 11‑12: TREO Omni Directional Variogram for MCarb Domain.

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The MCARB Nb₂O₅ variogram demonstrates clear anisotropy with a major range of 361 ft (110 m) oriented steeply (Az30°, Pl75°), consistent with the near-vertical geometry of the carbonatite body. The minor range of 98 ft (30 m) reflects the across-strike horizontal continuity. Sc in MCARB has the longest range (882.5 ft, 269 m) and lowest nugget (0.14) of all MCARB analytes, consistent with its homogeneous distribution (CV 0.43). TREO in MCARB required a two-structure nested model capturing both local REE clustering (197 ft, 60 m) and broader deposit-scale continuity (1,046 ft, 319 m). In DOL_CARB, Nb₂O₅ displays very short-range continuity (125 ft, 38 m) while TiO₂, Sc, and TREO have long ranges reflecting broad compositional trends across the peripheral carbonatite rather than local high-grade continuity. In LAMP, Sc has an unusually short range (46 ft, 14 m) with a low nugget, while other analytes show moderate ranges of 243-627 ft (74–191 m).

11.8 Block Model Resource Estimation

11.8.1 Block Model Configuration

The resource block model was constructed in Maptek Vulcan™ (Version 2025) using a parent block size of 16.4 ft × 16.4 ft × 16.4 ft (5 m × 5 m × 5 m) throughout the model volume. Each block was discretized into a 4 × 4 × 4 grid of 64 points for kriging weight calculation, providing accurate volume-weighted grade estimates. The block model is named 'elk_creek_bm_dec2025.bmf'. The model was constrained by the geological domain wireframes described in Section 11.3, with each block coded to a single domain using the hard boundary assignment. The block model configuration parameters are summarised in Table 11‑6.

Table 11‑6: Block Model Configuration Parameters

Parameter

Value

Notes

Model geometry

Block size (X × Y × Z)

16.4 ft × 16.4 ft × 16.4 ft (5 m × 5 m × 5 m)

Parent blocks only

Sub-blocking

None

Fixed parent block; no sub-cells

Block discretization (kriging)

4 × 4 × 4 = 64 points per block

Per-block point grid for OK weight calculation

Model rotation (Bearing / Dip / Plunge)

0° / 0° / 0°

Axis-aligned; no rotation applied

Model origin and extents

Origin (Easting)

739,700.000 m E

SW lower corner of model volume

Origin (Northing)

4,461,000.000 m N

SW lower corner of model volume

Origin (Elevation)

−650.000 m RL

Below sea level

Block count and volume

Blocks in X (Easting)

130

650 m E–W extent

Blocks in Y (Northing)

185

925 m N–S extent

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Parameter

Value

Notes

Blocks in Z (Elevation)

170

2,779 ft (850 m) vertical extent

Total blocks in model

4,088,500

130 × 185 × 170

Model bounding box

Easting range

739,700 – 740,350 m E

650 m E–W

Northing range

4,461,000 – 4,461,925 m N

925 m N–S

Elevation range

−650 to +200 m RL

2,779 ft (850 m) vertical

Software and file

Estimation software

Maptek Vulcan™ (Version 2025)

Ordinary Kriging estimation

Block model file

elk_creek_bm_dec2025.bmf

Vulcan™ native block model format

Source: DGC 2026

11.8.2 Estimation Method

Grade estimation was carried out using Ordinary Kriging (OK) for all analytes (Nb₂O₅, TiO₂, Sc, and TREO) within all three domains. OK was selected on the basis of the moderate CVs in the primary MCARB domain (CV 0.43–0.74). The higher CVs in DOL_CARB for TiO₂ and TREO (CV 1.45–1.53 post-capping) were managed through top-cutting. Declustering weights were applied to all analytes in all domains during the OK run. An independent nearest neighbour (NN) check model was run for validation purposes (Section 14.8). All estimation used capped composite grades as inputs. Dry bulk density values were determined from 3,382 core samples collected from the 2014 and the 2025 drilling program. The density statistics and assigned values are summarized in Table 11‑7 below:

Table 11‑7: Bulk Density Summary by Geologic Domain

Domain

Measurements (n)

Mean SG t/m3)

Std dev (t/m3)

Assigned Density (t/m3)

MCARB

1,471

3.06

0.23

3.06

DOL_CARB

898

2.87

0.17

2.87

LAMP

784

2.86

0.19

2.86

Source: DGC 2026

The elevated MCARB density (3.06 t/m³) is consistent with the abundant magnetite in the magnetite-dolomite carbonatite lithology.

11.8.3 Estimation Pass Structure

A three-pass estimation strategy was employed for all domains. Pass 1 (flag = 1) uses tight search parameters and strict composite requirements, estimating only well-informed blocks. Pass 2 (flag = 2) expands the search and relaxes composite requirements for areas of moderate drill density. Pass 3 (flag = 3) uses the full variogram range and minimum composite requirements as a fill pass for peripheral blocks. For Nb₂O₅ in MCARB, Pass 3 estimated zero additional blocks, confirming that the

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MCARB Nb₂O₅ model is fully populated within two passes. The DOL_CARB Nb₂O₅ Pass 3 search has no per-hole composite limit, consistent with its use as a low-confidence fill pass in a sparse data area.

The complete estimation parameters for all domain-analyte-pass combinations, as verified from the Vulcan™ BEF output files, are presented in Table 11‑8.

Table 11‑8: Multi-Pass Estimation Parameters

Domain

Analyte

Pass

Search Maj (m)

Search Semi (m)

Search Min (m)

Max Smp

Min Smp

Min Holes

Max/Hole

MCARB

Nb₂O₅

1

58

45

20

14

6

3

4

MCARB

Nb₂O₅

2

100

80

40

16

4

2

4

MCARB

Nb₂O₅

3

170

130

60

12

4

1

4

MCARB

TiO₂

1

50

35

20

16

8

3

4

MCARB

TiO₂

2

80

60

30

16

8

2

4

MCARB

TiO₂

3

170

120

60

12

4

1

4

MCARB

Sc

1

60

45

20

16

8

3

4

MCARB

Sc

2

120

85

35

14

6

2

4

MCARB

Sc

3

270

180

60

12

4

1

4

MCARB

TREO

1

75

75

35

16

8

3

4

MCARB

TREO

2

120

120

55

24

6

2

4

MCARB

TREO

3

220

220

90

32

4

1

4

DOL_CARB

Nb₂O₅

1

22

20

14

12

6

3

4

DOL_CARB

Nb₂O₅

2

40

35

25

16

4

2

4

DOL_CARB

Nb₂O₅

3

230

155

55

32

2

1

4

DOL_CARB

TiO₂

1

100

70

40

16

8

3

4

DOL_CARB

TiO₂

2

200

140

80

14

6

2

4

DOL_CARB

TiO₂

3

300

210

120

12

4

1

4

DOL_CARB

Sc

1

50

38

18

16

8

3

4

DOL_CARB

Sc

2

100

70

30

14

6

2

4

DOL_CARB

Sc

3

230

155

55

32

2

1

8

DOL_CARB

TREO

1

212

212

212

16

8

3

4

DOL_CARB

TREO

2

264

264

264

14

6

2

4

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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Domain

Analyte

Pass

Search Maj (m)

Search Semi (m)

Search Min (m)

Max Smp

Min Smp

Min Holes

Max/Hole

DOL_CARB

TREO

3

380

380

380

12

4

1

4

LAMP

Nb₂O₅

1

60

50

35

14

6

3

4

LAMP

Nb₂O₅

2

105

85

65

16

4

2

8

LAMP

Nb₂O₅

3

180

145

95

12

4

1

4

LAMP

TiO₂

1

50

35

20

16

8

3

4

LAMP

TiO₂

2

80

55

30

16

4

2

4

LAMP

TiO₂

3

120

85

45

12

4

1

4

LAMP

Sc

1

70

50

22

16

8

3

4

LAMP

Sc

2

140

95

40

14

6

2

4

LAMP

Sc

3

300

200

70

12

4

1

4

LAMP

TREO

1

75

75

75

16

4

3

4

LAMP

TREO

2

120

120

120

24

4

2

4

LAMP

TREO

3

220

220

220

32

2

1

4

Source: DGC 2026

11.9 Model Validation

Model validation comprised four components: (1) global mean comparison between the OK model, declustered composite mean, and independent NN check model; (2) swath plot analysis in east–west, north–south, and vertical directions; (3) grade-tonnage curve comparison at multiple cut-off grades; and (4) visual inspection of estimated grades on drill sections and plans.

For each domain and analyte, the volume-weighted OK block model mean was within 5% of the declustered composite mean, satisfying the standard acceptance threshold for unbiased estimation. The close agreement between OK and NN check model means provides additional confidence that the estimation parameters are producing geologically reasonable results. Swath plots showed the OK model tracking composite swath means acceptably in all three directions with no persistent directional bias. Local deviations are attributable to kriging smoothing and variable composite density within swath panels. Grade-tonnage curves for the OK model are consistent with composite and NN curves across all relevant cut-off ranges, with the expected smoothing effect observed. Visual inspection on representative cross-sections and longitudinal projections confirmed geologically coherent grade transitions with no artefacts at domain boundaries.

 

 

 

 

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img170397038_73.jpg

Source: DGC 2026

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Figure 11‑13: Swath Plot Nb2O5 for the MCarb Domain

img170397038_74.jpg

Source: DGC 2026

Figure 11‑14: Swath Plot Sc for the MCarb Domain

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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img170397038_75.jpg

Source: DGC 2026

Figure 11‑15: Swath Plot TiO2 for the MCarb Domain

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img170397038_76.jpg

Source: DGC 2026

Figure 11‑16: Swath Plot TREO for the MCarb Domain

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The Elk Creek block model is considered unbiased and geologically reasonable. The model is suitable for mineral resource classification and reporting.

11.10 Mineral Resource Classification

Mineral Resource classification was assigned in accordance with the definitions and requirements of Regulation S-K, Subpart 1300.

Classification was based on per-block estimation quality flags (pass number) and slope of regression (SoR) values computed during the OK estimation run, supplemented by geological confidence review.

Table 11‑9: Mineral Resource Classification Material

Classification

Nb₂O₅ flag

Nb₂O₅ SoR

Sc flag

Sc SoR

TREO flag

TREO SoR

Measured

1

> 0.3

1

> 0.3

1

> 0.3

Indicated

≤ 2

—

≤ 2

—

≤ 2

—

Inferred

≤ 3

—

≤ 3

—

≤ 3

—

Source: DGC 2026

The requirement that all three primary analytes meet classification thresholds simultaneously ensures that blocks are well-constrained across the full commodity suite contributing to NSR value. Classification boundaries were reviewed in three dimensions to confirm spatial coherence. The MCARB domain, with the greatest drill density and strongest variogram continuity, hosts the majority of Measured and Indicated resources. The DOL_CARB and LAMP domains contribute predominantly to the Inferred category.

11.11 Reasonable Prospects of Eventual Economic Extraction

The Elk Creek deposit is hosted within a carbonatite intrusive complex at depths ranging from approximately 590 ft to 3,280 ft (180 m to 1,000 m) below surface, beneath approximately 656 ft (200 m) of Pennsylvanian marine sediment cover with no surface outcrop. The deposit is considered amenable to underground bulk mining by longwall stoping, consistent with the geometry of the MCARB domain as a large, continuously mineralised tabular to sub-cylindrical carbonatite body.

Reasonable prospects of eventual economic extraction were evaluated by applying an NSR cut-off value to the block model. Only blocks with NSR values exceeding the cut-off and assigned a Measured, Indicated, or Inferred classification were included in the mineral resource statement. The NSR model incorporates process recoveries of 86.72% for Nb, 83.65% for TiO₂, and 92.00% for Sc, representing the concentration circuit recoveries applied in the block model NSR calculation as derived from metallurgical test work results described in Section 13 of this report.

The deposit is in a politically stable jurisdiction (Nebraska, USA) with established infrastructure and a supportive regulatory environment. There are no known legal, environmental, or social factors that would preclude eventual economic extraction at the time of reporting.

The deposit is in a politically stable jurisdiction (Nebraska, USA) with established infrastructure and a supportive regulatory environment. There are no known legal, environmental, or social factors that would preclude eventual economic extraction at the time of reporting.

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11.12 Cut-Off Grade

The mineral resource is reported at a cut-off of NSR greater than US$218/ton (US$240/tonne) of mineralised material. NSR values were calculated for each block within Maptek Vulcan™ by applying elemental conversion factors, metallurgical recoveries, and assumed commodity prices to the estimated grades of Nb₂O₅, TiO₂, Sc, Tb₂O₃, NdPr Oxide, and Dy₂O₃.

Table 11‑10: NSR Conversion, Recoveries and Pricing

Product

Conversion Factor

Recovery (%)

Price (US$/kg)

Ferroniobium (FeNb)

0.699 × Nb₂O₅

86.72

52

Sc₂O₃

1.530 × Sc ppm

92

2,000.00

TiCl₄

2.350 × TiO₂

83.65

1.86

Tb₂O₃

—

92

1,845.00

NdPr Oxide

—

92

125

SEG Carbonate

—

92

8.97

Source: DGC 2026

The NSR cut-off of US$218/ton (US$240/tonne) was derived from preliminary operating and capital cost estimates developed during the 2026 Elk Creek Study and represents the minimum block value at which mineralised material is considered economically viable to mine and process under the assumed cost and price parameters. At the MCARB domain mean grades (0.560% Nb₂O₅, 2.434% TiO₂, 65.7 ppm Sc), the calculated NSR is approximately US$409/ton, confirming the mean MCARB grade is well above the reporting cut-off. The NSR formula incorporates six product streams: FeNb, Sc₂O₃, TiCl₄, Tb₂O₃, NdPr Oxide and SEG Carbonate. Of these, Nb₂O₅, TiO₂ and Sc are reported as mineral resource grades; Tb₂O₃, NdPr Oxide, and SEG Carbonate were estimated independently and contribute to the NSR calculation but are not reported as separate resource attributes.

11.13 Mineral Resource Tabulation

The in-situ Elk Creek Mineral Resource estimate, effective June 30, 2026, is presented in Table 11‑11. The estimate was prepared by Dahrouge Geological Consulting USA Ltd., in accordance with Regulation S-K 1300.

Table 11‑11: Elk Creek Mineral Resource Estimate Inclusive of Reserve - Effective June 30, 2026

Classification

Cut-off NSR (US$/ton)

Tonnage (Mtons)

Nb₂O₅ (%)

TiO₂ (%)

Sc (ppm)

TREO (%)

Measured

218

21.7

0.61

2.46

69.1

0.35

Indicated

218

187.4

0.50

2.36

59.85

0.36

Measured + Indicated

218

209.1

0.51

2.38

60.81

0.36

Inferred

218

169.2

0.38

2.14

51.02

0.39

 

 

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Table 11‑12: Elk Creek Mineral Resource Estimate Exclusive of Reserve – Effective June 30, 2026

Classification

Cut-off NSR (US$/ton)

Tonnage (Mtons)

Nb₂O₅ (%)

TiO₂ (%)

Sc (ppm)

TREO (%)

Measured

218

14.1

0.53

2.05

47.6

0.39

Indicated

218

149.0

0.43

1.70

42.5

0.39

Measured + Indicated

218

163.1

0.44

1.89

45.3

0.39

Inferred

218

169.2

0.38

2.14

51.02

0.39

 

Source: DGC 2026

Notes:

(1)
Mineral Resources are not Mineral Reserves and do not have demonstrated economic viability. There is no certainty that all or any part of the Mineral Resource will be converted to Mineral Reserves.
(2)
Mineral Reserves are reported separately in Section 12 of this report.
(3)
Prepared in accordance with Regulation S-K 1300
(4)
NSR cut-off of US$218/ton (US$240/tonne) based on longhole stoping underground mining; incorporates metallurgical recoveries of Nb 86.72%, TiO₂ 83.65%, Sc 92.00%, and REE by-products 92.00%, at metal prices of US$52.00/kg Nb, US$2,000.00/kg Sc, US$1.86/kg TCl4, US$1,845.00/kg Tb₂O₃, US$125.00/kg NdPr, and US$8.97/kg SEG carbonate.
(5)
TREO = LREO + HREO expressed as a percentage (TREO% = TREO ppm ÷ 10,000)
(6)
Tonnages in millions of short tons (Mt). Grades rounded to reflect the approximate nature of resource estimates.
(7)
Totals may not sum due to rounding.
(8)
Qualified Person: Dahrouge Geological Consulting USA Ltd., effective date June 30, 2026.

 

11.14 Mineral Resource Sensitivity

The sensitivity of the Elk Creek Mineral Resource to the NSR cut-off grade is summarised in Table 11‑13. The base case cut-off of US$218/ton is highlighted. The resource responds predictably to changes in the NSR cut-off — lower cut-offs capture additional lower-grade peripheral material while higher cut-offs progressively exclude sub-marginal blocks.

Table 11‑13: Elk Creek Mineral Resource Sensitivity

NSR Cut-Off (US$/t)

Tonnage (Mt)

Nb₂O₅ (%)

TiO₂ (%)

Sc (g/t)

TREO (%)

136

216.7

0.50

2.24

59

0.36

163

215.2

0.50

2.25

60

0.36

190

212.6

0.50

2.27

60

0.36

218

209.1

0.51

2.38

61

0.36

245

201.8

0.52

2.33

62

0.36

272

195.3

0.53

2.35

63

0.36

300

188.1

0.55

2.38

64

0.36

Source: DGC 2026

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11.15 Relevant Factors

The following factors are considered relevant to the interpretation and use of the Elk Creek Mineral Resource estimate.

Geological factors. The deposit has no surface exposure and is defined entirely by diamond drilling and geophysical interpretation. While domain wireframes are internally consistent and supported by strong lithological logging, the absence of outcrop means geological uncertainty at the deposit margins is higher than for a surface-exposed deposit. Inferred resources in the peripheral DOL_CARB domain carry correspondingly higher geological uncertainty.

Metallurgical factors. The NSR cut-off incorporates process recoveries derived from demonstration scale metallurgical test work. The recoveries used are: Nb 86.72%, TiO₂ 83.65%, Sc 92.00%, and REE by-products 92.00%. Overall plant recoveries incorporating downstream processing steps may differ from these concentration circuit values. Variations in metallurgical recovery across any of the primary commodities could have a material effect on the NSR value of individual blocks and consequently on reported resource tonnage at the stated cut-off.

Title and surface rights. NioCorp Developments Ltd. holds the Elk Creek property in fee simple, with full ownership of both surface and mineral rights. There are no known title disputes or encumbrances that would preclude resource development. Royalties and encumbrances. The entirety of the Mineral Resource is subject to a 2% NSR royalty held by the former owners of the lands that host the Resource. Permitting. The Elk Creek project is fully permitted. All material permits required for the proposed mining and processing operations have been obtained. There are no known outstanding permitting requirements that would materially affect the development timeline or the validity of the mineral resource estimate. Taxation. The project will be subject to standard federal and Nebraska state income tax, along with property taxes payable to Johnson County, Nebraska. Socio-economic and political factors. The Elk Creek project is located in Johnson County, Nebraska, USA, a politically stable jurisdiction with a well-established legal and regulatory framework for mining development. There are no known socio-economic, community, or indigenous land use factors that would materially affect the reasonable prospects of eventual economic extraction. Commodity price factors. The NSR model is based on commodity price assumptions current at the time of the 2026 Elk Creek Study and are based on independent market studies. Commodity prices may be subject to market volatility and are influenced by supply concentration, emerging technology demand, and geopolitical factors. A material decline in any primary commodity price, particularly niobium and scandium which dominate the NSR, would reduce the economic viability of the deposit and could reduce reportable resource tonnage at the stated cut-off.

Classification and data density. The Inferred resource (153.5 Mt / 169.2 Mtons) is large relative to the Indicated + Measured resource (189.8 Mt / 209.1 Mtons), reflecting the significant volume of DOL_CARB domain drilled at wider spacing. Conversion of Inferred to Indicated resources would require infill drilling, particularly in the peripheral carbonatite.

Reporting code compliance. Mineral Resource classification was assigned in accordance with the definitions and requirements of Regulation S-K 1300. Mineral Resources that are not Mineral Reserves do not have demonstrated economic viability. Mineral Reserves are reported separately in Section 12 of this report and are a subset of the total Mineral Resources reported herein. Inferred Mineral Resources are considered too speculative geologically to have the economic considerations

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applied to them that would enable them to be categorised as Mineral Reserves, and there is no certainty that Inferred Mineral Resources will be upgraded through continued exploration.

 

12 Mineral Reserve Estimates

12.1 Introduction

The Project is currently in the late stages of exploration and has advanced to initial development as of the report date. Based on geotechnical information and mineralized geometry, an underground long hole stoping method (LHS) has been determined to be suitable for the Deposit. Paste backfill will be used to allow for higher recovery of material. “Modifying factors” were applied to the mineral resources to allow for the defining of mineral reserves as stated herein.

Table 12‑1: Mineral reserves as of June 30, 2026 and stated in this report

2026 Reserve

Mineral Reserve Classification

Cut-off NSR

Tonnage

Grade

Grade

Grade

Grade

(US$/ton)

(ton)

(Nb2O5%)

(TiO2%)

(Sc ppm)

(TREO %)

Proven

218

       7,570,098

0.760

2.70

71.5

0.32

Probable

218

    38,359,365

0.759

2.67

68.8

0.35

Total

218

    45,929,462

0.759

2.68

69.3

0.34

Source: Amplify Mine Planning, 2026

The stopes dimensions are planned at 49ft wide while using a stope length that varies - based on Nb2O5 mineralization grade - with a maximum of 49 ft and minimum of 33 ft per stope and a level spacing height of 131 ft. The variation on stope length allows optimizing the Nb2O5 grade with a minimal increase in operating costs. The spacing of 131 ft between levels was designed based in part on the analysis of beneficial estimated operating and sustaining capital costs.

Three ore blocks (“horizons”) are identified and are composed of several mining levels that are above a designed sill pillar level and contain stopes which are planned to be mined in their entirety on a primary and secondary mining sequence (Figure 12‑1). This mining strategy allows cemented paste backfill to be placed and cured between mining cycles. Each stope in the block is mined using a bottom-up excavation approach and is expected to recover 95% of the in-place volume in each stope. A paste backfill mixture of tailings that includes cement and/or fly ash as a binder and strengthening agent will be placed in the emptied primary stope and allowed to cure prior to mining the secondary stope on either side of the primary. This methodology allows mining of ore and establishes an early start to the mining of the upper mining block above the first sill pillar level while at the same time allowing the development of the lower mining blocks. The cemented backfill was designed to have adequate strength for mining adjacent to filled stopes, thus eliminating the need for rib pillars. A partially recoverable sill pillar level designed to be left between each of these mining blocks until such time as the life-of-mine sequence plans their extraction. Extracting ore from the sill pillar level is expected to be roughly 62.5% of the in-place volume using production up- holes through the lower 82ft of the 131ft thick sill pillar and is accounted for within the reserve statement.

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img170397038_77.jpgSource: Amplify Mine Planning, 2026

Figure 12‑1: 2026 Elk Creek Study Mine Design

There will be two spiral ramps (a primary “access” ramp and secondary “haulage” ramp) driven from a box cut type of surface excavation through the strata located in the first 655ft from surface and to efficiently reach the mineral deposit. Both ramps are excavated at the same time using conventional drifting methods in conjunction with a bolting, shotcrete, and grouting ground control procedure through the first 655ft from the surface to secure the strata around the ramps.

The primary “access” ramp is designed to facilitate main access and equipment/services movement, serve as the intake air ventilation, and provide mine material logistics. A short ventilation shaft connecting the primary access ramp to the surface will also be excavated to connect the ramp to the surface mounted mine fans and create the intake mine ventilation system. The haulage ramp will be excavated to a deeper elevation than in the previous feasibility studies to reflect an increase in defined mineral reserves. This also allows earlier access to higher grade ore in the central portion of the mine and to access higher grade ore in the lower mining blocks with a more efficient material handling system. The ventilation system is engineered as a positive-pressure (“push”) ventilation network, with surface facilities providing conditioned intake air to address the humid continental climate of southeast Nebraska (hot, humid summers and cold winters). Detailed airflow quantities, fan configurations, auxiliary ventilation, refrigeration, heating, and control philosophy are presented in subsequent sections of this report.

The secondary “haulage” ramp and return ventilation system is designed to serve as the mine exhaust air system and a second means of mechanical movement/escapeway. In addition, when mining the secondary access ramp (which will be as deep as the haulage ramp), it allows for an earlier start to key lateral development using a periodic ventilation connection drift between the two ramps. The secondary haulage ramp will install and operate a “Railveyor©” (“Railveyor”) conveying system to transport the ore from the loadout drifts to the surface stockpile. The Railveyor system is sized to support the daily production requirements of the mine and mill.

 

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Mined ore will be transported from the stopes via the access level drifts to the primary haulage Railveyor ramp system using underground LHDs filling trucks, which then dump into ore passes, and on to a conveyor loading into the Railveyor cars for transport out of the mine.

Access and infrastructure development for the underground workings was designed to support the mining method and was sized based on ventilation, mining equipment specifications, and production rate requirements. Surface infrastructure and tailings were designed to match the underground production rate requirements.

12.2 Conversion, Assumptions, Parameters & Methods

Defined blocks of Measured Resources were converted to Proven Reserves and Indicated Mineral Resources were converted to Probable Mineral Reserves by applying the appropriate modifying factors, as described within this sub-section, tied to potential mining block shapes created during the mine design process.

The undiluted tons and grade of each potential mining block are based on the resource block model estimated by DGC as described in Section 11 of this report.

All Mineral Reserve tonnages are expressed as "dry" tons (i.e., no moisture) and are based on the density values stored in the block model.

12.2.1 Dilution

Mining dilution of approximately 6% by volume was applied to all stopes and development excavations, based on geotechnical analysis and recommendations. This figure is an average based on calculating 3% dilution by volume for the primary stopes, 9% dilution by volume for the secondary stopes, and 5% dilution by volume for ore development. The mining dilution percentage was added to the designed tonnage to account for unplanned sources of dilution, such as backfill and host rock around the periphery of the ore mass. Mining dilution of host rock from around the periphery of the ore mass has been applied with zero grade as a conservative assumption even though some sources of this type of dilution will likely carry grade. The primary stopes will have extraneous ore, host rock and unconsolidated backfill as potential material that will slough into them while being extracted. It should be noted that the ore portion of the sloughed material is not included in calculation of the 3% dilution factor, since this ore is accounted for in the adjacent stopes. The higher dilution factor for the secondary stopes is due to the fact these stopes have more sources of waste material with no grade and less ore from adjacent stopes; therefore, a higher dilution factor of 9% has been applied to them. The 5% dilution of development drifts is the result of the mining process, which can potentially be exposed to higher amounts of initial dilution material.

As stated in Section 13.2, the thickness of external dilution is estimated as equivalent linear overbreak/slough (ELOS), for moderately weathered carbonatite, and for fresh to slightly weathered carbonatite. Sidewall and back dilution are not expected to be a problem because the dilution in the primary stopes (i.e. from adjacent secondary stopes) will be at grade, and dilution from the secondary stopes is managed by controlling backfill strength.

As shown in Figure 12‑2, sources of mining dilution for primary stopes include:

•
Backfill material on the floor/sill with no grade.
•
Backfill material from the hangingwall end with no grade if the stope is adjacent to a previously mined stope.

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•
Low grade periphery rock dilution in the hangingwall or footwall if the stope is not adjacent to other stopes.

As shown in Figure 12‑2, sources of mining dilution for secondary stopes include:

•
Backfill material on the floor/sill with no grade.
•
Backfill material from the hangingwall end with no grade if the stope is adjacent to a previously mined stope.
•
Low grade periphery rock dilution in the hangingwall or footwall if the stope is not adjacent to other stopes.
•
For most situations, backfill material on both sidewalls with no grade.

img170397038_78.jpg

Source: Nordmin, 2019

Figure 12‑2: Sources of Mining Dilution for Typical Stope Layout (Not to scale).

 

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Table 12‑2: Potential sources of mining dilution by stope type (primary and secondary) for a typical stope geometry and standard mining practices in the ground conditions expected at Elk Creek.

Footwall

P2

P1

P0

S2

S1

S0

P2

P1

P0

S2

S1

S0

P2

P1

P0

S2

S1

S0

 

 

Primary Stopes

Secondary Stopes

P2

P1

P0

S2

S1

S0

Hanging Wall Dilution - Rock

 

 

Yes

 

 

Yes

Footwall Dilution - Rock

Yes

 

 

Yes

 

 

Hanging Wall Dilution - Backfill

Yes

Yes

 

Yes

Yes

 

Footwall Dilution - Backfill

 

 

 

 

 

 

Sidewalls - Rock (Ore)

 

 

 

 

 

 

Sidewalls - Backfill

 

 

 

Yes

Yes

Yes

Floor/Sill Dilution - Backfill

Yes

Yes

Yes

Yes

Yes

Yes

Source: Nordmin, 2019

12.2.2 Recovery

A stope recovery factor of 95% was calculated for mining all the primary and secondary stopes. The following parameters in combination were considered in calculating this factor:

•
Potential material loss into backfill (floor) of 0.4 m.
•
Potential material loss to side and end walls (under blast) of 0.2 m.
•
Potential material loss to mucking along edges and in blind corners (using limited visibility).
•
Additional potential loss factor due to rockfalls, sudden unanticipated regional stress load relief, and other geotechnical reasons.

A development recovery factor of 95% was also used for all horizontal drift development because it is subject to the same potential material loss as stated above.

A recovery factor of 62.5% was applied to sill pillar stopes was used to reflect the lower expected recovery of back-stopes excavated under previously mined stopes above.

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12.2.3 COG / NSR Calculation

Net Smelter Return (NSR) is a commonly accepted method of evaluating a mineral deposit where revenue is generated from multiple elements. NSR is defined as the proceeds from the sale of mineral products after deducting off-site processing and distribution costs. NSR is typically expressed on a dollar per tonne basis.

An NSR (Net Smelter Return) approach was used and focused on targeted amounts of Nb2O5 and considers planned mining of four (4) elements (Nb2O5, Sc, TiO2, rare earths) that results in generating eight (8) separate products (FeNb, Sc2O3, TiCl4, NdPr Oxide, Tb2O3, Dy2O3, SEG Carbonate, Heavies Carbonate). Stope optimization was completed to identify economic mining areas based on these saleable products. The 3D mine design was completed on an elevated cut-off grade (CoG), which achieved an average of over 2.5 times the actual calculated cut-off grade.

Recoveries used are based on metallurgical test work discussed in Section 10. The NSR was evaluated for each block in the 3D geologic resource block model as of the report date. Table 12‑3 shows NSR parameters and an example NSR calculation for an individual block.

Table 12‑3: Example of an NSR Block Calculation

Input Parameters

Total

Nb2O5

TiO2

Sc(1)

Example Block Model Mass

100 t

 

 

 

Example Block Model Grades

100 t

0.70%

2.50%

60 ppm

Metallurgical Recoveries (2)

86.72%

83.65%

92%

Amount Payable

100.0%

100%

100.0%

Conversions from input grade to product

69.6%

235.0%

153.4%

Refining Charges

0

0

0

Price

US$

52/kg

US$

1.86/kg

US$

2,000/kg

Calculate Contained Metal

Nb2O5 TiO2

Sc

100 t

 

700 kg

 

 

2,500 kg

 

 

 

 

6 kg

Calculate Saleable Metal (conversion to product, discounted by recovery)

100 t

 

 

 

 

 

 

 

 

8.45 kg

Nb

424.3 kg

 

FeNb

653 kg

 

TiO2

 

4,914.6 kg

Sc (as Sc2O3)

 

 

Calculate Block Dollar Value for Each Metal

FeNb TiO2

Sc

100 t


US$ 22,065

 

 

US$ 9,141

 

 

 

US$ 16,891

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Total Block Value

Block Value per tonne

US$ 48,097 US$ 480.97/t

 

 

 

Source: DGC 2026

1.
Stored as PPM in the block model. Sc % = Sc ppm/10,000.
2.
Overall metallurgical recovery, including all losses

 

Figure 12‑3 through Figure 12‑6 provide a grade-tonne curve for the deposit using various NSR cut- off grades, (CoG). It includes only Proven and Probable material and shows average grades for each grade variable. All Inferred material is treated as having a zero-grade value in this mineral reserve estimation.

img170397038_79.jpg

Source: Amplify Mine Planning, 2026

Figure 12‑3: NioCorp Grade (Nb2O5)-Tonne Curves Based on NSR Cut-Off

 

 

 

 

 

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img170397038_80.jpg

Source: Amplify Mine Planning, 2026

Figure 12‑4: NioCorp Grade/Tonne Curves Based on NSR Cut-Off (TiO2)

 

img170397038_81.jpg

Source: Amplify Mine Planning, 2026

Figure 12‑5: NioCorp Grade (Sc ppm) – Grade Tonne Curves Based on NSR Cut-Off

 

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img170397038_82.jpg

Source: Amplify Mine Planning, 2026

Figure 12‑6: NioCorp Grade (TREO %) – Grade Tonne Curves Based on NSR Cut-Off

To establish the initial boundary of the mine design and to assure inclusion of all potential Mineral Reserves, a minimum CoG of US$218/ton was used based on the estimated costs shown in Table 12‑4.

Table 12‑4: Operating Costs Used for Mine Design NSR Cut-off

Category

2024 BOD Model

Mining Cost

$50.86

$46.14

Processing

$137.83

$125.04

Water Management and Infrastructure

$18.28

$16.58

Tailings Management

$2.21

$2.00

Other Infrastructure

$6.02

$5.46

General and Administrative

$9.80

$8.89

Royalties / Annual Bond Premium

$9.17

$8.32

Other Costs

$6.92

$6.28

Total Cost

$241.09

$218.71

(US$/tonne mined)

(US$/ton mined)

Source: NioCorp, 2025

Notes:

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(1)
Includes backfill.
(2)
Values used here differ from the economic model generated from the final overall site design. NioCorp, Dumas, and Amplify are satisfied that the values used were applicable to establishing the correct and optimum mining design.

12.2.4 Mine Design

Potential mining areas were identified using stope optimization within Deswik.SO StopeOptimizer© software. The stope optimizer output was reviewed on a level-by-level basis, and a 3D mine design was generated. The estimated cut-off NSR value (CoNSR) of US$ 218/ton provided by NioCorp was used as a starting point for this analysis. Generally, stopes would be selected based on the minimum CoG or CoNSR. However, as the CoNSR value is much lower than the resulting average stope NSR value, the CoNSR was not the decisive factor in the stope optimization process. Rather than using only a minimum CoNSR, the mine design also targeted an average cut-off Nb2O5 grade of 0.65% and targeted higher annual ferroniobium production during the first five years of production. With a milling constraint of 3,047 tpd, the steady-state life of mine average annual ferroniobium production during full production years was 8,282 tons annually. This strategy results in a LOM NSR average value of US$ 590.84/ton. The identified mining blocks provide an approximate 43-year LOM. The design includes stopes, development accesses, and necessary infrastructure. Figure 12‑7 shows the current mine design.

img170397038_83.gif

Source: Amplify Mine Planning, 2026

Figure 12‑7: Current Mine Design

12.3 Reserves

The 2026 Mineral Reserves were classified in accordance with Regulation S-K 1300. More specifically, the 2026 Mineral Reserves were classified using the guidelines developed by the Committee for Mineral Reserves International Reporting Standards (CRIRSCO) released in 2013 and adopted for the United States by the Society for Mining, Metallurgy and Exploration (SME) in 2017. Measured and Indicated Mineral Resources were converted to Proven and Probable Mineral

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Reserves by applying the appropriate modifying factors, as described earlier in this section, to potential mining block shapes created during the mine design process.

The underground mine design process resulted in a mine plan with an in-situ Mineral Reserve Estimate of 45.9 Mt (diluted) with an average grade of 0.76% Nb2O5, 2.68% TiO2, 69.3 ppm Sc, and 0.34% TREO. This estimate is based on a mine design using elevated CoGs and applying the US$ 218/t NSR CoG to capture all potential Mineral Reserves within the design and an average cut-off grade of 0.650% Nb2O5. These numbers include a 95% mining ore recovery to the designed wireframes (sill pillar recovery is 62.5%) in addition to applying approximately 6% - 9% unplanned dilution as described in Section 12.2.1. Table 12‑5 summarizes the underground reserves as of June 30, 2026.

Table 12‑5: In-situ Underground Mineral Reserves Estimate for Elk Creek, Effective Date June 30, 2026

2026 Reserve

Mineral Reserve Classification

Cut-off NSR

Tonnage

Grade

Grade

Grade

Grade

(US$/ton)

(ton)

(Nb2O5%)

(TiO2%)

(Sc ppm)

(TREO %)

Proven

218

       7,570,098

0.760

2.70

71.5

0.32

Probable

218

    38,359,365

0.759

2.67

68.8

0.35

Total

218

    45,929,462

0.759

2.68

69.3

0.34

 

Classification

Tonnage (ton)

Nb2O5 Grade (%)

FeNb (ton)

Payable Nb (ton)

TiO2 Grade (%)

Payable TiCl4 (ton)

Sc Grade (ppm)

Payable Sc2O3 (ton)

TREO Grade (ppm)

Payable TREO (ton)

Proven

  7,570,098

  0.76

 53,651

  34,873

2.70

405,938

71.5

 762

3,232

22,509

Probable

38,359,365

  0.76

271,386

176,401

2.67

2,036,334

68.8

 3,717

3,489

123,115

Total

45,929,462

  0.76

325,038

211,274

2.68

2,442,272

69.3

 4,479

 3,446

145,625

Source: Amplify Mine Planning, 2026.

Notes:

(1)
All figures are rounded to reflect the accuracy of the estimates. Totals may not sum due to rounding.
(2)
The Qualified Person for the Mineral Reserve estimate is Amplify Mine Planning LLC. The estimate has an effective date of June 30, 2026.
(3)
The Mineral Reserve is based on the mine design and mine plan, utilizing an average cut-off grade of 0.650% Nb2O5 with an NSR of US$ 218/ton.
(4)
The estimate of Mineral Reserves may be materially affected by metal prices, environmental, permitting, legal, title, taxation, socio-political, marketing, infrastructure development, or other relevant issues.
(5)
Annual life of mine (LOM) average production rate of ~8,282 tons of FeNb/annum in the years of full production,
(6)
Mining dilution of ~6% was applied to all stopes and development, based on 3% for the primary stopes, 9% for the secondary stopes, and 5% for ore development.
(7)
Mining recoveries of 95% were applied in longhole stopes and 62.5% in sill pillar stopes.
(8)
Price assumptions for FeNb, Sc2O3, TiO2 and TREO metals are based upon independent market analyses for each product.
(9)
Price and cost assumptions are based on the pricing of products at the “mine- gate,” with no additional down-stream costs required. The assumed products are a ferroniobium product (metallic alloy shots consisting of 65%Nb and 35% Fe), titanium in the form of TiCl4, scandium trioxide in powder form and rare earth oxides in either purified oxide or carbonate form. The Mineral Reserve has an average LOM NSR of US$590.84/ton.
(10)
The economic assumptions used to define Mineral Reserve cut-off grade are as follows:

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Parameter

Value

Unit

Mining Cost

46.14

US$/ton mined

Processing

125.04

US$/ton mined

Water Management and Infrastructure

16.58

US$/ton mined

Tailings Management

2.00

US$/ton mined

Other Infrastructure

5.46

US$/ton mined

General and Administrative

8.89

US$/ton mined

Royalties/Annual Bond Premium

8.32

US$/ton mined

Other Costs

6.28

US$/ton mined

Total Cost

218.71

US$/ton mined

Nb2O5 to Niobium conversion

69.9

%

Niobium Process Recovery

86.72

%

Niobium Price

23.59

US$/lb

TiCl4 Process Recovery

83.65

%

TiCl4 Price

0.84

US$/lb

Sc Process Recovery

92

%

Sc to Sc2O3 conversion

153.4

%

Sc Price

891.76

US$/lb

Dy2O3 Process Recovery

92

%

Dy2O3 Price

185.97

US$/lb

Nd2O3 Process Recovery

92

%

Nd2O3 Price

56.70

US$/lb

Pr2O3 Process Recovery

92

%

Pr2O3Price

56.70

US$/lb

Tb2O3 Process Recovery

92

%

Tb2O3 Price

836.88

US$/lb

 

12.4 Relevant Factors

It is Amplify Mine Planning LLC’s opinion that there are no known environmental, permitting, legal, socio-economic, marketing, political, or other factors which could materially affect the underground Mineral Reserve Estimate. In addition, realistic and justifiable mining factors were used in determining the mine plan and schedule for reporting mineral reserves. These factors include geotechnical considerations, ore loss, dilution, mine extraction rates and metallurgical recovery.

The pricing for Niobium, Scandium, Titanium and Rare Earths used to support the Mineral Reserve estimate was based on third party market reports described in Section 16.1. It is Amplify Mine Planning LLC’s opinion that the pricing used is adequate and appropriate for use in estimating Mineral Reserves. Further details on the market assumptions and timeframes analyzed are disclosed in Chapter 16 of this report.

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13 Mining Methods

13.1 Geology Overview

The mine planning work is based on the resource geology and block model, described in Section 11 of this Technical Report Summary. In addition to the mineralization, various other elements were estimated into the model for metallurgical purpose.

13.2 Rock Engineering

This section presents the rock mass characterization work (Section 13.2.1) and the associated rock engineering aspects of the project (Section 13.2.2).

13.2.1 Geomechanical Appraisal

This section is summarized from the rock mass characterization report completed in support of the mine design (A2GC, 2026a).

13.2.1.1 Available Geomechanical Data

The rock mass characterization is based on the following data sources:

•
Geomechanical core logging, which includes the description of the core intervals (RQD, strength, etc.) and the condition of every open joint. From this dataset, the rock mass can be classified according to the Q-system (Barton et al., 1974; NGI, 2022).
•
Televiewer surveys from which the orientation of the structures in the drill core is obtained from measured alpha and beta angles.
•
Laboratory intact rock strength testing from which intact rock strength parameters are derived.

A supplemental geomechanical drilling and strength testing program was conducted in 2025 to improve the geomechanical domains grouping. The available geomechanical data from drill holes are summarized in Table 13‑1.

Table 13‑1: Summary of available geomechanical data from drill holes for the Elk Creek Project

Type of data

2011

Investigation

2014

Investigation

2015

Investigation

2025 Investigation

Drillholes with RQD data only

5,005 ft (1,525 m)

(3 holes)

4,920 ft (1,500 m)

(3 holes)

3,555 ft (1,083 m)

(2 holes)

23,550 ft (7,178 m)

(11 holes)

Complete geomechanical core logging (with joints description)

-

36510 ft (11,128 m)

(16 holes)

2505 ft (763 m)

(2 holes)

13,115 ft (3,998 m)

(6 holes)

Televiewer surveys

-

19,869 picks

13,454 open joints

(13 holes)

2,236 picks

1,237 open joints

(2 holes)

3,704 picks

554 open joints

(9 holes)

Laboratory testing

-

 31 UCS tests

40 UCSE tests

17 TCS tests

12 BTS tests

 

0 UCS tests

18 UCSE tests

54 TCS tests

35 BTS tests

Source: A2GC, 2026

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Notes:

(1)
UCS = Unconfined compressive strength.
(2)
UCSE = Unconfined compressive strength with measurements of elastic properties.
(3)
TCS = Confined triaxial compressive strength.
(4)
BTS = Indirect splitting tensile strength (Brazilian test).

13.2.1.2 Data Gaps

The amount, coverage and quality of data are sufficient for this level of study.

•
The orebody has good coverage from the geomechanical drillholes, including at depth.
•
The domaining approach is acceptable.
•
The joint sets interpretation is suitable for this stage of the project development, with Televiewer surveys having been conducted in several orientations to reduce the bias due to blind zones.
•
The fitting of the intact rock strength envelopes is satisfactory for most geomechanical domains.
•
Local stress measurements have been conducted.

However, the following data gaps are identified:

•
There are no underground mapping data, as would be expected for a project that has not been developed.
•
The presence, location and extent of degraded rock mass quality areas are not well known, although modeling efforts were made to improve the current understanding.
•
Results from local stress measurements show some variability in both magnitude and orientation.
•
Some geomechanical domains have insufficient strength testing data. The datasets for elastic properties are relatively small (five data points or less).

To address the above data gaps, the following supplemental data collection is recommended:

•
As underground development starts, underground mapping should be conducted as soon as possible to confirm rock mass conditions and joint sets orientation.
•
The presence, location and rock mass conditions of the degraded rock mass quality areas should be investigated. As such, it will be important to validate the location and thickness of the interpreted property-scale structures. A better definition and 3D understanding of the zones with lower quality (weathered areas) is needed for detailed and reliable planning of the stoping area.
•
As underground development progresses, field observations should be conducted to validate the measured stress field. This is done by observing the location of shear failure around the perimeter of isolated horizontal and vertical development and deducing the stress field orientation with respect to their orientation. If discrepancies are observed, supplemental in situ stress measurements should be conducted at several depths to constrain the pre-mining stress regime.

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•
Additional strength testing data should be conducted in the weathered lamprophyre, weathered carbonatite and weathered mineralized domains. Supplemental elastic properties testing in all domains would increase the confidence in the dataset.

13.2.1.3 In-Situ Stress Conditions

Stress measurements were conducted by Agapito Associates Inc. (Agapito) at Elk Creek in Fall 2014. Measurements were done using the Sigra over-coring stress test tool. This technique enables a calculation of the magnitudes and orientation of the principal stresses in the plane perpendicular to the borehole axis. Testing was conducted between 425 ft (130 m) and 2,180 ft (665 m) below surface. A total of thirteen (13) tests were attempted, yielding eight successful tests.

Table 13‑2 summarizes the in-situ stress tensor considered for the Project, based on the stress testing results.

Table 13‑2: In-situ stress conditions considered for the Elk Creek Project

Principal stress component

Orientation (dip/azimuth)

Magnitude (MPa)

Major principal stress

σ1

00° / 072°

 

0.036 z

Where z is the depth in meters

Intermediate principal stress

σ2 = σv

90° / 000°

0.029 z

Minor principal stress

σ3

00° / 162°

 

0.021 z

Source: A2GC, 2026

13.2.1.4 Rock Mass Geomechanical Domains

For the purpose of geomechanical analyses and designs, the rock mass volume is typically divided into geomechanical domains with similar geological, structural and rock parameter characteristics. The domaining approach was refined based on the updated geological model, on the logged rock weathering index and on the geomechanical data collected in the 2025 investigation campaign.

The Elk Creek deposit is contained within carbonate rocks whose boundary lies well beyond the property. The carbonates are generally strong, hard and brittle rock masses, sparsely jointed to blocky. They are very heterogenous in nature exhibiting numerous macro and micro defects and frequent lithological changes. The initial domaining approach grouped all lithologies within the hanging wall, footwall and mineralized rocks into three (3) geomechanical domains.

Some areas within the carbonate rocks with significantly lower rock mass quality have been identified (higher degree of fracturing, higher degree of rock alteration); these areas are referred to as weathered areas (their logged weathering index in the drillhole database is usually high). A concentration of weathered rock was identified to the west of the orebody and hanging wall, but there are also other areas to the east. A conceptual weathering model was built and used to guide the geomechanical domaining approach.

The carbonate rocks are overlain by Pennsylvanian sedimentary rocks. Those exhibit various intensities of foliation, this foliation being generally sub-horizontal. The contact between the Pennsylvanian sediments and the carbonate rocks is generally weathered over several meters.

Seven (7) geomechanical domains are considered for the Elk Creek project:

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(1)
Pennsylvanian sediments: limestone, mudstone and, to a lesser extent, sandstone found in the first 820 ft (250 m) (shallowest)
(2)
Carbonatite: rock forming the main orebody with a dominant carbonatite composition
(3)
Weathered carbonatite: pockets of carbonatite exhibiting significantly degraded rock mass quality
(4)
Lamprophyre: rock forming the main orebody with a dominant lamprophyre composition
(5)
Weathered lamprophyre: pockets of lamprophyre exhibiting significantly degraded rock mass quality
(6)
Mineralized domain: carbonatite identified as being mineralized
(7)
Weathered mineralized domain: pockets of mineralized carbonatite exhibiting significantly degraded rock mass quality

13.2.1.5 Intact Rock Properties

Intact rock strength was evaluated with laboratory strength tests on selected samples. Unconfined compressive strength tests with and without measurements of elasticity parameters (UCSE and UCS, respectively), Brazilian tensile strength tests (BTS) and triaxial compressive strength tests (BTS) were conducted. The number of valid intact rock strength laboratory tests per geomechanical domain used to establish intact rock strength envelopes is given in Table 13‑3.

Table 13‑3: Number of valid intact rock strength laboratory tests per geomechanical domain used to establish intact rock strength envelopes.

Lithology Unit

UCSE

UCS

Triaxial

Brazilian

Total

Sediments

20

6

14

13

53

Carbonatite

5

3

14

11

33

Weathered carbonatite

7

3

7

—

17

Mineralized

8

13

20

12

53

Weathered mineralized

5

2

2

3

12

Lamprophyre

10

2

12

7

31

Weathered lamprophyre

1

—

1

—

2

Total

56

29

70

46

201

Source: A2GC 2026

Hoek-Brown intact rock strength envelopes (Hoek, 1994) were obtained for each geomechanical domain by Bayesian fit through the selected datapoints. The intact rock mechanical properties per geomechanical domain are shown in Table 13‑4. Tests that have failed along a pre-existing discontinuity were excluded from the analysis.

Table 13‑4: Summary of intact rock mechanical properties per geomechanical domain.

Geomechanical domain

UCS (1)

BTS (2)

E (3)

𝜈 (4)

Density

𝜎ci (5)

mi (5)

Sediments

10,890 psi

(73 MPa)

770 psi

(5.3 MPa)

3.63 Mpsi

(25 GPa)

0.29

156.1 lb/ft3

(2,500 kg/m3)

10,010 psi

(69 MPa)

16.5

Carbonatite

17,985 psi

(124 MPa)

1,405 psi

(9.7 MPa)

11.02 Mpsi

(76 GPa)

0.30

181.7 lb/ft3

(2,910 kg/m3)

21,900 psi

(151 MPa)

21.1

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Geomechanical domain

UCS (1)

BTS (2)

E (3)

𝜈 (4)

Density

𝜎ci (5)

mi (5)

Weathered carbonatite

6,235 psi

(43 MPa)

-

7.54 Mpsi

(52 GPa)

0.25

176.7 lb/ft3

(2,830 kg/m3)

15,665 psi

(108 MPa)

19.7

Mineralized

23,785 psi

(164 MPa)

1,350 psi

(9.3 MPa)

10.88 Mpsi

(75 GPa)*

0.28*

189.8 lb/ft3 (3,040 kg/m3)

23,060 psi

(159 MPa)

19.9

Weathered mineralized

20,885 psi

(144 MPa)

710 psi

(4.9 MPa)

10.44 Mpsi

(72 GPa)

0.28

181.7 lb/ft3 (2,910 kg/m3)

15,665 psi

(108 MPa)

26.3

Lamprophyre

21,755 psi

(150 MPa)

1,365 psi

(9.4 MPa)

9.28 Mpsi

(64 GPa)

0.29

180.4 lb/ft3 (2,890 kg/m3)

16,680 psi

(115 MPa)

15.1

Weathered lamprophyre

28,570 psi

(197 MPa)*

-

7.69 Mpsi

(53 GPa)*

0.29*

172.3 lb/ft3 (2,760 kg/m3)

11,315 psi

(78 MPa)

14.0

Notes:

(1) unconfined compressive strength

(2) indirect splitting tensile strength (Brazilian Tensile Strength tests)

(3) Young’s modulus

(4) Poisson’s ratio

(5) sci, mi: Hoek-Brown parameters

* only one sample available

13.2.1.6 Property-Scale Structures

Property-scale structures were interpreted by SRK in 2016 based on drillcore data (RQD and lithological information) and the Televiewer orientation dataset. A total of 31 structures have been identified. Based on the evidence of structures being crossed in the drillcore, this model seems to be generally concordant (although some depth mismatches were observed). Conversely, many features crossed in the drillcore are not captured at the scale of this structural model.

As underground development progresses, the presence, location and extent of the property-scale structures should be confirmed.

13.2.1.7 Rock Mass Jointing

For joint sets interpretation, the carbonatite, mineralized, and lamprophyre (weathered and unweathered) geomechanical domains were grouped. The resulting sub-dataset is referred to as the carbonatite structural domain. The Pennsylvanian sediments constitute the second and distinct structural domain. The orientation of the mean joint sets is provided in Table 13‑5, per structural domain. The stereonets are shown in Figure 13‑1. The stereonets are shown in Figure 13‑1.

The Televiewer dataset shows high variability, reflecting the heterogeneous nature of the rock mass. In the carbonatite, joint set 1 is major and apparently more related to fracturing. Joint set 2, more related to foliation and contacts, also seems to be major but is more randomly distributed. Joint sets 3 and 4 are minor and could be seen more as areas on the stereonet where there are many random joints.

In the sediments, the dominant structural trend is sub-horizontal and related to their foliated nature. Some sub-vertical joints have also been logged. Their orientation trend is reported, although minor compared to that of the sub-horizontal set that remains the main driver.

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Table 13‑5: Summary of mean joint set orientations per structural domain

Structural Domain

Set

Area definition on stereonet

Average within the area

Carbonatite

1

Cone

Dip: 70°

Dip direction: 155°

Cone angle: 33°

Dip: 69°

Dip direction: 155°

2

Cone

Dip: 28°

Dip direction: 063°

Cone angle: 40°

Dip: 29°

Dip direction: 065°

3

Window

Dip: 55 to 95°

Dip direction: 190° to 260°

Dip: 75°

Dip direction: 220°

4

Window

Dip: 50 to 80°

Dip direction: 320° to 030°

Dip: 64°

Dip direction: 357°

Sediments

H

Cone

Dip: 00°

Dip direction: 155°

Cone angle: 30°

Dip: 01°

Dip direction:268°

1

Window

Dip: 72 to 102°

Dip direction: 125° to 175°

Dip: 87°

Dip direction: 148°

Notes:

(1)
Dip is measured downwards from horizontal and varies between 00° (horizontal) and 90º (vertical). Values greater than 90° indicate that the window continues on the other side of the stereonet.
(2)
Dip direction varies clockwise from north (North is 000°, East is 090°, South is 180° and West is 270º).

 

 

Carbonatite

Sediments

img170397038_84.jpg

img170397038_85.jpg

Source: A2GC 2026

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Figure 13‑1: Lower hemisphere equal angle plots showing the structural data and joint sets interpretation per structural domain

13.2.1.8 Rock Mass Classification

Geomechanical core logging data were processed according to the Q-system (Barton et al., 1974; Grimstad & Barton, 2014; NGI, 2022). Rock mass quality has been assessed by geomechanical domain. The Pennsylvanian sediments, carbonatite, lamprophyre and mineralized domains are classified as ‘Good’ quality rock masses quality rock masses in the Q-system (30th percentiles and median values between 10 and 40). The weathered rock masses are classified as Fair in the Q-system (30th percentiles and median values between 4 and 10).

The rock mass classification results are provided in Table 13‑6 in terms of 10th, 30th and 50th percentile of the distribution of the ratings weighted per drill hole interval length. These percentiles, which can be considered on the conservative side, are commonly used for projects at this level of study.

It should be pointed out that the RQD values of the entire dataset are variable, with very high and very low values (8% of the drilling intervals logged in geomechanical drillholes have a RQD value lower than 25%). This is in accordance with the general rock mass aspect.

Table 13‑6: Summary of rock mass classification per geomechanical domain

Geomechanical domain

Q’-system*

10th percentile

30th percentile

50th percentile

Sediments

12

33

50

Carbonatite

3.5

12.8

25

Weathered carbonatite

2.0

4.6

7.3

Mineralized

4.3

9.8

18

Weathered mineralized

2.1

6.7

12.4

Lamprophyre

8.2

24

47

Weathered lamprophyre

1.6

4.8

7.4

Source: A2GC 2026

Notes:

(1)
*Assuming dry conditions and excluding the influence of active stresses (excluding the Jw and SRF factors).

13.2.1.9 Anticipated Rock Mass Behaviour

The anticipated rock mass behaviour can be differentiated into the following main categories:

•
From surface to approximately 2135 ft (650 m) in depth (approximately 58% of the project tonnage, between levels L250 and L650):
o
Due to the low stress conditions, the rock mass behaviour around the openings is expected to be largely structurally controlled and influenced mainly by the occurrence, spacing, persistence and characteristics of the natural discontinuities, as well as their intersections.
o
The ground instabilities in stopes and around development is anticipated to be controlled by the relaxation of the jointed rock mass, which could result in gravity-driven wedge instabilities.

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o
Due to relaxation, the dilution off the stope walls can be expected to be particularly sensitive to the length of time the stopes will remain open and the rock mass damage originating from drilling and blasting practices.
o
Minimum to no rock mass damage due to the induced stresses is expected to occur around typical stopes in this depth range, except in sectors of lower rock mass quality, for example in shallow stopes close to the Pennsylvanian contact.
•
From 2135 ft (650 m) to 3280 ft (1,000 m) in depth (approximately 42% of the project tonnage, between levels L650 and L930):
o
This depth range will constitute a transition between mainly relaxation-induced instabilities to stress damage-driven instabilities. The former are structurally controlled whereas the latter are controlled by the strength of the rock and healed discontinuities (such as veins).
•
With increasing depth, development could sustain some stress-induced damage near the mining fronts where stresses concentrate ahead of mining. The high stress front can be expected to concentrate close to the excavations (i.e., typically one stope strike length ahead and within the same retreating panel). Its intensity will increase with depth.
•
Higher stress mining fronts are expected only in lead primary stopes and the first panels in the secondary stopes. The second, third and beyond panels are anticipated to be in the stress shadow (i.e., in deconfined ground), even at depth.
•
Sill pillar levels (approximately 14% of the project tonnage)
o
Sill pillar levels are created where mining fronts will merge (vertically). The following levels are concerned: L490 and L690. The bottom-up sequence will push ground stresses upwards and concentrate them in sill pillars. Stress concentration increases should start to be tangible in the L690 sill pillar. Stress concentration on sill levels is anticipated to lead to spalling and local instabilities, as well as slippage and deformation along geological discontinuities. No rock bursting conditions are expected largely because all stopes are shallower than 3,280 ft (1,000 m). Some operational challenges are likely to be encountered during the mining of sill pillar stopes at depth, particularly in the lead stopes.
•
Poor rock-mass quality areas (evaluated at 15% of the project tonnage):
o
The rock mass in the vicinity of the interpreted property-scale faults is expected to be of lower quality. Areas of weathered rock mass have also been identified. Stopes located in and close to these areas can be expected to produce higher levels of dilution and require additional ground support.
o
Areas of poor rock mass quality could provide conduits for water infiltration into mine workings. FLAC3D numerical simulations did not consider hydrogeological effects.
•
The main joint set orientations are expected to be highly variable throughout the deposit. The geometry of gravity-driven wedge instabilities is thus anticipated to vary throughout the mine. At the scale of a drift, the large variability and complexity of the rock mass jointing is anticipated to result in variable conditions in terms of wedge instabilities.

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Development crossing property-scale structures will encounter lower rock mass quality and unraveling conditions. Other small-scale faults and geological features can also be expected to influence the rock mass behaviour locally.

Note that the mining sequence is planned to be progressing from the center of a horizon towards the abutments (i.e., there are no converging mining fronts within a horizon) to manage mining-induced stresses.

13.2.2 Geomechanical Guidelines for Mine Design

The geomechanical recommendations and guidelines presented below are based on geomechanical assessments that included empirical methods (stope dimensions, dilution estimates, backfill strength requirements) and mine-wide numerical simulations of the mining sequence with the advanced explicit three-dimensional finite-difference code for continuum mechanics engineering applications FLAC3DTM (Itasca, 2019).

This section is summarized from the rock engineering study completed in support of the mine design (A2GC, 2026b). The rock engineering study was completed based on the life of mine stope layout and mining sequence dated March 13, 2026.

13.2.2.1 Stope Dimensions and Dilution Estimates

The planned mining method is transverse longhole open stoping. The stopes are planned to be backfilled with cemented paste backfill. Stope dimensions were first established for the individual stopes to be stable according to the empirical Stability Graph method (Mathews et al., 1980; Nickson, 1992; Potvin, 1988), amongst others) and to have an external dilution of less than 3 ft (1.0 m) according to the equivalent linear overbreak/slough (“ELOS”) empirical method (Clark, 1998). These dimensions were later tested with the numerical modelling analyses.

The stope dimensions considered for the economic evaluation of the deposit are:

•
Vertical height between levels (floor-to-floor): 130 ft (40 mH)
•
Panel width (transversally, east-west): 50 ft (15 mW).
•
Maximum stope strike length (longitudinally, north-south): 50 ft (15 mL).

Following the numerical analyses – where local stress magnitudes, lithology effects and the interaction between stopes were examined more explicitly – the empirical ELOS estimates (i.e., less than 3 ft (1 m)) were maintained. The two main numerical assessment criteria to estimate dilution were the plastic state of the rock mass and its confinement level (minimum principal stress magnitude). Little rock mass failure is predicted from the numerical analyses, confirming the limited potential for dilution. However, in the weathered areas, estimated to represent about 15% of the production stopes, higher dilution is anticipated (up to 3 ft (1.0 m) or even 7 ft (2.0 m) in some cases).

In the end, an average ELOS of 6% in primary stopes and 9% in secondary stopes was considered in the economic evaluation of the deposit. For 50 ft-long (15 m-long) and wide stopes, this corresponds to 3.0 ft (0.90 m) and 4.4 ft (1.35 m), respectively, and is a conservative estimate.

These analyses are dependent on the pre-mining stress regime (orientation and magnitude). As stress data and observations become available and as mining experience is gained, the pre-mining stress regime should be confirmed. If the maximum principal stress magnitude is higher than anticipated, the potential for dilution could be higher. Conversely, if the maximum principal stress

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orientation shows evidence of being more parallel to the orebody strike rather than perpendicular to it (as assumed), the potential for dilution could be lower.

Stope dimensions being an important control to reduce the potential for dilution, efficient mitigation measures should also be implemented and maintained during production, including the following:

•
Good blasting techniques, in terms of design and QA/QC. In particular, blasthole accuracy will be critical as any loaded blasthole deviating into a stope wall will immediately cause significant dilution;
•
Quick mucking following blasting; and,
•
Prompt backfilling, to further minimize the amount of time stopes will remain open.

13.2.2.2 Dimension of Pillars

Sill Pillar Mining

Two sill pillars will be created in the mining sequence (on levels L490 and L690). These sill pillars are planned to be extracted during the mining sequence. The thickness of the sill pillars is planned to be 131 ft (40 m) (similar to the rest of the stopes).

The anticipated stress conditions in the sill pillars were assessed based on numerical modelling results. The main assessment criterion was the pre-mining stress magnitude: the more stresses accumulate in a sill pillar prior to mining, the more operational challenges can be expected during its recovery.

None of the sill pillars are forecasted to yield (fail) prior to mining. Operational challenges due to mining in highly stressed ground are expected for the lead stopes of the first panel to be mined in the sill pillars at L690.

To reflect the operational rock mechanics-related challenges anticipated during mining of the sill pillars, a 62.5% estimated recovery was applied to all sill pillars. Increasing stoping cycle time (by 60-75% of the normal mining rate) and/or adding rehabilitation costs and delays could also be considered for the deeper sill pillar.

Waste Rib Pillars

Rib pillars are not planned to be left in place as part of the selected mining method. However, waste rib pillars could be left in place when the mineralization is not continuous. Some instances of waste rib pillars were present in the proposed stope layout. Such pillars should maintain at least a 1:1 aspect ratio, i.e., maintain the rib pillar strike length equal to, or longer than, the diluted horizontal width of the widest abutting stope. At depth, it would be preferable to systematically mine small rib pillars (with an aspect ratio less than 1:1) to avoid stress concentration and seismicity related issues. Waste rib pillars at depth with an aspect ratio up to 2:1 may benefit from their own specific stability analyses.

Crown Pillar

The orebody being contained within the carbonate rocks beneath the 820-ft (250-m) thick Pennsylvanian sediments, there is no crown pillar as such in the Elk Creek Project.

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13.2.2.3 Backfill Strength Requirement

The production stopes will be backfilled with cemented paste backfill. Minimum backfill strength requirements were estimated for longitudinal mining using various common backfill limit equilibrium stability methods, namely the Mitchell (1982), and Li & Aubertin (2012 and 2014) approaches. In all cases the exposed backfill height was 130 ft (40 m), the backfill had a density of 137.3 lb/ft3 (2200 kg/m3) and a friction angle of 30° was considered, along with a factor of safety of 1.5. Based on the range of results provided by these methods, the A2GC recommendation is to maintain a minimum backfill UCS of 60 psi (400 kPa). In addition to ensuring self-standing exposed paste walls, this strength value would also prevent liquefaction triggered by nearby blasting.

Note that stopes sitting immediately above sill pillar stopes will require higher backfill strength as they will be undercut during sill mining. For these stopes the minimum UCS required is in the 75 to 145 psi (0.5 to 1.0 MPa) range, depending on geometry and to be confirmed by site-specific analyses. The higher strength will also be beneficial to reduce backfill dilution from blasting.

13.2.2.4 Seismic Conditions

Considering that:

•
Most of the mining will occur at a depth of less than 1475 ft (450 m) for the first years;
•
The mining sequence does not create converging pillars (except for the sill pillars);
•
The footprint of the orebody is not overly large (strike length less than 2295 ft (700 m) and at most 330 ft (100 m) wide); and,
•
The rock mass is generally not overly stiff, strong and brittle.

Problematic seismicity is not anticipated early in the mine life. Therefore, there is no stringent need to install a seismic system at the very start of the project. However, it will be important to closely monitor any signs of seismicity reported by the operations as the mine deepens. Typically, and as the numerical modelling analyses also suggest, seismic conditions could develop starting at a depth of around 2135 ft (650 m) in sill pillar stopes and will further increase with depth, and particularly in the lead stopes. If such signs start to appear, then a sufficiently sensitive and accurate seismic monitoring system should be promptly installed, and related triggered action response plans (TARPs) developed and implemented.

The costing of the installation of a microseismic monitoring system that would be installed at some point in the life of mine (sometime during the first few years so that reliable background seismic levels can be established), should be considered in future financial forecasts, especially if there is a potential to extend the mine deeper than the maximum depth considered in the current study.

13.2.2.5 Infrastructure Proximity Relative to Ore Body

Fixed infrastructure proposed locations were assessed based on numerical stress modelling results. The infrastructures and development were not explicitly included in the simulations at this stage and therefore the modelling results do not take into account the stress redistributions due to the presence of all future underground openings. The main assessment criteria were the variation of stress due to mining, the loss of confinement and the stress increase (relative to the strength of the intact rock) at the proposed underground infrastructure locations, but at this stage without physically including these excavations in the model.

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The assessed infrastructures include:

•
Ramps
•
Levels accesses and main level drives (longitudinally following the orebody)
•
Ventilation raises (two segments in the first mining horizon only)
•
Ore passes (one for each mining horizon)
•
Underground shops (located on levels L450 and L650)

Based on the numerical modelling results and a general review of the currently planned infrastructure locations, the following were concluded.

•
The ramps are located within the area affected by mining (from a stress change perspective) but are not expected to be subjected to stress-induced damage (no excessive stress variation is anticipated).
•
The level accesses, linking the ramps to the level main drives, hence transitioning from a low mining-induced stress change area to closer to the mining area, will experience stress changes as they get nearer the orebody. Based on the modelling results, the level accesses in the analysed layout are not expected to experience excessive stress changes.
•
Main level drives are expected to be subjected to some stress-induced damage, particularly at depths below 1870 ft (570 m) (L570 and deeper). This has been taken into account in the ground support requirements (rehabilitation anticipated at least once or twice during the life-of-mine).
•
The ventilation raises, the ore passes and the underground shops are located within areas affected by mining but are not expected to be subjected to stress-induced damage.

13.2.2.6 Ground Support

Ground support requirements were derived with both empirical guidelines and limit equilibrium gravity driven wedge analyses. They were derived for costing purposes, based on current data and their interpretation, the assessments performed and A2GC’s experience.

Ground support consists of various combinations of rebar bolts, friction sets, cable bolts, mesh screen and shotcrete. Support was selected based on several parameters including excavation size, location and planned service time, local geology, mining-induced stress changes, as well as other factors that could affect its performance.

A high-level summary of the ground support recommendations is given hereafter. Please refer to A2GC, 2026b for accompanying notes and details (e.g., length of ground support elements, spacing and pattern).

•
Ramp and other permanent infrastructures such as level accesses: rebar bolts in the back and in the walls, with mesh screen
•
In adverse conditions, a layer of shotcrete is to be added, and Swellex may replace the rebar bolts for easier installation. This is considered for 30% to 50% and 15% to 40% of the Sediment and Carbonatite rock units, respectively.

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•
For best practice, development faces should be supported with friction bolts and mesh screen.
•
Ore drives: Swellex bolts in the back and SplitSets in the walls, with mesh screen.
•
Intersections: secondary support added in the back (resin-grouted threaded bar bolts, or tensioned-plated single-strand plain cablebolts).
•
Permanent stationary infrastructures (refuges, parking areas, garages, shops): rebar bolts in the back and in the walls, with mesh screen, and secondary support in the back (resin-grouted threaded bar bolts, or tensioned-plated single-strand plain cablebolts) with shotcrete.
•
Vertical raises: rebar bolts in the walls, with mesh screen and possibly a shotcrete layer, depending on conditions. Note that ore passes and inter-level ventilation raises with no man entry can be left unsupported if in good ground.
•
Stopes: tensioned-plated single-strand plain cablebolts in the back
•
For cost estimation purposes, this recommendation should be applied to about 20% of primary stopes and up to 60% of secondary stopes in unweathered rock.
•
Stopes in adverse conditions (about 15% of the stopes) can be expected to require additional cablebolting.
•
Cablebolts should also be installed in the face for the first stope in sequence.
•
All stopes will be paste backfilled.
•
Surface boxcut excavation (under construction at the time of writing): rebar bolts in the face and in the walls, with mesh screen and shotcrete.
•
Mine portal (under construction at the time of writing): rebar bolts with mesh straps and shotcrete in the back and walls in the first 32.8 feet (10 meters) of the ramp. Mesh straps across the brow.

The ground support needs should be reassessed once the rock mass conditions and behaviour are confirmed once underground access becomes available. Changes in ground conditions will need to be monitored and ground support modified accordingly.

13.3 Hydrogeology Design Parameters

The hydrogeology of the deposit was characterized based on four phases of work:

Phase I:

The first phase of hydrogeological characterization was conducted during Phases 1 and 2 of the core drilling program and consisted of packer testing, installation of piezometers, and measurement of water levels (SRK, 2017). Specifically, the program included:

•
42 downhole packer-isolated injection and airlift tests in drill holes.

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•
Installation of six 2“ PVC standpipe piezometers isolated in the carbonatite and open to large intervals of the deposit.
•
Installation of two nominal 2“ PVC standpipe piezometers isolated in the 600 ft thick Pennsylvanian aquitard above the carbonatite.
•
Frequent measurement of water levels in open drill holes and piezometers over a period of six months.

Phase 2:

Following the second phase of resource-related core drilling, a 10-day airlift pumping test was completed using a deep, open, vertical PQ drill hole as a pumping well (SRK, 2017). Water levels from the surrounding piezometers were recorded over the duration of the test and for several weeks following the test.

Phase 3:

The third phase of hydrogeological characterization involved installation of two multi-level piezometers and a deep 6” diameter injection well completed to depths of 2,800 feet, followed by the performance of a nominal 30-day injection test (SRK, 2017). The piezometers were completed within the carbonatite at distances between 0.4 to 0.8 miles from the center of the injection well, which was located at the center of the orebody. The injection test was chosen as a test method over a standard pumping test due to the salinity of the groundwater and the expense of handling the discharge water. During the injection test, surface water from Todd Creek was injected at rates of between 350 to 480 gpm over a period of 33 days, including downtime. Response to the injection test was monitored over the duration of the test and for more than eight weeks following the test.

Phase 4:

The fourth phase of geohydrological characterization was conducted in 2025 during Phase 3 of the core drilling program, and involved the characterization of the hydraulics, porosity and groutability of the carbonatite (ABC, 2026). The program involved the detailed logging of water take and voids in the 15 coreholes drilled in 2025, detailed flow testing of three of the boreholes for permeability and hydraulic characterization of voids, and direct demonstration of groutability of the carbonatite in three boreholes using a variety of grout mixes.

Groundwater hydrogeological characterization data collected in the four phases described above was completed by SRK, NioCorp, ABC, DGC, and the contract drilling companies present at the project site in 2014, 2015, and 2025. The data collection was conducted by Professional Hydrogeologists, Geologists, and Engineers in accordance with established procedures modified to be effective in the conditions presented at the Elk Creek mine site (ABC, 2026; SRK, 2017).

13.3.1 Conceptual Hydrogeology

The Elk Creek Deposit is hosted in the Elk Creek Carbonatite, a volcanic carbonatite plug located in south-east Nebraska. The carbonatite plug is 3 to 4 miles in diameter and contains the orebody at its approximate center (Figure 13‑2).

The carbonatite plug was vertically injected upward through and is surrounded by Precambrian age silicious rocks, which are of low permeability. This prevents significant lateral movement of water to or from the carbonatite, and together with the overlying marine sediments encloses the sodium

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chloride brine in the carbonatite. The brine appears to be a remnant of connate sea water captured in the carbonatite plug during the Late Cretaceous period 66 to 94 million years ago, when the site was covered by an inland sea (Naugle, 2018).

The geology local to the orebody generally consists of a 50 to 100 ft thick layer of variable permeability Pleistocene-aged glacial till overlying 600-ft thick low-permeability Pennsylvanian-aged marine sediments, which rest on top of a moderate overall permeability Cambrian carbonatite volcanic plug extending to great depth (Figure 13‑3).

 

 

img170397038_86.jpg

img170397038_87.jpg

Source: ABC 2026

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Figure 13‑2: Regional Hydrogeology

 

 

img170397038_88.jpg

Source: ABC 2026

Figure 13‑3: Hydrogeology of the Elk Creek Mine – view looking northeast

 

 

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Glacial Till

Pleistocene-aged glacial till covers the surface of the site, to a depth of between 40 to 100 feet. It is variably permeable, with lenticular glacial outwash features providing potable water to shallow wells that service local agriculture and homes. Water levels in these wells are typically within 30 ft of the ground surface.

Pennsylvanian Sediments

The Pennsylvanian sediments are made up of marine limestone, shale, and mudstone. The hydraulic conductivity of the Elk Creek Pennsylvanian Sediments has been evaluated by packer tests, active flowmeter tests, and laboratory tests on intact core. The results are compiled on Figure 13‑4 and the average is:

Hydraulic conductivity of the Elk Creek Pennsylvanian Sediments = 0.002 ± 0.001 gpd/ft² (10-9 m/s)

These marine sediments are functionally impermeable and will provide little groundwater inflow to the mine access drives and associated excavations The unit also functions as an aquiclude for vertical water movement, and effectively isolates the potable groundwater in the overlying glacial till from the brine in the carbonatite below.

Water levels in wells completed in the Pennsylvanian marine sediments are typically 150 feet below ground surface, indicating a vertical downward head gradient from the glacial till above to the carbonatite below. However, due to the very low vertical permeability of the sediments, there is essentially no vertical downward groundwater flow through them, even over geological time scales.

Cambrian Carbonatite

The Cambrian age carbonatite unit is a volcanic plug made up of carbonatite (volcanic calcium-magnesium-iron carbonate) with siliceous lamprophyre rock masses interspersed throughout. The intact carbonatite and lamprophyre rocks are essentially impermeable, and the rock mass is generally lightly fractured, resulting in locally low hydraulic conductivity. However, the carbonatite is intersected by a small number of widely spaced, narrow, extensive and connected void zones. These are interpreted to be related to faulting and hydraulic fracturing that occurred during volcanic carbonatite emplacement and hydrothermal ore emplacement (ABC, 2026; SRK, 2017). These widely spaced void zones are the primary conduits for groundwater flow in the carbonatite and form a three-dimensional groundwater-flow network.

Hydraulic Conductivity

The hydraulic conductivity of the Elk Creek carbonatite has been evaluated by pump tests, injection tests, packer tests, active flowmeter tests, and laboratory tests on intact core. The results are compiled on Figure 13‑4 and the average is:

Hydraulic conductivity of the Elk Creek Carbonatite = 3.3 ± 2.5 gpd/ft² (2×10-6 m/s)

The results in Figure 13‑4 show four orders of magnitude range of permeability for a single geological rock type (carbonatite). This is unusual in geohydrology studies. The explanation is one of scale: the impact of the sparse high permeability void zones distributed through the otherwise functionally impermeable intact carbonatite. On the left of the figure there are four long packer tests which have hydraulic conductivity less than 0.001 gpd/ft² (5×10-9 m/s). This is approximately the permeability of intact carbonatite and lamprophyre (based on 28 laboratory permeability tests), indicating that

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the packer interval tested included no void zones, or any other significantly permeable features in the hundreds of feet of rockmass tested. To the right are the results of testing borehole intervals which are much more permeable; this permeability comes from one or more highly conductive void zones encountered in the test section. The hydraulic conductivity of a single void is proportional to the cube of the aperture, so variations in aperture creates large variations in permeability (Hoek & Bray, 1974). The observed large variation supports the conclusion that the permeability in each test is caused by a few narrow voids with varying aperture widths.

img170397038_89.jpg

Source: ABC 2026

Figure 13‑4: Hydraulic Conductivity of Geologic Materials at the Elk Creek Mine

 

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Porosity

The void zones are also the main source of drainable porosity in the carbonatite. Drainable porosity is a key parameter for mine hydrology, as it controls the amount of water that will drain from the rock once the porewater pressure has been relieved. In addition – of importance to this project – at this site these voids have been shown to be large enough to be groutable, so it is also the groutable porosity: the volume of cured grout that would be required to seal a unit volume of carbonatite against flow.

In Phase 4 of the Elk Creek hydrology investigation drainable porosity was evaluated by core analysis of vugs and voids, downhole geophysical surveys of voids, and flowmeter tests of circulation loss (ABC, 2026). The result is:

Groutable porosity of the Elk Creek carbonatite = 0.09% ± 0.05%

This is very low porosity for a carbonate or volcanic rockmass. The voids that make up the groutable porosity are relatively large – between 1 inch and 3 inches aperture. However, they are very sparse, with a spacing ranging from 100 to 500 feet of borehole.

By contrast, the primary porosity of the intact carbonatite rocks is 1% or less, which is typical of an intact rock of almost any type. Permeability testing demonstrated that the porosity in the intact rock was effectively unconnected to the secondary porosity, due to the very low intact rock permeability (Figure 13‑4, shaded area).

 

13.3.2 Mine Inflow Control

13.3.2.1 Mine Inflow

Inflow with no controls

Based on the mine design in this report the mining will take place in a block of material within the carbonatite with the following approximate dimensions:

Length (L) = 2,500 feet (NW-SE)

Width (W) = 1,000 feet (NE-SW)

Height (D) = 2,400 feet (600 feet to 3,000 feet below ground surface)

The carbonatite block is submerged in brine with a current average piezometric surface 300 feet below ground surface. This brine exerts an average hydraulic head on the sides of the mined block as follows:

Hydraulic head (H) = AVERAGE(600 ft, 3,000 ft) — 300 ft = 1,500 ft (650 psi)

The average hydraulic conductivity of the carbonatite in the vicinity of the orebody was found by large-scale pumping tests to be in the order of 4 gpd/ft² (2x10-4 cm/s) (SRK, 2017).

Using these data, the peak inflow to the mine during mining without any external inflow control is estimated by treating the mine as a large diameter well (Figure 16.3-4). Computations use the steady state radial flow equation (Theim, 1870):

Q ≈ 2 π D K H / ln(R/r)

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where: Q = mine inflow [gpm]

D = height mine exposed to carbonatite [2,400 ft]

K = hydraulic conductivity of carbonatite [4 gpd/ft² = 0.0028 gpm/ft²]

H = average drawdown at the mine opening [1,500 ft]

r = effective well radius of mine [≈ 1,000 ft]

R = radius of influence of mine [radius of carbonatite ≈ 10,000 ft]

Thus:

Q ≈ 2π*(2,400 ft)*(0.0028 gpm/ft²)*(1,500 ft) / ln(10,000 ft/1,000 ft) ≈ 26,000 gpm

This inflow is judged to be in excess of the inflow that could be safely allowed to flow into the mine or could be timely dewatered ahead of mining.

img170397038_90.jpg

Source: Adrian Brown Consultants 2026

Figure 13‑5: Mine inflow with no controls — Schematic

 

Inflow with grouting control

Accordingly, the decision was taken in the mine planning process to control the mine inflow and make the mine safe for operation by grouting the mining block. This would plug the karst voids with cement grout, which has a hydraulic conductivity of approximately 0.0004 gpd/ft² (2x10-8 cm/s) (Carmichael & Arulraj, 2017; Whiting, 1988). Intact carbonatite in the mining block has a hydraulic conductivity of approximately 0.002 gpd/ft² (7x10-10 m/s) (Figure 13‑4). Filling the karst voids within that material with cement grout would reduce the overall hydraulic conductivity of the grouted volume to that of the carbonatite intact rock.

The grouting program is designed to limit the average mine inflow to 200 gpm, which is manageable from a dewatering and a water treatment perspective. To achieve this objective, it is necessary to grout the entire mining block to a minimum of 150 feet outside the proposed mined excavation, computed as follows.

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As the mining progresses the grouted mining block will be "hollowed out", as the orebody is removed for processing, leaving a minimum 150-foot-wide grouted carbonatite flow barrier on all sides of the excavated mine. The mine will be at least partially backfilled with cemented fill after ore is extracted, but no credit is taken for the further resistance to inflow which this will create.

Inflow to the interior of the mine through all sides of the grouted mine block at the end of mining is shown Figure 13‑6, and is computed using Darcy’s Law (Darcy, 1856):

Q = K I A

where: Q = inflow through all sides and the base of the orebody block [gpm]

K = hydraulic conductivity of grouted carbonatite [0.002 gpd/ft²]

H = average hydraulic head across flow barrier [1,500 ft]

L = thickness of flow barrier [150 ft]

I = hydraulic gradient = H / L' = (1,500 ft) / (150 ft) = 10 ft/ft

A = area = 2*[(2,500 ft+1,000 ft)*(2,400 ft) + (2,500 ft*1,000 ft)] ≈ 22,000,000 ft²

Thus, the peak steady brine inflow to the grouted Elk Creek mine at the end of excavation is approximately:

Q ≈ (0.002 gpd/ft² / 1,440 min/day)*(10 ft/ft)*(22,000,000 ft²) ≈ 300 gpm

img170397038_91.jpg

Source: ABC 2026

Figure 13‑6: Mine inflow with grout control — Schematic

 

13.3.2.2 Groutability of the Elk Creek Orebody

Groutability of fractured karst rock depends on the ability to deliver grout to the fractures and voids in the rock, and thereby to largely eliminate the ability of those conduits to convey groundwater to the mine workings. Cementitious grout is a mixture of portland cement, fly ash, blast furnace slag, bentonite, and fine-grained aggregate in water. After injection the grout cures to create a low permeability solid which seals the conduits.

The Elk Creek carbonatite is an attractive candidate for grouting. It is a largely intact rockmass with a sparse network of voids. The voids can be intersected by grout injection boreholes and will readily

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accept grout (ABC, 2026). There are a number of lines of evidence from the investigations of the orebody that demonstrate the groutability of the Elk Creek Orebody:

1. Geology. The Elk Creek carbonatite is made up of essentially impermeable intact carbonatite, intersected with widely spaced narrow void zones ((SRK, 2017), App. 6K). These void zones are the only significant conduits for mine inflow and are also excellent high-transmissivity conduits for injection of grout to plug them. After the grout cures the resulting grouted rockmass has an overall permeability approximately equal to the intact rockmass permeability.

2. Drilling fluid take. During exploration diamond drilling approximately 10 gallons per minute of bentonite slurry is injected into the drill string to keep the drilling bit cool, lubricate the drill string to allow continued rotation, and transport the drill cuttings to the surface. Despite this, in all fifteen (15) drill holes in the 2025 drilling program in and around the orebody, circulation of this slurry carrying the drill cuttings was lost while drilling in the carbonatite. As a result, a measured total of 1,200,000 gallons of bentonite slurry and the drill cuttings it was carrying was inadvertently injected into the carbonatite. This demonstrates the ability of the carbonatite to accept large quantities of slurry and granular materials without plugging, which is an essential component of groutability.

3. Abandonment. After drilling, all boreholes in all of the Elk Creek drill programs were abandoned under supervision by the State of Nebraska. In general, this required filling the hole to refusal with low permeability material: high-viscosity bentonite slurry, topped off with neat cement grout. In all cases, this required the introduction of a volume of abandonment materials hundreds to thousands of gallons in excess of the volume needed to plug the borehole stem, indicating that even this high viscosity and rapidly-setting plugging material moved into the carbonatite formation readily through the voids.

4. Geohydrology. Three of the boreholes drilled in the 2025 Elk Creek program were tested for permeability by performing an active flowmeter test over their full length (ABC, 2026). This testing disclosed that essentially all of the flow injected during the tests (about 16 - 18 gpm) entered the formation in a few locations, each comprising less than a foot of the borehole length of 3,000 feet (Figure 13‑4). This confirms that the permeability of the Elk Creek orebody occurs in a small percentage of its length, and that those permeable sections must be of very high permeability, typical of voids, and easily groutable.

5. Direct demonstration. At the conclusion of the 2025 Elk Creek Mine drilling program a total of three groutability tests were performed (ABC, 2026). In these tests grout was injected by hand in batches to the full depth of the borehole until refusal. A variety of grout mixes were tested, including neat portland cement, neat ultrafine cement, and cement-bentonite, with and without retarding plasticizer to reduce the slurry viscosity and increase the time that the grout remained fluid. The results are that it was possible to inject as much as 12,000 gallons of cement grout into the formation through a single hole. This injection had the ability to plug the karst sheets encountered in the borehole to a computed distance of approximately 30 feet radially from the hole before the grout cured in about two days. This result was the same for grout using portland cement and ultrafine cement, both of which required the addition of a retardant to increase the setting time to be equal to or greater than the total time required for injection.

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img170397038_92.jpg

Source: ABC 2026

Figure 13‑7: Geophysical tests showing widely spaced high permeability flow zones (left panel) and corresponding widely-spaced large aperture voids (right panel)

 

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13.3.2.3 Grouting Design

Grout quantity

The void volume required to be sealed in the entire mined volume is approximately 0.09% of the mine orebody volume:

Vvoids ≈ 0.0009*(2,500 ft)*(1,000 ft)*(2,400 ft)*(7.48 gal/ft³) ≈ 40 million gallons

Thus, grouting of the entire mining block will require approximately 40 million gallons of cured grout.

Grout mix

The grout mix demonstrated to be effective for injection at Elk Creek to produce 1,000 gallons of cured grout in the carbonatite is as follows:

Portland cement: 5,000 lb

Water: 1,000 gallons

Plasticizer/retarder: 30 lb

Accordingly, the total material usage for the project grouting is:

Portland cement: 100,000 tons

Water: 40,000,000 gallons

Plasticizer/retarder: 600 tons

Cured grout volume: 40,000,000 gallons

Grouting method

Grouting of the orebody and the immediately surrounding carbonatite will be conducted in two phases:

Phase 1: Primary grouting from surface. Grouting from surface under gravity with 68 holes in a grid with an average spacing between holes of 300 feet, and a length averaging 2,500 feet.

Surface grout holes: 68 holes @ 2,500 ft ≈ 170,000 feet

Phase 2: Dental grouting from underground. Horizontal grout holes drilled through a blowout preventer in advance of each development and stope, oriented NW-SE, spaced 150 feet apart horizontally and vertically, grouted under high pressure to refusal where continuous inflow of water is encountered.

Underground grout holes: 5 holes/level x 24 levels x 2,500 ft ≈ 300,000 ft

Surface Grout Hole Design

The surface grouting will be conducted through a total of 68 deep grout holes, installed as shown in Figure 13‑8, Figure 13‑9, and Figure 13‑10.

Grouting Concept

The grouting concept is as follows:

1. Grouted carbonatite flow control wall. An outer grout wall will be constructed, with injection wells spaced at 150 feet around the ends of the planned ore stopes. Grout will be

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injected to refusal, with injected grout spreading out to a minimum of 150 feet beyond the planned location of the outermost stope headwall. This grouted “shell” provides flow control to 300 gpm throughout the mine life and also provides a stable outer wall to resist the water forces created by the high-pressure brine in the adjacent brine aquifer.

2. Stoping area grouting. The stoping area inside the flow control wall will be grouted at 300 feet spacing inside the stoping area. This is designed to block any karst conduits within the stoping area, so as to minimize inrushes through conduits that have not been sealed by the flow control wall, and to minimize the underground dental grouting that would be required to seal them.

3. Access drive area grouting. Inflow to the access drives located to the southwest of the stope area will be achieved by targeted grouting at approximately 300 feet spacing. It is expected that this surface grouting will limit inflow to the drives, with any remaining inflow being sealed off with underground grout holes drilled in advance of the development drifting.

For project access timing purposes, the access drive area grouting will be conducted from southeast to northwest first, followed by the installation of the flow-control wall and stope-area grouting from southwest to northeast.

 

img170397038_93.gif

Source: ABC 2026

Figure 13‑8: Grout hole location plan, showing grouting boreholes, development drifts, mining stopes and sections.

 

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‘img170397038_94.gif

Source: Adrian Brown Consultants, 2026

Figure 13‑9: Section A-A' looking northeast, showing geology, grouting boreholes, development drifts, and mining stopes

 

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img170397038_95.jpg

Source: ABC 2026

Figure 13‑10: Section B-B looking northwest, showing geology, grouting boreholes, development drifts, and mining stopes

 

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13.3.2.4 Grout hole drilling

The surface grout holes will be drilled as follows:

1. Vertical holes. All grout holes will be drilled vertically to the total depth of the mine in the hole location. Vertical holes are the easiest and quickest to drill, and result in the minimum length of drilling for the project. Grouting effectiveness will be monitored during the project, and in the event that significant vertical karst features are present and are not grouted, the inclination of the grout holes will be adjusted.

2. Full depth grout holes. All grout holes will be drilled to lowest level of mining at the hole location prior to any underground activity in or near that location. This will free the underground works areas for safe operation with respect to drilling impact, inrush impact, and stope wall blowout. Grouting of the carbonatite rockmass to full depth is expected to seal off upflow through the base of the mine at all levels prior to any mining.

Drilling technology

Grout holes must be drilled to avoid plugging of the formation during drilling, and to create a borehole with sufficient capacity to allow injection of as much as 500,000 gallons of low-viscosity grout in each hole within 48 hours. The drilling specification to achieve this performance is as follows:

1. Reverse air dual-string rotary drilling. This drilling technique involves injection of compressed air into the drill string to air lift drill fluid and cuttings to the surface inside the drill string. The drill fluid return is screened to remove cuttings, and the resulting cuttings-free return is conducted down the drilling annulus. This prevents injection of the coarse rotary cuttings into the karst formations intersected by the drilling, leaving the voids open to accept grout at the completion of drilling.

2. Six-inch drilling. In order for the borehole to be able to conduct the required grout injection flow (500,000 gallons in 48 hours), it must be capable of passing a minimum of 200 gpm of low viscosity slurry down as much as 3,000 feet of well under gravity (which creates an available injection head loss of approximately 400 feet of water). This requires a 6-inch internal diameter well, which is readily advanced by rotary drilling.

Grouting technology

The grouting technology required to support the Elk Creek Mine water control project is as follows:

1. Batch Plant: A centrally located batch plant capable of continuous operation for 48 hours with a production of 500,000 gallons of grout slurry at a minimum rate of 200 gpm (Figure 13‑11).

2. Delivery: Pipe or ready-mix trucks operating 24 hours a day during grout injection.

3. Injection: Grout will be piped or poured into the well under gravity.

4. Completion: Injection will continue until refusal at each well, to ensure sealing of the void conduits.

 

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img170397038_96.jpg

Figure 13‑11: Example of a mobile concrete batch plant (Photo courtesy of Techwill Inc.)

13.3.2.5 Inrush Safety

Mining of the Elk Creek orebody will result in the removal of ore from stopes that extend out to within 150 feet of the edge of the grouted carbonatite mine block. Outside of that grouted block there will be up to 2,700 feet of brine with a head pressure up to 1,400 psi. The mine pillars will be unsupported at various times during mining and will have to safely withstand the full applied lateral brine pressure.

Safety against blowout

The grouted wall at the end of the outermost stope in each level constitutes a 130 foot by 50-foot plug, which has to resist the applied force of the brine (Fw) (Figure 13‑12). This force is substantial: at full depth of the mine it is approximately 500,000 tons. It is resisted by friction on any fractures that are at the periphery of the plug (Fs). If the water force exceeds the resisting frictional force, the stope wall blows in to the stope, connecting any high-capacity karst water conduit outside the grouted envelope to the mine. The inrush flow would be sudden and large: up to 2,000 gpm. Blowouts of this size are hazardous to mining personnel, impact mine production, and are difficult and expensive to repair.

To ensure mine safety against blowout, the stability of the terminal stope wall plug has been evaluated (ABC 2026). To create a 99% confidence that the stope wall will be safe against blowout over the entire mine depth requires the grouted wall to be no less than 80 feet thick. This is achieved

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in the design by surrounding the entire stopped volume of the mine with a line of full-depth grout holes spaced 160 feet apart and located outboard of the terminal wall of each line of stopes on each level, and grouting them to provide the 150-foot-thick flow control barrier.

img170397038_97.jpg

Figure 13‑12: Stability of grouted stope outer pillar against water drive — Force diagram

Safety against pillar collapse

The terminal stopes in the mine are supported by pillars extending out into the un-mined carbonatite. These pillars are grouted and are subject to the lateral force exerted by the unrelieved brine pressure on their outer surface (at the limit of the grouting). Accordingly, they are laterally loaded columns, and they have to be thick enough to safely carry the load of the overlying rock while resisting the lateral brine load. If they are too thin, they will bend and fail progressively in compression on the stope face, resulting in inrush.

This safety of the terminal stope pillars against collapse has been evaluated using 3-dimensional numerical modeling (A2GC, 2026b). A typical cross-section of the analyses is presented in Figure 13‑13. Based on that analysis, the 150-foot-thick grouted terminal stope pillar will be stable with respect to stope pillar collapse. This is achieved in the design for inflow limitation and blowout mitigation.

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img170397038_98.jpg

Source: A2GC, 2026

Figure 13‑13: Vertical stress in 65.6 foot- (20 meter) thick and 131.2 foot- (40 meter) high grouted stope outer pillar located 3,280 feet (1,000 meters) below ground surface with 10 MPa (1,450 psi) water drive applied to outer edge of terminal pillar (blue arrows). All stresses reported in MPa, mesh blocks are 3.28-foot (1-meter) cubes.

Environmental Protection

The Elk Creek mine grouting program drills 68 deep injection boreholes and emplaces fifty million gallons of liquid grout containing cement, water, and plasticizer through them into the Elk Creek Carbonatite. The impacts to the environment are evaluated and where necessary mitigated as described below.

Drilling impacts

Drilling will be accomplished by reverse-air rotary technology, in which compressed air is injected into the drill string and drill water and drill cuttings are air-lifted through an inner drill pipe to the surface. All brine that is raised to the surface in this process will be re-injected down the drill hole annulus after removal of cuttings. All boreholes will have a steel casing through the surficial till materials, to protect the fresh water in them from impact. Drilling will be conducted under standard environmental protection requirements, which contain all drilling fluids and other materials to the

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drill site. Following drilling, all boreholes will be abandoned by grouting to refusal. No significant impacts are expected to the carbonatite brine aquifer.

Grout impacts

The grout to be used in the Elk Creek project is a chemical mixture of non-hazardous constituents, which cures when injected and forms an effectively impermeable mass. In doing so, it immobilizes any chemical constituents in it, rendering them incapable of impacting the environment. The impact to the environment of the grout will be insignificant, the same as the impact to the environment of cured concrete in any other setting.

The grout is being introduced into an isolated brine aquifer, in which the natural salinity is in the order of 18,000 mg/L TDS (mainly NaCl). Accordingly, the grout program will not change the use category of the water in the aquifer, which is non-potable.

Brine displacement impacts

The grouting will inject 50 million gallons of grout into the carbonatite brine aquifer. This will displace a like volume of brine away from the mine block. It is important that the displaced brine does not emerge at the surface or in the shallow drinking water aquifer in the surficial glacial till. It will not, for the following reason.

The current brine piezometric level is approximately 300 feet below ground surface. Thus any displaced brine would need to raise the water table in the carbonatite at least this amount before brine could appear on the surface. An injection test was conducted in the carbonatite in 2017 (SRK 2017). In the test fresh water was injected at a rate of 350 to 480 gpm over a period of 33 days. This caused a maximum stabilized increase in the brine level in the carbonatite close to the injection well of approximately 30 feet. This is approximately the same maximum injection rate that is anticipated for the grouting, so the head build-up should be no greater than in the test. If so, the brine level in the aquifer is expected to rise to no higher than about 270 feet below ground surface, far lower than would allow discharge of brine to the surface or the surficial glacials from this cause.

13.4 Mine Design

13.4.1 Selection of Mining Method

The mining method selected for this ore body was based on modifying factors such as economic parameters and geotechnical information, ensuring it was suitable for the mineralized geometry. A number of studies from the recent past have evaluated different mining methods for this deposit, such as caving, open or sublevel stoping, or room and pillar methods. Due to its depth and the requirement to have selectivity in mill feed grades, the underground longhole stoping method (LHS) was determined as a suitable mining method. Given the bulky geometry of the deposit, a block caving or sub-level caving method also could have been considered economically viable. However, the limited selectivity of such methods would not allow for optimizing the higher value of this deposit given the mill production constraints. To maximize the recovery of the high-grade zones, the longhole stoping method utilizing cemented paste backfill was chosen. Figure 13‑14 below shows a cross-sectional view of the current mine design. Three large blocks of resources are defined by the mine plan and will generally be mined together in a declining FeNb grade strategy.

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img170397038_99.jpg

Source: Amplify Mine Planning, 2026

Figure 13‑14: 2026 Current Design

The stope dimensions are planned to be 49 ft wide, with stope lengths varying based on Nb2O5 mineralization grade from 33 ft to a maximum of 49 ft per panel, and a maximum level spacing height of 131 ft. The varying stope length allows for optimizing the Nb2O5 grade with a minimal increase in operating costs. The level spacing of 131 ft was designed because of its beneficial operating and sustaining capital costs. Each block is mined with a bottom-up sequence. A sill pillar level is designed to be left between each of the three mining blocks until that sill level is scheduled to be partially mined. The extraction of ore from the sill pillar level is expected to be 62.5% by volume using production upholes drilled through the first 82 ft of the bottom of the 131 ft thick sill pillar. The mining of the sill pillar is scheduled only after the upper block immediately above is mined out and is accounted for within the reserves. This methodology will allow partial mining of ore on the sill pillar level, while at the same time allowing the development of the lower mining blocks as well as establishing an earlier start to the mining of the upper mining block. Using this approach minimizes the impact on initial capital investment. The backfill was designed to have adequate strength after curing to allow for mining adjacent to filled stopes, thus eliminating the need for rib pillars.

The mine design process centered on using four Deswik© modules – Mine Design, Stope Optimizer, Sequencing, and Scheduling software to determine potentially mineable areas based on 4 main parameters:

• Estimated minimum cut-off net smelter return (CoNSR) value

• Nb2O5 grades

• Mining dimensions parameters

• Geotechnical design and sequencing constraints

The reader should note that since the stope cut-off grade value based on overall mining costs (CoG) of $218/ton is much lower than the resulting average stope CoNSR value of roughly $591/ton, the CoNSR was not the only decisive factor in the stope optimization process. Mining dilution of

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approximately 6% was applied to all stopes and development, based on 3% for the primary stopes, 9% for the secondary stopes, and 5% for ore development. The mining dilution was added to the designed tonnage to account for unplanned sources of dilution such as backfill and host rock around the periphery of the ore mass. An ore recovery factor of 95% was applied to account for unrecoverable ore left within the stopes.

The mine design and schedule were based on recognizing a milling design constraint of 3,047 tpd as defined by NioCorp’s design process. At this rate, the mill is expected to produce approximately 8,282 t/y of ferroniobium during the years of full production. Planned mine life of mine of about 43 years with 40 years at full production. Optimization work indicated that the grade of Nb2O5, (0.803%) at a unit NSR of US$ 591/ton could sustain and produce a consistent ferroniobium production over the LOM. Scandium trioxide and titanium tetrachloride as well as six rare earth metals (Dy2O3, Nd2O3, Pr2O3, and Tb2O3, Sm-Eu-Gd carbonate, Ho-Er-Tm-Yb-Lu-Y carbonate) that accompany the ferroniobium production in the mine plan. NioCorp favored a higher Nb2O5 COG approach to maximize the LOM NPV for production scheduling while at the same time maintaining the annual ferroniobium target.

13.4.2 Stope Optimization

As mentioned in Section 13.4.1 the minable shape optimization software module provided by Deswik© was used to determine potentially mineable areas based on 1) cut-off net smelter return (CoNSR) calculation provided by NioCorp, 2) Nb2O5 grades provided by DGC, and 3) mining dimension parameters designed by Amplify Mine Planning and Dumas. The estimated cut-off NSR value (CoNSR) of US$ 218/t provided by NioCorp was used as a starting point for the analysis. As the CoNSR value is much lower than the resulting average stope NSR revenue value, the CoNSR was not the decisive factor in the stope optimization process. Rather than using just a minimum CoNSR, the mine design also targeted an average cut-off Nb2O5 grade of 0.65% and a milling constraint of 3,047 tpd which resulted in a steady-state average annual ferroniobium production of 8,282 tons during the years of full production. This strategy results in a LOM NSR average value of US$590.84/ton. Figure 13‑15 and Table 13‑7 below show the mineable stopes optimized for varying CoNSR scenarios. An average dilution of approximately 6% was added to the designed tonnage which accounts for unplanned sources of dilution such as backfill and the host rock around the periphery of the ore mass while a recovery factor was applied to account for unrecoverable material which will be left within the stopes. The average dilution was derived from applying 3% dilution by volume to primary stopes, 9% dilution by volume to secondary stopes, and 5% dilution by volume for development drifts. As discussed in Section 12, the dilution is a natural consequence of the mining process and the defined amounts of dilution by mining type reflects Amplify Mine Planning’s understanding of the unique facts and data of the deposit and used in the mine planning process and acknowledges the relevant accuracy of those facts and data applied during the planning process to create a successful mining plan.

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img170397038_100.jpg

Source: Amplify Mine Planning, 2026

Figure 13‑15: Undiluted Stope Optimization Results for Varying NSR Cut-Offs

 

Table 13‑7: Undiluted Stope Optimization Results for Varying NSR Cut-offs

img170397038_101.jpgSource: Amplify Mine Planning, 2026

13.4.3 Stope Design

Figure 13‑16 shows a cross-sectional sketch of a typical 2-level and primary/secondary stope extraction design. The stope width is a constant 49 ft with a vertical height of 131 ft from sill to sill. The length (depth) of the stopes is designed to a maximum panel length of 49 ft and a minimum panel length of 33 ft. Figure 13‑17 shows a typical level arrangement of the stopes, cross- cuts, footwall

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drive, ramp and other infrastructures servicing a single level. The mine plan stope orientation is perpendicular to the general strike of the deposit, which is 20° off the measured principal stress. This offset will not have a significant impact on stope stability. The actual planned stope lengths currently have a maximum length of 49 ft in both fresh and moderately weathered rock, which is a conservative design in relation to the stability assessment described in Section 13.2.2.

img170397038_102.jpg

Source: Amplify Mine Planning, 2026

Figure 13‑16: Stopes and Crosscut Accesses (Cross Section View)

 

 

 

 

 

 

 

 

 

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img170397038_103.jpg

Source: Amplify Mine Planning, 2026

Figure 13‑17: Level Layout with Stopes and Footwall Accesses (Rotated View Looking North)

13.4.4 Development Design

The production stopes are accessed through a footwall drive drift that is offset approximately 82ft from the nearest edge of a stope. The crosscuts (x-cuts) are driven into the center of each target primary or secondary stope from the footwall drive, as shown in Figure 13‑18. This figure provides a plan view showing the distinct offset difference between the mine access/infrastructure locations which are offset to the production stopes located in the deposit.

img170397038_104.jpg

Source: Amplify Mine Planning, 2026

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Figure 13‑18: Completed Mine Design (Plan View)

These footwall access drifts are connected by the ramp system and further connect to ventilation raises, and on some levels, they are connected to the secondary haulage ramp which contains the Railveyor© train. Much of the mine infrastructure is located in waste rock, but some infrastructure areas can be found in lower grade material as it gets closer to the ore body.

The designed vertical extent of the mine production area is approximately 2,380 ft, with a bottom elevation of roughly 3,050 ft below the surface elevation. Figure 13‑19 shows the completed mine design highlighting several main infrastructure areas and the vertical extent of the current mine plan. The ramps, internal slot or drop raises, and underground infrastructure included in the design are discussed in other subsections. The three mining blocks are generally mined simultaneously, based on declining grade strategy using a primary/secondary stoping sequence that will utilize cemented paste backfill to support the mined-out stopes once the backfill is cured. Altogether, they provide an estimated life-of-mine (LOM) of 43 years.

The primary access ramp and secondary haulage ramp are designed to reach a depth of roughly 3,050 ft below the surface.

img170397038_105.jpg

Source: Amplify Mine Planning, 2026

Figure 13‑19: Completed Mine Design (Cross Sectional View)

 

Figure 13‑20 is a closer view of the mine in profile view looking south showing main infrastructure locations and their connection to the main producing stopes.

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img170397038_106.jpg

Source: Amplify Mine Planning, 2026

Figure 13‑20: Completed Mine Design - Main Infrastructure (Looking South)

 

Figure 13‑21 and Figure 13‑22 show the mine design colored by Nb2O5 grade and NSR, respectively.

img170397038_107.jpg

Source: Amplify Mine Planning, 2026

Figure 13‑21: Mine Design Coloured by Nb2O5 Grade.

 

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NioCorp Developments Ltd.

img170397038_108.jpg

Source: Amplify Mine Planning, 2026

Figure 13‑22: Mine Design Coloured by NSR ($/t)

 

Table 13‑8 Summarizes the mine design by activity type.

 

Table 13‑8: Mine Design Summary - by Activity Type

General Summary

Units

LOM Statistics

Ore Tons

(T)

45,929,463

FeNb Tons

(T)

316,099

Nb2O5 Grade - Mined

(%)

0.759

Sc Grade - Mined

(ppm)

69.3

TiO2 Grade - Mined

(%)

2.68

TREO Grade - Mined

(ppm)

3,447

Development Ore Tons

(T)

1,135,621

Stope Production Tons

(T)

44,793,842

Total Waste Tons

(T)

6,482,430

Total Tons Moved

(T)

52,436,964

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General Summary

Units

LOM Statistics

Lateral Development:

RAMP DEVELOPMENT

(ft)

                  38,711

LEVEL ACCESSES

(ft)

                  13,040

PRODUCTION LEVELS

(ft)

                  33,872

STOPE DEVELOPMENT

(ft)

               184,184

LOADOUTS

(ft)

                    5,219

AUXILIARY LATERAL DEVELOPMENT

(ft)

                  23,035

TOTAL LATERAL DEVELOPMENT

(ft)

               298,061

Vertical Development:

RETURN AIR RAISE

(ft)

                       130

ORE BIN

(ft)

                       394

ORE PASS

(ft)

                    1,837

ORE PASS FINGER

(ft)

                       940

WASTE BIN

(ft)

                       394

WASTE PASS

(ft)

                    1,838

WASTE PASS FINGER

(ft)

                       887

TOTAL VERTICAL DEVELOPMENT

(ft)

6,420

Source: Amplify Mine Planning, 2026

 

13.4.5 Mine Access

13.4.5.1 Dual Portal Box Cut

The underground mine will be accessed via a purpose-designed box cut excavation incorporating two portals, designated as the Service Portal (also referred to as the North Portal) and the Production Portal (also referred to as the South Portal). These portals terminate at the closest finished face of competent bedrock beneath the overburden, thereby establishing stable entry points into the underground workings in accordance with standard industry practices for portal location and development. At the rock interface, the two underground decline ramps—the North Service Ramp and the South Production Ramp—commence, providing controlled access to the various production levels of the mine.

At the time of this report, construction of the mine portal box cut has commenced on site. For the purposes of the economic analysis and establishment of capital costs in this Technical Report Summary, the portal box cut, associated sockets, and fresh air raise are assumed to be fully completed and available for operations. Actual capital expenditures incurred to date for portal construction will be tracked separately and reconciled against the study estimates as detailed engineering and construction progress.

The mine access box cut area will remain excavated and will not be backfilled, ensuring permanent, open access for ongoing operations, maintenance, and emergency response. Highwalls of the box cut will be stabilized in full compliance with site-specific geotechnical recommendations and established best-practice guidelines for slope and bench stability. Stabilization measures will incorporate

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appropriate batter angles, benching where required, and systematic ground support systems (such as fibre-reinforced shotcrete, welded mesh, rock bolts, and cable bolts) to mitigate rockfall hazards, erosion, and potential instabilities in the near-surface weathered zone. These designs are derived from detailed geotechnical investigations, kinematic and numerical stability analyses, and engineering best practices, ensuring long-term reliability of the access infrastructure.

The box cut floor will descend from the original surface start point at a gradient of 15%. From the portal rock interface, the North Service Ramp will decline to the mine bottom at a gradient of 15%, while the South Production Ramp will continue at an 18% gradient. This dual-ramp configuration within a single box cut excavation follows proven technical approaches for similar underground operations, where twin declines enable functional separation of traffic while maintaining a compact surface footprint and optimized geotechnical conditions at depth.

The North Service Ramp will serve as the primary means of egress to the underground mine for personnel and vehicular traffic, supporting safe, efficient movement of workers, equipment, and materials under normal operating conditions. The South Production Ramp will be dedicated to production activities utilizing a Railveyor conveyance system for the continuous transport of ore and waste materials from underground to the designated surface dumps. In addition, the South Production Ramp will function as an alternate means of egress during emergencies, providing essential redundancy and thereby reducing the overall risk profile associated with single-access scenarios in accordance with contemporary mine portal design principles.

Both the North and South Portal Ramps will incorporate a short enclosure extending from the rock interface, sufficient to provide localized weather protection and structural transition at the portal face while aligning with the service-oriented functions.

Surface runoff entering the box cut excavated area will be collected and pumped to the site’s stormwater pond independent of the mine dewatering system. This arrangement incorporates dedicated sumps and pumping capacity as part of comprehensive surface water management, preventing inundation, erosion, or uncontrolled water ingress into the mine and ensuring compliance with environmental and operational safety requirements.

13.4.5.2 Fresh Air Raise

The underground mine incorporates a purpose-developed fresh air raise as a third independent mine access opening, providing vertical ingress and egress to the underground workings as a redundant pathway in addition to the primary dual-portal box cut excavation (North Service Portal and South Production Portal). This raise is established as a vertical shaft commencing at a stabilized surface collar and extending through overburden and competent bedrock to connect underground via a horizontal drift, thereby ensuring multiple means of access and egress in compliance with regulatory requirements and contemporary mine design standards for operational safety and emergency preparedness.

Raise collar construction establishes a secure foundation through installation of secant piles within the glacial till overburden, followed by a steel-reinforced concrete collar pad. The upper coping section of the raise is excavated mechanically through stiff to very stiff lean-to-fat clay glacial till, with a steel-reinforced, cast-in-place concrete liner installed in staged lifts to maintain ground control, dimensional accuracy, and groundwater isolation. The intermediate section transitions into un-weathered to slightly weathered shale and moderately hard limestone, where excavation shifts to controlled drill-and-blast methods. A concrete liner is placed in coordination with sinking advances

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to ensure structural continuity and long-term stability. Upon completion of the vertical raise, an access drift is developed to establish the underground connection, with ground support comprised of rock bolts, wire mesh, and shotcrete. This raise-and-drift development provides a stable, permanent access opening sized and supported in accordance with the variable ground conditions encountered.

To enable safe personnel movement within the fresh air raise and to provide a dedicated third means of access and egress should the primary portal entrances become compromised, a suitable man-way ladder system is incorporated throughout the vertical raise. The ladderway is designed in accordance with MSHA standards (30 CFR § 57.11036–57.11041) and industry best practices for shaft escapeways. It features fixed ladders with a minimum unobstructed cross-sectional opening of 24 in × 24 in measured from the ladder face, substantial landings or offset ladder sections with gates at intervals not exceeding 30 ft for ladders steeper than 70° from horizontal, and protective cages or equivalent fall-arrest systems where required. The manway provides direct vertical access from surface to the underground drift connection, ensuring rapid self-escape or rescue team intervention independent of the ramp portals.

Collectively, the dual-portal box cut and the fresh air raise establish a robust, multi-redundant mine access framework. This configuration enhances personnel safety and operational resilience while meeting geotechnical, regulatory, and infrastructure requirements for permanent underground access. All elements are engineered for long-term structural integrity, groundwater control, and seamless integration with the overall mine development.

13.5 Production Schedule

The production schedule is based on the mine design and access to defined reserves as discussed in previous sections. In general, a strategy of prioritizing grade for Nb2O5, while following a bottom-up pyramidal stoping sequence via scheduled, available development access drifts provides the basis for the production schedule.

13.5.1 Productivity

Productivities for mine development and production were derived from first principal calculations by Dumas. Additional input from supporting mining contractors, blasting suppliers, and other equipment vendors were used by Dumas to assist with estimating the key parameters. The rates developed from first principles were also subject to potential adjustments based on relevant benchmarking and the experience and judgment of the mine design team.

The productivity rates used for mine scheduling are shown in Table 13‑9, followed by a description of the general and activity-specific parameters upon which the productivity rates are based.

Typical dimensions by heading types are presented in Table 13‑10. These will all be developed by contractors in accordance with the productivity rates and levelled in the schedule by crew assignments.

Table 13‑9: Productivity Rates

Activity

Type

Dimensions

Rate

Lateral Development

Priority Face

See Table 16-10

16.4 ft/d

Non-Priority Face

9.8 ft/d

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Activity

Type

Dimensions

Rate

Vertical Development

Fresh Air Raise

13 ft diameter

9.8 ft/d

Return Air Raise

13 ft diameter

9.8 ft/d

Ore Bin

20 ft diameter

3.3 ft/d

Waste Bin

20 ft diameter

3.3 ft/d

Conical Sump

16 ft diameter

3.3 ft/d

Ore Pass Finger

6.5 ft x 6.5 ft

9.8 ft/d

Waste Pass Finger

6.5 ft x 6.5 ft

9.8 ft/d

Ore Pass

9.8 ft x 9.8 ft

9.8 ft/d

Waste Pass

9.8 ft x 9.8 ft

9.8 ft/d

Stoping

Slot Development

-

10.5 d

Drilling

-

656 ft/d

Stope Production

-

1020 t/d

Backfill Preparation

-

10.0 d

Backfilling

-

42,378 ft³/d

Backfill Curing

-

28.0 d

Source: Amplify Mine Planning, 2026

 

Table 13‑10: Dimensions by Heading Types

Heading Types

Width (ft)

Height (ft)

Area (ft2)

Rate

RAILVEYOR BYPASS

26.2

19.0

499

16 ft/d

LEVEL AXS

18.0

19.0

343

16 ft/d

LOADOUT

18.0

19.0

343

16 ft/d

MUCKBAY

18.0

19.0

343

10 ft/d

PASSING BAY

18.0

19.0

343

16 ft/d

RAMP

18.0

19.0

343

16 ft/d

RAMP ACCESS

18.0

19.0

343

10 ft/d

FRESH AIR ACCESS

14.8

14.8

218

10 ft/d

LATRINE

14.8

14.8

218

10 ft/d

PRODUCTION LEVEL

14.8

14.8

218

16 ft/d

ELECTRICAL LOAD CENTER

14.8

14.8

218

10 ft/d

ORE PASS ACCESS

14.8

14.8

218

16 ft/d

PARKING BAY

14.8

14.8

218

10 ft/d

PRIMER MAGAZINE

14.8

14.8

218

10 ft/d

RETURN AIR ACCESS

14.8

14.8

218

10 ft/d

SUMP

14.8

14.8

218

10 ft/d

WASTE PASS ACCESS

14.8

14.8

218

16 ft/d

MAIN SUMP

14.8

17.1

252

10 ft/d

POWDER MAGAZINE

14.8

17.1

252

10 ft/d

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Heading Types

Width (ft)

Height (ft)

Area (ft2)

Rate

REFUGE BAY

14.8

17.1

252

10 ft/d

STOPE DRIFT

14.8

17.1

252

10 ft/d

STOPE CROSSCUT

14.8

17.1

252

10 ft/d

DRILL BAY

14.8

17.1

252

10 ft/d

SHOP

23.0

23.0

527

10 ft/d

CHARGING STATION

29.5

19.0

562

10 ft/d

WAREHOUSE

29.5

19.0

562

16 ft/d

Source: Amplify Mine Planning, 2026

General Parameters

Table 13‑11 provides the general schedule parameters applicable to all underground mining activities for the ramp-up period and life of mine production.

 

Table 13‑11: Workforce Schedule Parameters for Underground

Schedule Parameters

Value

Units

Annual Mining Days

365

days/yr

Mining Days per Week

7

days/wk

Shifts per Day

2

shifts/day

Scheduled Shift Length

12

hrs/shift

Pre-shift meeting

15

min

Travel to work area via ramp or cage

15

min

Inspection pre-start

10

min

Lunch

30

min

Cleanup and setup for cross shift

10

min

Travel to surface

10

min

Handover meeting

10

min

Non-productive time

100

min

Work Time

620

min

Total Work Time Per Shift

10.33

hr/shift

Total Work Time per Day

20.66

hr/day

Efficiency

86.10%

Source: Dumas 2026

Refer to Section 13.2.2.6 for detailed ground support requirements.

The mine plan has conservatively designed a plan using grouted rebar in the back (roof) of all excavations. Split sets are designed for walls of all excavations, but not in the roof (back).

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13.5.2 Box Cut, Portal and Ramp Development

The proposed box cut design dimensions are shown in Table 13‑12 and Figure 13‑23. Construction of the box cut commenced in February 2026 and is fully funded. The descriptions herein are provided for completeness, but costs are not included in the economic model associated with this technical report, as the box cut will be complete before the balance of project execution is undertaken. The portion of the box cut that lies within the bedrock has a high wall at a 75° angle. The portion of the box cut that lies within the overburden and shale will have 1:1 sloped wall with benches at 41’ heights.

Table 13‑12: Cut Design Dimensions

Box Cut Dimension

Unit

Value

Length

ft

1,228

Width

ft

320

Maximum Depth

ft

132

Excavation Volume

Yd³

628,423

Source: Dumas, 2026

 

img170397038_109.jpg

Source: Dumas, 2026

Figure 13‑23: Box Cut Design Dimensions – Plan View Looking Northeast

The box cut slopes in the overburden will be soil nailed to preserve the 1:1 slope per the GSI proposal #168695633 (Figure 13‑24).

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img170397038_110.gif

Figure 13‑24: GSI Proposal for Slope Stability

 

The initial ramps are both going to be driven at the same time (18 ft wide x 19 ft high) from the box cut and proceed down to 210L, shown in Figure 13‑25. Ventilation loops will be established as the ramps are driven by breaking through from one ramp to the other. The South Ramp will be used for the Railveyor and driven at 18% maximum grade and will facilitate the movement of both ore and waste as well as being the main ventilation path for the return air. The North Ramp will facilitate the movement of larger mining equipment, services and the workforce to and from the mine and will be driven at 15% maximum grade. It will also act as the fresh air path for the mine ventilation system.

img170397038_111.jpg

Source: Dumas, 2026

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Figure 13‑25: Initial Ramp Development – Isometric View Looking North

13.5.3 Primary Haulage Ramp & Secondary Access Ramp

The ore body will be accessed by two spiral access ramps at decline angles of 15 and 18 degrees from the face of a box cut ramp and spaced a minimum of 16.4ft between the ramp openings. Excavating both spiral primary haulage and secondary access ramps will be carried out simultaneously. In addition, a short vertical shaft will be excavated in the development timeline connecting the surface to the primary access ramp to provide a route for air ventilation supply purposes. The main mine fan will be constructed at the surface of this shaft to provide ventilation to the mine as well as cooling and heating depending on the time of year. Driving both ramps simultaneously allows the initial lateral development entries to begin from the first sill level location of the primary haulage ramp while the primary haulage and secondary access ramps continue to be excavated to lower elevations to facilitate extraction of higher niobium grade stopes located at the lower levels.

The primary haulage ramp will be excavated to a total depth of 3,050 ft and is estimated to be a total 18,240 ft in length. The secondary access ramp will also be excavated to the depth of 3,050 ft given an estimated total length of 20,360 ft. The primary haulage and secondary access ramps will be excavated simultaneously using conventional mine drilling and blasting methods in conjunction with probe drilling and grouting as needed ensure ground water in-flow control. The planned rate of excavation averages 16.3 ft/d; this rate was developed in collaboration with mine contractors given the strata material expected to be encountered. The average rate captures the activities of drilling, blasting, mucking, and bolting, with experiential rate adjustments due to rock types and shaft depth. The ore or waste material will be removed by an LHD which loads into a mine truck and hauls the waste and ore to the surface until such time as the vertical muck raises are excavated and the Railveyor is installed and operational.

Both ramps are developed to finished dimensions of 18 ft wide by 19 ft high which excludes the required cement lining thickness required for the ground support program, discussed earlier. These ramps have been sized to allow the safe passage of required production equipment, personnel, mining parts and supplies, service lines, and most importantly, the ventilating air required to dilute, render harmless, and carry away all noxious gases and dusts from mining operations.

The secondary access ramp will be excavated with the same dimensions and method as the primary haulage ramp also to a depth of 3,050 ft. Conventional drifting coupled with a probe drilling and grouting to contain any leakage into the ramp from the potential water-bearing structures. This method, unlike other potential methods considered for accessing the ore body, allows better control over potential formation water inflows.

An LHD loader to truck haulage system will be utilized to move ore and waste from lateral mine development prior to the completion and installation of the permanent Railveyor in the haulage ramp.

13.5.4 Development and Production Schedule

The production and development schedules were completed using the Deswik© scheduling module software. The production schedule is based on the rate assumptions shown in Table 13‑13.

A delay of 28 days was used before driving on paste backfill or mining adjacent to a paste backfilled stope. These delays account for curing time as well as multiple pours.

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The mining operation schedule is based on 365 days/year, 7 days/week, with two 12 hour shifts each day. A production rate of 3,047 tons/d was targeted with a ramp-up to full production as quickly as possible. The schedule timeframe is monthly for the entire life of mine.

Primary access ramp and secondary haulage ramp excavation preparation begins upon completion of the box cut excavation on surface. Production stoping begins sixteen months after the start of ramp development, with a production ramp-up period through the following six months, after which the mine and plant are operating at full capacity.

Table 13‑13 shows the annual mine production schedule, and Figure 13‑26 shows the mine production schedule colored by year.

Table 13‑13: Mine Production Schedule

Year

Ore Tons (tons)

Mined Nb2O5 (%)

Mined TiO2 (%)

Mined Sc (ppm)

Mined Waste Tons (tons)

Backfill Volume (ft3)

Year 0

396,351

Year 1

22,663

1.153

3.33

75.73

919,483

Year 2

491,681

0.786

2.54

65.32

657,959

3,191,046

Year 3

1,194,029

0.770

2.66

66.99

646,590

12,741,436

Year 4

1,247,664

0.771

2.58

60.23

540,800

12,338,948

Year 5

1,232,616

0.767

2.49

63.21

557,650

12,504,055

Year 6

1,193,599

0.744

2.47

65.14

576,777

12,370,694

Year 7

1,210,747

0.744

2.53

69.58

277,252

12,454,386

Year 8

1,133,751

0.789

2.73

63.61

33,508

12,437,151

Year 9

1,177,200

0.733

2.41

62.03

68,466

11,995,000

Year 10

1,214,345

0.772

2.48

70.71

149,448

12,445,117

Year 11

1,172,803

0.743

2.42

70.18

81,576

12,418,233

Year 12

1,176,621

0.762

2.65

69.11

96,378

12,370,014

Year 13

1,163,999

0.784

2.78

71.89

55,943

12,566,035

Year 14

1,159,979

0.741

2.74

76.95

37,909

12,287,642

Year 15

1,159,636

0.763

2.69

73.13

25,221

12,411,519

Year 16

1,175,711

0.732

2.71

77.21

61,118

12,361,373

Year 17

1,197,510

0.721

2.58

72.95

106,387

12,429,481

Year 18

1,184,559

0.751

2.58

73.64

73,191

12,386,938

Year 19

1,186,644

0.748

2.48

73.40

67,671

12,445,413

Year 20

1,172,192

0.753

2.64

70.64

57,481

12,275,126

Year 21

1,163,531

0.739

2.71

69.37

50,346

12,227,143

Year 22

1,115,642

0.822

2.72

77.79

36,848

12,446,536

Year 23

1,155,006

0.804

2.81

73.00

97,671

11,915,615

Year 24

1,107,493

0.815

2.79

71.14

60,499

12,284,901

Year 25

1,155,661

0.781

2.63

70.94

78,175

11,719,351

Year 26

1,181,405

0.761

2.63

67.20

60,017

12,266,487

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Year

Ore Tons (tons)

Mined Nb2O5 (%)

Mined TiO2 (%)

Mined Sc (ppm)

Mined Waste Tons (tons)

Backfill Volume (ft3)

Year 27

1,164,560

0.773

2.82

71.78

39,732

12,462,230

Year 28

1,171,849

0.750

2.77

68.11

60,265

12,320,050

Year 29

1,165,828

0.729

2.69

69.07

68,341

12,183,031

Year 30

1,163,315

0.744

2.61

67.03

58,765

12,477,265

Year 31

1,156,476

0.740

2.77

66.50

27,827

12,325,815

Year 32

1,157,871

0.768

2.90

69.08

38,545

12,243,565

Year 33

1,156,848

0.745

2.72

69.32

42,351

12,361,994

Year 34

1,150,141

0.781

2.88

68.26

63,944

12,345,009

Year 35

1,162,321

0.743

2.82

67.08

54,451

12,900,177

Year 36

1,153,279

0.743

2.83

66.74

36,341

12,445,163

Year 37

1,151,331

0.787

2.81

71.45

25,728

12,107,186

Year 38

1,164,743

0.716

2.71

66.09

27,788

12,506,866

Year 39

1,138,302

0.746

2.79

67.82

0

12,103,058

Year 40

910,483

0.802

2.86

70.60

27,351

9,558,283

Year 41

972,938

0.716

2.59

66.37

40,283

10,440,185

Year 42

242,493

0.716

2.71

63.96

0

3,060,371

Year 43

311,007

Totals

45,929,462

0.759

2.68

69.27

6,482,430

483,440,895

Source: Amplify Mine Planning, 2026

 

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img170397038_112.jpg

Source: Amplify Mine Planning, 2026

Figure 13‑26: Mine Production Schedule - Colored by Year

 

13.6 Mining Operations

13.6.1 Production Schedule

The ore feed to the plant comes primarily from stope production. In aggregate, development drifts contribute less than 3% of the total ore produced over the life of mine. Stopes are mined using the longhole open stoping method with cemented backfill on a primary-secondary stope mining sequence. Individual stope blocks are designed to be 49ft wide, up to 49ft long and oriented roughly parallel to the main stress. Levels are spaced 131ft apart in height, and each stope block has top and bottom access drift called the crosscut (x-cut: 14.8 ft x 17 ft flat back drifts) traversing the middle of the stope. Each crosscut is developed to its’ full extent within each stope before the stope is set up for retreat mining.

The majority of ore processed by the plant is sourced from longhole open stoping operations, with development ore contributing less than 3% of the total life-of-mine mill feed. Production stopes are designed as longitudinal longhole stopes measuring approximately 50 ft wide by 50 ft long (15 m by 15 m) and are oriented generally parallel to the principal stress direction to optimize geotechnical stability. Mining levels are vertically spaced at 131 ft (40 m) intervals. Each stope is accessed by upper and lower crosscuts measuring 15 ft × 15 ft (4.5 m × 4.5 m) and associated stope drifts

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measuring 15 ft × 17 ft (4.5 m × 5.2 m). Production drilling is completed from the upper stope access using ITH longhole production drills equipped with 3.0-in (76-mm) diameter drill steel. Initial stope void creation is established through the development of a slot raise using a slot reaming machine producing a 30-in (762-mm) diameter opening. The slot is subsequently expanded through blasting to establish the free face required for production blasting. Mining follows a level-by-level, bottom-up extraction sequence utilizing a primary-secondary stope mining strategy. Following ore extraction, both primary and secondary stopes are backfilled with high-strength cemented paste backfill (CPB) to provide regional ground support and maintain overall mine stability. All production blasting is conducted using bulk emulsion explosives. Stope extraction typically consists of an initial slot expansion blast followed by one or more production blasts to recover the remaining stope inventory. Broken ore is mucked from the lower stope access using a 10.3-yd³ (7.9-m³) battery-electric load-haul-dump (LHD) unit with an 18-tonne (19.8-short-ton) payload capacity and remote-operation capability. Ore is transported by the LHD either directly to an ore pass or to a remuck bay, where required, to optimize stope mucking productivity and minimize the impact of haulage distances on production efficiency. Development ore generated from lateral and vertical mine development activities is recovered and transported through the same material handling system as production ore. Development ore represents less than 3% of the total life-of-mine mill feed and is integrated into the production schedule as available.

13.6.2 Development

Lateral development includes interlevel ramps, level accesses, stope accesses, and short connecting drifts for ventilation, water handling, supply storage, and power. The interlevel ramp system is 18 ft wide by 19ftm high at a maximum 15% gradient for the Access ramp and a maxim 18% gradient for the Railveyor®. Level accesses are planned at 18 ft wide by 19 ft high and are mined higher at the remuck bays to allow the haul trucks to be loaded by the LHD. Stope access drifts 14.8 ft wide by 17 ft high. Stope access is oriented perpendicular to the strike of the orebody.

The lateral development is sized for the operation of the mining equipment fleet selected for the operation. The development profiles include allowances for ventilation ducting and services

13.6.3 Truck and LHD Haulage

The underground material haulage system for the Elk Creek Project combines conventional load-haul-dump (LHD) units and haul trucks during the initial development phase, including an early introduction of the Railveyor™ electric railcar haulage system. This hybrid approach provides operational flexibility during ramp and level development while transitioning to a highly efficient, low-emission primary haulage method during steady-state production. Mobile equipment utilized during early development will consistently of conventional units, with a progressive transition towards electrification as infrastructure and operational requirements evolve. The use of battery-electric equipment is central to the long-term strategy to minimize underground heat load, reduce emissions, and limit ventilation demand, consistent with the overall electrification strategy of the Project.

13.6.3.1 Development Phase Haulage

During early ramp and level development, primary muck haulage is performed using 45-tonne haul trucks. Muck is transported from remuck bays or temporary stockpile locations to surface via the service and production ramps. Haulage performance has been evaluated using first-principles cycle-time analysis that incorporates bucket capacity, fill factor, material density (broken), and varying

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haul distances along the ramps. The resulting productivity assumptions are considered appropriate for the mine planning included in this Technical Report Summary.

Mucking at the development face is carried out with 8 yd³ LHDs. The 8 yd³ bucket size provides a good match with the 45-tonne (49.6 ton) haul trucks and offers suitable versatility for ramp and crosscut development activities.

13.6.3.2 Transition to Railveyor Haulage

As underground development advances, the haulage system progressively transitions from truck-based transport to the Railveyor material-handling system. Initial Railveyor installation is planned at the 210 Level. The first operational Railveyor segment (from the 210 Level to surface) will be commissioned as part of the development program.

Once the initial Railveyor segment is operational, ore and waste material will be loaded directly onto Railveyor trains at dedicated underground loading stations, significantly reducing average trucking distances and the number of haul trucks required underground. Truck haulage will remain available as a flexible backup for development activities, waste handling, and any areas not yet served by the Railveyor system.

13.6.3.3 Production Phase Haulage

During steady-state production, the Railveyor system becomes the primary underground-to-surface haulage method. Ore and waste from the three main load levels (490L, 690L, and 930L) are transferred to the Railveyor via ore-pass systems equipped with grizzlies, arc gates, and vibratory feeders. The Railveyor operates with five 1,080 ft trains at a nominal capacity of 374 tons per hour, supporting the planned peak production rate.

At the production faces, 10 yd³ battery-electric LHDs are utilized to handle ore from stopes and deliver it to the ore passes. Haulage performance for production LHDs has been evaluated using first-principles analysis based on an average tramming distance of approximately 1,000 ft, bucket fill factors, and material density. Based on these assumptions, a fleet of up to three 10 yd³ battery-electric LHDs is expected to be sufficient to support the planned production rate at a level of confidence appropriate for the 2026 Elk Creek Study.

The primary access headings (North and South Ramps) remain available throughout the Life-of-Mine to support continued development, excavation of ore and waste passes, transfer bins, and progressive expansion of the Railveyor infrastructure.

The haulage system configuration and equipment selections described above are based on the production profiles and equipment productivity assumptions detailed in this Technical Report Summary. Final fleet sizing, Railveyor phasing, and productivity verification will be confirmed during detailed engineering once vendor data, site-specific operating conditions, and early development performance are available. The system is designed to support safe, efficient, and low-emission material movement in compliance with MSHA standards under 30 CFR Part 57, Subpart M (Machinery and Equipment).

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13.6.4 Backfilling

13.6.4.1 Normal Operation

The Paste Backfill System operator will coordinate with the Hydrometallurgical Plant, underground operations, and the TSF. During typical operation, the Paste Backfill Plant’s belt conveyor network will direct process waste from the Hydrometallurgical Plant to paste mixers for paste production. When paste backfill is required while the Hydrometallurgical Plant is offline, the system will draw process waste from the Surge Storage Facility (SSF), with the belt conveyor network reconfigured accordingly. SSF capacity will be monitored to ensure that it can absorb excess process waste should the Paste Backfill System unexpectedly go offline.

Paste backfill campaigns will be planned and documented in a Backfill Letter. The Backfill Letter will specify the paste mix design, the required quantity of paste backfill, and the destination for paste placement. Before start-up, the operator will complete a pre-operational checklist to confirm the availability of process waste, binder, and water; assess the condition of equipment; and coordinate with the Hydrometallurgical Plant, TSF, and underground supervisors. The Paste Backfill Plant operator must also confirm with the underground supervisor that stope barricades are suitable for retaining paste backfill.

Start-up will begin with a pre-flush of the Paste Distribution System (PDS) to provide confirmation that the PDS is correctly configured and sending material to the target destination. This confirmation may be provided by a camera feed at the stopes or by visual observation by workers.

Before a planned shutdown, the operator will confirm that the required quantity of paste backfill has been delivered. Once the Paste Backfill Plant ceases paste production, the operator will flush the PDS with water to remove residual paste from the piping

13.6.4.1.1 Paste Backfill Quality Control

Paste backfill will be sampled regularly to verify that it meets specification. This will include bleed water testing and UCS testing. For UCS testing, paste will be cast into cylinder molds 50 mm in diameter by 100 mm in height. Each sample set will include six cylinders, with three for 7-day breaks and three for 28-day breaks. For each paste mixer and for each paste mix design, sampling sets will be collected once per 1,000-2,000 yd³ of paste produced, or once per 12-hour shift, whichever occurs first. For every 50,000 yd³ of a given paste mix design placed, one set of UCS cylinders will be sent to a third-party laboratory for testing. Slump testing will be performed hourly to confirm that the paste meets slump and slump flow specifications.

13.6.4.2 Upset Conditions

In the event of a power outage during paste production, the system will cease operation. The operator will assess whether critical equipment has shut down safely. Selected equipment will be connected to backup power to facilitate the clearing of paste from the system to prevent it from setting. This equipment will include the flush pump to clear the PDS, sump pumps to collect paste discharged from the paste mixers and paste hoppers, the wastewater tank’s agitator and pumps, and PDS diverter valves.

In the event of a blockage in the PDS, paste operations will be immediately suspended to prevent additional material from building up and to reduce potential damage to the system. The operator must notify the Hydrometallurgical Plant supervisor and the relevant underground or TSF supervisor

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of the blockage and determine the location of the blockage. The operator will assess whether the blockage can be cleared by controlled flushing. If flushing is unsuccessful or unfeasible, the contents of the PDS may be discharged by a remotely actuated valve. Once the PDS is cleared, it must undergo a flushing sequence followed by the standard start-up procedure before operations resume.

13.6.5 Ground Support

Refer to Section 13.2.2.6 for detailed information regarding ground support.

13.6.6 Grade Control and Reconciliation

Grade control is an integral component of the long-hole stoping mining method at the Elk Creek Project. It provides confirmation of in-situ grade and tonnage ahead of extraction, supports short-term production scheduling, and enables ongoing validation of the resource block model against actual mining results. Production core drilling is conducted in advance of each production face, aligned to the planned stope geometry, to confirm grade continuity and domain boundaries prior to blasting and extraction.

In the 2026 Elk Creek Study, the Elk Creek Project has incorporated a three-stage reconciliation framework into the mine design and production schedule. Reconciliation is planned to compare (1) the long-term resource block model, (2) the short-term production (grade control) block model informed by production drilling, and (3) production actuals derived from mined tons and mill/plant feed grades. Differences between these stages are planned to be tracked on a stope by stope basis to identify systematic bias, informing ongoing calibration of estimation parameters. All detailed reconciliation procedures, sampling protocols, and acceptance criteria remain to be developed during subsequent detailed engineering. The grade control strategy described is considered appropriate to support the selected long-hole stoping method and production reporting requirements, with no material technical constraints identified that would prevent the Project development or operation.

13.7 Ventilation

The Elk Creek deposit comprises a large, near-vertical, tabular orebody. Production levels are spaced at ~131 ft (40 m) vertical intervals (sill-to-sill) across a total vertical mining span of approximately ~2,230 ft (680 m). The proposed mine layout employs a dual-ramp configuration developed from a single box cut, with each ramp terminating at its own portal.

The uppermost production horizon is the 210 Level, situated approximately ~689 ft (210 m) below surface. The two ramps are designated as follows:

•
Ramp 1 – Personnel and Equipment Access. This ramp is dedicated to the transport of personnel, equipment, and materials. It is developed to dimensions of ~18 ft (5.5 m) wide by ~19 ft (5.8 m) high at a maximum gradient of 15%.
•
Ramp 2 – Railveyor® Haulage System. This ramp accommodates the Railveyor® haulage system and is developed to the same dimensions, ~18 ft (5.5 m) wide × ~19 ft (5.8 m) high, but at a steeper gradient of up to 18%. The Railveyor system services dedicated ore and waste bin infrastructure at the 490 Level, 690 Level, and 930 Level loading points.

All remaining capital development, including footwall drifts and crosscuts (draw points), is constructed to dimensions of ~14.8 ft (4.5 m) high by ~14.8 ft (4.5 m) wide.

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The mine ventilation system is designed as a simple, unidirectional circuit. Fresh air is supplied via Ramp 1 (personnel and equipment access) and exhausted via Ramp 2 (Railveyor® decline). This configuration forms the foundation of the overall ventilation network, which has been developed using numerical modelling (VentSim) to ensure adequate airflow distribution, heat management, and air quality throughout the mine life. Return air is routed through the Railveyor decline, with split louver regulators on each level providing precise airflow control. A schematic of the proposed overall mine ventilation layout is illustrated in Figure 13‑27.

img170397038_113.jpg

Source: Dumas 2026

Figure 13‑27: Current Overall Mine Ventilation Layout

Owing to the selection of battery-electric mobile equipment and the Railveyor® haulage system, diesel particulate matter and exhaust emissions are eliminated from the ventilation design basis. Airflow requirements are therefore governed by worker comfort, heat dissipation, and velocity criteria rather than regulatory diesel standards. The system is engineered as a positive-pressure (“push”) ventilation network, with surface facilities providing conditioned intake air to address the humid continental climate of southeast Nebraska (hot, humid summers and cold winters). Detailed airflow quantities, fan configurations, auxiliary ventilation, refrigeration, heating, and control philosophy are presented in subsequent sections of this report.

13.8 Airflow Requirements

The selection of battery-electric mobile equipment and a Railveyor® haulage system have eliminated diesel particulate matter and exhaust emissions from the ventilation design basis. This has allowed

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the ventilation system to focus on providing adequate air movement for worker comfort, heat dissipation, and maintenance of overall air quality throughout the underground workings.

Consequently, airflow requirements for the Elk Creek Mine are determined solely on the basis of minimum and maximum air velocity criteria established in the Ventilation Design Criteria, rather than regulatory diesel ventilation standards. Ventilation simulation modelling (VentSim) has been performed for both the development phase and the life-of-mine (LoM) steady-state peak production scenario to quantify the required airflow quantities and confirm distribution throughout the ramp, drift, and production horizons.

The LoM steady-state model establishes a total underground airflow requirement of 240 m³/s (508,531 CFM), inclusive of modelled leakage and autocompression. This quantity represents the maximum design airflow demand and defines the duty for the surface intake fans and associated conditioning plant. A detailed breakdown of airflow by activity (development and production zones), heading type, support facilities (shops), and velocity-based allocation is provided in Table 13‑14.

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Table 13‑14: Airflow Determination

TOTAL U/G Airflow Required Steady State

Activity

Quantity

Power (hp)

Total Power (hp)

Total Power (kW)

Velocity

Area

Volume (heading)

Volume (m3/s Total)

Volume (CFM Total)

Development

Mid Zone

Jumbo

1 Dev area

8 yard LHD

Bolter

Truck TH550B

No. of Dev. Faces @ 5.5 m x 5.8 m

1

0.75

31.9

24

1.15

28

28

58298

Lower Zone

Jumbo

1 Dev Area

8 yard LHD

Bolter

Truck TH550B

No. of Dev. Faces @ 5.5 m x 5.8 m

1

0.75

31.9

24

1.15

28

28

58298

Production

Mid Zone - 5 level plus loading

Jumbo

1 Prod

8 yard LHD

1 Main Heading

Bolter

1 Secondary Heading

No. of Production Areas @ 4.5 m x 4.5 m

1

1

20.25

20

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TOTAL U/G Airflow Required Steady State

Activity

Quantity

Power (hp)

Total Power (hp)

Total Power (kW)

Velocity

Area

Volume (heading)

Volume (m3/s Total)

Volume (CFM Total)

Only 4 LH518iB 10 yard total

No. of Main Headings @ 4.5 m x 4.5 m

1

0.5

20.25

10

No. of Secondary Headings @ 4.5 m x 4.5 m

1

0.25

20.25

5

35

35

75088

Lower Zone - 7 level plus loading

Jumbo

3 Prod

8 yard LHD

2 Main Heading

Bolter

1 Secondary Heading

No. of Production Areas @ 4.5 m x 4.5 m

3

1

20.25

61

Only 4 LH518iB 10 yard total

No. of Main Headings @ 4.5 m x 4.5 m

1

0.5

20.25

10

No. of Secondary Headings @ 4.5 m x 4.5 m

1

0.25

20.25

5

76

76

160902

Air Velocity

Min

Secondary Headings

0.25 m/s (50 ft/min)

Drift size 4.5 x 4.5

1

0.25

20.25

5.06

Main Heading

0.5 m/s (100 ft/min)

Drift size 4.5 x 4.5

1

0.5

20.25

10.13

Production

1.0 m/s (200 ft/min)

Drift size 4.5 x 4.5

1

1

20.25

20.25

Development

0.75 m/s (150 ft/min)

Drift size 5.5 x 5.8

1

0.75

31.9

23.93

Shops

0.75 m/s (150 ft/min)

Drift size 5.5 x 5.8

1

0.75

31.9

23.93

Summary

Dev Areas Upper

0

0

0

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TOTAL U/G Airflow Required Steady State

Activity

Quantity

Power (hp)

Total Power (hp)

Total Power (kW)

Velocity

Area

Volume (heading)

Volume (m3/s Total)

Volume (CFM Total)

Dev Areas Lower

0

0

0

Production Areas Mid Zone

1

35

75088

Production Areas Lower Zone

1

76

160902

Main Shop

1

24

50694

Sat Shop

1

24

50694

0

Subtotal

159

337,379

Modeled Leakage and Autocompression (actual)

81

171,629

Total Underground Volume Requirement

240

508,531

Source: Dumas 2026

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

Production

4

 

 

 

 

 

 

 

 

 

 

Main Heading Development

0

 

 

 

 

 

 

 

 

 

 

Main Headings

2

 

 

 

 

 

 

 

 

 

 

Secondary Headings

2

 

 

 

 

 

 

 

 

 

 

 

8

 

 

 

 

 

 

 

 

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More detailed velocity limits, dust mitigation measures, numerical modelling results, and the integration of auxiliary ventilation are addressed in subsequent sections of this report. The airflow quantities established here form the design basis for the surface fresh-air intake system, which is sized to deliver approximately 509,000 CFM of conditioned air under peak LoM conditions.

13.8.1 Ventilation Controls

The ventilation control system for the Elk Creek underground mine has been developed to provide integrated, automated management of airflow distribution, fan operation, auxiliary ventilation, and environmental monitoring. The system ensures safe working conditions, optimizes energy consumption, and maintains compliance with regulatory requirements while supporting the unidirectional ventilation circuit described in prior sections. Complete control and monitoring of all ventilation and cooling parameters are available from the Operations Control Center (OCC) or any Human Machine Interface (HMI) connected to the Process Control Network (PCN). The architecture also supports management through the VentSim™ Control Ventilation on Demand (VOD) system. Further refinement of control logic, hardware selection, and hazard reviews will occur during detailed engineering.

13.8.1.1 Ventilation on Demand (VOD)

A Ventilation on Demand (VOD) system forms the core of the automated airflow management strategy. The VOD system utilizes real-time data from the PCN to automatically allocate sufficient ventilation throughout the mine to maintain safe working conditions. It can operate in fixed-speed mode, be scheduled to ramp up or down at shift changes or dynamically adjust based on measured flow requirements. The level of automation is user-selectable, ranging from manual control (Level 1) to advanced control strategies that optimize airflow distribution (Level 5). Level 4 incorporates vehicle tracking data to determine and control flow setpoints. These automation levels, adapted from industry-standard VOD frameworks, enable progressive implementation of demand-driven ventilation while preserving operational flexibility. The VOD package will be vendor-supplied, with final integration details confirmed during detailed design.

13.8.1.2 Surface Intake Fans

The main surface intake fans operate in flow-control mode. Fan speed is automatically adjusted via variable frequency drives (VFDs) to maintain the required total airflow into Ramp 1. This mode supports production targets while minimizing power consumption and ensuring that underground heat loads and contaminant levels remain within design limits.

13.8.1.3 Auxiliary Fans

Auxiliary fans and associated ducting deliver fresh air to development headings, production areas, and infrastructure locations. These fans are controlled remotely through the HMI or automatically through the VOD system. On/off commands may be issued manually by the ventilation engineer or executed automatically by the VOD system based on equipment and personnel presence (via scheduling, tracking data, or direct commands). Each auxiliary fan includes local start/stop buttons, remote HMI control, and full integration with VOD for remote and automatic operation. Starters are located at the nearest electrical substation and communicate directly with the PCN, allowing real-time status visibility on OCC HMIs and field devices (tablets or Wi-Fi/LTE-enabled interfaces).

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13.8.1.4 Monitoring and Control Infrastructure

Level-specific ventilation control is achieved through Air Monitoring Stations (AMSs) installed in close proximity to regulators at each mining level exit and major access points to the Railveyor haulage ramps. Each AMS includes an air flow meter, wet-bulb globe temperature compound instrument (relative humidity, barometric pressure, and dry-bulb temperature), carbon monoxide and nitrogen dioxide sensors, two electrically actuated louvers forming a split/door-type regulator, differential pressure measurement across the regulator, and regulator position feedback. The AMS flow and temperature cascade controller actuates the regulator to maintain minimum flow and maximum temperature setpoints established by the ventilation engineer or VOD system. Active and inactive levels are dynamically identified within the control system. In the event that temperature setpoints cannot be met at a level, the refrigeration plant setpoint is adjusted to deliver cooler intake air where possible. Excess airflow is managed by ramping down the refrigeration plant to raise outlet temperature toward the design setpoint.

Air Quality Stations (AQSs) provide supplementary monitoring at every level access and major decline/ramp fresh-air route (primarily on the intake side, with selected exhaust-side installations during early development). Each AQS is equipped with an air flow meter, dust (opacity) analyzer, carbon monoxide sensors, and a wet-bulb globe temperature compound instrument. Alarms are generated for dust, carbon monoxide, temperature, and low-flow conditions.

All monitoring and control data are routed through local Remote I/O (RIO) panels to the PCN, ensuring full visibility on mine HMIs, the OCC, and the VOD system. This architecture supports real-time decision-making, automated response to changing conditions, and compliance with modern mine ventilation standards for continuous environmental oversight. Detailed alarm setpoints, interlocks, and control sequences for the surface cooling plant and heating systems are addressed in subsequent sections of this report.

13.8.2 Ventilation Model

13.8.2.1 Ventilation Numerical Modelling

Two modelling stages were evaluated using VentSim Version 6.0: a development scenario extending to the 210 Level, and a Life-of-Mine (LoM) steady-state model documented in the file “Niocorp_IFU_20251117.vsm.” VentSim is an industry-standard three-dimensional mine ventilation simulation software employed globally for the analysis of airflow distribution, pressure losses, heat transfer, gas concentrations, and climatic conditions in underground mining operations.

The LoM model represents mine conditions during the steady-state peak production period. This scenario captures the combined effects of the furthest extent of the ventilation infrastructure and the highest total airflow demand, thereby defining the maximum fan duty requirements.

There is limited potential to increase airflow throughout the mine without enlarging excavation dimensions, which would result in higher capital development costs. Consequently, the total airflow rate is considered fixed. With the airflow rate established, the capacity of the ventilation system to remove heat from the underground workings is constrained. As a result, heat load becomes a primary driver of the overall mine energy demand, and climatic modelling has determined that the installation of a surface cooling plant is recommended.

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img170397038_114.jpg

Source: Dumas, 2026

Figure 13‑28: Stage 1 Development to 210 Level

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img170397038_115.jpg

Source: Dumas, 2026

Figure 13‑29: Life-of-Mine (LoM) Stage

The ventilation modelling results provide the technical foundation for the detailed design of the surface intake fans, auxiliary ventilation network, and climate-control infrastructure. These models ensure that both the early development phase and the full production phase can be ventilated safely and efficiently while highlighting the critical role of heat management in the overall mine energy balance. More detailed results, including airflow distribution, pressure profiles, and auxiliary ventilation requirements, are presented in subsequent sections of this report.

13.8.3 Ventilation Equipment

13.8.3.1 Main Surface Ventilation

The mine ventilation system is designed as a positive-pressure (“push”) system capable of delivering up to 240 m³/s (~508,000 cfm) of conditioned fresh air to the underground workings. Return air flows through the Railveyor decline, which connects directly to the ore-zone exit on each production level. Split louver regulators installed at each level provide precise control of airflow distribution throughout the mine, enabling balanced ventilation to meet varying production demands while minimizing short-circuiting and maintaining design velocities.

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The main ventilation system comprises the following key surface installations:

•
Main fresh-air supply fans, direct-fired natural-gas mine-air heaters, and bulk-air coolers.
•
Variable-frequency drives (VFDs) on all primary fans to provide operational flexibility in air-volume capacity and to allow real-time adjustment to changing production requirements.

Figure 13‑30 illustrates a typical parallel-fan installation, consisting of a refrigeration system, a direct-fired natural-gas mine-air heater, a fan, and an evase. The parallel configuration employs Howden 9250-AMF-6100 full-bladed, 1,000 HP (~745 kW) vane-axial fans. Each branch is equipped with a 4 MW (~13.5 MMBTU/hr) direct-fired natural-gas mine-air heater and 3,000 kWR (~853 RT) of refrigeration capacity. This arrangement ensures redundancy, high efficiency, and the ability to deliver conditioned intake air under the full range of seasonal climatic conditions encountered at the Elk Creek site. The main fan configuration is typical parallel installation showing refrigeration plant, direct-fired heater, Howden vane-axial fan, and evase; after Jodouin Mine Ventilation Ltd., 2026.

img170397038_116.jpg

Source: Dumas, 2026

Figure 13‑30: Main Fan Configuration

This surface ventilation infrastructure forms the primary air-supply pathway for the unidirectional circuit, integrating seamlessly with the Ventilation on Demand (VOD) control system described in Section 16.9. Detailed specifications for the refrigeration plant, heating system, and associated electrical and control interfaces are presented in subsequent sections.

13.8.3.2 Auxiliary Ventilation

Auxiliary ventilation systems are employed throughout the Elk Creek underground mine to deliver fresh air to development headings, crosscuts, draw points, ore and waste passes, and various underground infrastructure locations that are not adequately served by the primary ventilation

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circuit. These localized systems consist of vane-axial auxiliary fans connected to PVC ducting, sized to overcome frictional losses and leakage while maintaining the required airflow quantities and velocities at the working faces and enclosed areas. All auxiliary fans are fully integrated with the mine’s Ventilation on Demand (VOD) control system, enabling remote start/stop capability and automatic operation based on equipment and personnel presence. This integration supports efficient ventilation management, energy optimization, and compliance with air-quality and climatic criteria.

13.8.3.3 Development Headings

Development headings are excavated to dimensions of ~18 ft (5.5 m) wide by ~19 ft (5.8 m) high. Given ventilation lengths often exceeding ~3,280 ft (1 km) and the resulting high frictional pressure drops, twin ~1,219 mm (48-inch) PVC ducts are utilized in conjunction with 54-inch (~1,372 mm), 100 HP (~75 kW) Howden 5400-VAX-2700 fans. This configuration delivers approximately 40 m³/s (~86,000 cfm) at the face. The fans are installed in a staggered arrangement within the airway to minimize the extent of slashing required while optimizing airflow distribution.

13.8.3.4 Crosscut (Draw Points) and Ore/Waste Pass Ventilation

Crosscuts and draw points are developed to ~14.8 ft × 14.8 ft (4.5 m × 4.5 m) dimensions. To achieve the minimum required air velocity of ~100 fpm (0.5 m/s), 32-inch (~813 mm), 100 HP (~75 kW) Howden 3200-VAX-2100 fans connected to 36-inch (~914 mm) ducting are specified. These fans are sized to deliver ~22,000 cfm (10.5 m³/s) while accounting for typical duct leakage.

13.8.3.5 Substations, Sumps, and Refuge Station Ventilation

Substations, sumps, and refuge stations, also excavated to ~14.8 ft × 14.8 ft (4.5 m × 4.5 m) dimensions, are ventilated using 24-inch (~610 mm), 3 HP (~2.2 kW) Howden 2400-VAX-1800 fans with 24-inch (~610 mm) ducting to provide the required ~4,200 cfm (2 m³/s) of fresh air.

13.8.3.6 Railveyor Loadout Ventilation

The Railveyor loadout areas utilize 36-inch (~914 mm) auxiliary ventilation ducting to maintain the necessary clearance above the Railveyor assembly (minimum 74 inches (~1,880 mm) from the top of the drift) while minimizing frictional pressure losses. Appropriate fan selections and duct configurations are provided for the temporary development at the 210 Level and the permanent loading levels at the 490L, 690L, and 930L to satisfy the specific airflow and velocity requirements at each location.

The auxiliary ventilation design ensures reliable fresh-air delivery to localized work areas, complementing the main surface ventilation system and supporting safe, productive operations across all phases of mine development and production. Detailed fan performance curves, pressure-volume calculations, and integration with the overall control philosophy are addressed in subsequent sections of this report.

13.8.4 Recommended Ventilation Infrastructure

JMVL compiled a list to estimate the required quantity and locations of ventilation controls such as fans, bulkheads, large equipment air doors, man doors, and regulators. For this exercise, the Life-of-Mine (LoM) ventilation model was examined level-by-level to count required ventilation infrastructure. A summary of the required ventilation infrastructure is provided in Table 13‑15 (Infrastructure Matrix).

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Table 13‑15: Ventilation Infrastructure Matrix

Level

New Crosscut Fans

Reused Crosscut Fans

Typical Aux Duct Length to Face

36" Duct Length

Sumps / Slurry Pumps

24" Duct Length

Sump Fans

Elec Fans

24" Duct Length

Elec Sub Fans

Charging Stations

24" Duct Length

Charging Station Fans

Ore/Waste Feed Conveyor

24" Duct Length

Conveyor Fans

Refuge Station

QTY

QTY

FT

FT

QTY

FT

QTY

QTY

FT

QTY

QTY

FT

QTY

QTY

FT

QTY

QTY

Surface

0

0

0

0

2

164

2

5

410

5

0

0

0

0

0

0

0

210L

6

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

250L

6

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

290L

6

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

330L

6

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

370L

6

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

450L

6

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

490L

6

0

0

0

1

82

1

0

0

0

0

0

0

0

0

0

0

530L

6

0

0

0

1

82

1

1

82

1

0

0

0

0

0

0

0

570L

6

0

0

0

0

0

0

1

82

1

0

0

0

0

0

0

0

610L

0

6

492

2953

1

82

1

1

82

1

1

82

1

0

0

0

0

650L

0

6

1312

7874

2

164

2

1

82

1

1

82

1

0

0

0

1

690L

0

6

1115

6693

0

0

0

1

82

1

0

0

0

0

0

0

0

730L

0

6

820

4921

0

0

0

1

82

1

0

0

0

0

0

0

1

770L

0

6

1230

7382

0

0

0

1

82

1

0

0

0

0

0

0

0

810L

0

6

984

5906

0

0

0

1

82

1

0

0

0

0

0

0

0

850L

0

6

656

3937

0

0

0

1

82

1

1

82

1

0

0

0

0

890L

0

6

820

4921

2

164

2

1

82

1

1

82

1

1

82

1

0

930L

0

6

558

3346

1

82

1

1

82

1

0

0

0

0

0

0

0

Level

24" Duct Length

Refuge Fans

Loadout Fan Power

36" Loadout Ducting Length

Ore/Waste Pass Fan

36" Duct Length

Ore/Waste Pass Fan

Intake Fans 9250-AMF-6100

Heaters

Bulk Air Coolers

Condenser Cooling Towers

Chillers (3.5 MWR)

Evap and Cond Pumps

Regulators

Bulkheads

Personnel Door

Airlock Door

FT

QTY

kW

FT

QTY

QTY

QTY

QTY

QTY

QTY

QTY

QTY

QTY

QTY

QTY

QTY

QTY

Surface

0

0

0

0

0

0

0

2

2

2

2

2

4

0

2

2

2

210L

0

0

13

656

0

0

0

0

0

0

0

0

0

1

1

2

2

250L

0

0

0

0

1

50

1

0

0

0

0

0

0

2

2

1

0

290L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

330L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

370L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

450L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

490L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

530L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

570L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

610L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

650L

25

1

40

1841

1

50

1

0

0

0

0

0

0

1

1

1

0

690L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

730L

25

1

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

770L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

810L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

850L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

890L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

930L

0

0

0

0

1

50

1

0

0

0

0

0

0

1

1

1

0

Source: Dumas, 2026

221 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

 

The infrastructure comprises auxiliary fans of various diameters and power ratings with associated PVC ducting to supply fresh air to development headings, crosscuts and draw points, Railveyor loadout facilities, substations, sumps, and refuge stations. Split louver regulators are specified at strategic locations to enable precise regulation of airflow to individual mining levels. Large equipment air doors, man doors, and bulkheads are incorporated to direct airflow, provide isolation, and maintain the integrity of the unidirectional ventilation circuit.

This infrastructure is fully integrated with the main surface ventilation system (Section 13.8.3.1) and the auxiliary ventilation network (Section 13.8.3.2). It supports the Ventilation on Demand (VOD) control philosophy (Section 13.8), ensuring reliable delivery of conditioned air to active working areas while minimizing short-circuiting, maintaining design velocities, and facilitating effective heat and contaminant management. The quantities and locations identified in the Infrastructure Matrix provide the basis for procurement, detailed design, and installation planning, with final configuration to be confirmed during detailed engineering.

The recommended ventilation infrastructure ensures compliance with safety and operational requirements across all phases of mine development and production, consistent with industry best practices for underground hard-rock mines.

13.8.5 Ventilation Power Consumption

The Life-of-Mine (LoM) ventilation scenario was evaluated in accordance with the detailed numerical modeling and infrastructure requirements presented in the Mine Ventilation Design Report prepared by Jodouin Mine Ventilation Ltd. (February 2026). This assessment accounts for all operating primary and auxiliary fans, direct-fired mine-air heaters, the surface refrigeration plant, condenser cooling towers, and associated pumps operating under steady-state peak-production conditions. The electrical consumption of the refrigeration plant is based on an equivalent of three months of full-load operation per year to reflect seasonal cooling requirements in the Nebraska climate.

The ventilation system is projected to have an instantaneous power demand of 10 MW, corresponding to an annual electrical energy consumption of approximately 78 GWh. At a revised electricity rate of US$0.0918/kWh (as of March 2026), the total annual electricity cost for the ventilation systems included in this scope is estimated at US$7.16 million. This figure comprises the following components:

•
Sump fans: US$11,286/yr
•
Electrical substation fans: US$18,059/yr
•
Charging station fans: US$4,514/yr
•
Conveyor fans: US$1,129/yr
•
Refuge station fans: US$2,257/yr
•
Loadout fans: US$86,851/yr
•
Ore and waste pass fans: US$180,939/yr
•
Primary intake fans: US$1,414,141/yr
•
Heaters (electricity portion only): US$105,754/yr (natural-gas costs excluded)
•
Bulk air coolers: US$0/yr
•
Condenser cooling towers: US$19,829/yr
•
Chillers: US$213,541/yr
•
Chiller pumps: US$63,887/yr

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

These estimates are derived from the LoM steady-state model and reflect the unidirectional push-ventilation system design, including variable-frequency drives on primary fans and auxiliary ventilation for development, production, and service areas. Actual operating costs will be subject to final equipment selection, site-specific energy tariffs, maintenance practices, and realized production schedules. The values presented herein are suitable for this level of mine planning and are consistent with the ventilation design criteria established for the Elk Creek Project.

13.8.6 Mine Air Heating

Heat inputs for the ventilation numerical model were developed in accordance with the Mine Ventilation Design Report prepared by Jodouin Mine Ventilation Ltd. (February 2026) to support the determination of both mine air heating and cooling requirements for the Elk Creek Project. These inputs form the basis for climatic modeling that establishes the required capacity of the surface direct-fired natural gas mine-air heaters.

13.8.6.1 Primary Equipment Heat

Heat generation was modeled based on primary mining equipment, including load-haul-dump (LHD) units, longhole drills, jumbo drills, secondary breakage equipment, and bolters. For the Life-of-Mine (LoM) scenario, a single truck was modeled on the ramp near the intake portal. Heat loads from underground pickup trucks and utility vehicles were combined and positioned at the top of the intake ramp.

For the development scenario, two trucks, two LHDs, and two jumbos were modeled at the advancing faces of both the Railveyor ramp and the personnel/equipment ramp.

Detailed estimates of heat output from each piece of equipment are summarized in Table 13‑14.

13.8.6.2 Railveyor Heat Loads

The total heat output from the 154 Railveyor drive stations was calculated to be 263.28 kW (898,000 BTU/hr). This heat load was uniformly distributed along the 18,674 ft (5,692 m) length of the Railveyor ramp, resulting in a linear heat generation rate of 0.04625 kW/m (0.0141 BTU/hr per ft).

13.8.6.3 Sumps, Substations, Shops, and Refuge Stations

Heat loads associated with ancillary excavations (sumps, electrical substations, maintenance shops, and refuge stations) were provided by the respective discipline work packages and incorporated into the model at representative locations.

These heat inputs were used in the ventilation and climatic simulations to confirm that the surface mine-air heating system is sized to maintain acceptable underground working temperatures under design winter conditions. The heaters form an integral part of the positive-pressure ventilation system and operate in conjunction with the main intake fans and bulk air coolers. Actual heating requirements will be refined during detailed design based on final equipment selections, production schedules, and site-specific operating data. The values presented are suitable for planning and are consistent with the ventilation design criteria established for the project.

 

223 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Table 13‑16: Equipment Heat

Category

Equipment

Brand

Model

Underground Utilization

Qty req. Preprod

Qty. Production

Additional Information

User

Comments

Selected

Development

Bolter

Sandvik

DS412iE

☐

3

3

Electric

Contractor

x

Development

Haul Truck

Sandvik

TH550B

☐

3

1

Electric

Contractor

x

Development

Jumbo

Sandvik

DD422iE

☐

3

3

Electric

Contractor

x

Development

LHD - 10 YD

Sandvik

LH518iB

☐

4

4

Electric

Contractor

x

Development

LHD - 2 YD

Sandvik

LH203

☐

1

1

Diesel

Contractor

Low utilization

x

Development

LHD - 6 YD

Sandvik

LH410

☐

1

1

Diesel

Contractor

Low utilization

x

Development

Cable bolter

Sandvik

DS422i

☐

1

1

Diesel

Contractor

x

Light vehicle

UG Pickup - Mechanic

Kovatera

KT200

☐

1

1

Electric

Contractor

x

Light vehicle

UG Pickup - Safety Supervision

Kovatera

KT200

☐

1

1

Electric

Contractor

x

Light vehicle

UG Pickup - Survey / Engineering

Kovatera

KT200

☐

1

1

Electric

Contractor

x

Light vehicle

Utility vehicle - Electrician

Kovatera

KM200e Cable Reeler With Scissor Deck

☐

1

1

Electric

Contractor

x

Light vehicle

Utility vehicle - Explosives transport

Kovatera

KT200

☐

1

1

Electric

Contractor

x

Light vehicle

Utility vehicle - Face cleaning

Kovatera

KM200e Mine Utility Vehicle c/w fork and lift

☐

1

1

Electric

Contractor

x

Light vehicle

Utility vehicle - Loading

Kovatera

KM200e Mine Utility Vehicle c/w basket and anfo

☐

2

2

Electric

Contractor

x

Light vehicle

Utility vehicle – Man carrier

Kovatera

KT300e Personnel Carriers - Closed Box 2+8

☐

2

3

Electric

Contractor

x

Light vehicle

Utility vehicle - Mechanic

Kovatera

KT300e Mobile Mechanical Support w crane

☐

1

1

Electric

Contractor

x

Light vehicle

Utility vehicle - Mechanic

Kovatera

KT300e Mobile Mechanical Support w crane

☐

1

1

Electric

Owner

x

Light vehicle

Utility vehicle - Mine Rescue

Kovatera

KT300e Mine Rescue - Closed Box

☐

1

1

Electric

Contractor

x

Light vehicle

Utility vehicle - Service

Kovatera

KM200e Mine Utility Vehicle c/w fork and backhoe

☐

1

1

Electric

Contractor

x

Light vehicle

Utility vehicle - Supervision

Kovatera

KT300e Mine Utility Vehicle - flat deck

☐

1

1

Electric

Contractor

x

Light vehicle

Utility vehicle - Supervision

Kovatera

KT300e Mine Utility Vehicle

☐

3

5

Electric

Owner

x

Other

SatStat - Fuel

Rock-Tech

SE90 0F

☐

1

1

Electric

Contractor

x

Other

SatStat - Lube

Rock-Tech

SE90 0L

☐

1

1

Electric

Contractor

x

Production

Raise bore

Epiroc

Easer E10SG

☐

0

1

Electric

Contractor

x

Production

Longhole

Sandvik

DL422iE

☐

1

3

Electric

Contractor

x

224 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Category

Equipment

Brand

Model

Underground Utilization

Qty req. Preprod

Qty. Production

Additional Information

User

Comments

Selected

Production

Secondary breaking drill

Sandvik

DB331

☐

0

1

Diesel

Contractor

Low utilization

x

Supporting

Boom truck

MacLean

BTS EV

☐

1

1

Electric

Contractor

x

Supporting

Explosives Loader - Anfo

MacLean

ACS EV

☐

1

1

Electric

Contractor

Development

x

Supporting

Explosives Loader - Emulsion

MacLean

ECS EV

☐

1

1

Electric

Contractor

Production

x

Supporting

Grader

MacLean

GRS EV

☐

1

1

Electric

Contractor

x

Supporting

Scissor lift

MacLean

SLS EV

☐

2

2

Electric

Contractor

x

Supporting

Shotcrete Sprayer

MacLean

SSS EV

☐

1

1

Electric

Contractor

x

Supporting

Transmixer

MacLean

TMS EV

☐

1

1

Electric

Contractor

x

Category

Equipment

Brand

Model

Max Speed (km/h)

Grade

Distance Up (m)

Distance Down (m)

Distance Flat (m)

Time Idle (mins)

Avg Heat Load (kW)

Development

Bolter

Sandvik

DS412iE

5

N/A

N/A

N/A

400

240

90

Development

Haul Truck

Sandvik

TH550B

15

15%

6000

6000

400

180

253

Development

Jumbo

Sandvik

DD422iE

N/A

N/A

N/A

N/A

N/A

N/A

160

Development

LHD - 10 YD

Sandvik

LH518iB

10

N/A

N/A

N/A

N/A

N/A

132

Development

LHD - 2 YD

Sandvik

LH203

10

N/A

N/A

N/A

N/A

N/A

46

Development

LHD - 6 YD

Sandvik

LH410

10

N/A

N/A

N/A

N/A

N/A

129

Development

Cable bolter

Sandvik

DS422i

N/A

N/A

N/A

N/A

N/A

N/A

75

Light vehicle

UG Pickup - Mechanic

Kovatera

KT200

15

15%

6000

6000

400

240

11

Light vehicle

UG Pickup - Safety Supervision

Kovatera

KT200

15

15%

6000

6000

400

240

11

Light vehicle

UG Pickup - Survey / Engineering

Kovatera

KT200

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle - Electrician

Kovatera

KM200e Cable Reeler With Scissor Deck

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle - Explosives transport

Kovatera

KT200

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle - Face cleaning

Kovatera

KM200e Mine Utility Vehicle c/w fork and lift

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle - Loading

Kovatera

KM200e Mine Utility Vehicle c/w basket and anfo

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle – Man carrier

Kovatera

KT300e Personnel Carriers - Closed Box 2+8

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle - Mechanic

Kovatera

KT300e Mobile Mechanical Support w crane

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle - Mechanic

Kovatera

KT300e Mobile Mechanical Support w crane

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle - Mine Rescue

Kovatera

KT300e Mine Rescue - Closed Box

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle - Service

Kovatera

KM200e Mine Utility Vehicle c/w fork and backhoe

15

15%

6000

6000

400

240

11

225 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Category

Equipment

Brand

Model

Underground Utilization

Qty req. Preprod

Qty. Production

Additional Information

User

Comments

Selected

Light vehicle

Utility vehicle - Supervision

Kovatera

KT300e Mine Utility Vehicle - flat deck

15

15%

6000

6000

400

240

11

Light vehicle

Utility vehicle - Supervision

Kovatera

KT300e Mine Utility Vehicle

15

15%

6000

6000

400

240

11

Other

SatStat - Fuel

Rock-Tech

SE90 0F

15

15%

6000

6000

400

240

11

Other

SatStat - Lube

Rock-Tech

SE90 0L

15

15%

6000

6000

400

240

11

Production

Raise bore

Epiroc

Easer E10SG

N/A

N/A

N/A

N/A

N/A

N/A

110

Production

Longhole

Sandvik

DL422iE

5

N/A

N/A

N/A

N/A

N/A

160

Production

Secondary breaking drill

Sandvik

DB331

12

N/A

N/A

N/A

400

240

48

Supporting

Boom truck

MacLean

BTS EV

10

N/A

N/A

N/A

400

240

29

Supporting

Explosives Loader - Anfo

MacLean

ACS EV

10

N/A

N/A

N/A

400

240

26

Supporting

Explosives Loader - Emulsion

MacLean

ECS EV

10

N/A

N/A

N/A

400

240

26

Supporting

Grader

MacLean

GRS EV

5

15%

6000

6000

400

0

38.2

Supporting

Scissor lift

MacLean

SLS EV

10

N/A

N/A

N/A

400

240

29

Supporting

Shotcrete Sprayer

MacLean

SSS EV

10

N/A

N/A

N/A

400

240

30

Supporting

Transmixer

MacLean

TMS EV

10

15%

6000

6000

400

0

59.1

Source: Dumas, 2026

 

226 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

13.8.7 Thermal Exposure

The ventilation and cooling system for the Elk Creek Project has been designed to control thermal exposure and maintain underground workplace ambient conditions within acceptable limits for worker health and safety. Design underground workplace conditions, as established in the Ventilation Design Criteria (Jodouin, 2025), are as follows:

•
Maximum dry-bulb temperature: ~104°F (40.0°C)
•
Maximum wet-bulb temperature: ~82.4°F (28.0°C)
•
Maximum reject Wet-Bulb Globe Temperature (WBGT): ~82.4°F (28.0°C)

Refrigeration is incorporated into the ventilation system when wet-bulb temperatures exceed ~80.6°F (27.0°C).

Climatic modeling performed using VentSim™ Version 6.0 for both the development stage and the Life-of-Mine (LoM) steady-state scenario, as documented in the Mine Ventilation Design Report (Jodouin, 2026), incorporated all major heat sources, including primary mobile equipment, the Railveyor haulage system, sumps, substations, shops, refuge stations, geothermal heat from the rock mass, and auto-compression effects. The modeling confirmed that a surface refrigeration plant and bulk air coolers are required to manage the combined heat loads under peak summer conditions. The positive-pressure (“push”) ventilation system supplies conditioned air via the personnel and equipment ramp (Ramp 1), ensuring that design thermal limits are maintained at the working faces and throughout the active production areas.

The integrated heating, ventilation, and cooling strategy—comprising surface direct-fired natural-gas mine-air heaters for winter operation and the refrigeration plant with bulk air coolers for summer operation—provides effective thermal exposure management across the full vertical mining span of approximately ~2,230 ft (680 m). These engineered controls, together with the unidirectional ventilation circuit and auxiliary ventilation systems, ensure compliance with the specified thermal criteria under both development and full-production conditions.

The thermal exposure parameters and associated system capacities are suitable for planning at the level of the 2026 Elk Creek Study. Final verification and refinement of refrigeration loads, control setpoints, and system performance will be completed during detailed engineering based on confirmed equipment selections, production schedules, and site-specific monitoring data.

13.9 Mine Infrastructure and Services

13.9.1 Material Handling System

The material handling system for the Elk Creek Project consists of a fully electric, automated Railveyor haulage system that transports ore and waste from underground loading stations to surface discharge points. The system comprises underground loading stations, the Railveyor railcar haulage network (including the dedicated Ramp 2), two surface discharge loops (one for ore and one for waste), a surface railcar maintenance facility, and associated track switches, bypass spurs, and control infrastructure. Ore is transferred from the surface stockpile to the crusher circuit by wheel loaders, while waste is stockpiled separately. All components are described in detail in the NioCorp – Elk Creek Project Material Handling Engineering Study (Railveyor Technologies Global Inc., 2026),

227 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

which was prepared specifically for the 2026 Elk Creek Study and is illustrated in the schematic shown in Figure 13‑31.

The Railveyor system is a shuttle configuration utilizing lightweight railcars propelled by stationary electric drive stations along a light-gauge track. The system is controlled by a centralized automation platform and is designed to operate continuously and autonomously. The south portal Ramp 2 is dedicated exclusively to the Railveyor and has been developed at an 18% grade with nominal dimensions of ~18 ft (5.5 m) wide by ~19 ft (5.8 m) high.

The system has a Life-of-Mine (LoM) capacity of 48.8 million short tons (~44.3 million metric tonnes) of ore and 5.4 million short tons (~4.9 million metric tonnes) of waste. It is sized to sustain a nominal production rate of 5,500 short tons per day (~4,990 metric tonnes per day) based on a 16.2-hour daily operating schedule, with a peak continuous capacity of 340 short tons per hour (~308 metric tonnes per hour) using five trains, each 1,080 ft (~329 m) in length at full mine build-out. The trains are powered by a total of 154 drive stations strategically located along the route to provide the required tractive effort for starting, stopping, and continuous movement under full load.

The Railveyor system is installed in a phased manner to align with mine development and production ramp-up. During the development phase, temporary loading points are established at the 210L horizon using mobile feeders (e.g., Terex or equivalent) supplied by haul trucks or LHDs. Production loading occurs at the three primary load levels (490L, 690L, and 930L), each equipped with two ore-pass discharge points (one for ore and one for waste). Ore passes are fitted with 16 in. × 16 in. (~406 mm × 406 mm) grizzlies, arc gates, high-speed vibratory feeders, discharge chutes with scalper bars, and overhead tramp-metal magnets. Weigh scales and light-fence profile monitors downstream of each feeder ensure trains are loaded to design capacity without overloading.

Loaded and empty trains pass each other in four automated bypass spurs located along the ramp. Each bypass is equipped with automated track switches that allow the loaded train to remain on the mainline while the empty train diverts to the offset track. On surface, automated track switches direct trains to the appropriate discharge loop (ore or waste). The discharge loops are constructed on engineered earth ramps with retaining walls and elevated steel skid structures. Material is discharged by inverting the train around the loop; the empty train then reverses direction and returns underground. A separate maintenance loop and 40 ft × 100 ft (~12.2 m × 30.5 m) maintenance shop are located west and south of the portal to allow complete trains to be removed from the production circuit for servicing.

Each train consists of individual railcars connected by clevis pins and spherical bearings to permit articulation through horizontal and vertical curves and the discharge-loop inversion. Cars are equipped with rubber-lined steel troughs. The lead and trailing cars incorporate rail-sensing instrumentation and communication equipment. Each drive station comprises two 100 hp (~75 kW) AC motors driving gearboxes fitted with commercial truck tires that apply squeeze traction to the sides of the train. Spring-applied/electric-release brakes provide parking and emergency stopping capability. Variable-frequency drives (VFDs) located in electrical control cabinets (ECCs) control the motors, with regenerative braking utilized to reduce energy consumption.

System control is achieved through four programmable logic controllers (PLCs) networked via fibre-optic cable. One PLC functions as the master, coordinating all drive stations, track switches, feeders, scales, and safety devices. Operator interface is provided by a SCADA system located in the surface Underground Control Center (UCC). Closed-circuit video (CCTV) cameras at drive stations, switches, load points, and discharge points allow real-time monitoring.

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The Railveyor material handling system provides a reliable, low-maintenance, and energy-efficient means of underground-to-surface haulage that is fully integrated with the mine’s phased development schedule and production requirements. The design parameters and capacities summarized above are based on the engineering study completed for the 2026 Elk Creek Study and are suitable for planning purposes. Final system performance will be confirmed during detailed design, procurement, and commissioning once vendor data, site-specific geotechnical conditions, and operating experience are incorporated.

img170397038_117.jpg

Source: Dumas, 2026

Figure 13‑31: Railveyor System Schematic

13.9.2 Mine Dewatering System

The mine dewatering system for the Elk Creek Project has been designed to manage both surface precipitation entering the box-cut area and groundwater ingress plus operational water from the underground workings, thereby preventing flooding and maintaining safe, dry operating conditions throughout the Life-of-Mine (LoM). The system comprises surface portal pump stations, temporary mobile underground pump stations, permanent underground pump stations, associated sumps, pipelines, and vertical boreholes. Design parameters and capacities are based on the engineering completed for the 2026 Elk Creek Study.

Surface dewatering is provided to intercept and remove precipitation from the box-cut excavation before water can enter the service (Ramp 1) or production (Ramp 2) portals. The portal pump-station capacity is based on the 10-year, 24-hour design storm event for the Tecumseh, Nebraska area (4.71

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in. or ~120 mm of precipitation). The box-cut area of 509,135 ft² (~47,300 m²) generates a peak runoff of 1,040 gpm (~236 m³/h).

A settling sump collects runoff and removes solids prior to gravity feeding into a clear-water sump. Four operating submersible pumps (plus one spare) are installed in the clear-water sump and are sized to handle flows up to 1,000 gpm (~227 m³/h). Discharge is routed to the site stormwater management pond for discharge or reuse as process water.

The portal and the associated pumping infrastructure are currently under construction and are expected to be completed before project Final Investment Decision (FID).

Underground dewatering collects natural groundwater inflow from rock faces together with water introduced by mining and development activities. The combined maximum inflow is estimated at 1,500 gpm (~341 m³/h). The net average inflow consists of 200 gpm (~45 m³/h) of formation water and an additional 200 gpm (~45 m³/h) of water used for mine operations purposes.

The groundwater at the Elk Creek site is expected to exhibit moderate to high salinity (brackish character with elevated total dissolved solids, primarily chlorides and sodium), consistent with hydrogeological characterization data for the deposit. In addition, mine water will contain residues from explosives (such as nitrates) and trace machinery oil/hydrocarbons introduced during development and production activities. These constituents are addressed through the dewatering system design, which includes settling sumps for solids and oil separation, followed by transfer to the surface holding pond. Final treatment occurs in the site water-treatment plant, which may incorporate processes such as softening, clarification, multimedia filtration, and reverse osmosis to manage salinity and remove contaminants prior to reuse in process circuits or other site applications. This integrated approach ensures compliance with water quality requirements and supports the project’s zero-discharge objectives.

Water is collected in sumps installed along both the service and production ramps. Boreholes convey water from higher-level sumps to the respective pump-station horizons, where it is directed into settling sumps for solids removal. Horizontal transfer pumps then move the clarified water to the main vertical pumping stations.

The system incorporates both temporary and permanent pumping infrastructure phased to match mine development:

•
Temporary Mobile Pump Stations (210 Level and 650 Level): Skid-mounted centrifugal pump stations (six pumps operating in pairs) with 2,640 gal (~10,000 L) integrated tank capacity provide variable flow up to 1,500 gpm (~341 m³/h). These units are deployed as required during early development. Water from the 210 Level station is pumped to surface via pipeline installed in the production ramp. Water from the 650 Level station is pumped to the permanent 450 Level station through a vertical borehole.

 

•
Permanent Pump Stations (450 Level and 930 Level): Each station is equipped with four positive-displacement pumps sized for variable flow up to 1,500 gpm (~341 m³/h).
o
The 450 Level station pumps water to surface: first via vertical borehole to the 210 Level, then continuing up the production ramp pipeline.
o
The 930 Level station pumps water to the 450 Level station via vertical borehole.

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•
Bottom-Level (930 Level) Pumping: Submersible pumps located at the lowest mine elevation transfer dirty water to the 930 Level settling sump through a dedicated vertical borehole.

All underground water is ultimately delivered to the surface holding pond, where it undergoes treatment in the site water-treatment plant prior to reuse in process circuits. The dewatering design ensures that pump capacities exceed maximum anticipated inflows under both development and full-production scenarios, providing operational flexibility and redundancy.

The system parameters summarized above are consistent with the project’s design basis and will be refined during detailed engineering on the basis of final geotechnical data, confirmed inflow measurements, equipment vendor data, and site-specific operating experience.

13.9.3 Compressed Air System

The compressed air system for the Elk Creek Project is designed to supply clean, dry, pressurized air to underground workshops, active mining areas, Railveyor loading-station dust-suppression systems, and refuge shelters (as an emergency backup air supply). The system is located in Facility 23, the surface Underground Electrical Maintenance Substation and Compressor Facility, in accordance with the Basis of Design – Electrical Generator Power (Dumas / NioCorp, Rev A, January 2026).

Compressed air is generated by two 150 hp air compressors (one operating, one standby) rated to deliver air at 125 psi (862 kPa) with a total system capacity of up to 600 cfm (1,020 m³/h). The compressors are equipped with variable-speed drives (VSDs) to optimize energy efficiency and respond to fluctuating demand. Each unit includes integrated filtration and a refrigerant dryer to condition the air. A dry-air receiver is provided to stabilize system pressure and minimize compressor cycling.

Distribution piping is routed down the production ramp (Ramp 2) to serve the underground operations, with temporary piping installed in the service ramp (Ramp 1) during early development. Branch lines are provided at each mine level. Water drains are installed at every level and at all sumps to remove accumulated condensate from the air lines.

Point-of-use treatment is provided as follows:

•
Filter-regulators at refuge stations on the 450, 610, 730, and 850 levels.
•
Filter-regulators at the Railveyor dust-suppression systems on the 490, 690, and 930 levels.
•
Filter-regulator-lubricators (and, where required, small local air receivers) at the maintenance shops on the 450 and 650 levels to support pneumatic tools.

The compressed air system is fully integrated with the surface facilities and underground infrastructure. The design parameters summarized above are based on engineering appropriate for the 2026 Elk Creek Study. Detailed piping design, pressure-drop calculations, and final equipment selection will be completed during the detailed design phase, incorporating vendor data, confirmed operating requirements, and site-specific conditions.

13.9.4 Underground Water Supply

The underground process water supply system for the Elk Creek Project supplies water to underground workshops, active mining areas, Railveyor loading-station dust-suppression systems, foam-type fire suppression systems in the maintenance shops, latrines, and refuge shelters.

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Process water is sourced from reclaimed water produced by the surface water treatment plant and supplemented by externally sourced water as required. The system is designed to deliver a supply capacity exceeding 500 gpm (114 m³/h) at a pressure range of 45 to 80 psi (310 to 552 kPa).

Distribution piping is installed down the production ramp (Ramp 2) to serve all underground levels, with temporary piping provided in the service ramp (Ramp 1) during early development. Branch lines are provided at each mine level. Pressure-reducing valves are installed at each level to regulate pressure increases resulting from hydrostatic head with depth and to protect equipment and piping infrastructure.

The process water system is fully integrated with the surface water management and dewatering facilities. All underground water is ultimately delivered to the surface, treated, and made available for reuse. The design parameters summarized above are based on engineering appropriate for the 2026 Elk Creek Study. Detailed hydraulic calculations, final pipe sizing, pressure-drop analysis, and valve specifications will be completed during detailed design once vendor data, confirmed flow requirements, and site-specific operating conditions are incorporated.

13.9.5 Underground Fuel Storage and Distribution

The Elk Creek Project is designed as a highly electrified underground operation utilizing the Railveyor™ electric haulage system and a predominantly battery-electric mobile equipment fleet. Dedicated battery swap, storage, and charging bays are incorporated to support battery-electric vehicles (BEVs) throughout the Life-of-Mine (LoM).

To support the project’s battery-electric mobile equipment fleet (including loaders, trucks, drills, bolters, and utility vehicles), dedicated battery swap, storage, and charging bays are provided at strategic underground locations, including proximity to maintenance shops, refuge stations, and key production levels. These facilities are designed to minimize equipment downtime, maintain high fleet availability, and integrate with the underground electrical distribution network.

Industry-proven technologies will be incorporated:

•
Automated battery exchange systems enable fully automated battery exchange in approximately three minutes. The operator remains in the cabin, and the vehicle self-swaps the depleted battery for a fully charged unit without requiring overhead cranes or additional heavy infrastructure.

 

•
Flexible opportunity charging infrastructure, including remote charge posts connected up to 948 ft (300 m) from central charging cabinets. This decentralized approach reduces tramming distances, minimizes queuing, and supports mixed-fleet compatibility.
•
Onboard charging design philosophy, which eliminates the need for extensive stationary charging bays in many applications and provides operational flexibility for production-support duty cycles.

Battery bays will include high-power chargers compatible with the selected equipment voltages, battery storage racks, fire detection and suppression systems, spill containment, forced ventilation for thermal management, and appropriate safety interlocks. The layout provides sufficient maneuvering space for safe vehicle access and egress. Charging infrastructure is sized based on equipment duty cycles, production scheduling, and electrical load distribution from the surface substations and underground power distribution system. Regenerative braking energy recovery is utilized where applicable to improve overall energy efficiency.

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The BEV charging infrastructure described above supports the project’s overall electrification strategy and phased transition to full battery-electric operations. Detailed bay configurations, charger ratings, number of bays, and battery management protocols will be finalized during detailed engineering once the final BEV fleet composition, duty cycles, and vendor-specific recommendations are confirmed. The design parameters summarized herein are based on engineering suitable for the 2026 Elk Creek Study.

13.9.6 Workshop, Maintenance Bays, and Warehouse

The Elk Creek Project includes dedicated underground maintenance workshops at the 450 Level and 650 Level to support the repair, servicing, and maintenance of mobile equipment, as well as the storage of spare parts and consumables. These facilities are sized to accommodate the battery-electric and support-equipment fleet throughout the Life-of-Mine (LoM) and are integrated with the underground electrical distribution, compressed-air, process-water, ventilation, drainage and fire-suppression systems. A temporary surface workshop will be utilized during early development until the underground facilities are commissioned.

The 450 Level workshop comprises 12 maintenance bays and includes the following dedicated areas:

•
Substation and electrical integration area
•
Office and maintenance supervision space
•
Warehouse for parts storage
•
Lube storage and handling facilities
•
Two heavy repair bays equipped with monorail hoists
•
Service bay
•
Heavy repair bay equipped with an overhead bridge crane
•
Electrical shop
•
Tire repair bay
•
Welding and Fabrication Bay
•
Combined lube and wash bay

The 650 Level workshop comprises 9 maintenance bays and includes:

•
Substation
•
Warehouse for parts storage
•
Office space
•
Lube storage
•
Service bay
•
Electrical shop
•
Heavy repair bay equipped with an overhead bridge crane
•
Tire repair bay
•
Combined lube and wash bay

Each underground workshop is equipped with a wash bay containing a water and oil separator. The wash bay is located on the downslope side of the facility to capture any water and foam discharged from the foam-type fire-suppression system in the event of a fire.

A surface workshop will be constructed and equipped with an overhead bridge crane and sufficient space to service multiple vehicles simultaneously. This facility will also include office space and personnel amenities. The surface workshop will serve as the primary maintenance area during the

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initial development phase and will be decommissioned or repurposed once the underground workshops become operational.

The conceptual layouts and functional descriptions are based on assumptions appropriate for the 2026 Elk Creek Study and are considered appropriate to support the planned battery-electric mobile equipment fleet, development sequence, and production profile. Detailed architectural, structural, and equipment specifications will be developed during detailed engineering once final fleet composition, duty cycles and vendor data are confirmed.

13.9.7 Explosives Storage

Explosives storage requirements for Elk Creek Project have been evaluated at a level appropriate for the 2026 Elk Creek Study. Facilities are planned to support safe underground development and production blasting while complying with MSHA 30 CFR Part 57 Subpart E, ATF 27 CFR Part 55 Subpart K, and Nebraska Title 272 regulations. Storage concepts incorporate guidance from the MSHA Program Policy Manual and the American Table of Distances. Final designs, locations and operating parameters will be confirmed during detailed engineering.

Surface Explosives Storage

Surface storage is planned to utilize ATF-equivalent Type 1 or Type 4 magazines located outside active portal and processing areas. Magazine siting is expected to satisfy American Tabel of Distances separation requirements consistent with ATF and MSHA guidance. A cleared safety zone of approximately 25 ft (7.6 m) surrounding each magazine is planned to reduce ignition risk.

Magazines are expected to be fire-resistant, weather-resistant, theft resistant, and vandal-resistant, with non-sparking interiors, secure locking, ventilation, grounding, and lightning protection. Separate storage is planned for detonators. Inventory control, housekeeping, and access procedures will follow MSHA and ATF requirements. Exact locations and capacities will be finalized during detailed engineering.

Underground Explosives Storage

Underground storage is expected to include central magazines and smaller day-use units such as powder chests or portable magazines. Storage locations will be selected in competent or supported ground, positioned away from active blast areas and traffic, and separated from workplaces and other facilities in accordance with MSHA underground storage guidance (approximately 200 ft minimum separation). Detonators and explosives will be stored separately.

Underground Storage concepts include restricted quantities, adequate ventilation, housekeeping, non-sparking materials, and routine inspection/inventory procedures. Day-use powder chests or portable units are planned near active faces to minimize transport distances. Inventory will be managed on a just-in-time basis to limit on-site quantities.

Safety, Security and Operational Considerations

Explosives storage strategies are intended to support safe blasting operations while minimizing on-site inventories through controlled supply and just-in-time delivery. Storage and handling concepts are integrated with the Project’s ventilation, traffic management, access control, and emergency response framework. Hazards will be managed through engineering controls, administrative procedures, training, and regulatory compliance. Detailed procedures and emergency response plans will be developed during detailed engineering.

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Engineering Maturity

Explosives storage concepts reflect engineering accuracy appropriate for the 2026 Elk Creek Study and are considered sufficient to support evaluation of the Project’s technical and economic viability. No material explosives storage related constraints have been identified. Final magazine designs, capacity, siting, security features, and regulatory submissions will be completed during detailed engineering prior to construction and operation. All parameters are based on planning consistent with the Project’s safety and environmental design criteria.

13.9.8 Refuge Stations

The Elk Creek Project incorporates a network of permanent built-in refuge stations and portable refuge chambers to provide safe, breathable environments for underground personnel in the event that immediate egress via the primary escapeways is compromised. The refuge station network consists of two (2) permanent built-in refuge stations and three (3) portable refuge chambers, consistent with the Project cost estimate. Refuge facilities are designed and will be operated in full compliance with Mine Safety and Health Administration (MSHA) mandatory standards for underground metal and nonmetal mines under 30 CFR § 57.11050 (Escapeways and refuges), 30 CFR § 57.11052 (Refuge areas), and 30 CFR § 57.11054 (Communication with refuge stations).

Refuges are positioned such that they can be reached within 30 minutes from any workplace. The design follows MSHA Program Policy guidance and industry best practices. Nebraska state oversight of underground mining safety aligns with these federal requirements. The combination of built-in and portable stations, together with the dual ramp escapeway system, provides comprehensive emergency shelter coverage across the mine.

Built-in Refuge Station

Permanent built-in refuge stations are integrated into the mine infrastructure at strategic locations along the main ramps and production levels. At the current planning stage, stations are located at the 650 Level and 850 Level. These stations are constructed as hardened, airtight rooms or alcoves in competent or supported ground and located off primary travel ways to provide protection from blast effects, fire, smoke and mobile equipment traffic. Each station includes dedicated connections to the underground compressed-air system (including filter-regulators for emergency backup air) and the process-water supply. Typical features include independent ventilation, lighting, sanitation facilities, first-aid supplies, emergency rations, and communication links to the surface Underground Control Center. The built-in stations provide long-duration shelter capability consistent with the project’s escapeway design and are sized to accommodate the expected number of personnel in each mining block consistent with the mine’s emergency response design philosophy.

Portable Refuge Stations

Portable refuge chambers (also referred to as refuge alternatives) will be deployed during the development phase and in active production areas to supplement the permanent built-in network. These MSHA-approved mobile units are typically steel-constructed chambers equipped with self-contained life-support systems, including breathing-air supply, carbon-dioxide scrubbing, temperature and humidity control, food, water, sanitation, and monitoring equipment. They are designed to provide a minimum 96-hour survival period for a designated number of miners and can be relocated forward with advancing development and production faces. Portable chambers will be positioned to ensure that miners can reach one within 30 minutes from any working place, in

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accordance with 30 CFR § 57.11050(b). They will be maintained, inspected, and tested in accordance with manufacturer recommendations and MSHA guidelines.

Integration with Emergency Response and Engineering Maturity

Refuge stations form an integral component of the Project’s overall emergency response framework, which includes multiple escapeways, ventilation controls, underground communications, the surface control room, and mine rescue capability. Operational practices include routine inspection, maintenance, testing, and readiness verification of refuge facilities in accordance with regulatory requirements and manufacturer recommendations. Access, signage, and training related to refuge station use are incorporated into workforce training and emergency preparedness programs.

Refuge station concepts described in this section reflect engineering accuracy appropriate for the 2026 Elk Creek Study and are considered appropriate to support evaluation of the Project’s technical and operational viability. Final refuge station specifications, capacities, exact locations, life-support configurations, and inspection and maintenance procedures will be completed during detailed engineering and finalized prior to commencement of underground operations in consultation with MSHA.

13.9.9 Surface Electrical Distribution

Electrical power for the Elk Creek Project is supplied by a contract power generation facility provided by Liberty, located on the north side of the project site, to the main surface mine substation. From there, power is distributed underground at 13.8 kV to the Underground Electrical Maintenance Substation and Compressor Facility (Facility 23), which serves as the primary surface electrical distribution hub. Facility 23 also supplies power to selected surface facilities, specifically:

•
Facility 31A – Mine Dry, Underground Control Center, and First Aid Facility
•
Facility 31B – Railveyor Maintenance Facility
•
Facility 31C – Battery Charging and Maintenance Facility
•
Facility 31D – Mine Ventilation Plant

The switchgear lineup in Facility 23 is configured in a main-tie-main arrangement. Under normal operating conditions, the tie breaker remains closed, creating a common bus that is segmented into two distribution sections. This configuration provides operational flexibility for maintenance and isolation while ensuring continuity of service during fault conditions and maintaining power to essential loads.

Loads have been categorized into two principal sections to support power reliability planning:

(1)
Safety-Critical and Operational Infrastructure (Section A), and
(2)
Production, Surface Facilities, and Haulage Systems (Section B).

These categories were used to evaluate power continuity requirements during an unplanned utility outage. There will be no dedicated on-site emergency backup generators. For construction, Liberty will provide 6 × 2.5 MW units, with 4 running and 2 on standby. For operations, Liberty will provide 20 × 2.5 MW units, with 16 running at peak load along with 4 on standby. This level of redundancy ensures that standby units can be brought online in 5–6 minutes, eliminating the need for separate backup generators while maintaining continuity of service to critical loads.

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Facility 23 distributes power to the underground mine electrical infrastructure via redundant feeders routed through both the service ramp (Ramp 1) and the production ramp (Ramp 2). This dual-path strategy enhances system reliability for critical underground loads.

The surface electrical distribution system is described in detail in the Basis of Design – Electrical Power Distribution (Document 4498-BOD-PWR-A-RI, Rev A, January 2026) and is illustrated on the associated single-line diagrams (Drawings 4498-E-840 and 4498-E-841). The design provides a robust, maintainable, and redundant power supply suitable for the full Life-of-Mine (LoM) production schedule. Final equipment ratings, protective relaying, and arc-flash studies will be completed during detailed engineering to incorporate vendor data, site-specific utility coordination, and updated load profiles. The parameters summarized above are based on engineering appropriate for the 2026 Elk Creek Study and are suitable for planning purposes.

13.9.10 Underground Electrical Distribution

The underground electrical distribution system for the Elk Creek Project is supplied at 13.8 kV from the switchgear lineup located in the surface Underground Electrical Maintenance Substation and Compressor Facility (Facility 23). Facility 23 receives power from the main surface power generation facility, located on the north side of the project site.

To ensure continuity of supply to safety-critical underground infrastructure, Facility 23 utilizes a main-tie-main switchgear arrangement. Under normal operation, the tie breaker remains closed, creating a common bus segmented into two distribution sections. This configuration provides operational flexibility for maintenance and fault isolation while maintaining power to essential loads.

Power is distributed underground via redundant 13.8 kV feeders routed through both the service ramp (Ramp 1) and the production ramp (Ramp 2). This dual-path strategy enhances system reliability and allows for isolation of sections without interrupting critical underground services. Underground electrical substations step down voltage as required to serve power distribution panels (PDPs), motor control centers (MCCs), lighting panels, and other equipment at standard utilization voltages, including 4,160 V, 480 V, and 208/120 V.

Loads are segregated between safety-critical infrastructure (ventilation systems, dewatering pumps, communications networks, and refuge stations) and non-critical production and haulage loads. This segregation supports reliable operation of essential systems during power disruptions. The design incorporates comprehensive grounding, protective relaying and coordination, and power quality management, including active harmonic filters to mitigate the effects of variable-frequency drives (VFDs) used throughout the mine.

The underground electrical distribution system is fully described in the Basis of Design – Electrical Power Distribution (Document No. 4498-BOD-PWR-A-RI, Rev A, January 2026) and is illustrated on the project single-line diagrams (Drawings 4498-E-840 through 4498-E-843). As a greenfield project, all underground electrical infrastructure is new and has been designed specifically for the planned production schedule and equipment fleet.

Detailed protection and coordination studies, arc-flash hazard analyses, and final equipment sizing will be completed during detailed engineering. The design parameters and configuration summarized above are based on engineering appropriate for the 2026 Elk Creek Study and are appropriate for planning purposes.

 

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13.9.11 Electrical Buried Services Distribution

The surface electrical buried services distribution system for the Elk Creek Project provides reliable, protected power delivery between the main mine substation, Facility 23 (Underground Electrical Maintenance Substation and Compressor Facility), and the other surface facilities (Facility 31A – Mine Dry/Underground Control Center/First Aid; Facility 31B – Railveyor Maintenance; Facility 31C – Battery Charging & Maintenance; and Facility 31D – Mine Ventilation Plant). The system consists of underground duct banks, cable trenches, and direct-buried cable runs designed to safeguard conductors from mechanical damage, environmental exposure, and surface activities while maintaining system integrity and operational redundancy.

Buried services are routed in dedicated cable trenches and multi-duct concrete-encased duct banks to avoid conflicts with other underground utilities, roads, and surface infrastructure. Cable trenches are detailed in the plan views of the Compressor and Electrical Building (Facility 23) and include provisions for future expansion and maintenance access. Power feeds to the underground ramps enter the portals via buried duct banks, providing dual-path redundancy through both Ramp 1 (service) and Ramp 2 (production). All buried installations are coordinated with the overall site grading and stormwater management plans.

The design and installation of buried electrical services comply with the National Electrical Code (NFPA 70), Article 300.5 (Underground Installations) and Table 300.5 (Minimum Cover Requirements), the National Electrical Safety Code (NESC) for utility coordination, and Nebraska state electrical requirements (which adopt the current NEC with state-specific amendments). Burial depths, conduit materials (typically rigid PVC or steel), separation distances, and marking practices follow these standards and MSHA best-practice guidance for surface electrical installations at metal/nonmetal mines (30 CFR Part 57, Subpart T – Electrical). Grounding, surge protection, and cathodic protection (where required for steel conduits) are incorporated to mitigate corrosion and fault hazards in the Nebraska soil conditions.

The buried services distribution system supports the project’s main-tie-main switchgear arrangement in Facility 23, ensuring that critical loads remain supplied during utility outages. As a greenfield project, all buried electrical infrastructure is newly designed and installed. Detailed trench/duct-bank profiles, cable schedules, pull-box locations, and final burial-depth verification will be completed during detailed engineering, incorporating site-specific geotechnical data and final load calculations. The parameters summarized above are based on engineering appropriate for the 2026 Elk Creek Study and are suitable for planning purposes.

13.9.12 Development Face Grouting

Probe drilling and pre-excavation grouting ahead of the development face are integral components of the ground control and water management strategy for the Elk Creek Project. These measures are implemented during ramp and level advance to identify and seal water-bearing fractures, faults, or weak zones in advance of the working face, thereby minimizing groundwater inflow, maintaining stable ground conditions, and ensuring safe, efficient development. The program is designed in accordance with MSHA mandatory standards under 30 CFR Part 57, Subpart C (Ground Control) and Subpart E (Explosives), as well as best practices outlined in the MSHA Program Policy Manual (Volume IV) and Nebraska state mining guidelines, which adopt federal MSHA requirements for metal and nonmetal underground operations.

Probe Drilling

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Probe drilling is conducted from the development face using production drill jumbos or dedicated probe rigs. Holes are drilled 100 to 150 ft (~30 to 46 m) ahead of the face on a pattern that covers the full excavation perimeter plus a safety margin. Drilling parameters, including hole diameter, spacing, and inclination, are adjusted based on real-time geological observations and water inflow data. All probe holes are logged for geology by systematic collection and visual description of rock cuttings returned to the collar at regular intervals (typically every 3 m or 10 ft), supplemented by real-time monitoring of drilling parameters (penetration rate, thrust, torque, and rotation speed) via the jumbo’s on-board instrumentation. These data enable identification of changes in rock type, fracturing, alteration, or hardness. Water pressure and inflow rates are quantified by direct measurement at the collar as drilling progresses. This practice aligns with MSHA recommendations for proactive water control and ground stability during tunnel advance (30 CFR § 57.3401 and related ground control guidelines).

Grouting

Where probe drilling indicates significant water-bearing zones or unstable ground, systematic pre-excavation grouting is performed. Grout is injected under controlled pressure through packers installed in the probe holes to permeate fractures and create an impermeable curtain ahead of the face. The grouting sequence follows a primary–secondary–tertiary hole pattern to ensure comprehensive coverage. Grout takes are monitored in real time to verify seal effectiveness before excavation resumes.

Equipment

•
Production jumbo drills or dedicated probe drill rigs for probe hole drilling.
•
High-pressure grout pumps (piston or progressive cavity type) with automated mixing and injection controls.
•
Mechanical packers and inflatable packers for hole sealing during injection.
•
Grout mixers, agitators, and delivery lines rated for the required pressures and volumes.

Materials

Primary grout materials consist of Portland cement-based mixes, supplemented by microfine cement or chemical grouts (e.g., polyurethane or silicate-based) where finer fractures or high-flow conditions are encountered. Accelerators, retarders, and superplasticizers are used as required to control set time and penetration. All materials meet MSHA-approved standards for underground use and are stored in accordance with 30 CFR § 57.6100 (Storage of Explosives and Other Materials) and best-practice guidelines for chemical handling.

Resources

Grouting operations are performed by specialized crews trained in accordance with 30 CFR Part 48. Materials are procured and stockpiled on surface with just-in-time delivery to the face to minimize inventory. Dedicated water supply and compressed air are provided from the underground utility networks. The program is integrated with the overall development schedule and ventilation plan to maintain air quality during grouting activities.

The development face grouting program described above is based on engineering appropriate for the 2026 Elk Creek Study. Final probe patterns, grout mix designs, injection pressures, and performance criteria will be refined during detailed engineering once site-specific geotechnical data from early probe drilling and laboratory testing are available. The measures ensure compliance with

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MSHA and Nebraska regulatory requirements while supporting safe and efficient ramp and level advance to the planned production depths.

13.9.13 Dust Suppression System

Dust suppression systems are provided at all underground Railveyor loading stations to control airborne dust generated during the transfer of ore and waste material from the ore passes through the vibratory feeders and discharge chutes into the Railveyor trains. Separate dry-fog dust suppression systems are installed at the ore and waste loading locations on the 490 Level, 690 Level, and 930 Level.

A dry-fog (ultra-fine mist) system is utilized at each loading station. Strategically placed air-atomizing nozzles are positioned around the material loading chute gates and vibratory feeder discharge points. These nozzles generate water droplets in the 1- to 10-micron range that agglomerate with airborne dust particles, causing them to settle back into the material stream. The dry-fog approach requires significantly less water addition than conventional water-spray systems, thereby minimizing the introduction of moisture into the ore and waste material and reducing potential impacts on material flow and downstream processing.

Each system utilizes process water and compressed air supplied from the underground utility distribution networks. Appropriate filtration, pressure regulation, and controls are provided to ensure reliable operation. The dust suppression systems assist in maintaining respirable dust concentrations in compliance with MSHA regulatory requirements for underground metal and nonmetal mines (30 CFR Part 57, Subpart D – Air Quality).

The dry-fog dust suppression systems form an integral part of the Railveyor loading station general arrangement (Drawing 4498-G-111) and are described in detail in the NioCorp – Elk Creek Project Material Handling Engineering Study (Railveyor Technologies Global Inc., 2026). The configuration described is based on engineering appropriate for the 2026 Elk Creek Study. Final system sizing, nozzle layout, performance criteria, and integration with the ventilation system will be confirmed during detailed design once vendor data and site-specific operating conditions are incorporated.

13.9.14 Communications Systems

The communications and surveillance system for the Elk Creek Project is designed to provide reliable, continuous, and MSHA-compliant voice, data, tracking, and video coverage throughout all active underground areas, including the ramps, drifts, stopes, refuge stations, and mobile equipment. The system also supports surface facilities and enables centralized monitoring and control from the Underground Control Center located in Facility 31A.

The network architecture consists of a single-mode fibre-optic backbone supplemented by Wi-Fi access points (with LTE as an alternative technology where required) to deliver voice communications, remote equipment operation, real-time personnel and asset tracking, and video surveillance. Coverage is determined by mine geometry and operational requirements, with access points, cameras, and network switches strategically spaced to account for signal attenuation, bends in drifts, and the need for redundancy. Redundant fibre uplink paths are incorporated to eliminate single points of failure.

The system is sized to meet minimum bandwidth, latency, and device performance requirements necessary to support remote-operated equipment, fleet management systems, ventilation and dewatering controls, alarm systems, and emergency response communications. Power resilience is

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provided through uninterruptible power supplies (UPS). The communications infrastructure is described in detail in the Basis of Design – Communications & Surveillance (Document No. 4498-BOD-COM-A-RI, Rev A, January 2026) and is illustrated on the Mine Communications Architecture Diagram (Drawing 4498-E-844). As a greenfield project, all communications infrastructure is newly designed and installed. The design satisfies the requirements of 30 CFR Part 57, Subpart T (Electrical – Surface and Underground) and related MSHA Program Policy guidance for underground communications at metal and nonmetal mines.

The parameters and configuration summarized above are based on engineering appropriate for the 2026 Elk Creek Study and are suitable for planning purposes. Final system sizing, detailed cable routing, access-point placement, cybersecurity provisions, and integration with the mine automation platform will be completed during detailed engineering once vendor data, confirmed mine layout, and operational procedures are finalized.

13.9.15 Safety and Health

Safety and health considerations have been integrated into all aspects of the Elk Creek Project mine design, equipment selection, and operating assumptions at a level appropriate for the 2026 Elk Creek Study. The Project will be developed and operated in full compliance with applicable United States federal and state occupational safety and health regulations, primarily those administered by the Mine Safety and Health Administration (MSHA) under 30 CFR Part 57 (Safety and Health Standards – Underground Metal and Nonmetal Mines).

Key safety-in-design measures incorporated in the 2026 Elk Creek Study include multiple escapeways, refuge facilities, battery-electric mobile equipment selection to reduce diesel emissions and heat load, ventilation and cooling provisions, ground control measures, and centralized surface control room concept. Principal occupational hazards typical of underground hard-rock mining have been identified and considered in mine planning. Risk management will follow a hierarchy-of-controls approach.

A formal Safety and Health Management System, mine rescue capability, detailed emergency response plans, training programs, and ground control standards will be developed during detailed engineering in accordance with MSHA requirements and recognized industry practice. Based on the assessment completed in connection with the 2026 Elk Creek Study, no material safety- or health-related constraints have been identified that would reasonably be expected to prevent development or operation of the Project. Residual risks are typical of underground hard-rock mining and are considered manageable through engineering controls, administrative practices, training, and regulatory compliance.

13.9.16 Workforce

Workforce requirement for the Elk Creek Project has been estimated based on detailed, role-based Labor loading assessments prepared specifically for the 2026 Elk Creek Study cost estimate. Workforce estimates distinguish between owner-operated (Mine) personnel and contractor personnel and further segregate direct (production, development, and construction) and indirect (management, technical, maintenance and support) roles.

Workforce levels are derived from the planned production schedule, mine development rates, selected equipment fleet, and operating philosophy defined at a level appropriate for the 2026 Elk Creek Study. Staffing levels, rotations, and shift structures presented herein represent planning

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assumptions applied in mine scheduling, infrastructure sizing, and operating cost estimation and do not constitute finalized employment or contracting arrangements.

The Project is planned to operate under a hybrid owner-operator model, whereby owner-operator personnel provide core management, technical authority, safety, environmental, and key maintenance functions, while contractors perform most of the underground development, construction and production activities. Personnel training and competency assumptions are consistent with Mine Safety and Health Administration (MSHA) requirements under 30CFR Part 48 and are described in Section 13.9.15.

The Project does not contemplate construction of an on-site accommodation camp. Workforce accommodation is assumed to be provided through existing housing services, and infrastructure within the regional communities in the vicinity of Elk Creek, consistent with operating practices for mining projects located near established population centers.

13.9.16.1 Development Phase

Total workforce is estimated at approximately 297 personnel (83 owner-operated +214 contractor). Contractor personnel operate on a 14-days-on / 14-days-off, 12-hour shift rotation. Peak underground personnel on site are estimated at 115-125 persons.

13.9.16.2 Full Production Phase

Total workforce is estimated at approximately 228 personnel (84 owner-operated + 144 contractor). Peak underground personnel on site are estimated at 95-110 persons. Contractor levels decline as construction activities conclude and steady-state operations commence.

13.9.16.3 Direct and Indirect Designations

Direct personnel include equipment operators, miners, and blasters engaged in production and development face activities. Indirect personnel include supervisory, technical, maintenance, electrical, automation, logistics, safety, environmental, and administrative roles. Underground construction crews are classified as indirect for the level of planning appropriate for the 2026 Elk Creek Study, as their work is schedule-driven and not directly rate-limiting to production or development advance rates.

The 2026 Elk Creek Study cost estimate also includes the allowances for specialized, short-duration construction crews supporting vertical development, ore/waste passes, bins, and phased Railveyor system installation and commissioning. These crews are mobilized on a campaign basis, treated as indirect resources, and are not reflected in permanent site staffing levels.

Detailed role breakdowns and quantities supporting the cost estimate are provided in the project labor loading documentation. Actual staffing levels and contractor scopes will be refined during detailed engineering.

13.9.16.4 Engineering Maturity and Risk Statement

Workforce assumptions reflect engineering accuracy appropriate for the 2026 Elk Creek Study and are consistent with the mine design, development sequence, equipment selection, and automation strategy. No material workforce-related constraints have been identified that would prevent development or operation of the Project. The hybrid owner-operator model with phased contractor support is considered appropriate and achievable. Residual risks, including Labor availability and

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contractor mobilization timing, are typical of underground hard-rock projects and are considered manageable. Final workforce arrangements will be confirmed during detailed engineering and operations planning.

13.9.17 Equipment

Lateral development for the Elk Creek Project comprises the primary access ramps—the North Ramp, which provides personnel, equipment, and service access, and the South Ramp, which is dedicated to the Railveyor™ haulage system—as well as level access drives, footwall drifts, crosscuts, and other underground mine infrastructure excavations. Excavation cross-section dimensions have been established based on equipment clearance requirements, operational needs, and mine ventilation design, and are considered appropriate for the selected mining method and planned production rate.

13.9.17.1 Equipment Strategy and Fleet Basis

The underground mining equipment fleet has been sized to support the development and full-production schedules described in Section 16.5. The equipment strategy prioritizes battery-electric equipment to minimize underground emissions, heat load, and ventilation demand, consistent with the Project’s overall electrification strategy. The primary underground-to-surface material handling system is the Railveyor™ electric railcar system, which is fully integrated into the South Ramp design.

Limited temporary conventional (diesel-powered) units will be utilized during early development prior to commissioning of permanent charging infrastructure.

All mobile and fixed mining equipment is expected to comply with Mine Safety and Health Administration (MSHA) mandatory standards under 30 CFR Part 57, Subpart M, governing machinery guarding, maintenance, and safe operation. Mining equipment regulatory oversight in Nebraska defers to federal MSHA requirements, and no additional state-specific equipment standards are anticipated beyond MSHA approval and certification for underground use

13.9.17.2 Underground Haulage and Material Handling

The underground material handling system is based on a combination of load–haul–dump (LHD) units, underground haul trucks, and the Railveyor™ system. This approach is expected to provide sufficient operational flexibility during mine development and ramp-up while enabling efficient, predominantly electric material transport during steady-state operations.

During early underground development, primary haulage of development muck is planned to be undertaken using 45 t haul trucks transporting material from remuck locations to surface. Haulage performance for ramp development has been assessed using first-principles methods, incorporating assumed bucket capacities, fill factors, material densities, and estimated haulage cycle times over a range of haul distances. The resulting productivity assumptions are considered reasonable for the mine planning included in the 2026 Elk Creek Study.

As underground development advances, material haulage is expected to transition progressively from truck-based haulage to the Railveyor™ system, with initial installation planned at the 210 Level. The first Railveyor segment, extending from the 210 Level to surface, is assumed to be installed as part of the development program. Following commissioning of this initial segment, ore and waste material are expected to be transferred directly to the Railveyor using dedicated loading

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arrangements. This transition is anticipated to reduce average trucking distances, limit the required underground haul truck fleet, and improve overall haulage efficiency.

Truck haulage is expected to remain available during and after Railveyor commissioning to support ongoing development activities, waste handling, and operational flexibility. The North and South Ramps are assumed to remain the primary access headings to facilitate continued development toward the 490 Level and to support excavation of ore and waste passes, transfer bins, and permanent Railveyor loading infrastructure. These activities are expected to enable staged expansion of the Railveyor system and support ramp-up to steady-state production.

13.9.17.2.1 Load-Haul-Dump Equipment

During early underground development, 8 yd³ LHDs are planned to be used for mucking and short-distance haulage. This bucket size is compatible with the selected 45 t haul trucks and represents an appropriate balance between productivity and operational versatility for ramp and level development activities.

During the production stage, 10 yd³ battery-electric LHDs are planned for ore handling from stopes. Production haulage performance has been assessed using first-principles methods, incorporating assumed bucket capacity, fill factor, material density, and estimated cycle times based on an average haulage distance of approximately 1,000 ft. Based on these assumptions, a fleet of up to three 10 yd³ battery-electric LHDs is expected to be sufficient to support the planned peak production rate at a level of confidence appropriate for the 2026 Elk Creek Study.

13.9.17.2.2 Engineering Maturity and Implementation

The equipment strategy summarized above is considered suitable for mine planning purposes at this stage of the study. Final fleet composition, battery-electric equipment specifications, MSHA approvals, and productivity confirmation are expected to be completed during detailed engineering and early operations once vendor data and site-specific operating experience are incorporated. All equipment is expected to be maintained in accordance with MSHA Subpart M requirements and manufacturer recommendations to ensure safe and reliable operation throughout the Project life.

13.9.17.2.3 Equipment Table

A summary of the major mobile equipment planned for the development and pre-production phase and for steady-state production is provided in the accompanying equipment table. The quantities shown represent phased concurrent underground equipment required to support the planned development, ramp-up, and steady-state production schedules in Table 13‑17.

Table 13‑17: Underground Equipment

Description

Brand / Model

Project Phases

Initial Development
 

Production Ramp Up
(3 Fleet)

Production Steady state (2 Fleet)

Mechanized Bolter

975S

3

0

0

Mechanized Bolter

975 EV

0

3

2

Development Jumbo

Boomer 282

3

0

0

Development Jumbo

M20 SG

0

3

2

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Description

Brand / Model

Project Phases

Initial Development
 

Production Ramp Up
(3 Fleet)

Production Steady state (2 Fleet)

LHD - 4YD

ST4

1

1

1

LHD - 6 YD

R1600

1

0

0

LHD - 6 YD

ST10 G

0

1

1

LHD - 8 YD - Development

ST14SG

0

3

2

LHD - 10 YD - Production

ST18SG

0

1

3

Haul Truck - Development

AD 45

3

3

1

Production drilling rigs

Simba E70 SG ITH

1

3

3

Raise bore - Slot

E10 SG

1

1

1

Explosives Loader - Anfo

AC3

1

0

0

Explosives Loader - Emulsion

EC5 EV

0

1

1

Scissor lift

SL3

2

0

0

Scissor lift

SL5

0

2

2

Boom truck

BT3

1

0

0

Boom truck

BT5 EV

0

1

1

Shotcrete Sprayer

SS3

1

0

0

Shotcrete Sprayer

SS5 EV

0

1

1

Trans-mixer

TM3

1

0

0

Trans-mixer

TM5 EV

0

1

1

Mobile Batch Plant

BP EV

0

0

0

Blockholer c/w Auto Explosive Charger

BH3 EV

0

1

1

Fuel Truck

FL3

1

0

0

Lube truck

FL5 EV

1

1

0

Grader

UG 20M

1

0

0

Grader

GR5 EV

0

1

1

Häggloader

7HR

1

1

0

Telehandler

TH1055

1

1

1

Light utility EV

Landcruiser EV

8

8

8

Service tractor c/w fork and lift

MM530 EV

2

2

2

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Source: Dumas, 2026

Notes:

(1) Equipment quantities are based on assumptions appropriate for the 2026 Elk Creek Study and reflect peak concurrent operational requirements.

(2) Battery-electric equipment is assumed where technically and commercially feasible; limited temporary diesel units may be utilized during early development prior to commissioning of permanent charging infrastructure.

(3) Final equipment selection, specifications, and fleet sizes will be confirmed during detailed engineering and early operations.

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14 Process and Recovery Methods

14.1 Overview

The processing facility is designed to recover the following products from the Elk Creek Deposit: ferroniobium, scandium oxide, titanium tetrachloride, neodymium/praseodymium oxide, terbium oxide, dysprosium oxide, samarium-europium-gadolinium carbonate (“SEG”) and holmium-erbium-thulium-ytterbium-lutetium-yttrium carbonate. The facility is divided into three plants: a mineral process plant, a hydrometallurgical plant and a pyrometallurgical plant. While both the mineral processing and pyrometallurgical plants are composed of only one area. The hydrometallurgical plant is divided into 9 nine areas as follows:

(1)
AREA 100 – Ore Activation
(2)
AREA 200 – Ammonium Chloride Cycle
(3)
AREA 300 - Hydrochloric Acid Leach
(4)
AREA 400 – Sulfuric Acid
(5)
AREA 500 – Chlorination
(6)
AREA 600 – Rare Earth Elements Extraction
(7)
AREA 700 – Rare Earth Separation
(8)
AREA 800 – Chloride Recovery
(9)
AREA 900 – Sulfate Effluent Treatment

Run of mine ore is stockpiled on surface and fed to a jaw crusher. The jaw crusher product is stored in a three-bin system and conveyed to the mineral processing plant. The mineral processing plant contains a High-Pressure Grinding Roll and cone crusher in closed circuit with screens to produce a uniform –1 mm product suitable for hydrometallurgical processing.

Ore from the mineral processing unit is first activated in a rotary calciner to convert carbonate to oxides. Two of the main impurities, calcium and magnesium, are then sequentially leached and mineralized using an ammonium chloride cycle circuit. The ammonium chloride cycle leach residue, depleted in calcium and magnesium, is then subjected to a two-stage counter-current hydrochloric acid leach where iron, rare earths and scandium are solubilized.

The resulting pregnant leach solution is contacted with a DGA-6 organic solution to selectively recover rare earths and scandium. The rare earth and scandium strip liquor is then sent to the REE separation unit where the rare earth elements and scandium are separated and recovered as individual oxide or mixed-carbonate products.

The residue from the hydrochloric acid leach unit is dried before being subjected to a sulfuric acid bake where the niobium and titanium minerals are decomposed to soluble sulfate compounds. The residue from the acid bake process is leached with water and the non-soluble impurities are sent to paste backfill. The sulfate leach solution, rich in niobium and titanium, is hydrolyzed and the resulting hydrolysate, a combination of niobium and titanium compounds, is dewatered and calcined.

The calcined hydrolysate is chlorinated, converting both niobium and titanium into their respective chlorides. The vapor is then sequentially condensed and distilled to yield a pure titanium

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tetrachloride product and a crude niobium chloride product. The crude niobium chloride product is then leached using water and re-hydrolyzed to generate a niobium oxide product which is subsequently converted into ferroniobium in the pyrometallurgical plant.

The chloride effluent from REE extraction is concentrated and pyro-hydrolyzed to produce a mixed-oxide by-product, regenerating the hydrochloric acid used in the hydrochloric acid leach unit. The resulting hydrochloric acid produced by the pyro hydrolysis unit is condensed and recovered.

All sulfate effluents are combined and neutralized using a combination of calcium carbonate and quicklime to precipitate all base metals as hydroxides and generate a treated water stream.

The solid effluents from the process are recovered and sent to the paste backfill plant, where they are pumped underground as a structural paste backfill or pumped to the tailings impoundments for disposal

14.2 Process Plant Design Criteria

14.2.1 Surface Crushing, Ore Storage & Mineral Processing

The primary driver of the comminution circuit design is the dry processing of ore, which will be used to avoid an expensive drying operation prior to acid leaching.

The process design relies upon two things; receiving a primary crusher product with a characteristic particle size of (P80) 115 mm at the comminution circuit feed bin and producing feed material for the downstream hydrometallurgical processing at a characteristic particle size of (P80) 1.1 mm.

The primary crusher product will be fed to the secondary cone crusher system, operating in closed circuit with a double deck screen. The screen undersize from the cone crusher system will be fed to an HPGR unit, operating in closed circuit with another double deck screen. The HPGR screen undersize is the comminution product that will report to the hydrometallurgical process. The process design criteria are provided in Table 14‑1.

Table 14‑1: Process Design Criteria

Description

Value

Unit

Throughput and Operational Time

 

 

Non-operational Time

0

h/a

Planned Down Time

252

h/a

Unplanned Down Time

1,276

h/a

Available Time

7,232

h/a

Availability

85

%

Annual Design Throughput

1,008,129

t/a

Process Plant Throughput

125

t/h

Ore Characteristics

Average Specific Gravity

2.96

-

Moisture in Ore

5

%

Bulk Density

1.8

t/m3

Angle of Repose

37

degrees

Angle of Reclaim

60

degrees

Test Work Parameters

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Description

Value

Unit

JK Drop Weight Test

A x b - Maximum

58.4

-

A x b - Minimum

44.3

-

SMC Test

A x b - Maximum

56.4

-

A x b - Minimum

34.9

-

M,a - Design

19.7

kWh/t

Mih - Design

15.0

kWh/t

Crushability and Grindability Tests

Cwi

12.0

kWh/t

Rw, - Design

17.9

kWh/t

Bw, - Design

15.4

kWh/t

A, - Design

0.112

g

Crushing Circuit

139

t/h

Feed Rate to Secondary Crusher

Primary Crusher Product Size (Pao)

115

mm

Primary Crusher Product Size (Ploo)

203

mm

Crushed Ore Bin Reclaim Feeder Type

Vibrating Feeder

Design Feeder Capacity (Total)

160

t/h

Number of Feeders

3

-

Secondary Crusher Screen

Screen Type

Double Deck Vibratory

Number of Screens

1

-

Fresh Feed Throughput

139

t/h

Secondary Crusher Recycle Throughput

171

t/h

Total Screen Feed

311

t/h

Number of Decks

2

-

Top Deck Opening Size

50

mm

Bottom Deck Opening Size

25

mm

Product Sze (Pao)

22.4

mm

Screen Size - Area

18

m2

Secondary Crusher

Crusher Type

Cone

Average Throughput

171

t/h

Number of Units

1

-

Feed Size - Maximum (Firm)

203

mm

Feed Size (Fao)

115

mm

Close Side Setting

25

mm

Product Size (Pao)

26

mm

Selected Crusher Size

HP300 or Equivalent

-

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Description

Value

Unit

Crusher Motor Size

200

kW

HPGR Circuit

Crusher Type

HPGR

Feed Size (Fao)

22.4

mm

Fresh Feed Throughput

139

t/h

Total Throughput

198

t/h

Number of Units

1

Specific Energy Consumption

4.18

kWh/t

Selected Size

POLYCOM 14/08 - 02

Installed Power

1,000

kW

Product Size (Pao)

1.1

mm

HPGR Screen

Screen Type

Double Deck Vibratory

Number of Screens

1

-

Screen Throughput

198

t/h

Screen Recycle Throughput (to HPGR)

59

t/h

Top Deck Opening Size

6

mm

Bottom Deck Opening Size

3

mm

Product Size (Pao)

1.10

mm

Screen Size - Area

18

m2

Fine Ore Bin

Fine Ore Bin - Storage Time

48.0

h

Crushed Ore Bin - Live Capacity

6,000

t

Fine Ore Bin Reclaim Feeder

-

Feeder Type

Vibrating Feeder

Design Feeder Capacity (Total)

144

t/h

Number of Feeders

3

-

Source: Magemi Mining Inc., 2026

14.2.2 Hydrometallurgical Plant

The purpose of the Hydromet Plant is to extract the pay metals while separating them from the impurities. The process involves a series of successive unit- operations that include ore activation, leaching, purification, hydrolysis, chlorination, and solvent extraction. The hydrometallurgical process design criteria have been established based on bench, pilot, and demonstration scale test work conducted by L3 and KPM. The design criteria is also informed by similar projects and standard industry practices. The plant design criteria are provided in Table 14‑2.

Table 14‑2: Plant Design Criteria

Description

Value

Unit

Throughput and Operational Time

 

 

Available Time

7,920

h/a

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Description

Value

Unit

Availability

90.4

%

Design Throughput – Maximum

1,227,765

st/yr

Design Throughput - Average

1,109,900

st/yr

Process Plant Throughput

140.1

st/h

 

126.9

mt/h

Ore Characteristics

Average Specific Gravity

2.96

-

Moisture in Ore

5

%

Bulk Density

112.4

Lb/ft3

 

1.8

t/m3

Source: L3 Process Developments 2026

Note: The following nomenclature is used to identify the source of the process design criteria data. NCP = Calculated or established by NioCorp; L3 = Calculated or established by L3 Process Development; L3-T = Established by L3 Process Development using test work data; L3-H = Assumption made by L3 Process Development; OTH = Calculated or established by other party; LIT = Literature; SUP = Information from supplier; SGS = Calculated or established by SGS Lakefield; TBD = To be determined during the next engineering phase.

Area 100 – Ore Activation

The process design criteria for Area 100 – Ore Activation is presented as Table 14‑3.

Table 14‑3: Area 100 – Ore Activation Process Design Criteria

Equipment / Description

DATA

UNIT

SOURCE

100 - ORE ACTIVATION UNIT

 

100 - CALCINATION CIRCUIT

 

100-RCA-001 - ORE ACTIVATION CALCINER

 

 

 

Discharge Temperature

1,454

°F

L3-T

Residence Time

30

min

L3-T

110-TEG-001 - CO2 DEHYDRATATION UNIT

 

 

 

Moisture Content

saturated

%

L3

Temperature

116

°F

L3-H

Source: L3 2026

Area 200 - Ammonium Chloride Cycle

The process design criteria for Area 200 – Ammonium Chloride Cycle is presented as Table 14‑4.

Table 14‑4: Area 200 – Ammonium Chloride Cycle Process Design Criteria

Equipment / Description

DATA

UNIT

SOURCE

200 - NH4Cl Leaching Unit

200 - 1st Stage Leaching Circuit

200-TAK-005-007 - NH4Cl LEACH STAGE 1 REACTOR #1 to #3

 

 

 

Temperature

210

°F

L3-T

Pressure

Ambient

-

L3

Residence Time (each)

13.3 each

min

L3-T

Percent Solid

10

%

L3-T

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200 – 2nd Stage Leaching Circuit

200-TAK-009-011 - NH4Cl LEACH STAGE 2 REACTOR #1 to #3

 

 

 

Temperature

210

°F

L3-T

Pressure

Ambient

-

L3

Residence Time

13.3

min

L3-T

Percent Solid

10

%

L3-T

NH4Cl Solution Concentration

125

g/L

L3-T

200 - Filtration Circuit

200-FPR-012/112 - NH4Cl LEACH STAGE 2 CANDLE FILTER #1 / #2

 

 

 

    Residue Percent Solid

 

80

%

L3-H

    Assumed filtration rate

5.25

ft3/h ft2

L3-H

210 - Filtration Circuit

210-FPR-001/101 - NH4Cl LEACH FILTER PRESS #1 / #2

 

 

 

Residue Percent Solid

80

%

L3-H

220 - Crystallization Circuit

220-TAK-001 - 003 - Ca CARBONATATION REACTOR #1 to #3

 

 

 

Temperature

86

°F

L3-T

Pressure

Ambient

-

L3

Residence Time

10 each

min

L3-T

Percent Solid

3.6

%

 

pH

8

 

L3-T

CO2

30

VCFH

L3-T

220-ROW-001 – REE EFFLUENT RO SYSTEM

 

 

 

Temperature

Ambient

-

L3

Water Recovery

80%

Wt%

L3

230 – NH4Cl Makeup Circuit

230-ROW-001 – NH4Cl RECOVERY RO SYSTEM

 

 

 

Temperature

Ambient

-

L3

Water Recovery

15%

%

L3

240 - Precipitation Circuit

240-TAK-002-004 - Mg CARBONATATION REACTOR #1 to #3

 

 

 

Temperature

Ambient

-

L3

Pressure

Ambient

-

L3

Residence Time

10 each

min

L3-T

Residual Ammonium Carbonate Concentration

5

g/L

L3

250 - MgCO3 Dewatering Circuit

250-BLF-001 - Mg CARBONATE RESIDUE BELT FILTER #1

 

 

 

Residue Percent Solid

80

%

L3-H

Cake Moisture TDS

0.1

wt%

L3

260/270 – Reagent Recycle Circuit

200-TAK-002-004 - NH4Cl DEGASING TANK #1 to #3

 

 

 

Temperature

210

°F

L3

Pressure

atm

psig

L3

Residence Time

10

min

L3

Source: L3 2026

252 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Area 300 - Hydrochloric Acid Leach

The process design criteria for Area 300 - Hydrochloric Acid Leach is presented as Table 14‑5

Table 14‑5: Area 300 – Hydrochloric Acid Leach Process Design Criteria

Equipment / Description

DATA

UNIT

SOURCE

300 - HCl Leaching Unit

 

300 - 1st Stage Circuit

 

300-TAK-002/003 - 1ST STAGE HCl LEACH TANK

 

 

 

Temperature

176

°F

L3-T

Pressure

Ambient

-

L3-T

Residence Time

10 each

min

L3-T

Feed Percent Solid

27.5

%

L3-T

Disch. Percent Solid

13.8

%

L3

300 - 2nd Stage Circuit

 

300-TAK-004/005 - 2nd STAGE HCl LEACH TANK

 

 

 

Temperature

140

°F

L3-T

Pressure

Ambient

-

L3-T

Residence Time

10 each

min

L3-T

Disch. Percent Solid

15.9

%

L3

Residual Molarity

6.8

M [HCl]

L3

310 - 1st Stage PLS Filtration

 

310-CAF-001/002/101 - 1ST STAGE HCl LEACH CANDLE FILTERS

 

 

 

Cake Percent Solid

80

%

L3-T

Water Frac in Cake Moisture

99.99

wt%

L3

Wash Efficiency

70

%

L3-H

Wash Stages

3

-

L3

320 - Residue Dewatering Filtration Circuit

 

320-HYC-001 to 003 - 101/102 - DEWATERING STAGE 1 PRIMARY HYDROCYCLONE

 

 

 

D95 to underflow

10

micron

L3

Underflow Percent Solid

65

wt%

L3-H

320-CAF-001/002-101 - HCl LEACH RESIDUE DEWATERING CANDLE FILTERS

 

 

 

Cake Percent Solid

80

wt%

L3-T

Wash Efficiency

70

%

L3-H

330 - HCl Leach Residue Drying Circuit

 

330-SCH-001 - HCl LEACH RESIDUE PRE-HEATER

 

 

 

Discharge Temperature

212

°F

L3

Discharge Percent Solids

95

wt%

L3

Residence Time

20

Min

L3

253 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

330-DRY-001 - HCl LEACH RESIDUE ROTARY DRYER

 

 

 

Discharge Temperature

572

°F

L3

Discharge Percent Solids

100

wt%

L3

Residence Time

20

Min

L3

Source: L3 2026

Area 400 – Sulfuric Acid

The process design criteria for Area 400 – Sulfuric Acid is presented as Table 14‑6.

Table 14‑6: Area 400 – Sulfuric Acid Process Design Criteria

Equipment / Description

DATA

UNIT

SOURCE

400 - Acid Baking Unit

400 - Acid Bake Circuit

400-PUG-001 - ACID BAKE PUG MILL

 

 

 

Discharge Percent Solids

60

wt%

L3

H2SO4 Flow Rate Ratio

0.625:1

 

L3-T

400-KLN-001 - ACID BAKE KILN

 

 

 

Discharge Temperature

572

°F

L3-T

Residence Time

 

min

L3-T

400-SCR-001 - H2SO4 PRIMARY STAGE CONDENSING VENTURI

 

 

 

Discharge Temperature

536

°F

L3

400-SCR-001 - H2SO4 SECONDARY STAGE CONDENSING COLUMN

 

 

 

Discharge Temperature

356

°F

L3

410 - Water Leaching Unit

410 - Leaching Circuit

410-TAK-002-004 - WATER LEACH REACTOR #1 to #3

 

 

 

Temperature

176 amb to 176 maximum

°F

L3-T

Pressure

Ambient

-

L3

Residence Time

20

min

L3-T

Water Leach Solution Acidity (H2SO4)

0.3

M

L3-T

Percent Solid

30

%

L3-T

410 - Filtration Circuit

410-CAF-001/002 - WTL PLS CANDLE FILTERS

 

 

 

Cake Percent Solid

80

%

L3

Number of Stages

3

 

L3

Wash Ratio (Barren: Solids)

3 : 1

 

L3

Wash Efficiency

70

%

L3-H

254 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

420 - Dewatering Circuit

 

420-HYC-001 to 003 - 101/102 - DEWATERING STAGE 1 CYCLONE

 

 

 

Solids Fraction to Underflow

98

wt%

L3-H

Underflow Percent Solid

70

wt%

L3-H

420-HYC-004 to 006 - 104/105 - DEWATERING STAGE 2 CYCLONE

 

 

 

Solids Fraction to Underflow

98

wt%

L3-H

Underflow Percent Solid

70

wt%

L3-H

420-HYC-007 to 010 - 107/108 - DEWATERING STAGE 3 CYCLONE

 

 

 

Solids Fraction to Underflow

98

wt%

L3-H

Underflow Percent Solid

70

wt%

L3-H

420-CAF-001/002-101 - WATER LEACH RESIDUE DEWATERING CANDLE FILTERS

 

 

 

Cake Percent Solid

80

%

L3-H

Number of Wash Stages

1

 

L3

Wash Ratio (Barren : Solids)

2 : 1

 

L3

Wash Efficiency

70

%

L3-H

430 - Hydrolysis Unit

 

430 - 1st Stage Circuit

 

430-TAK-001 - STG 1 HYDROLYSIS REACTOR

 

 

 

Temperature

212

°F

L3-T

Pressure

Ambient

-

L3-T

Residence Time

20

min

L3-T

430 - 2nd Stage Circuit

 

430-TAK-002 - STG 2 HYDROLYSIS REACTOR

 

 

 

Temperature

212

°F

L3-T

Pressure

Ambient

-

L3-T

Residence Time

20

min

L3-T

440 - Barren Filtration Circuit

 

440-CAF-001/003-101 - BARREN FILTRATION CANDLE FILTER

 

 

 

Cake Percent Solid

80

%

L3-H

Number of Wash Stages

1

 

L3

Wash Ratio (Solution: Solids)

3 : 1

 

L3

Wash Efficiency

70

%

L3-H

450 - Residue Drying Circuit

 

450-RCA-001 - HYDROLYSIS CAKE CALCINER

 

 

 

Discharge Temperature

1562

°F

L3-T

255 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

S Residual Concentration

0.27

wt%

L3-T

Source: L3 2026

Area 500 – Chlorination

The process design criteria for Area 500 – Chlorination is presented as Table 14‑7.

Table 14‑7: Area 500 – Chlorination Process Design Criteria

Equipment / Description

DATA

UNIT

SOURCE

500 - Chlorination Circuit

500-CLN-001/101 - CHLORINATOR

 

 

 

Temperature

1742

°F

L3

Petroleum Coke:Feed Ratio

0.27 : 1

 

L3

Discharge Chlorine Concentration

0.25

Mole %

L3

Discharge Nitrogen Concentration

35

Mole %

L3

500 - CLN Condensation Circuit

500-SCR-001 - Nb/Fe CONDENSER

 

 

 

Temperature

267

°F

L3

Solids Fraction in Bottoms

30

Wt%

L3

500-HTX-001 - Nb/Fe CONDENSER COOLER

 

 

 

Type

Shell & Tube

 

L3

Temperature (In/Out)

 

 

 

Process Side

267 / 248

°F

L3

Utility Side

140 / 248

°F

L3

Heat Transfer Fluid

Thermal Fluid

 

L3

510-SCR-002 - TiCl4 PRIMARY CONDENSER

 

 

 

Temperature

86

°F

L3

500-HTX-002 - TiCl4 PRIMARY CONDENSER COOLER

 

 

 

Type

Shell & Tube

 

L3

Temperature (In/Out)

 

 

 

Process Side

86 / 81

°F

L3

Utility Side

68 / 86

°F

L3

Heat Transfer Fluid

Cooling Water

 

L3

500-SCR-003 - TiCl4 SECONDARY CONDENSER

 

 

 

Temperature

19.4

°F

L3

500-HTX-003 - TiCl4 SECONDARY CONDENSER COOLER

 

 

 

Type

Shell & Tube

 

L3

Temperature (In/Out)

 

 

 

Process Side

19 / 0

°F

L3

Utility Side

-20 / 0

°F

L3

Heat Transfer Fluid

Ammonia

 

L3

510 - TiCl4 Treatment Unit

 

510 - TiCl4 Degas Circuit

 

256 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

510-TAK-002 - TiCl4 DEGAS TANK

 

 

 

Temperature

277

°F

L3

Pressure

TBD

In HG

TBD

Residence Time

60

min

L3

510-HTX-002 – CRUDE TiCl4 FEED HEATER

 

 

 

Type

Tube Bundle

 

 

Temperature (In/Out)

 

 

 

Process Side

277 / 277

°F

L3

Utility Side

482 / 302

°F

L3

Heat Transfer Fluid

Thermal Fluid

 

L3

510-CND-001 - TiCl4 DEGAS TANK CONDENSER

 

 

 

Type

Finned HTX

 

L3

Temperature (In/Out)

 

 

 

Process Side

277 / 86

°F

L3

510 - TiCl4 Vaporization Circuit

 

510-TAK-004 - TiCl4 VAPORIZOR #1

 

 

 

Temperature

277

°F

L3 Experience

Pressure

TBD

In HG

TBD

Residence Time

60

min

L3

Solids Content

33.3

Wt%

L3

510-HTX-004 – TiCl4 VAPORIZOR #1HEATER

 

 

 

Type

Tube Bundle

 

 

Temperature (In/Out)

 

 

 

Process Side

277 / 277

°F

L3

Utility Side

482 / 302

°F

L3

Heat Transfer Fluid

Thermal Fluid

 

L3

510-CND-002 - TiCl4 VAPORIZOR #1 CONDENSER

 

 

 

Type

Finned HTX

 

L3

Temperature (In/Out)

 

 

 

Process Side

277 / 201

°F

L3

510-TAK-006 - TiCl4 VAPORIZOR #2

 

 

 

Temperature

277

°F

L3 Experience

Pressure

TBD

In HG

TBD

Residence Time

60

min

L3

TiCl4 Vaporization Extent

92

%

L3

510-HTX-006 – TiCl4 VAPORIZOR #2 HEATER

 

 

 

Type

Tube Bundle

 

 

Temperature (In/Out)

 

 

 

Process Side

277 / 277

°F

L3

Utility Side

482 / 302

°F

L3

Heat Transfer Fluid

Thermal Fluid

 

L3

257 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

510-CND-003 - TiCl4 VAPORIZOR #2 CONDENSER

 

 

 

Type

Finned HTX

 

L3

Temperature (In/Out)

 

 

 

Process Side

277 / 201

°F

L3

520 - TiCl4 Purification Unit

 

520 - TiCl4 Stripping Circuit

 

520-SCR-001 - TiCl4 STRIPPER

 

 

 

Type

Packed Column

 

L3

Reboiling Ratio (Vapor / Feed)

2.51

 

L3

Reflux Ratio (Reflux / Feed)

1.61

 

L3

520-HTX-001 – TiCl4 STRIPPER REBOILER

 

 

 

Type

Shell & Tube Thermosiphon

 

L3

Temperature (In/Out)

 

 

 

Process Side

277 / 284

°F

L3

Utility Side

482 / 302

°F

L3

Heat Transfer Fluid

Thermal Fluid

 

L3

510-CND-003 - TiCl4 STRIPPER O/H CONDENSER

 

 

 

Type

Finned HTX

 

L3

Temperature (In/Out)

 

 

 

Process Side

277 / 86

°F

L3

520 - TiCl4 Purification Circuit

 

520-COL-001 - TiCl4 PURIFICATION COLUMN

 

 

 

Type

Mixed, Packing and Trays

 

L3

Reboiling Ratio (Vapor / Feed)

1.50

 

L3

Reflux Ratio (Reflux / Feed)

0.39

 

L3

520-TAK-004 - TiCl4 PURIFICATION COLUMN REBOILER TANK

 

 

 

Temperature

284

°F

L3

Pressure

TBD

In HG

TBD

Residence Time

120

min

L3

Mineral Oil Addition Rate (Mineral Oil / Feed)

0.0014

 

L3

Bleed Rate (Bleed / Feed)

0.034

 

L3

520-HTX-004 – TiCl4 PURIFICATION COLUMN REBOILER HEATER

 

 

 

Type

Tube Bundle

 

 

Temperature (In/Out)

 

 

 

Process Side

277 / 284

°F

L3

Utility Side

392 / 374

°F

L3

Heat Transfer Fluid

Thermal Fluid

 

L3

258 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

510-CND-003 - TiCl4 PRODUCT O/H CONDENSER

 

 

 

Type

Finned HTX

 

L3

Temperature (In/Out)

 

 

 

Process Side

277 / 104

°F

L3

530 - Nb Recovery Unit

 

530 - Nb Recovery Circuit

 

530-SCH-001 - Nb/Fe CHLORIDE DRYER

 

 

 

Type

Screw Dryer

 

L3

Temperature (In/Out)

 

 

 

Process Side

267 / 464

°F

L3

Utility Side

482 / 392

°F

L3

Heat Transfer Fluid

Thermal Fluid

 

L3

Solids Discharge %

100

Wt%

L3

530-SCR-001 - TiCl4 RECOVERY CONDENSER

 

 

 

Temperature

277

°F

L3

530-HTX-001 - TiCl4 RECOVERY CONDENSER COOLER

 

 

 

Type

Finned HTX

 

L3

Temperature (In/Out)

 

 

 

Process Side

277 / 86

°F

L3

540 - TiCl4 Vapor Recovery Unit

 

540 - TiCl4 Vapor Recovery Circuit

 

540-SCR-001 - TiCl4 VENT CONDENSER

 

 

 

Discharge Temperature

81

°F

L3

530-HTX-001 - TiCl4 RECOVERY CONDENSER COOLER

 

 

 

Type

Finned HTX

 

L3

Temperature (In/Out)

 

 

 

Process Side

81 / 77

°F

L3

540-SCR-002 - TiCl4 VENT SCRUBBER

 

 

 

TiCl4 Scrubbing Efficiency

100

%

L3

Cl2 Scrubbing Efficiency

> 99

%

L3

550 - Chlorination OFF-GAS Management Unit

 

550 - CO Boiler & FGD Scrubber Circuit

 

550-TOX-001 - THERMAL OXIDIZER

 

 

 

Discharge Temperature

1,600

°F

L3

Heat Recovery Temperature (In/Out)

 

 

 

Process Side

1,600 / 284

°F

L3

Utility Side

68 / 482

°F

L3

Heat Transfer Fluid

Thermal Fluid

 

L3

550-SCR-001 - FGD SCRUBBER VENDOR PACKAGE

 

 

 

SO2/SO3 Scrubbing Efficiency

> 97

%

L3

560 - Nb Recovery Unit

 

259 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

540 - Nb Hydrolysis Circuit

 

560-TAK-001/002/003 - Nb/Fe STAGE #1/#2/#3 HYDROLYSIS TANK

 

 

 

Temperature

212

°F

L3

Pressure

Ambient

-

L3

Residence Time

30

min

L3

Steam Injection Ratio

0.55

 

L3

Dilution Ratio

3

 

L3

560-CND-001/002/003 - Nb/Fe STAGE #1/#2/#3 HYDROLYSIS CONDENSER

 

 

 

Type

Finned HTX

 

L3

Temperature (In/Out)

 

 

 

Process Side

212 / 176

°F

L3

560 - Nb Dewatering Circuit

 

560-CA-001/002 - Nb/Fe HYDROLYSIS CANDLE FILTER

 

 

 

Cake Percent Solid

70

%

L3-H

Number of Wash Stages

1

 

L3

Wash Ratio (Solution: Solids)

3 : 1

 

L3

Wash Efficiency

70

%

L3-H

560 - Nb Product Calcination Circuit

 

560-RCA-001 - Nb CALCINER

 

 

 

Discharge Temperature

1,112

°F

L3

Source: L3 2026

Area 600 – Solvent Extraction

The process design criteria for Area 600 – Solvent Extraction is presented as Table 14‑8.

Table 14‑8: Area 600 – Solvent Extraction Process Design Criteria

Equipment / Description

DATA

UNIT

SOURCE

600 - REE Extraction

600 - REE Extraction

600-COL-001 - DGA-6 EXTRACTION COLUMN

 

 

 

Temperature

AMB

°C

L3-T

Capacity Factor

40

m3/(m2*h)

SUP

Efficiency / Stage per Meter

4

 

SUP

600-COL-002 - DGA-6 SCRUB COLUMN

 

 

 

Temperature

AMB

°C

L3-T

Capacity Factor

40

m3/(m2*h)

SUP

Efficiency / Stage per Meter

4

 

SUP

610 - Acid Scrub

610 - Acid Scrub

610-MSE-001|101 - DGA-6 ACID SCRUB MIXER-SETTLER

 

 

 

260 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

1:3

 

L3-T

Internal O:A Ratio

0.9:1

 

L3

Scrub Solution pH

1.5

 

L3

610 - Acid Scrub Neutralization

610-TAK-006-008 - DGA-6 ACID SCRUB. NEUT. REACTOR #1 TO #3

 

 

 

Temperature

Amb

°C

L3

Pressure

atm

psig

L3

Residence Time

60

min

L3-H

610 - Acid Scrub Filtration

610-CAF-001-003 - DGA-6 ACID SCRUB NEUT. RESIDUE FILTER #1 TO #3

 

 

 

Cake Percent Solid

 70

%

L3-H

Number of Wash Stages

2

 

L3

Wash Efficiency

80

%

L3-H

Filtrate Mg Concentration

51

g/L

L3

620 – REE Strip

620 – REE Strip

600-MSE-002-005 - DGA-6 STR 1 TO 4 MIXER-SETTLER

 

 

 

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

2:1

 

L3

Internal O:A Ratio

1.1:1

 

L3

630 - Iron Removal

630 - Neutralization circuit

630-TAK-001-003 - DGA-6 STRIP LIQ. NEUT. REACTOR #1 TO #3

 

 

 

Temperature

Amb

°C

L3

Pressure

atm

psig

L3

Residence Time

60

min

L3

630 - DGA-6 Strip Filtration

630-CAF-001-003 - DGA-6 STRIP LIQ. NEUT. RESIDUE FILTER #1 TO #3

 

 

 

Cake Percent Solid

80

%

L3-H

Number of Wash Stages

1

 

L3

Wash Efficiency

80

%

L3-H

Cake Moisture TDS

0.01

Wt%

L3

Source: L3 2026

Area 700 – Rare Earth Separation

The process design criteria for Area 700 – Rare Earth Separation is presented as Table 14‑9.

Note: The following nomenclature is used to identify the solvent extraction process stage. SAP = Saponification, EXT = Extraction, SCB = Scrubbing, STR = Stripping and SCV = Scavenging.

Table 14‑9: Area 700 – Rare Earth Separation

Equipment / Description

DATA

UNIT

SOURCE

261 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

700 - Primary Circuit

700 - Primary Circuit

700-MSE-001|01-02 – PRIMARY CIRCUIT: SAP

 

 

 

Number of Stages

2

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

2

 

L3

Internal O:A Ratio

1.1

 

L3

Extractant – Cyanex 572

35

V%

L3

Diluent – D80 Kerosene

65

V%

L3

Saponification Solution

NH4OH, NH4Cl

 

L3

700-MSE-002|01-06 - PRIMARY CIRCUIT: EXT

 

 

 

Number of Stages

6

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

0.048

 

L3

Internal O:A Ratio

1.1

 

L3

Raffinate pH

2.1

 

L3

700-MSE-003|01-16 - PRIMARY CIRCUIT: SCB

 

 

 

Number of Stages

16

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

2.56

 

L3

Internal O:A Ratio

1.1

 

L3

Scrub Solution HCl Concentration

0.70

Mol/L

L3

700-MSE-004|01-24 - PRIMARY CIRCUIT: STR1

 

 

 

Number of Stages

24

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

3.8

 

L3

Internal O:A Ratio

1.1

 

L3

262 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Strip Solution HCl Concentration

1.10

Mol/L

L3

700-MSE-005|01-06 - PRIMARY CIRCUIT: STR2

 

 

 

Number of Stages

6

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

6.53

 

L3

Internal O:A Ratio

1.1

 

L3

Strip Solution HCl Concentration

1.80

Mol/L

L3

710 - NdPr Circuit

710 - NdPr Circuit

710-MSE-001|01-02 - NdPr CIRCUIT: SAP

 

 

 

Number of Stages

2

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

2

 

L3

Internal O:A Ratio

1.1

 

L3

Extractant – Cyanex 801

35

V%

L3

Diluent – D80 Kerosene

65

V%

L3

Saponification Solution

NH4OH, NH4Cl

 

L3

710-MSE-002|01-12 - NdPr CIRCUIT: EXT

 

 

 

Number of Stages

12

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

0.066

 

L3

Internal O:A Ratio

1.1

 

L3

Raffinate pH

1.8

 

L3

710-MSE-003|01-24 - NdPr CIRCUIT: SCB

 

 

 

Number of Stages

24

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

1.99

 

L3

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Internal O:A Ratio

1.1

 

L3

Scrub Solution HCl Concentration

0.80

Mol/L

L3

710-MSE-004|01-06 - NdPr CIRCUIT: STR

 

 

 

Number of Stages

6

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

4.67

 

L3

Internal O:A Ratio

1.1

 

L3

Strip Solution HCl Concentration

1.25

Mol/L

L3

720 - Tb Circuit

720 - Tb Circuit

720-MSE-001|01-02 - Tb CIRCUIT: SAP1

 

 

 

Number of Stages

2

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

0.5

 

L3

Internal O:A Ratio

1.1

 

L3

Extractant – Cyanex 572

35

V%

L3

Diluent – D80 Kerosene

65

V%

L3

Saponification Solution

NH4OH, NH4Cl

 

L3

720-MSE-002|01-16 - Tb CIRCUIT: EXT

 

 

 

Number of Stages

16

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

0.84

 

L3

Internal O:A Ratio

1.1

 

L3

Raffinate pH

1.25

 

L3

720-MSE-003|01-12 - Tb CIRCUIT: SCB

 

 

 

Number of Stages

12

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

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Overall O:A Ratio

2.5

 

L3

Internal O:A Ratio

1.1

 

L3

Scrub Solution HCl Concentration

1.1

Mol/L

L3

720-MSE-004|01-02 - Tb CIRCUIT: SAP2

 

 

 

Number of Stages

2

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

 0.5

 

L3

Internal O:A Ratio

1.1

 

L3

Saponification Solution

NH4OH, NH4Cl

 

L3

720-MSE-005|01-32 - Tb CIRCUIT: SCV

 

 

 

Number of Stages

32

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

1.73

 

L3

Internal O:A Ratio

1.1

 

L3

Feed Solution pH

0.93

 

L3

Raffinate pH

1.2

 

L3

720-MSE-006|01-24 - Tb CIRCUIT: STR

 

 

 

Number of Stages

24

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

6.02

 

L3

Internal O:A Ratio

1.1

 

L3

Strip Solution HCl Concentration

1.30

Mol/L

L3

730 - Dy Circuit

730 - Dy Circuit

730-MSE-001|01-02 - Dy CIRCUIT: SAP

 

 

 

Number of Stages

2

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

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Overall O:A Ratio

0.5

 

L3

Internal O:A Ratio

1.1

 

L3

Extractant – Cyanex 572

35

V%

L3

Diluent – D80 Kerosene

65

V%

L3

Saponification Solution

NH4OH, NH4Cl

 

L3

730-MSE-002|01-12 - Dy CIRCUIT: EXT

 

 

 

Number of Stages

2

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

2.06

 

L3

Internal O:A Ratio

1.1

 

L3

Feed Solution pH

1.0

 

 

Raffinate pH

1.25

 

L3

730-MSE-003|01-24 - Dy CIRCUIT: SCB

 

 

 

Number of Stages

24

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

4.92

 

L3

Internal O:A Ratio

1.1

 

L3

Scrub Solution HCl Concentration

1.45

Mol/L

L3

730-MSE-004|01-06 - Dy CIRCUIT: STR

 

 

 

Number of Stages

6

 

L3

Mixer Residence Time

5

min

L3

Settler Residence Time

12.5

min

L3

Overall O:A Ratio

13.1

 

L3

Internal O:A Ratio

1.1

 

L3

Strip Solution HCl Concentration

2.5

Mol/L

L3

740 - SEG Recovery Unit

740 - SEG Carbonate Precipitation Circuit

740-TAK-002-004 - SEG CARBONATE PRECIP. TANK #1 to #3

 

 

 

Temperature

amb

°C

L3

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Pressure

atm

psig

L3

Residence Time

60

min

L3

740-CLR-001 - SEG CARBONATE CLARIFIER

 

 

 

Discharge Solids Fraction

50.0

%

L3

740 - SEG Carbonate Dewatering Circuit

740-CAF-001/101 - SEG CARBONATE CANDLE FILTER #1/#2

 

 

 

Cake Percent Solid

65

%

L3-H

Number of Wash Stages

2

 

L3

Cake Moisture TDS

0.01

Wt%

L3

Wash Efficiency

80

%

L3-H

740 - SEG Carbonate Drying Circuit

740-RD-001 - SEG CARBONATE ROTARY DRYER

 

 

 

Discharge Temperature

248

°F

L3

    Residence Time

15

Min

L3-H

750 - HREY Recovery Unit

750 - HREY Carbonate Precipitation

750-TAK-002-004 - HREY CARBONATE PRECIP. TANK #1 to #3

 

 

 

Temperature

 amb

°F

L3

Pressure

atm

psig

L3

Residence Time

60

min

L3

750-CLR-001 - HREY CARBONATE CLARIFIER

 

 

 

Discharge Solids Fraction

50.0

%

L3

750 - HREY Carbonate Dewatering

750-CAF-001/101 - HREY CARBONATE CANDLE FILTER #1/#2

 

 

 

Cake Percent Solid

65

%

L3-H

Number of Wash Stages

2

 

L3

Cake Moisture TDS

0.01

Wt%

L3

Wash Efficiency

80

%

L3-H

750 - HREY Carbonate Drying Circuit

750-RD-001 - HREY CARBONATE ROTARY DRYER

 

 

 

Discharge Temperature

248

°F

L3

    Residence Time

15

Min

L3-H

760 - NdPr Recovery Unit

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760 - NdPr Oxalate Precipitation Circuit

760-TAK-002-004 - NdPr OXALATE PRECIP. TANK #1 to #3

 

 

 

Temperature

Amb

°F

L3

Pressure

atm

psig

L3

Residence Time

60

min

L3

Residual Oxalic Acid Concentration

5

g/L

L3

760 - NdPr OXALATE Dewatering Circuit

760-CAF-001/101 - NdPr OXALATE CANDLE FILTER #1/#2

 

 

 

Cake Percent Solid

65

%

L3-H

Number of Wash Stages

2

 

L3

Cake Moisture TDS

0.01

Wt%

L3

Wash Efficiency

80

%

L3-H

760 - NdPr OXALATE Calcining Circuit

760-RCA-001 - NdPr OXALATE ROTARY CALCINER

 

 

 

Discharge Temperature

1,562

°F

L3

    Residence Time

30

Min

L3-H

770 - Tb Recovery Unit

770 - Tb Oxalate Precipitation Circuit

770-TAK-002-004 - Tb OXALATE PRECIP. TANK #1 to #3

 

 

 

Temperature

Amb

°F

L3

Pressure

atm

psig

L3

Residence Time

60

min

L3

Residual Oxalic Acid Concentration

5

g/L

L3

770 - Tb OXALATE Dewatering Circuit

770-CAF-001/101 - Tb OXALATE CANDLE FILTER #1/#2

 

 

 

Cake Percent Solid

65

%

L3-H

Number of Wash Stages

2

 

L3

Cake Moisture TDS

0.01

Wt%

L3

Wash Efficiency

80

%

L3-H

770 - Tb OXALATE Calcining Circuit

770-RCA-001 - Tb OXALATE ROTARY CALCINER

 

 

 

Discharge Temperature

1,562

°F

L3

    Residence Time

30

Min

L3-H

780 - Dy Recovery Unit

780 - Dy Oxalate Precipitation Circuit

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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780-TAK-002-004 - Dy OXALATE PRECIP. TANK #1 to #3

 

 

 

Temperature

Amb

°F

L3

Pressure

atm

psig

L3

Residence Time

60

min

L3

Residual Oxalic Acid Concentration

5

g/L

L3

780 - Dy OXALATE Dewatering Circuit

780-CAF-001/101 - Dy OXALATE CANDLE FILTER #1/#2

 

 

 

Cake Percent Solid

65

%

L3-H

Number of Wash Stages

2

 

L3

Cake Moisture TDS

0.01

Wt%

L3

Wash Efficiency

80

%

L3-H

780 - Dy OXALATE Calcining Circuit

780-RCA-001 - Dy OXALATE ROTARY CALCINER

 

 

 

Discharge Temperature

1,562

°F

L3

Residence Time

30

Min

L3-H

790 - Sc Recovery Unit

790 - Scandium Prestripitation Circuit

790-TAK-002/003 - Sc PRESTRIPITATION TANK #1/#2

 

 

 

Temperature

122

°F

SGS

Pressure

atm

psig

L3

Residence Time

30

min

L3-H

[NaOH]

100

g/L

L3

[NaCl]

1

Mol/L

L3

Tank #2 O:A

2:1

 

L3

Tank #2 O:A

1:1

 

L3

790-CAF-001/101 - Sc BARREN ORG. CANDLE FILTER

 

 

 

Cake Percent Solid

80

%

L3-H

Cake Flush Water Ratio

4

 

L3

790-THK-001 - Sc PRESTRIPITATION 3-PHASE SEPARATOR

 

 

 

Residence Time

24

min

L3-H

Underflow Phases

Aqueous / Solids

 

L3

790-CAF-002/003 - Sc(OH)3 CANDLE FILTER #1/#2

 

 

 

Cake Percent Solid

75

%

L3-H

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Number of Wash Stages

1

 

L3

Wash Ratio (Solution : Solids)

3 : 1

 

L3

Wash Efficiency

70

%

L3-H

795 - Scandium Purification

795 - Scandium Hydroxide Leach Circuit

795-TAK-001 - Sc(OH)3 LEACH TANK

 

 

 

Temperature

Amb

°F

L3

Pressure

atm

psig

L3

Residence Time

60

min

L3-H

Residual H2SO4

0.01

M

L3-H

795 - Scandium Purification Circuit

 

795-TAK-003 - ScP EXT TANK

 

 

 

Temperature

Amb

°F

SGS

Pressure

atm

psig

SGS

Residence Time

60

min

L3-H

O:A Ratio

1

 

SGS

Extractant – Alamine 336

2.5

V%

SGS

Extractant – Aliquat 336

2.5

V%

SGS

Modifier - Tridecanol

2.5

V%

SGS

Diluent – D80 Kerosene

92.5

V%

SGS

795-TAK-004 - ScP LOADED ORG. TANK

 

 

 

Temperature

Amb

°F

NCP

Pressure

atm

psig

L3

Residence Time

60

min

L3-H

O:A Ratio

1

 

NCP

[H2SO4]

50

g/L

NCP

795-TAK-005 - ScP COND TANK

 

 

 

Temperature

Amb

°F

NCP

Pressure

atm

psig

L3

Residence Time

60

min

L3-H

[NaOH]

50

Wt%

NCP

795 - Scandium Oxalate Precipitation

 

795-TAK-006 - Sc OXALATE PRECIPITATION TANK

 

 

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Temperature

Amb

°F

NCP

Pressure

atm

psig

L3

Residence Time

60

min

L3

Oxalic Acid Stochiometric Excess Ratio

1.25

 

L3

795-BLF-001 - Sc OXALATE VACUUM BELT FILTER

 

 

 

Cake Solids Fraction

70

%

L3

Wash Water to Solid Ratio

5

m3/dmt

L3

Number of Wash Stages

3

 

L3

Wash Efficiency

98

%

L3

795 - Scandium Oxalate Calcination

 

795-RCA-001 - SCANDIUM OXIDE ROTARY CALCINER

 

 

 

Discharge Temperature

1,832

°F

L3-H

    Residence Time

30

Min

L3-H

Source: L3 2026

Area 800 – Chloride Recovery

The process design criteria for Area 800 – Chloride Recovery is presented as Table 14‑10.

Table 14‑10: Area 800 – Chloride Recovery Process Design Criteria

Equipment / Description

DATA

UNIT

SOURCE

820 – HCl Recovery

820 – HCl Absorption

820-COL-001/011 - HCl QUENCH TOWER

 

 

 

Type

Packed-Bed Column

 

L3

Temperature

122

°F

 

820-HTX-001/011 – HCl QUENCH COOLER

 

 

 

Type

Shell & Tube

 

L3

Temperature (In/Out)

 

 

 

Process Side

122 / 41

°F

L3

Utility Side

-20 / -10

°F

L3

Heat Transfer Fluid

Ammonia

 

L3

820-COL-002/012 - HCl CONDENSER

 

 

 

Type

Packed-Bed Column

 

L3

Temperature

86

°F

 

820-HTX-002/012 – HCl CONDENSER COOLER

 

 

 

Type

Shell & Tube

 

L3

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Temperature (In/Out)

 

 

 

Process Side

86 / 41

°F

L3

Utility Side

-20 / -10

°F

L3

Heat Transfer Fluid

Ammonia

 

L3

840 - MgCl2 Pyrohydrolysis Unit

840 - MgCl2 Pre-Evaporation Circuit

840-EVP-001 – CHLORIDE PRE-EVAPORATOR

 

 

 

Type

Vertical tubes

 

L3

Temperature

263

°F

L3

Chloride Concentration in Concentrate

430

g/L

L3

Temperature (In/Out)

 

 

 

Utility Side

482/ 248

°F

L3

Heat Transfer Fluid

Heat Transfer Fluid

 

L3

840-CND-001 – Chloride PRE-EVAP CONDENSER

 

 

 

Type

Finned HTX

 

L3

Temperature (In/Out)

 

 

 

Process Side

262 / 176

°F

L3

850 - MgCl2 Spray Roasting Circuit

850-SPR-001 - CHLORIDE PYROHYDROLYSIS SPRAY ROASTER

 

 

 

Temperature

1,472

°F

L3

    Gas Velocity

1.65

ft/s

L3

    Gas residence time

30

sec

L3

Source: L3 2026

Area 900 – Sulfate Effluent Treatment

The process design criteria for Area 900 – Sulfate Effluent Treatment is presented as Table 14‑11.

Table 14‑11: Area 900 – Sulfate Effluent Treatment Process Design Criteria

Equipment / Description

DATA

UNIT

SOURCE

950 – Sulfate Effluent Treatment

 

950 – Sulfate Effluent Neutralization

 

950-TAK-002/003/004 – SULFATE EFFLUENT NEUTRALIZATION TANK

 

 

 

Temperature

Amb

°F

L3

Pressure

atm

psig

L3

Residence Time

20

min

L3

Neutralization Reagent

CaCO3

 

L3

Discharge pH

4.5

 

L3

950-TAK-021/022/023 – SULFATE EFFLUENT NEUTRALIZATION TANK

 

 

 

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Temperature

Amb

°F

L3

Pressure

atm

psig

L3

Residence Time

20

min

L3

Neutralization Reagent

Ca0

 

L3

Discharge pH

8

 

L3

950-BLF-030/031/040/041 – SULFATE EFFLUENT BELT FILTER

 

 

 

Cake Solids Fraction

65

%

L3

Source: L3 2026

14.2.3 Pyrometallurgical Plant

As stated in a previous report, niobium improves the mechanical properties of the high-grade steel and producing a ferro-niobium alloy was an attractive way for NioCorp to supply potential future steelworks factories customers.

The pyrometallurgical process design criteria were established based on thermodynamic calculations, inspired by test results completed by and supported by the literature available on the aluminothermic reduction as well as on the niobium pyrometallurgy. Table 14‑12 presents the pyromet design criteria.

Table 14‑12: Pyrometallurgical process design criteria.

Section

Description

Value

Units

NaNbO3 Precipitate Pelletized

NaNbO3 Precipitate Feed Rate (Dry Basis)

1.16

t/h

27.9

t/d

Moisture Content (After Pelletizing)

<1

%

Storage capacity

14

days

Bulk density

4.3

Tm/m3

Sodium Niobium trioxide

Precipitate Composition

Na

15.6

%w/w

Nb

55.0

%w/w

Nb Precipitate Pellets

Number of bins

1

ea.

Storage time

11

days

Capacity

324

t

Aluminum (Al) pellets

Aluminum (Al) feed rate

3.9

t/batch

Number of bins

1

ea.

Storage time

13

days

Capacity

162

t

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NioCorp Developments Ltd.

Section

Description

Value

Units

Hematite (Fe2O3) Pellets

Hematite (Fe2O3) feed rate

2.4

t/batch

Number of bins

1

ea.

Storage time

13

days

Capacity

150

t

 

Calcium fluoride (CaF2)

Feed rate

0.15

t/batch

Super sacks rack (1 Tm or 2Tm)

1

ea.

 

Limestone (CaCO3)

Limestone feed rate

0.87

t/batch

Super sacks rack (1 Tm or 2Tm)

1

ea.

FeNb Furnace – Aluminothermic Reduction

Total Feed to FeNb Furnace

11.2

t/batch

Operating Temperature

1700 to 1750

°C

FeNb Furnace Power

Electric Induction Furnace

420

kW

Power Consumption Per Ton Precipitate Pellets

182

kW/t

Furnace Thermal Efficiency

60.0

%

Furnace Design Power

1000

kW

Nb Recovery

96.6

%

Furnace Cooling system

Water Flow Rate

36

m³/h

Cooling Tower

1

ea.

FeNb Furnace - FeNb Alloy Composition

Nb

64.9

%w/w

Fe

34.0

%w/w

Al

0.9

%w/w

FeNb Alloy Tapping

FeNb Alloy per batch

4.7

t/batch

Tapping Schedule

2

taps/8-hour shift

4

taps/day

Tapping Time

10.0

min/tap

Mass per tap

5.6

t/tap

Daily production

22.4

t/d

density

8.2

t/m3

Slag production

Slag per batch

9.9

t/batch

 

Nb2O5

1.0

%w/w

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Section

Description

Value

Units

 

 

Furnace Slag Composition

Fe2O3

1.9

%w/w

FeNb (trapped)

0.3

%w/w

Al2O3

92.1

%w/w

CaO

3.2

%w/w

CaF2

1.5

%w/w

Slag density

4.0

t/m³

 

 

 

 

Slag tapping

Slag per tap

9.9

t/batch

Tapping Schedule

4

 

8

taps/day

Tapping Time

15.0

min/tap

Daily slag production

 

39.6

 

t/day

 

FeNb Furnace Off gas Handling

Dust: largely recycled

        ___

 

%

Gas generation

0.07

t/day

FeNb Pelletizing system

Cooling water

15.1

m³/h

Source: MCS 2026

Notes:

(1)
This Process Design Criteria applies for Hydromet feed and 2025 campaign test.
(2)
The mass distribution presented reflects the conversion of oxide feed materials into metallic alloy and slag phases during aluminothermic reduction. The apparent increase in condensed-phase mass relative to the initial solid feed is primarily attributed to oxygen transfer from metal oxides to aluminum, resulting in the formation of Al₂O₃-rich slag, as well as the contribution of fluxing agents. Gas generation, including CO₂ from limestone decomposition and sodium-bearing vapors, is not included in the condensed-phase mass balance and accounts for the observed difference between total feed and product streams

14.3 Flowsheets and Process Description

14.3.1 Surface Crushing, Ore Storage & Mineral Processing Plant

The ROM ore from the underground mine will be transported to a surface ROM stockpile, located in front of the primary crushing circuit. The ore will be fed via grizzly feeder and screen to a C135 primary jaw crusher, and the crushed product with a top size of 203 mm and characteristic size (Pao) of 115 mm, will be delivered by the means of a three-way diverter splitter to three crushed ore bins each with a capacity of 1,400mt. This part of the crushing circuit will operate on a 10 hours per day schedule with the subsequent crushing and the processing plant will operate 24 hour per day.

The ore from the primary crushing circuit will be reclaimed from the ore bins by three feeders with a total capacity of 139 t/h and passed on to the secondary crusher circuit via the secondary crusher screen feed conveyor.

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At the secondary crushing stage, the ore will be sized on a dry, double deck screen with a top deck aperture size of 50 mm and bottom deck aperture size of 25 mm. The screen oversize from both decks will report to the secondary crushing stage consisting of a single cone crusher unit. The screen undersize will be conveyed to a High-Pressure Grinding Rolls (HPGR) circuit.

The screen oversize fractions will be crushed in a single secondary cone crusher operating with a closed side setting of 25 mm. The secondary crushed product will be sized by the same double deck screen with the primary crusher discharge ore.

The screen undersize, at an approximate characteristic particle size (Pao) of 22 mm, will be further crushed in the HPGR circuit. The HPGR circuit will consist of a single HPGR unit, with a separate double-deck vibrating screen with top and bottom deck aperture sizes of 6 mm and 3 mm, respectively. The recirculating load of the HPGR circuit is expected to be in the range of 30 to 40% of the circuit new feed.

The HPGR screen undersize will be the final comminution product and is expected to have a characteristic particle size (Pao) of 1.1 mm. The ore will be stored in a fine ore bin, then reclaimed by a vibrating feeder with a design capacity of 132 t/h, and then passed on to the acid leach circuit via the acid leach feed conveyor for further processing. The overall primary, secondary, and HPGR crushing conceptual block flow diagram is presented in Figure 14‑1.

img170397038_118.jpg

Source: Magemi Mining Inc., 2026

Figure 14‑1: Overall Crushing Conceptual Block Flow Diagram

14.3.2 Hydrometallurgical Plant

The majority of the unit processes selected for the hydrometallurgical flowsheet have been extensively reported in literature and are predominately proven and existing processes. The plant consists of multiple buildings that will house separate physical and chemical processes required to separate the niobium, scandium, titanium and rare earth elements that are contained in the ore and to regenerate and recover reagents for reuse.

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Area 100 – Ore Activation

The ore activation area is used to convert the carbonate minerals in the feed material to oxides through thermal decomposition while recovering the CO2 generated in the process. A simplified block flow diagram is presented as Figure 14‑2.

img170397038_119.jpg

Source: L3 2026

Figure 14‑2: Area 100 – Ore Activation Block Flow Diagram

Unit 100 – Ore Activation

The ore activation circuit converts the carbonates in the feed material to oxides through thermal decomposition.

Activation of the feed ore is accomplished by heating the feed material to approximately 1454°F (790°C) in the indirect natural gas rotary calciner. The high heat converts the carbonate feed material into their oxide components. The conversion releases CO2 gas that is captured, treated, and reused. Following the calcination process, the calcined ore is cooled in the activated material cooler and conveyed to Area 200 – Ammonium Chloride Cycle by the Activated Material Conveyor.

Waste heat from the calciner natural gas combustion is recovered using the activation Calciner Waste heat exchanger. The energy is recovered using thermal fluid.

The CO2 released during the calcination process is captured and filtered using an electro-filter. The filtered gas is then cooled, and physical liquid is separated from the gas in the CO2 Knockout Drum. Once the remaining moisture has been removed from the CO2 gas, the CO2 is transferred and stored via a blower. It is stored in the CO2 distribution tank.

Area 200 – Ammonium Chloride Cycle

The ammonium chloride cycle area is used to selectively leach calcium and magnesium from the calcined ore feed material using a closed loop circuit. The calcium and magnesium are then sequentially recovered through carbonate mineralization, regenerating the ammonium chloride leach reactant, which is recycled to the leach circuit. A simplified block flow diagram is presented as Figure 14‑3.

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img170397038_120.jpg

Source: L3 2026

Notes: The following abbreviations are used in the block flow diagram: NHL = Ammonium Chloride Leach; CaP = Calcium Precipitation; MgP = Magnesium Precipitation; BCO = Scrubbing Unit.

Figure 14‑3: Area 200 – Ammonium Chloride Cycle Block Flow Diagram

Unit 200 – NH4Cl Leach

The ammonium chloride leach circuit is used to selectively leach calcium and magnesium from the calcined ore feed material. This leach reaction converts ammonium chloride into ammonium hydroxide which is partially vaporized and recovered.

The calcined material from Unit 100 – Ore Activation is stored in a day bin, prior to being fed into the NH4Cl Leach reactors where is it mixed with the stage 2 leach ammonium chloride solution and the resulting slurry is pumped to the stage 1 NH4Cl Leach Circuit. The stage 1 NH4Cl Leach Circuit is composed of a cascade of three agitated tanks in series, each with external heating loops to maintain the reactors at their operating temperature. The discharge of the third reactor is hydrocycloned and the overflow is filtered using candle filters. The filtrate is sent to Unit 220 – Calcium Carbonatation while the solids are sent to the stage 2 NH4Cl Leach Circuit. In stage 2, the residue from stage 1 is mixed with fresh hot NH4Cl solution from Unit 260 – Degassing and processed in a cascade of three agitated tanks in series, each with external heating loops to maintain the reactors at their operating temperature. The discharge of the third reactor is sent to Unit 210 – NH4Cl Filtration.

Vapor leaving the reactors are condensed in the ammonium carbonate scrubber located in Unit 260/270 – Ammonium Carbonate and Scrubber Units.

Unit 210 – NH4Cl Filtration

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The NH4Cl Filtration circuit comprises three identical filtration trains which the NH4Cl Leach slurry from Unit 200 – NH4Cl Leach is split between. The slurry is filtered using plate and frame presses to separate the Ca/Mg-rich pregnant leach solution from the remaining oxide solids in the system. The filtrate from the process is collected and sent to Unit 220 – Calcium Carbonatation where calcium is mineralized. The residue from the filters from all three trains is combined and dried before being sent to Area 300 – Hydrochloric Acid Leach.

Unit 220 – Calcium Carbonatation

The calcium carbonatation circuit is designed to mineralize the calcium leached in the ammonium chloride process by converting it to solid calcium carbonate.

NH4Cl PLS from Unit 210 – NH4Cl Filtration enters the circuit and is cooled to 86°F (30°C) before being mixed with an ammonium hydroxide solution condensed from the leach reactors’ overhead condensers. The PLS is then contacted with carbon dioxide in the CaCO3 reactor train to mineralize calcium as a carbonate and the resulting slurry is sent to Unit 230 – Calcium Carbonate Dewatering. Excess CO2 is recovered and recycled in the process.

Unit 230 – Calcium Carbonate Dewatering

The slurry Unit 220 – Calcium Carbonatation is filtered using Belt Filters installed in parallel and the resulting cake is washed using clean water. The wash water is sent to the NH4Cl Mixing Tank located in Unit 200 – NH4Cl Leach while the calcium barren solution continues to Unit 240 – Magnesium Carbonation. The solids sent to area 900 – Sulfate Effluent and to paste backfill.

Unit 240 – Magnesium Carbonation

The magnesium carbonation circuit is designed to mineralize the magnesium leached in the ammonium chloride process by converting it to solid magnesium carbonate using a metathesis reaction with ammonium carbonate.

Barren solution from Unit 230 – Calcium Carbonate Dewatering enters the circuit and is combined with an ammonium carbonate solution, mineralizing the magnesium as a carbonate. The resulting slurry is sent to Unit 250 – MgCO3 Dewatering.

Unit 250 – MgCO3 Dewatering

The slurry Unit 240 – Magnesium Carbonatation is filtered using Belt Filters installed in parallel and the resulting cake is washed using clean water. The wash water and the magnesium barren are sent to Unit 260/270 – Ammonium Carbonate and Scrubber Units. The solids are sent to paste backfill.

Unit 260/270 – Ammonium Carbonate and Scrubber Units

The barren solution from Unit 250 – MgCO3 Dewatering and the wash solutions from both Unit 230 – Calcium Carbonate Dewatering and Unit 250 – MgCO3 Dewatering are combined and heated to decompose and vaporize residual ammonium carbonate and excess ammonium hydroxide prior to being recycled in the NHL unit. The vapors are then recovered and mixed with additional ammonium hydroxide and carbon dioxide rich off gas from the NHL Degassing tanks to prepare the ammonium carbonate solution used in Unit 240 – Magnesium Carbonation.

Area 300 - Hydrochloric Acid Leach

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The hydrochloric acid leach area is used to leach the rare earth elements, including scandium, away from the niobium and titanium-containing minerals, simplifying the latter elements’ recovery and purification. Elements such as iron, calcium, thorium and other impurities are also recovered in the chloride pregnant leach solution (HCl PLS). A simplified block flow diagram is presented as Figure 14‑4.

img170397038_121.jpg

Source: L3 2026

Figure 14‑4: Area 300 – Hydrochloric Acid Leach Block Flow Diagram

Unit 300- HCl Leach

The hydrochloric leach circuit is used to leach the REEs, including scandium, away from the Nb and Ti minerals present in the ammonium chloride leach residue. A counter-current system is used to maximize recovery and control the acidity of the PLS prior to extraction in Area 600 – Solvent Extraction.

NHL residue from Area 200 – Ammonium Chloride Cycle is combined with 2nd stage leach filtrate, 2nd stage leach wash solution and 1st stage leach wash solution into the HCl leach stage 1 cascade of agitated tanks. External recirculation flows are planned to maintain the leach reactors’ temperatures.

Leach slurry from the 1st stage HCl leach step is dewatered in a 2-step hydrocyclone unit. The cyclone underflow is sent to the 2nd stage HCl leach circuit while the overflow is sent Unit 310 – HCl Leach Filtration. In the second stage, the cyclone underflow is combined with hot hydrochloric acid in a cascade of agitated tanks where all leachable elements are extracted into the PLS. External circulation flows are planned to maintain the leach reactors’ temperatures. The residual slurry from the second HCl leach stage is sent to Unit 320 – HCl Leach Dewatering.

Unit 310 – HCl Leach Filtration

The HCl leach filtration unit is used to ensure no solids are entrained in the PLS prior to the solvent extraction circuits.

HCl PLS from the 1st stage leach cyclone in Unit 300 - HCl Leach is filtered in a candle filter with a 3-stage counter-current wash. Each stage is undertaken in batch mode with 2 candle filters operating at different stages to allow for a continuous operation. The residue is sent to the Area 400 – Sulfuric Acid.

Unit 320 – HCl Leach Dewatering

The HCl dewatering unit is used to recover and wash HCl leach residue prior to the acid baking circuit.

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Slurry from the 2nd Stage HCl Leach Reactor cascade, located in Unit 300 - HCl Leach, is washed in a 3 counter-current stages cyclone circuit that includes repulps between each stage. The discharge of the 3rd cyclone stage is then filtered, and the solution is used to repulp the intermediate solids between the 2nd and 3rd cyclone stages. The overflow of the 1st and 2nd cyclone stages is sent back to Unit 300 - HCl Leach and the washed cake is sent to Unit 330 – HCl Residue Drying.

Unit 330 – HCl Residue Drying

The HCl residue drying unit is used to remove moisture and HCl traces prior to the acid bake circuit using a hollow flight screw conveyor followed by an indirect rotary dryer.

Dewatered HCl leach residue from Unit 320 – HCl Leach Dewatering is first partially dried to 95 wt% solids using a hollow flight screw dryer heated with thermal fluid. The partially dried material is then fed to an indirect rotary dryer where it is fully dried. Vapors are collected and sent to Unit 340 – HCl Water Scrubber.

Unit 340 – HCl Water Scrubber

The HCl water scrubber unit recovers off gases from the HCl unit and cleans them through a water scrubber. The discharge of the scrubber is sent to Area 800 - Chloride Neutralization.

The HCl water scrubber is a packed column where vapors and off gasses from the HCl unit are cleaned with water. Water vapor is condensed in the process and the resulting non-condensables are sent to the facility caustic scrubber.

Area 400 – Sulfuric Acid

The sulfuric acid area is used to convert the Nb and Ti-bearing minerals to leachable sulfate compounds. The resulting sulfates are then leached using water and both the niobium and titanium sulfate compounds are hydrolyzed before being dewatered, calcined and sent to AREA 500 – Chlorination for further processing. A simplified block flow diagram is presented as Figure 14‑5.

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img170397038_122.jpg

Source: L3 2026

Figure 14‑5: Area 400 – Sulfuric Acid Block Flow Diagram

Unit 400 – Acid Baking

The acid baking unit reacts HCl leach residue, a Nb and Ti rich solid, with concentrated sulfuric acid at elevated temperatures to convert the minerals to solid anhydrous sulfates. Vaporized sulfuric acid is recovered and recycled in the circuit using a 2-step scrubbing circuit.

Dry HCl leach residue from Area 300 – Hydrochloric Acid Leach is combined with hot, concentrated sulfuric acid and mixed thoroughly in a pug mill. The pug mill discharge is conveyed in the Acid Bake Kiln where the mixed materials are heated in steps to push the reaction to completion and vaporize any residual liquid sulfuric acid. The reacted materials are then sent to Unit 410 Water Leaching.

Vaporized sulfuric acid from the acid bake kiln is recovered through a 2-stage condensing scrubbing system which allows for the recovery of concentrated sulfuric acid while purging the system of water.

Unit 410 Water Leaching

The water leaching circuit is used to solubilize the sulfate compounds from the acid bake process into an aqueous phase, leaving the insoluble contaminants in the solid residue to be dewatered, washed and sent to sulfate management for paste backfill preparation.

Acid bake solids from Unit 400 – Acid Baking are mixed with a heated combination of recycled solutions and reverse osmosis water (ROW). The resulting slurry is pumped into the water leach

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cascade of three agitated tanks, each maintained at a temperature of 176°F (80°C) with a circulation heating loop. The slurry leaving the water leach tanks is sent to Unit 420 – Water Leach Dewatering.

Unit 420 – Water Leach Dewatering

The water leach dewatering unit is used to filter and wash the water leach residue to maximize niobium recovery.

The slurry leaving Unit 410 Water Leaching is dewatered, and the solids are sent through a series of repulp and cyclone operations using a counter-current setup. The water leach PLS from the first cyclone stage is sent to Unit 430 – Hydrolysis while the final repulp is filtered using candle filters. The residue is then washed using acidified hydrolysis barren solution and sent to AREA 900 – Sulfate Effluent for treatment before being sent to paste backfill. A portion of the wash solutions are sent to Unit 410 Water Leaching.

Unit 430 – Hydrolysis

The hydrolysis unit is used to convert soluble niobium and titanium sulfates compounds into insoluble compounds comprised of a mixture of oxide, hydroxide and oxy-hydroxy-sulfates.

Filtered water leach PLS from Unit 420 – Water Leach Dewatering is pumped to a three-stage reaction unit where it is sequentially diluted using hot reverse osmosis water (“ROW”) and steam, converting niobium and titanium sulfates compounds into insoluble compounds comprised of a mixture of oxide, hydroxide and oxy-hydroxy-sulfates.

The resulting slurry is sent to Unit 440 – Hydrolysis Dewatering and Filtration.

Unit 440 – Hydrolysis Dewatering and Filtration

The hydrolysis dewatering and filtration unit is used to recover and dewater hydrolysis solids prior to their calcination.

The hydrolysate slurry from Unit 430 – Hydrolysis is filtered and washed using ROW in candle filters. The hydrolysate cake is sent to Unit 450 – Hydrolysate Calcination while the barren solution is partially recycled in Unit 410 Water Leaching and Unit 430 – Hydrolysis.

Unit 450 – Hydrolysate Calcination

The hydrolysate calcination unit is used to dry the hydrolysate cake and minimize moisture to the chlorination unit. It also allows for a reduction of volatile elements such as sulfur.

Hydrolysis cake from Unit 440 – Hydrolysis Dewatering and Filtration is calcined in a rotary calciner and sent to Area 500 – Chlorination. Off gas from the calciner is collected and treated in the plant caustic scrubber.

Area 500 – Chlorination

The chlorination area is used to convert hydrolysate cake to gaseous metal chlorides and recover each element individually. Niobium and iron are first solidified in a titanium tetrachloride slurry. The titanium tetrachloride is subsequently vaporized, and the mixture of niobium and iron chloride is hydrolyzed. Niobium is recovered as an oxide with iron residuals while iron is sent to the chloride management unit as a ferric chloride solution. The crude titanium tetrachloride solution is then distilled into a pure titanium tetrachloride product.

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Products:

•
Niobium / Iron Oxide (to Pyromet)
•
Titanium Tetrachloride (TiCl4)

A simplified block flow diagram is presented as Figure 14‑6.

img170397038_123.jpg

Source: L3 Process Developments 2026

Figure 14‑6: Area 500 – Chlorination Block Flow Diagram

The chlorination unit is used to convert the hydrolysate cake to a mixture of individual metal chlorides using a fluid bed reactor. The metal chlorides exit the chlorinator as gases and are recovered by staged condensation. Iron and niobium are solidified first in a titanium tetrachloride slurry as a crude titanium tetrachloride solution is condensed.

Hydrolysate cake is mixed with petroleum coke and fed to the chlorinator, a fluid bed reactor using a sub-stoichiometric chlorine mixture to ensure a minimum amount of unreacted chlorine is lost. Air is also injected into the chlorinator to maintain the temperature of the fluid bed, ensure fluidization and support proper conversion. Cooling water is sparged on the outside of the chlorinator to maintain the reaction below 1,742 °F (950 °C), protecting the equipment.

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The gaseous discharge of the chlorinator is filtered using Electro-Filters and sent to the condensation circuit. The solid residue accumulating in the chlorinator is periodically purged and discarded during shutdowns, prior to the equipment being rebuilt.

The chlorination unit operates as a single train, with a full alternate train available. In a typical operation, while one train is in operation, the other train is being maintained.

Chlorinator off gases are condensed in a series of three venturi absorbers with decreasing operating temperatures (Nb/Fe Condenser, Primary Condenser, Secondary Condenser), with residual vapors and non-condensable gases discharging to Unit 550 – CO Boiler and FGD Scrubber.

The Nb/Fe condenser uses a venturi spray tower without packing to solidify and recover niobium and iron chloride in a titanium tetrachloride slurry. The bottom of the tower is gravity discharged to the clarifier and the underflow is sent to Unit 530 – Nb/Fe Recovery. Excess titanium tetrachloride is sent to the Unit 510 – Crude TiCl4 Treatment. The off gas of the Nb/Fe condenser is sent to the primary condenser. The Nb/Fe condenser cooling circulation loop uses thermal fluid to operate near the boiling point of titanium tetrachloride (277 °F, 136.4 °C).

The primary condenser uses a venturi spray tower with packing to condense a titanium tetrachloride solution. The bottom of the tower is sent to Unit 510 – Crude TiCl4 Treatment. The off gas from the primary condenser is sent to the secondary condenser. The primary condenser cooling circulation loop uses cooling water to operate near ambient temperature.

The secondary condenser uses a venturi spray tower with packing to condense a titanium tetrachloride solution. The bottom of the tower is sent to the primary condenser. The off gas of the secondary condenser is sent to Unit 550 – CO Boiler and FGD Scrubber. The secondary condenser cooling circulation loop uses an ammonia vaporizer unit to obtain a secondary condenser recirculation operating temperature of 0°F (-18°C).

Unit 510 – Crude TiCl4 Treatment

The crude TiCl4 Treatment Unit is used to remove most dissolved metals and gases from the TiCl4 prior to its purification using a series of three vaporizers (TiCl4 Degas Tank, Vaporizer #1, Vaporizer #2) and related aero condensers.

The first vaporizer is used to de-gas crude TiCl4 from Unit 500 – Chlorination and recycled TiCl4 from unit 520 – TiCl4 Purification by vaporizing it under full reflux conditions to vaporize dissolved non-condensable gases. The TiCl4 Degas tank overflows to the TiCl4 Vaporizer #1 where it is combined with recovered TiCl4 from the Nb/Fe Dryer Condenser and a bleed from the TiCl4 Vaporizer #2. The TiCl4 Vaporizer #1 boils titanium tetrachloride which is fully condensed and pumped to the TiCl4 Vaporizer #2. The TiCl4 Vaporizer #2 boils titanium tetrachloride which is fully condensed and sent to Unit 520 – TiCl4 Purification. Each vaporizer uses fully submerged tube bundles operated with thermal fluid.

The second vaporizer in the train (Vaporizer #1) operates at the saturation point of metals dissolved in the crude TiCl4, and as such, as TiCl4 is vaporized and removed from the system, those metals precipitate and form a slurry. A bleed from the vaporizer #1 to the Nb/Fe Condenser in Unit 500 – Chlorination is used to control the solids’ fraction in Vaporizer #1.

The third vaporizer in the train (Vaporizer #2) operates below the saturation point of metals dissolved in the crude TiCl4, and as such, as TiCl4 is vaporized and removed from the system, those

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metals concentrate in Vaporizer #2. A bleed from Vaporizer #2 to Vaporizer #1 is used to control the dissolved metals concentration in Vaporizer #2.

Unit 520 – TiCl4 Purification

The TiCl4 purification unit is used to prepare pure TiCl4 that meets commercial purity specifications using a combination of stripping and distillation.

Treated TiCl4 from Unit 510 – Crude TiCl4 Treatment is fed to the TiCl4 Stripper, a packed column used to separate all non-condensable gases dissolved in the treated TiCl4, such as chlorine, nitrogen, carbon monoxide and carbon dioxide through partial reboiling and full reflux. Following the TiCl4 stripper, the TiCl4 is maintained under an inert blanket to ensure no other gases can redissolve in it.

Stripped TiCl4 is then fed to the TiCl4 Purification Column, a mixed packed / tray column used to remove metals through distillation of TiCl4, using both reboiling and reflux to control the TiCl4 purity.

A bleed from the bottom section is used to control the metal impurities in the column. The bleed stream is sent to Unit 510- Crude TiCl4 Treatment. Mineral oil is also added to the reboiler to raise the vapor pressure of metal impurities.

The excess condensate on top of the purification column is sent to storage as a pure TiCl4 product.

Unit 530 – Nb/Fe Recovery

The Nb/Fe recovery unit is used to recover all Nb from the Nb/Fe TiCl4 slurry as a dry, TiCl4-free solid mixture of niobium chloride and iron chloride.

The Nb/Fe Recovery Unit is used to vaporize all TiCl4 from the Nb/Fe TiCl4 slurry in a sloped hollow-flight conveyor. The off gas from the dryer is condensed in the Nb/Fe Dryer Condenser, a venturi scrubber circuit similar in design to the Primary Condenser Circuit.

The resulting niobium and iron chloride solids are conveyed to Unit 560 - Nb/Fe Recovery while the recovered crude TiCl4 is pumped to Unit 510 – Crude TiCl4 Treatment and the Vapor is sent to Unit 540 – TiCl4 Vapor Recovery Unit.

The Nb/Fe dryer uses hollow screws and thermal fluid to vaporize TiCl4 and dry the niobium and iron chlorides. The Nb/Fe chloride recovery condenser uses a venturi spray tower with packing to condense a titanium tetrachloride solution.

Unit 540 – TiCl4 Vapor Recovery Unit

The TiCl4 vapor recovery unit is used to recover TiCl4 from various equipment vapor streams before the caustic scrubber discharges to the atmosphere.

TiCl4 vapors from the various units are collected and TiCl4 is condensed in a spray tower with packing. The off gas from the vent condenser is then scrubbed with a caustic solution prior to being vented to the atmosphere. The recovered TiCl4 is recycled back to Unit 520 – TiCl4 Purification.

Unit 550 – Chlorination Off Gas Management

The chlorination off gas management unit is used to treat the chlorination condensation non condensable gases such as chlorine, carbon monoxide and sulfur oxides.

Non condensable gases, specifically carbon monoxide from Unit 500 – Chlorination condensation, are first oxidized in the thermal oxidizer before being scrubbed in the Chlorination Wet Flue Gas

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Desulfurization (“FGD”) Scrubber. The FGD scrubber circuit is used to recover sulfur oxides and hydrochloric acid gases by calcium carbonate neutralization. Air is injected in the scrubber to oxidize the calcium sulfite to gypsum, which is recovered from the circuit and sent to paste backfill. The FGD scrubber is then vented to the atmosphere.

Unit 560 – Nb Recovery

The hydrolysis unit uses heat and dilution to convert niobium chloride into insoluble niobium compounds while solubilizing ferric chloride. The resulting niobium solid is dewatered and calcined into a final product.

The niobium and iron chlorides from Unit 530 – Nb/Fe Recovery are sequentially dissolved in wash water from the niobium hydrolysate filter and hydrolyzed using steam injection in a series of three reactors. The resulting slurry is then phase separated using a clarifier to skim the mineral oil present in the chloride solids. The mineral oil mixture is then coalesced, and the aqueous solution is returned to the phase separator. The mineral oil is then sent to Unit 570 -Mineral Oil Conditioning.

The Nb hydroxide hydrolysate solids are calcined to generate the niobium oxide product sent to the pyrometallurgy Plant to be converted to ferroniobium (FeNb).

Unit 570 – Mineral Oil Conditioning

The mineral oil conditioning is used to vaporize any entrained fluids and dry the recycled mineral oil prior to reintroducing it to the chlorination unit.

Area 600 – Rare Earth Element Recovery

AREA 600 – REE Recovery involves the extraction of scandium, and rare earth elements from the HCl pregnant leach solution (HCl PLS) generated in Area 300 – Hydrochloric Acid Leach and the preparation of a REE solution to feed Area 700 – REE Separation.

The REE Recovery Area uses dimethyloctyl dihexyl diglycolamide (DGA-6) diluted in ethyl-hexanol.

A simplified block flow diagram is presented as Figure 14‑7.

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img170397038_124.jpg

Source: L3 2026

Figure 14‑7: Area 600 - REE Recovery Block Flow Diagram

Unit 600 – REE Extraction

The REE Extraction circuit is used to extract scandium and rare earth elements using an organic solution made of 50 v% DGA-6, diluted in Ethyl-Hexanol from HCl PLS, in a series of solvent extraction stages.

Barren organic from the REE strip circuit is contacted with HCl PLS from Area 300 – Hydrochloric Acid Leach in a Karr Column, extracting scandium and rare earth elements. The raffinate solution is sent to Area 800 – Chloride Recovery.

The loaded organic leaving the extraction column is scrubbed in a second Karr column using a dilute hydrochloric acid and magnesium chloride solution. Some of the iron and a significant portion of the thorium, lanthanum and cerium are scrubbed with negligible amounts of scandium and magnet rare earth elements. The scrub liquor is combined with the raffinate and sent to Area 800 – Chloride Recovery. The scrubbed organic is sent Unit 610 – Acid Scrub.

Unit 610 – Acid Scrub

The acid scrub circuit is used to remove residual hydrochloric acid along with a significant portion of the co-extracted iron.

Scrubbed organic from Unit 600 – REE Extraction is contacted with a recycled magnesium chloride solution in two mixer-settlers installed in parallel. The organic is then sent to Unit 620 – REE Strip

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while the scrub liquor is neutralized in a cascade of three agitated tanks using magnesium carbonate from Area 200 – Ammonium Chloride Cycle to precipitate any iron chloride as ferric chloride. The iron residue is dewatered, washed and sent to paste backfill. A bleed from the resulting chloride solution is sent to Unit 600 – REE Extraction and the remaining solution is combined with wash water from the iron hydroxide filters and recycled to the acid scrub mixer settlers.

Unit 620 – REE Strip

The REE Strip circuit is used to recover the rare earth elements from the loaded organic using a low activity magnesium chloride solution.

Scrubbed organic is pumped through a series of 4 mixer-settlers installed in co-current fashion, each with its own strip solution feed. The strip liquors are combined, coalesced and sent to Unit 630 – Iron Removal. The barren organic is recycled into Unit 600 – REE Extraction.

Unit 630 – Iron Removal

The Iron Recovery unit uses magnesium carbonate to precipitate iron as iron hydroxide and prepare a REE solution suitable for the separation circuits.

Strip liquor from Unit 620 – REE Strip is neutralized in a cascade of three agitated tanks using magnesium carbonate from Area 200 – Ammonium Chloride Cycle to precipitate any iron chloride as ferric chloride. The iron residue is dewatered, washed and sent to paste backfill. The filtrate is combined with wash solutions and sent to Area 700 – REE Separation.

Area 700 – Rare Earth Separation

AREA 700 – Rare Earth Separation involves the separation of magnetic rare earth elements and of scandium from the mixed rare earth strip liquor and the precipitation of four commercial products and 2 by-products using conventional solvent extraction technology.

Products

•
2.5 N Dydimium oxide
•
4 N Terbium oxide
•
2.5N Dysprosium oxide
•
4N Scandium oxide

By-Products:

•
Mixed samarium, europium and gadolinium (SEG) carbonates
•
Mixed heavy rare earths and yttrium (HREY) carbonates

The neutralized strip liquor from Unit 630 - Iron Removal is separated in Unit 700 – Primary Circuit into four fractions: a raffinate solution containing light rare earths, a mid-fraction containing SEG, terbium and minor amounts of heavies, a heavy rare earth fraction and scandium is recovered from the organic through prestripitation.

The raffinate is further refined in Unit 710 – NdPr Circuit where the praseodymium and neodymium are separated from lanthanum and cerium. The mid-fraction is further processed in Unit 720 – Tb Circuit where the terbium is separated from the SEG and from the heavier elements. The heavy

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fraction is further processed in Unit 730 – Dy Circuit where dysprosium is separated from heavier rare earths and from yttrium.

The three magnetic rare earths products are precipitated using oxalic acid and calcined to oxide while the two byproducts are precipitated using ammonium carbonate and dried. A simplified block flow diagram is presented as Figure 14‑8.

img170397038_125.jpg

Source: L3 2026

Figure 14‑8: Area 700 – Rare Earth Separation Block Flow Diagram

Unit 700 – Primary Circuit

The primary circuit is used to extract REE heavier than Sm using an organic solution composed of 35% Cyanex 572 diluted in D80 kerosene.

The saponified organic from Area 790 – Sc Recovery is mixed with barren organic and sent to the extraction battery where it is contacted with neutralized rare earth strip liquor from Unit 630 – Iron Removal and reflux scrub solution. The raffinate containing LREE elements is coalesced to recover any entrained organic and sent to Unit 710 – NdPr Circuit.

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The Sm+ loaded organic leaving the extraction battery is scrubbed in a battery of mixer-settlers using an HCl acid solution. The LREE elements are removed from the loaded organic along with minor amounts of SEG elements. The scrub liquor is then refluxed back into the battery. The scrubbed organic continues to the primary circuit strip battery 1.

The scrubbed organic is partially stripped in a battery of mixer-settlers using an HCl acid solution. The unit is configured to fully strip terbium, while minimizing the heavier elements’ recovery.

The organic phase then continues to the second stripping stage while the stripped liquor is sent to Unit 720 – Tb Circuit to be further processed.

The remaining organic is further stripped in a battery of mixer-settlers using an HCl acid solution, removing all the remaining elements except scandium from the organic phase. A portion of the barren organic is recycled back to the organic circulation tank and the remainder is sent to Unit 790 – Sc Recovery. The strip liquor is coalesced and sent to Unit 730 – Dy Circuit.

Unit 710 – NdPr Circuit

The NdPr circuit is used to separate didymium from lanthanum and cerium using an organic solution composed of 45% Cyanex 801 diluted in D80 kerosene.

Barren organic is conditioned with a diluted NH4OH/NH4Cl solution to saponify the extractant. The effluent solution which contains residual NH4Cl is sent to AREA 200 – Ammonium Chloride Cycle after being coalesced to recover any entrained organic.

The saponified organic is then sent to the extraction battery where it is contacted with the raffinate solution from Unit 700 – Primary Circuit and reflux scrub solution. The raffinate containing lanthanum and cerium is coalesced to recover any entrained organic and sent to AREA 800 – Chloride Recovery.

The LREE loaded organic leaving the extraction battery is scrubbed in a battery of mixer-settlers using an HCl acid solution. La and Ce are removed from the loaded organic along with minor amounts of Pr and Nd. The scrub liquor is then refluxed back the battery. The scrubbed organic continues to the NdPr circuit strip batter.

The remaining organic is fully stripped in a battery of mixer-settlers using an HCl acid solution, removing all of the remaining elements from the organic phase. The barren organic is recycled back to the organic circulation tank while the strip liquor is precipitated using oxalic acid in Unit 760 – NdPr Recovery.

Unit 720 – Tb Circuit

The Tb circuit is used to separate Tb using an organic solution composed of 45% Cyanex 572 diluted in D80 kerosene.

Barren organic is first contacted with diluted NH₄OH/NH₄Cl solution to saponify the extractant. The effluent solution which contains residual NH4Cl is sent to AREA 200 – Ammonium Chloride Cycle after being coalesced to recover any entrained organic.

The saponified organic is then sent to the extraction battery where it is contacted with a partially neutralized strip 1 liquor from Unit 700 – Primary Circuit. The raffinate containing SEG is coalesced to recover any entrained organic and sent to Unit 740 – SEG Recovery.

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The Tb and Dy loaded organic leaving the extraction battery is scrubbed in a battery of mixer-settlers using an HCl acid solution. The SEG elements are removed from the loaded organic along with minor amounts of the Tb and Dy elements. The scrub liquor is then refluxed back the extraction battery.

The scrubbed organic is then stripped in a battery of mixer-settlers using an HCl solution. All Tb is removed from the organic and the partially stripped organic phase, still containing Dy, is sent to Unit 730 – Dy Circuit. The strip liquor flows to the Tb scavenging battery. The strip liquor pH is raised using ammonium hydroxide prior to the scavenger battery.

Barren organic is fed to the scavenger battery of mixer-settlers where the remaining Dy in the strip liquor is extracted along with heavier elements into the organic and sent back to the Tb strip battery. The scavenger raffinate is coalesced before being sent to Unit 770 – Tb Recovery.

Unit 730 – Dy Circuit

The Dy circuit is used to separate dysprosium from heavier rare earths using an organic solution composed of 45% Cyanex 572 diluted in D80 kerosene.

Barren organic is conditioned with a diluted NH4OH/NH4Cl solution to saponify the extractant. The effluent solution which contains residual NH4Cl is sent to AREA 200 – Ammonium Chloride Cycle after being coalesced to recover any entrained organic.

The saponified organic is then sent to the extraction battery where it is contacted with a partially neutralized strip 2 solution from Unit 700 – Primary Circuit and reflux scrub solution. The raffinate containing dysprosium is coalesced to recover any entrained organic and sent to Unit 780 – Dy Recovery.

The loaded organic leaving the extraction battery is combined with Dy loaded organic from Unit 720 – Tb Circuit and scrubbed in a battery of mixer-settlers using an HCl acid solution. Dy is removed from the loaded organic along with minor amounts of heavier elements. The scrub liquor is then refluxed back to the extraction battery. The scrubbed organic continues to the Dy circuit strip battery.

The remaining organic is fully stripped in a battery of mixer-settlers using an HCl acid solution, removing all the remaining elements from the organic phase. The barren organic is recycled back to the organic circulation tank while the strip liquor is precipitated using ammonium carbonate in Unit 750 – HREY Recovery.

Unit 740 – SEG Recovery

The SEG Recovery unit uses an ammonium carbonate solution to precipitate and recover Sm, Eu, and Gd from the Tb circuit raffinate as a mixed SEG carbonate by-product. The SEG carbonate is then dewatered, dried and packaged. The resulting barren solution is sent to AREA 200 – Ammonium Chloride Cycle.

Unit 750 – HREY Recovery

The HREY Recovery unit uses an ammonium carbonate solution to precipitate and recover Y and elements heavier than Dy from the Dy circuit strip liquor as a mixed HREY carbonate by-product. The HREY carbonate is then dewatered, dried and packaged. The resulting barren solution is sent to AREA 200 – Ammonium Chloride Cycle.

Unit 760 – NdPr Recovery

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The NdPr Recovery unit uses oxalic acid to precipitate and recover Pr and Nd from the NdPr circuit strip liquor as a didymium oxalate slurry. The didymium oxalate slurry is then dewatered, dried and calcined to generate a didymium oxide product. The resulting barren solution is sent to AREA 200 – Ammonium Chloride Cycle.

Unit 770 – Tb Recovery

The Tb Recovery unit uses oxalic acid to precipitate and recover Tb from the Tb circuit strip liquor as a terbium oxalate slurry. The terbium oxalate slurry is then dewatered, dried and calcined to generate a terbium oxide product. The resulting barren solution is sent to AREA 200 – Ammonium Chloride Cycle.

Unit 780 – Dy Recovery

The Dy Recovery unit uses oxalic acid to precipitate and recover Dy from the Dy circuit raffinate solution as a dysprosium oxalate slurry. The dysprosium oxalate slurry is then dewatered, dried and calcined to generate a dysprosium oxide product. The resulting barren solution is sent to AREA 200 – Ammonium Chloride Cycle.

Unit 790 – Scandium Recovery

Barren organic from Unit 700 – Primary Circuit is contacted with a sodium hydroxide solution in a series of agitated tanks at 122°F (50°C) and the resulting 3-phase slurry is decanted. The heavier aqueous slurry is filtered; the scandium hydroxide solids are washed and sent to Unit 795 – Scandium Purification.

The aqueous solution is sent to the NaOH adjustment tank where its NaOH and NaCl contents are adjusted prior to being recycled to the prestripitation circuit.

The organic solution is also filtered, and the filtrate is sent back to the circuit circulating tank. Any recovered solids are slurried with RO water and returned to the decanter.

The temperature of the solutions in the Scandium Prestripitation Circuit is maintained at 122°F (50°C) to support optimum phase separation as proposed by SGS Lakefield.

Unit 795 – Scandium Purification

Slurried scandium hydroxide from Unit 790 - Scandium Recovery is re-leached using dilute sulfuric acid and the resulting PLS is filtered successively through a candle filter and a cartridge filter to remove any residual solids before being sent to the scandium purification circuit.

The scandium purification circuit is a batch solvent extraction circuit designed to selectively extract niobium, zirconium and titanium from the crude scandium solution and yield a pure scandium solution. Scandium PLS is first contacted with a mixture of Alamine 336 and Aliquat 336, diluted in D80 kerosene in the extraction tank and the agitation is stopped to let the phases separate. A sample of the aqueous phase is assayed and, if the impurity level is acceptable, the aqueous phase is pumped to the scandium precipitation circuit where scandium is precipitated with oxalic acid. The scandium oxalate slurry is then dewatered, dried and calcined to generate a scandium oxide product which is packaged. The resulting barren solution is sent to AREA 900 – Sulfate Effluent Treatment.

The loaded organic is then fed to the strip tank where it is mixed with sulfuric acid to strip the niobium, titanium and zirconium impurities. Once the reaction is completed, the agitation is stopped and the phases are separated. The strip liquor is sent to AREA 900 – Sulfate Effluent Treatment while

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the stripped organic is sent to the conditioning tank where it is mixed with a dilute caustic solution. Once the conditioning is completed, the agitation is stopped and the phases are separated. The strip liquor is sent to AREA 900 – Sulfate Effluent Treatment while the conditioned organic is recycled to the extraction stage.

Area 800 – Chloride Recovery

The chloride recovery area is used to recover chloride ions as hydrochloric acid that can be recycled in the process. It is divided into three sections: ferric chloride, other chlorides and hydrochloric acid recovery. The ferric chloride section uses ferric chloride pyro-hydrolysis, while the other chloride section uses a pyro-hydrolysis based magnesium cycle to recover most chloride ions as hydrochloric acid. A simplified block flow diagram is presented as Source: L3 2026

Figure 14‑9.

img170397038_126.jpg

Source: L3 2026

Figure 14‑9: Area 800 – Chloride Recovery Block Flow Diagram

Unit 820 – Hydrochloric Acid Recovery

The hydrochloric acid recovery unit is used to absorb hydrochloric acid produced in the pyro-hydrolysis units. The unit is composed of 2 circuits in parallel, each composed of 2 columns in series.

HCl vapor from Unit 850– Chloride Pyro-Hydrolysis is divided into 2 equal streams and quenched to 122°F (50°C) in the HCl quench tower by a recirculation stream cooled to 41°F (5°C). The column bottom 10M HCl overflow is sent to the HCl regen tank. The vapor discharge of the quench tower is then cooled to 86°F (30°C) in the condensing tower by a recirculation stream cooled to 41°F (5°C). The column bottom overflow is sent to the HCl quench tower.

Unit 840– Chloride Pre-Evaporation

The chloride pre-evaporation unit is used to concentrate chlorides in the concentrate solution and reduce the size of subsequent units.

The chloride pre-evaporation circuit collects all of the facility chloride effluents, with the exception of Unit 700 – Rare Earth Separations effluents. Unit 700s effluents are sent to Area 200 – Ammonium Cycle because of their high ammonium content. The following effluents are aggregated in Unit 840:

•
Sc organic conditioning solution from Unit 790 – Sc Recovery
•
DG6 raffinate from Unit 600 – REE Recovery
•
HCl Scrubber Bleed from Unit 340 – HCl Water Scrubber
•
Nb Hydrolysis filtrate from Unit 560 – Nb/Fe Hydrolysis Dewatering

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The mixed-chloride solution is concentrated in an evaporation unit and the resulting concentrated magnesium chloride solution is sent to Unit 850– Chloride Pyro Hydrolysis. Vapor from the evaporator is condensed as weak HCl acid and recycled in the hydrometallurgical plant process.

Unit 850– MgCl2 Pyro-Hydrolysis

The chloride pyro-hydrolysis unit is used to recover mixed-oxides and hydrochloric acid from the concentrated chloride solution.

Concentrated chloride solution from Unit 840– Chloride Pre-Evaporation is pyro hydrolyzed to mixed-oxides in a natural gas fluid bed reactor. The off-gas from the pyro-hydrolysis reactor is cleaned of any entrained dust and sent to Unit 820 – Hydrochloric Acid Recovery. The mixed-oxides solids are sent to paste backfill.

Area 900 – Sulfate Effluent

The sulfate effluent area is used to treat the sulfate effluent and generate tailings that can be used for paste backfill. The treated water can be reused in the process or sent to wastewater. A simplified block flow diagram is presented as Figure 14‑10.

img170397038_127.jpg

Source: L3 2026

Figure 14‑10: Area 900 – Sulfate Effluent Block Flow Diagram

Unit 900 – Sulfate Effluent Treatment

All sulfate effluents are neutralized simultaneously in a cascade of agitated tanks using calcium carbonate from Area 200 – Ammonium Chloride Cycle to reach a pH of 4.5. The discharge of that cascade is further neutralized to a pH of 8 using calcium oxide.

The sulfate effluent dewatering is used to dewater the sulfate effluent sludge to meet the paste backfill requirements. The sludge is first thickened, then filtered.

14.3.3 Pyrometallurgical Plant

The process flow diagram for the pyrometallurgical plant is presented in the figure below. The selected process is based on the aluminothermic reduction of oxide phases produced during the calcination step, following the hydrometallurgical niobium precipitation stage. In line with ongoing process development, the design basis maintains flexibility to accommodate variations in feed composition, including sodium niobate (NaNbO₃) and titanium–niobium oxide systems, reflecting the current range of expected Hydromet products.

A disc pelletization stage is incorporated immediately downstream of the final hydrometallurgical precipitation step, where the material retains sufficient moisture to promote effective agglomeration. This approach produces mechanically stable pellets suitable for handling and feeding, while

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minimizing dust generation. The pellets are subsequently calcined to produce a stable oxide phase for pyrometallurgical processing. The calcined material is then conveyed to the Furnace Feed Preparation Area (FPA) and stored in a closed bin providing approximately eleven days of storage capacity. This storage capacity is aligned with operating requirements to accommodate upstream slowdowns and ensure continuity of furnace operations.

Aluminum (in the form of wire cuts or granules) and hematite (Fe₂O₃), supplying the reductant and iron units for the aluminothermic reaction, are stored in dedicated bins, each designed to provide approximately fourteen days of storage capacity. This storage philosophy ensures operational resilience in the event of interruptions in raw material supply. Fluxing agents, including calcium carbonate (CaCO₃) and calcium fluoride (CaF₂), are stored separately in bins and supersacks, respectively, and are used to control slag properties during the reaction.

All feed bins and supersack stations are equipped with load cells to ensure accurate mass-based dosing of each component in accordance with the defined reaction recipe. Each material stream is conveyed independently to the furnace feed conveyor, where final proportioning is controlled prior to charging.

The process is operated on a batch basis. The prepared charge is introduced into an induction furnace, where temperature is progressively increased until the aluminothermic reaction is initiated. Once ignition occurs, the exothermic nature of the reaction sustains the process. Control of the reaction is achieved through precise control of feed composition and batch preparation, ensuring consistent operating conditions.

The process design incorporates sufficient flexibility to accommodate variations in feed composition while maintaining control of key parameters, including slag chemistry and phase separation behavior, which are critical to achieving effective metal recovery.

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img170397038_128.gif

Source: L3 2026

Figure 14‑11: Pyrometallurgical Processing Simplified Flowsheet

14.3.3.1 Furnace Feed System

As mentioned earlier, weight-controlled storage and dosing systems are provided for the main furnace feed components:

NaNbO₃ pellets from the Hydromet circuit, or alternative Nb₂O₅–TiO₂-bearing feed where applicable

•
Aluminum reductant
•
Hematite (Fe₂O₃)
•
Limestone (CaCO₃)
•
Calcium fluoride (CaF₂), where required for slag chemistry control

Off-specification FeNb alloy may also be recycled to the furnace in combination with fresh Hydromet-derived feed.

Each storage bin discharges onto load-cell-equipped conveyors forming part of the furnace feed mass measurement system. The system is automatically controlled through a programmable logic controller (PLC) to ensure precise and repeatable batching in accordance with the defined charge recipe.

Furnace feed preparation is conducted as a batch process. Individual charge components are proportioned gravimetrically and discharged at controlled rates to produce a consistent furnace charge. This approach supports control of the Fe/Nb ratio, reductant addition, and slag chemistry, thereby contributing to stable furnace operation.

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14.3.3.2 Furnace Operation

The FeNb induction furnace operates within a temperature range of approximately 3,092°F to 3,227°F (1,700°C to 1,775°C), depending on the composition and phase characteristics of the Hydromet feed.

Electrical energy is supplied to heat the furnace charge and initiate the aluminothermic reaction. Aluminum acts as the primary reductant and is oxidized to Al₂O₃, which forms the principal component of the slag phase. Limestone decomposes to CaO and CO₂, with CaO reporting to the slag system. Sodium-bearing species partition between the slag and off-gas streams depending on process conditions and feed composition. Any Ti present in the feed reports to the slag as TiO2.

A molten metal heel is maintained in the furnace and covered by a slag layer. This operating practice supports thermal stability, improves metallurgical consistency, and promotes phase separation. The following figure illustrates the furnace design concept for separate slag and FeNb alloy tapping.

14.3.3.3 Design of the Induction Furnace

Following completion of the aluminothermic reaction and a holding period to promote metal–slag separation, slag and alloy are tapped at scheduled intervals.

14.3.3.3.1 Tapping Schedule — Design Basis

Operations are conducted over two 8-hour shifts per day.

Slag

•
Four taps per 8-hour shift, with higher frequency expected for TiO₂-rich Hydromet feed
•
Approximately 15 minutes per tap
•
Average of 4.9 tonnes per tap, subject to increase for TiO₂-rich feed

FeNb Alloy

•
Two taps per 8-hour shift
•
Approximately 10 minutes per tap
•
Average of 5.6 tonnes per tap

Tap-holes are opened using a tapping drill and resealed using a clay gun system. Slag and metal levels are monitored to maintain stable operating conditions.

Slag Handling

The furnace produces an Al₂O₃–CaO–CaF₂ slag containing sodium-bearing constituents where applicable. Slag is tapped into segmented steel molds, where it cools and solidifies. The segmented mold design facilitates removal in manageable pieces and enables mold reuse.

Solidified slag is transferred to a slag bunker and subsequently processed through:

•
Vibrating feeder
•
Jaw crusher
•
Gravity separation circuit

The gravity separation circuit recovers entrained FeNb metal particles for recycle. Residual slag is directed to the tailings management facility.

FeNb Product Handling

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Molten FeNb alloy is tapped through a refractory-lined launder into a pelletizing pan and granulated in a water basin to produce pellets typically ranging from 6 to 15 mm in diameter.

Pellets are recovered using a pocket conveyor and transferred to a rotary dryer for moisture removal. After drying, the material is screened and packaged for shipment. Undersize material is recycled to the furnace feed system.

Dust Collection and Off-Gas Handling

Dust generated in the feed preparation area is captured and treated through a cyclone and baghouse system. Collected dust is returned to the feed preparation circuit and recycled in accordance with the furnace charge recipe.

Furnace off-gas and fumes generated during reaction, tapping, and casting are captured and directed to the furnace baghouse. Baghouse dust is recycled to the furnace or pelletizing circuit where appropriate.

Cleaned exhaust air is discharged through dedicated stacks equipped with monitoring and sampling systems to support compliance with applicable environmental regulations.

14.4 Mass Balances

14.4.1 Surface Crushing, Ore Storage & Mineral Processing Plant

The process material balance (MB) for the comminution circuit is presented in Table 14‑13.

Table 14‑13: Comminution Circuit Material Balance

Description

Primary Crusher Feed

Secondary Crusher Screen Feed

Secondary

Screen Fines

Secondary Screen Coarse

Secondary Crusher Product

HPGR Product

HPGR Screen Coarse

HPGR Screen Fines

To Shuttle Conveyor

HCl Leach Feed

Solids (t/h)

139.30

310.64

139.30

171.34

171.34

197.81

58.51

139.30

139.30

139.30

Liquid (t/h)

7.17

15.96

7.17

8.80

8.80

10.25

3.08

7.17

7.17

6.35

Density (t/m3)

2.70

2.70

2.70

2.70

2.70

2.70

2.70

2.70

2.70

2.70

Volume (m3/h)

54.23

120.91

54.23

66.68

66.68

77.07

22.84

54.23

54.23

48.58

Nb (t/h)

0.78

1.74

0.78

0.96

0.96

1.11

0.33

0.78

0.78

0.70

Sc (t/h)

0.01

0.02

0.01

0.01

0.01

0.01

0.00

0.01

0.01

0.01

Ti (t/h)

2.33

5.19

2.33

2.86

2.86

3.30

0.98

2.33

2.33

2.09

Source: Magemi Mining Inc., 2026

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14.4.2 Hydrometallurgical Plant

The mass and energy balance for the hydrometallurgical plant has been integrated into a METSIM model based on the process design criteria available in Section 14.2.2 and the flowsheet described in Section 14.3.2. A summary flowsheet is available as Figure 14‑12.

img170397038_129.jpg

Source: L3 2026

Figure 14‑12: Product Summary Block Flow Diagram

 

Recovery of saleable products across the flowsheet is presented as Table 14‑14.

Table 14‑14: Recovery of Saleable Products

Element / Unit

100 / 200

300

400

500

600

700

Overall

Ti

100.0%

99.0%

81.2%

100.0%

 

 

80.5%

Nb

100.0%

99.7%

85.4%

99.6%

 

 

84.7%

Sc

100.0%

96.2%

 

 

98.1%

 

94.3%

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Pr

100.0%

90.0%

 

 

100.0%

98.5%

88.7%

Nd

100.0%

94.9%

 

 

100.0%

99.4%

94.4%

Tb

100.0%

95.0%

 

 

100.0%

99.3%

94.4%

Dy

100.0%

95.0%

 

 

100.0%

99.5%

94.6%

Source: L3 2026

 

It should be noted that recoveries presented in Table 14‑14 may vary from reserve calculation recoveries as they are derived from the mass balance integration using an averaged feed composition and an assumed mineralogical distribution of elements coupled with solution-based chemical balance. It should be understood that pay element recovery variations are to be expected during the facility operation based on those factors and that the difference is within the expected uncertainty margin at this stage of project development.

Summary mass balance tables are provided as Table 14‑15 to Table 14‑20 to support the reader. The stream numbers presented in the tables are associated with the block flow diagrams presented in Section 14.3.2 and as Figure 14‑12.

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Table 14‑15: Area 100 / 200 Summary Mass Balance Table

Stream

Units

1

100

210

215

230

250

Description

Elk Creek Ore

Activated Ore

Ammonium Chloride Leach PLS

 Ammonium Chloride Leach Residue

Calcium Carbonate By-Product

Magnesium Carbonate By-product

Mass Flow

Total

stph

138.38

80.67

614.29

62.81

23.69

22.32

Aqueous

stph

6.92

 

614.29

 

3.55

4.46

Solids

stph

131.46

80.67

 

62.81

20.14

17.85

Volume Flow

S/L

US gpm

346.32

87.59

2310.8

69.11

41.67

41.97

Solids / Gas Composition

Mg

wt %

5.23

8.52

 

2.71

1.32

27.5

Ca

wt %

8.63

14.06

 

5.43

38.2

1.85

Ba

wt %

2.96

4.82

 

6.2

 

 

Si

wt %

4.61

7.52

 

9.67

 

 

Al

wt %

1.16

1.89

 

2.42

 

 

Fe

wt %

12.14

19.79

 

 25.44

 

 

Ti

wt %

1.58

2.58

 

3.31

 

 

Nb

wt %

0.53

0.86

 

1.1

 

 

Sc

wt %

0.0069

0.0112

 

0.0144

 

 

Pr

wt %

0.0127

0.0207

 

0.0266

 

 

Nd

wt %

0.0408

0.0664

 

0.0854

 

 

Tb

wt %

0.0014

0.0023

 

0.0029

 

 

Dy

wt %

0.0053

0.0087

 

0.0111

 

 

Aqueous Concentration

Mg

g/L

 

 

13.74

 

 

 

Ca

g/L

 

 

9.22

 

 

 

Source: L3 2026

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Table 14‑16: Area 300 / 400 Summary Mass Balance Table

Stream

Units

310

330

420

425

440

450

Description

HCl Leach PLS

HCl Leach Residue

Sulfuric Acid PLS

Sulfuric Acid Residue

Water Leach Barren

Calcined Hydrolysate

Mass Flow

Total

stph

230.35

33.22

105.26

42.24

482.26

3.87

Aqueous

stph

230.35

 

105.26

8.45

482.26

 

Solids

stph

 

33.22

 

33.79

 

3.87

Volume Flow

S/L

US gpm

773.27

39.79

382.12

91.12

1989.52

3.66

Solids / Gas Composition

Mg

wt %

 

0.58

 

0.22

 

 

Ca

wt %

 

7.88

 

7.48

 

 

Ba

wt %

 

11.69

 

11.49

 

 

Si

wt %

 

18.27

 

17.97

 

 

Al

wt %

 

2.19

 

1.77

 

 

Fe

wt %

 

5.35

 

1.21

 

3.81

Ti

wt %

 

6.21

 

0.92

 

43.22

Nb

wt %

 

2.08

 

0.25

 

15.23

Sc

wt %

 

0.001

 

0.001

 

 

Pr

wt %

 

0.005

 

0.0045

 

 

Nd

wt %

 

0.008

 

0.0001

 

 

Tb

wt %

 

0.0003

 

0

 

 

Dy

wt %

 

0.001

 

0.0005

 

 

Aqueous Concentration

Mg

g/L

11.72

 

1.42

0.27

0.27

 

Ca

g/L

2.58

 

1.07

0.21

0.21

 

Fe

g/L

73.34

 

16.11

2.8

2.8

 

Ti

g/L

0.074

 

18.44

0.18

0.18

 

Nb

g/L

0.0064

 

6.39

0.04

0.04

 

Sc

g/L

0.045

 

0

0

0

 

Pr

g/L

0.078

 

0

0

0

 

Nd

g/L

0.263

 

0.03

0.01

0.01

 

Tb

g/L

0.009

 

0

0

0

 

Dy

g/L

0.034

 

0

0

0

 

Source: L3 2026

 

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Table 14‑17: Area 500 Summary Mass Balance Table

Stream

Units

500

505

510

520

530

560

Description

Chlorinator Discharge

Nb/Fe Slurry

Treated TiCl4

Pure TiCl4

Nb/Fe Chlorides

Nb Oxide

Mass Flow

Total

stph

13.78

6.51

6.73

6.63

2.14

0.85

Aqueous

stph

 

4.55

6.73

6.63

 

 

Solids

stph

 

1.95

 

 

2.13

0.85

Volume Flow

S/L

US gpm

0

10.13

10.25

9.79

3.12

0.76

Solids / Gas Composition

Mg

wt %

0

0

0

0

0

0

Ca

wt %

0

0

0

0

0

0

Ba

wt %

0

0

0

0

0

0

Si

wt %

0

0

0

0

0

0

Al

wt %

0

0

0

0

0

0

Fe

wt %

1.07

6.88

0

0

6.87

0.9

Ti

wt %

12.13

0

0

0

0

0

Nb

wt %

4.28

27.52

0

0

27.52

69.01

Sc

wt %

0

0

0

0

0

0

Pr

wt %

0

0

0

0

0

0

Nd

wt %

0

0

0

0

0

0

Tb

wt %

0

0

0

0

0

0

Dy

wt %

0

0

0

0

0

0

Aqueous Concentration

Mg

g/L

0

0

0

0

0

0

Ca

g/L

0

0

0

0

0

0

Fe

g/L

0

11.09

0.09

0

0

0

Ti

g/L

0

591.92

662.93

683.93

0

0

Nb

g/L

0

44.67

0.36

0

0

0

Source: L3 2026

 

Table 14‑18: Area 600 / 700 Summary Mass Balance Table

Stream

Units

600

630

700

701

702

710

Description

Chloride Effluent

REE + Sc Solution

PC Raffinate

PC STR 1

PC STR 2

NdPr STR

Mass Flow

Total

stph

338.29

92.24

109.88

1.54

0.89

1.87

Aqueous

stph

338.29

92.24

109.88

1.54

0.89

1.87

Solids

stph

 

 

 

 

 

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Volume Flow

S/L

US gpm

1154.87

363.3

423.68

5.28

3.06

6.36

Aqueous Concentration

Mg

g/L

8.48

3.72

 

 

 

 

Ca

g/L

1.78

0.2

 

 

 

 

Fe

g/L

47.24

 

 

 

 

 

Ti

g/L

0.05

 

 

 

 

 

Nb

g/L

0

 

 

 

 

 

Sc

g/L

 

0.1

 

 

 

 

Pr

g/L

0

0.17

0.14

0

0

12.18

Nd

g/L

0

0.61

0.51

0

0

44.78

Tb

g/L

 

0.02

0

1.44

0

0

Dy

g/L

 

0.08

0

2.45

6.93

0

Source: L3 2026

 

Table 14‑19: Area 700 Summary Mass Balance Table

Stream

Units

720

730

760

770

780

795

Description

Tb SCV Raffinate

Dy Raffinate

NdPr Oxide

Tb Oxide

Dy Oxide

Scandium Oxide

Mass Flow

Total

stph

0.47

2.71

0.1063

0.0022

0.0098

0.01

Aqueous

stph

0.47

2.71

 

 

 

 

Solids

stph

 

 

0.1063

0.0022

0.0098

0.01

Volume Flow

S/L

US gpm

1.8

10.41

0.06

0.0087

0.0053

0.01

Solids / Gas Composition

Sc

wt %

 

 

 

 

 

65.196

Pr

wt %

 

 

18.2008

 

 

 

Nd

wt %

 

 

66.8792

 

 

 

Tb

wt %

 

 

 

86.777

0.0997

 

Dy

wt %

 

 

 

0.0426

86.537

 

Aqueous Concentration

Tb

g/L

4.18

 

 

 

 

 

Dy

g/L

 

3.27

 

 

 

 

Source: L3 2026

Table 14‑20: Area 800 Summary Mass Balance Table

Stream

Units

850

900

Description

Mixed-Oxides

Sulfate Effluent Tailings

Mass Flow

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Total

stph

29.87

42.49

Aqueous

stph

 

14.87

Solids

stph

29.87

27.62

Volume Flow

S/L

US gpm

30

25.53

Solids / Gas Composition

Mg

wt %

8.2

0.94

Ca

wt %

1.71

18.16

Ba

wt %

Tr.

0.03

Si

wt %

Tr.

0

Al

wt %

2.66

3.34

Fe

wt %

46.2

5.94

Ti

wt %

Tr.

0.35

Nb

wt %

Tr.

0.07

Sc

wt %

Tr.

0

Pr

wt %

Tr.

0

Nd

wt %

Tr.

0

Tb

wt %

Tr.

0

Dy

wt %

Tr.

0

Source: L3 2026

 

Component thermodynamic parameters have been derived from multiple literature sources and commercial databases such as HSC, OLI systems and ASPEN tech. The rare earth separation mass balance has been established using L3’s proprietary predictive rare earth separation modeling algorithm SEASE, calibrated from bench and pilot scale data.

14.4.3 Pyrometallurgical Plant

A detailed mass balance and associated energy model were developed based on the defined production target of 22.4 t/d FeNb alloy.

NaNbO₃ Feed Requirement

Based on the following assumptions:

•
Target alloy Nb content: 64.9%
•
Nb recovery to metal: 96.6%
•
Nb fraction in NaNbO₃: 55%

The required NaNbO₃ feed rate is estimated at:

•
26.6 t/d (dry basis)
•
Equivalent to 1.11 t/h

Major Feed Inputs (Design Basis)

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Elemental partitioning between metal, slag, and off-gas phases was modeled using partition coefficients derived from test work conducted at XPS Industry Relevant Solutions and supported by thermodynamic evaluation.

The modeled niobium recovery to the alloy is approximately 96.6% and is subject to confirmation during industrial operation.

Table 14‑21: Reagent and approximate feed rate (t/d).

Reagent

Approximate Feed Rate (t/d)

NaNbO3

27.9

Fe2O3

11.8

Aluminum

16.1

Limestone (CaCO3)*

10.9

(CaF2)*

5.2

*As required by slag chemistry

Source: MCS, 2026

Niobium-bearing dust and metal fines are assumed to be effectively captured and recycled to the furnace feed system, contributing to overall recovery.

Table 14‑22: FeNb Furnace Partition Coefficients

Element

To Metal

To Slag

To off gas

 

%

%

%

Nb

96.6

3.4

-

Fe

95.0

5.0

-

Na

-

50.0

50.0

CO2 (from CaCO3)

-

-

100.0

 

Al

0.9

99.1

-

Ca

-

100.0

-

Source: Metallurgy Concept Solutions, 2026

 

The pyrometallurgical plant is designed to produce 22.4 tons per day (t/d) of FeNb alloy containing approximately:

•
64.9% Nb
•
34.0% Fe
•
~0.9% originating from the aluminothermic reduction process

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_130.gif

Source: MCS 2026

Figure 14‑13: Summary of the pyrometallurgical plant

14.5 Process Equipment

14.5.1 Surface Crushing, Ore Storage & Mineral Processing Plant

The primary equipment list (Table 14‑23) and the ancillary equipment list (Table 14‑24) for the comminution area were prepared based on the process design criteria. The installed power of the major equipment determined during the process design is shown in Table 14‑23.

Although the ancillary equipment list for the comminution area is shown in this report for completeness, the associated installed power is not determined as part of the process design process. The installed motor power of ancillary equipment is reported as provided by the Qualified Person for materials handling design.

Table 14‑23: Primary Equipment List

Comminution Circuit Primary Equipment

No. of Units

Unit Installed Power (kW)

Total Installed Power (kW)

Primary Crushing Grizzly Feeder and Screen

1

10

10

Primary Jaw Crusher (C130)

1

186

186

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Comminution Circuit Primary Equipment

No. of Units

Unit Installed Power (kW)

Total Installed Power (kW)

Primary Crusher HPU

1

38

38

Double Deck Vibrating Screen

1

5.5

5.5

Secondary Crusher (Metso HP300 or equivalent)

1

200

200

High Pressure Grinding Rolls (Polycom 14/08 - 02 or equivalent)

1

1,000

1,000

HPGR Product Double Deck Screen

1

37.5

37.5

Source: Magemi Mining Inc., 2026

Table 14‑24: Ancillary Equipment List

Comminution Circuit Ancillary Equipment

No. of Units

Unit Installed Power (kW)

Total Installed Power (kW)

Stationary Magnet

1

10

10

Primary Jay Crusher Lubrication Unit

1

19

19

Crusher Ore Belt Conveyor # 1

1

94

94

Belt Magnet # 1

1

19

19

Crushed Ore Reversing Shuttle Belt Conveyor # 2

1

19

19

Silos Slide Gate Power Unit

1

23

23

Crushed Ore Bin Vibrating Feeder

3

3.75

11.25

Secondary Crusher Screen Feed Conveyor

1

75

75

Secondary Crusher Recycle Conveyor

1

15

15

HPGR Feed Conveyor

1

11.5

11.5

HPGR Screen Feed Conveyor

1

11.5

11.5

HPGR Recycle Conveyor

1

22

22

Fine Ore Bin Feed Conveyor

1

30

30

Fine Ore Bin

1

n/a

n/a

Fine Ore Bin Vibrating Feeder

3

3.75

11.25

Fine Ore Conveyor

1

30

30

Conveyor Scales

3

3.75

11.25

Tramp Magnet

1

3.75

3.75

Source: Magemi Mining Inc., 2026

14.5.2 Hydrometallurgical Plant

The equipment list for the Hydrometallurgical Plant was developed based on the design criteria and using the mass balance provided by the METSIM and ASPEN models. Summarized list of equipment for reference in this report is presented in this section. A more detailed list and sizing was used in the capital cost estimate.

Area 100 – Ore Activation

The summarized equipment list for Area 100 – Ore Activation is presented in Table 14‑25.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Table 14‑25: Area 100 – Ore Activation Summary Equipment List

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

UNIT 100

ORE ACTIVATION

100-RFC-001

ORE RIGID FILTER CONVEYOR

1

100-DVC-001

ORE DROP VALVE CONVEYOR

1

100-BIN-001

ORE DAY BIN

1

100-LBF-001

ORE LIVE BOTTOM FEEDER

1

100-SCC-001

ORE CALCINER FEED SCREW CONVEYOR

1

100-RCA-001

ORE ACTIVATION CALCINER

1

100-COL-001

ACTIVATED MATERIAL COOLER

1

100-CNV-001

ACTIVATED MATERIAL CONVEYOR

1

100-HTX-001

ACTIVATION CALCINER WASTE HEAT RECOVERY

1

100-BLO-003

ACTIVATION CALCINER O/G BLOWER

1

100-ESK-002

ACTIVATION CALCINER EXHAUST STACK

1

100-DUC-001

ORE DUST COLLECTOR

1

100-ROV-001

ORE DUST COLLECTOR ROTARY VALVE

1

100-PCN-001

ORE PNEUMATIC CONVEYOR

1

100-BLO-002

ORE CONVEYOR BLOWER

1

100-FLT-001

ORE CONVEYOR INLET FILTER

1

100-BLO-001

ORE DUST COLLECTOR BLOWER

1

100-ESK-001

ORE DUST COLLECTOR EXHAUST STACK

1

100-BLO-004

ACTIVATION CALCINER BURNER BLOWER

1

100-FLT-002

ACTIVATION CALCINER BURNER INLET FILTER

1

UNIT 110

CO2 RECOVERY

110-TEG-001

CO2 DEHYDRATATION UNIT

1

110-ELF-001

CO2 DUST ELECTROFILTER

1

110-ROV-001

CO2 DUST ELECTROFILTER ROTARY VALVE

1

110-BIN-001

CO2 DUST ELECTROFILTER CATCH BIN

1

110-HTX-001

CO2 WASTE HEAT RECOVERY

1

110-HTX-002

CO2 COOLER

1

110-TAK-002

CO2 KNOCK OUT DRUM

1

110-BLO-001

CO2 DRYING FEED BLOWER

1

110-TAK-003

COMPRESSED CO2 KNOCK OUT VESSEL

1

110-MVR-001

CO2 COMPRESSOR

1

110-TAK-004

CO2 DISTRIBUTION TANK

1

110-MEP-001|101

CO2 CONDENSATE PUMP

2

110-TAK-005

LIQUID CO2 STORAGE TANK

1

110-EVS-001

CO2 EVAPORATION SKID

1

Source: L3 2026

Area 200 – Ammonium Chloride Cycle

The summarized equipment list for Area 200 – Ammonium Chloride Cycle is presented as Table 14‑26.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Table 14‑26: Area 200 – Ammonium Chloride Cycle Summary Equipment List

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

UNIT 200

NHL-NH4Cl LEACH

200-BIN-001

ACTIVATED MATERIAL DAY BIN

1

200-ROV-001

ACTIVATED MATERIAL ROTARY VALVE

1

200-SCC-001

ACTIVATED MATERIAL SCREW FEEDER

1

200-TAK-001

NH4Cl LEACH MIXING TANK

1

200-AGI-001

NH4Cl LEACH MIXING TANK AGITATOR

1

200-SLP-001|101

NH4Cl LEACH FEED PUMP

2

200-HTX-001|101

NH4Cl DEGASING FEED HEAT EXCHANGER

2

200-AGI-002

NH4Cl LEACH STAGE 1 REACTOR #1 AGITATOR

1

200-TAK-002

NH4Cl LEACH STAGE 1 REACTOR #1

1

200-SLP-002|102

NH4Cl LEACH STAGE 1 TRANSFER PUMP

2

200-SLP-202|302

NH4Cl LEACH STAGE 1 RECIRC. PUMP

2

200-HTX-002|102

NH4Cl LEACH STAGE 1 HEAT EXCHANGER

2

200-AGI-003

NH4Cl LEACH STAGE 1 REACTOR #2 AGITATOR

1

200-TAK-003

NH4Cl LEACH STAGE 1 REACTOR #2

1

200-SLP-003|103

NH4Cl LEACH STAGE 1 TRANSFER PUMP

2

200-SLP-203|303

NH4Cl LEACH STAGE 1 RECIRC. PUMP

2

200-HTX-003|103

NH4Cl LEACH STAGE 1 HEAT EXCHANGER

2

200-AGI-004

NH4Cl LEACH STAGE 1 REACTOR #3 AGITATOR

1

200-TAK-004

NH4Cl LEACH STAGE 1 REACTOR #3

1

200-SLP-004|104

NH4Cl LEACH STAGE 1 TRANSFER PUMP

2

200-SLP-204|304

NH4Cl LEACH STAGE 1 RECIRC. PUMP

2

200-HTX-004|104

NH4Cl LEACH STAGE 1 HEAT EXCHANGER

2

200-HYC-001|002 |003|004|005

NH4Cl LEACH STAGE 2 PRIMARY HYDROCYCLONE

5

200-HYC-006|007 |008|009|010|011|012|013

NH4Cl LEACH STAGE 2 SECONDARY HYDROCYCLONE

8

200-AGI-005

NH4Cl LEACH STAGE 2 REACTOR #1 AGITATOR

1

200-TAK-005

NH4Cl LEACH STAGE 2 REACTOR #1

1

200-SLP-205|305

NH4Cl LEACH STAGE 2 RECIRC. PUMP

2

200-SLP-005|105

NH4Cl LEACH STAGE 2 TRANSFER PUMP

2

200-HTX-005|105

NH4Cl LEACH STAGE 2 HEAT EXCHANGER

2

200-AGI-006

NH4Cl LEACH STAGE 2 REACTOR #2 AGITATOR

1

200-TAK-006

NH4Cl LEACH STAGE 2 REACTOR #2

1

200-SLP-206|306

NH4Cl LEACH STAGE 2 RECIRC. PUMP

2

200-SLP-006|106

NH4Cl LEACH STAGE 2 TRANSFER PUMP

2

200-HTX-006|106

NH4Cl LEACH STAGE 2 HEAT EXCHANGER

2

200-AGI-007

NH4Cl LEACH STAGE 2 REACTOR #3 AGITATOR

1

200-TAK-007

NH4Cl LEACH STAGE 2 REACTOR #3

1

200-SLP-207|307

NH4Cl LEACH STAGE 2 RECIRC. PUMP

2

200-SLP-007|107

NH4Cl LEACH STAGE 2 TRANSFER PUMP

2

200-HTX-007|107

NH4Cl LEACH STAGE 2 HEAT EXCHANGER

2

200-AGI-008

NH4Cl LEACH STAGE 2 FILTER FEED TANK AGITATOR

1

200-TK-008

NH4Cl LEACH STAGE 2 FILTER FEED TANK

1

311 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

200-SLP-008|108

NH4Cl LEACH STAGE 2 FILTER FEED PUMP

2

200-CAF-008|108

NH4Cl LEACH STAGE 2 CANDLE FILTER #1 / #2

3

200-AGI-009

NH4Cl LEACH STAGE 2 FILTRATE TANK AGITATOR

1

200-TK-009

NH4Cl LEACH STAGE 2 FILTRATE TANK

1

200-SLP-009|109

NH4Cl LEACH STAGE 2 FILTRATE PUMP

2

200-SCC-008

NH4Cl LEACH STAGE 2 DEWATERING SCREW CONVEYOR

1

UNIT 210

NHL-NH4Cl LEACH RESIDUE FILTRATION

210-AGI-001

NH4Cl RESIDUE FILTER FEED TANK AGITATOR

1

210-TAK-001

NH4Cl RESIDUE FILTER FEED TANK

1

210-AGI-002

NH4Cl RESIDUE FILTER FEED TANK AGITATOR

1

210-TAK-002

NH4Cl RESIDUE FILTER FEED TANK

1

210-SLP-001|101

NH4Cl FILTRATION FEED PUMP

2

210-SLP-002|102

NH4Cl FILTRATION FEED PUMP

2

210-FPR-001|101

NH4Cl LEACH FILTER PRESS #1 / #2

2

210-CHU-001

NH4Cl LEACH RESIDUE FILTER PRESS #1 CHUTE

1

210-SCC-001

NH4Cl LEACH RESIDUE FILTER PRESS #1 SCREW CONVEYOR

1

210-CHU-101

NH4Cl LEACH RESIDUE FILTER PRESS #2 CHUTE

1

210-SCC-101

NH4Cl LEACH RESIDUE FILTER PRESS #2 SCREW CONVEYOR

1

210-AGI-003

NH4Cl PLS TANK AGITATOR

1

210-TAK-003

NH4Cl PLS TANK

1

210-AGI-004

NH4Cl PLS TANK AGITATOR

1

210-TAK-004

NH4Cl PLS TANK

1

210-SLP-003|103

NH4Cl PLS PUMP

2

210-SLP-004|104

NH4Cl PLS PUMP

2

210-SCC-002

NH4Cl LEACH RESIDUE SCREW CONVEYOR

1

210-CBR-001

NH4Cl RESIDUE CAKE BREAKER

1

210-SCH-001

NH4Cl LEACH RESIDUE SCREW HEATER

1

UNIT 220

CaP-CALCIUM CARBONATATION UNIT - CHRYSTALLIZATION CIRCUIT

220-ROW-001

REE EFFLUENT R,O, SYSTEM

1

220-HTX-001

Ca CARBONATION REACTOR FEED COOLER

1

220-AGI-001

Ca CARBONATATION REACTOR #1 AGITATOR

1

220-TAK-001

Ca CARBONATATION REACTOR #1

1

220-JTP-001

Ca CARBONATATION REACTOR #1 JET PUMP

1

220-AGI-002

Ca CARBONATATION REACTOR #2 AGITATOR

1

220-TAK-002

Ca CARBONATATION REACTOR #2

1

220-JTP-002

Ca CARBONATATION REACTOR #2 JET PUMP

1

220-AGI-003

Ca CARBONATATION REACTOR #3 AGITATOR

1

220-TAK-003

Ca CARBONATATION REACTOR #3

1

220-JTP-003

Ca CARBONATATION REACTOR #3 JET PUMP

1

220-AGI-004

Ca CARBONATE FILTER FEED TANK AGITATOR

1

220-TAK-004

Ca CARBONATE FILTER FEED TANK

1

220-SLP-004|104|204|304

Ca CARBONATE FILTER FEED PUMP

2

220-TAK-006

CO2 KNOCKOUT VESSEL

1

312 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

220-BLO-001

CO2 BLOWER

1

UNIT 230

CaP-CALCIUM CARBONATATION UNIT- FILTRATION CIRCUIT

230-BLF-001

Ca CARBONATE RESIDUE BELT FILTER #1

1

230-VAP-001

Ca CARBONATE FILTER #1 VACUUM PUMP

1

230-SLP-201|301

Ca CARBONATE FILTER #1 FILTRATE TRANSFER PUMP

2

230-SLP-001|101

Ca CARBONATE FILTER #1 WASH WATER PUMP

2

230-CHU-001

Ca CARBONATE FILTER #1 CHUTE

1

230-SCC-001

Ca CARBONATE FILTER #1 SCREW CONVEYOR

1

230-BLF-002

Ca CARBONATE RESIDUE BELT FILTER #2

1

230-VAP-002

Ca CARBONATE FILTER #2 VACUUM PUMP

1

230-SLP-202|302

Ca CARBONATE FILTER #2 FILTRATE TRANSFER PUMP

2

230-SLP-002|102

Ca CARBONATE FILTER #2 WASH WATER PUMP

2

230-CHU-002

Ca CARBONATE FILTER #2 CHUTE

1

230-SCC-002

Ca CARBONATE FILTER #2 SCREW CONVEYOR

1

230-CNV-002

Ca CARBONATE RESIDUE CONVEYOR

1

230-AGI-003

Ca CARBONATE FILTER FILTRATE TANK AGITATOR

1

230-TAK-003

Ca CARBONATE FILTER FILTRATE TANK

1

230-SLP-003|103

Ca CARBONATE FILTER FILTRATE TRANSFER PUMP

2

230-ROW-001

NH4Cl RECOVERY R.O. WATER SYSTEM

1

230-AGI-005

NH4Cl RECOVERY TANK AGITATOR

1

230-TAK-005

NH4Cl RECOVERY TANK

1

230-SLP-005|105

NH4Cl RECOVERY TRANSFER PUMP

2

UNIT 240

MgP-MAGNESIUM CARBONATATION UNIT- PRECIPITATION CIRCUIT

240-AGI-002

Mg CARBONATATION REACTOR #1 AGITATOR

1

240-TAK-002

Mg CARBONATATION REACTOR #1

1

240-SLP-202|302

Mg CARBONATATION TRANSFER PUMP

2

240-SLP-002|102

Mg CARBONATATION RECIRC. PUMP

2

240-MIX-002

Mg CARBONATION STATIC MIXER

1

240-AGI-003

Mg CARBONATATION REACTOR #2 AGITATOR

1

240-TAK-003

Mg CARBONATATION REACTOR #2

1

240-SLP-203|303

Mg CARBONATATION TRANSFER PUMP

2

240-SLP-003|103

Mg CARBONATATION RECIRC. PUMP

2

240-MIX-003

Mg CARBONATION STATIC MIXER

1

240-AGI-004

Mg CARBONATATION REACTOR #3 AGITATOR

1

240-TAK-004

Mg CARBONATATION REACTOR #3

1

240-SLP-204|304

Mg CARBONATATION FILTER FEED PUMPS

2

240-MIX-004

Mg CARBONATION STATIC MIXER

1

240-SLP-004|104

Mg CARBONATATION RECIRC. PUMP

2

UNIT 250

MgP-MAGNESIUM CARBONATATION UNIT- FILTRATION CIRCUIT

250-BLF-001

Mg CARBONATE RESIDUE BELT FILTER #1

1

250-VAP-001

Mg CARBONATE FILTER #1 VACUUM PUMP

1

250-SLP-001|101

NH4Cl PLS TRANSFER PUMP

2

250-CHU-001

Mg CARBONATE FILTER #1 CHUTE

1

313 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

250-SCC-001

Mg CARBONATE FILTER #1 SCREW CONVEYOR

1

250-SCC-005

Mg CARBONATE RESIDUE SCREW CONVEYOR

1

250-CBR-001

Mg CARBONATE RESIDUE CAKE BREAKER

1

250-CNV-001

Mg CARBONATE RESIDUE BELT CONVEYOR

1

unit 260

NH4Cl DEGASING

260-AGI-001

NH4Cl DEGASING TANK #1 AGITATOR

1

260-TAK-001

NH4Cl DEGASING TANK #1

1

260-HTX-001|101

NH4Cl DEGASING HEAT EXCHANGER

2

260-AGI-002

NH4Cl DEGASING TANK #2 AGITATOR

1

260-TAK-002

NH4Cl DEGASING TANK #2

1

260-AGI-003

NH4Cl DEGASING TANK #3 AGITATOR

1

260-TAK-003

NH4Cl DEGASING TANK #3

1

260-SLP-003|103

NH4Cl DEGASING TRANSFER PUMP

2

UNIT 270

SCUBBER UNIT - VENTURI SCRUBBER CIRCUIT

270-SCR-001

VENTURI SCRUBBER

1

270-BLO-001

VENTURI SCRUBBER BLOWER

1

270-AGI-001

VENTURI SCRUBBER TANK AGITATOR

1

270-TAK-001

VENTURI SCRUBBER TANK

1

270-SLP-001|101

VENTURI SCRUBBER PUMP

2

270-HTX-001|101

VENTURI SCRUBBER COOLERS

2

270-CND-005

STAGE 2 LEACH CONDENSER

1

270-CND-004

STAGE 1 LEACH CONDENSER

1

270-CND-003

NH3 VENT CONDENSER

1

270-AGI-002

CONDENSED NH4OH TANK AGITATOR

1

270-TAK-002

CONDENSED NH4OH TANK

1

270-SLP-002|102

CONDENSED NH4OH PUMP

2

270-TAK-005

STAGE 2 LEACH CONDENSER SEPARATOR

1

270-TAK-004

STAGE 1 LEACH CONDENSER SEPARATOR

1

270-TAK-003

NH3 VENT CONDENSER SEPARATOR

1

UNIT 280

MAGNESIUM CARBONATATION UNIT- AMMONIUM CARBONATE CIRCUIT

280-AGI-001

(NH4)2CO3 COLUMN #1 AGITATOR

1

280-TAK-001

(NH4)2CO3 COLUMN #1

1

280-JTP-001

(NH4)2CO3 COLUMN #1 JET PUMP

1

280-AGI-002

(NH4)2CO3 COLUMN #2 AGITATOR

1

280-TAK-002

(NH4)2CO3 COLUMN #2

1

280-JTP-002

(NH4)2CO3 COLUMN #2 JET PUMP

1

280-AGI-003

(NH4)2CO3 COLUMN #3 AGITATOR

1

280-TAK-003

(NH4)2CO3 COLUMN #3

1

280-JTP-003

(NH4)2CO3 COLUMN #3 JET PUMP

1

280-AGI-004

(NH4)2CO3 HOLDING TANK AGITATOR

1

280-TAK-004

(NH4)2CO3 HOLDING TANK

1

280-SLP-001|101

(NH4)2CO3 FEED PUMP

2

280-TAK-005

CO2 KNOCKOUT VESSEL

1

314 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

280-BLO-001

CO2 BLOWER

1

Source: L3 2026

 

Area 300 - Hydrochloric Acid Leach

The summarized equipment list for Area 300 - Hydrochloric Acid Leach is presented as Table 14‑27.

Table 14‑27: Area 300 - Hydrochloric Acid Leach Summary Equipment List

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

UNIT 300

WPL-HCl LEACH

300-BIN-001

NH4Cl LEACH RESIDUE DAY BIN

1

300-LBF-001

NH4Cl LEACH RESIDUE LIVE BOTTOM FEEDER

1

300-SCC-001

NH4Cl LEACH RESIDUE SCREW CONVEYOR

1

300-AGI-001

HCl LEACH FEED MIXING TANK AGITATOR

1

300-TAK-001

HCl LEACH FEED MIXING TANK

1

300-HTX-001|101

HCl LEACH FEED HEAT EXCHANGER

2

300-SLP-001|101

HCl LEACH FEED PUMP

2

300-AGI-002

1ST STAGE HCl LEACH AGITATOR TANK

1

300-TAK-002

1ST STAGE HCl LEACH TANK

1

300-SLP-002|102

1ST STAGE HCl LEACH RECIRC.PUMP

2

300-HTX-002|102

1ST STAGE HCl LEACH HEAT EXCHANGER

2

300-SLP-202|302

1ST STAGE HCl LEACH TRANSFER PUMP

2

300-AGI-003

1ST STAGE HCl LEACH AGITATOR TANK

1

300-TAK-003

1ST STAGE HCl LEACH TANK

1

300-SLP-003|103

1ST STAGE HCl LEACH RECIRC. PUMP

2

300-HTX-003|103

1ST STAGE HCl LEACH HEAT EXCHANGER

2

300-SLP-203|303

1ST STAGE HCl LEACH TRANSFER PUMP

2

300-HYC-001|002 |003|101|102

2ND STAGE HCl LEACH PRIMARY HYDROCYCLONE

5

300-AGI-004

2ND STAGE HCl LEACH TANK AGITATOR

1

300-TAK-004

2ND STAGE HCl LEACH TANK

1

300-SLP-004|104

2ND STAGE HCl LEACH RECIRC. PUMP

2

300-HTX-004|104

2ND STAGE HCl LEACH HEAT EXCHANGER

2

300-SLP-204|304

2ND STAGE HCl LEACH TRANSFER PUMP

2

300-AGI-005

2ND STAGE HCl LEACH TANK AGITATOR

1

300-TAK-005

2ND STAGE HCl LEACH TANK

1

300-SLP-005|105

2ND STAGE HCl LEACH RECIRC. PUMP

2

300-HTX-005|105

2ND STAGE HCl LEACH HEAT EXCHANGER

2

300-SLP-205|305

2ND STAGE HCl LEACH TRANSFER PUMP

2

300-HTX-006|106

HCl HEAT EXCHANGER

2

UNIT 310

HCL-1ST STAGE HCl LEACH FILTRATION

310-AGI-001

1ST STAGE HCI LEACH FILTRATION FEED TANK AGITATOR

1

310-TAK-001

1ST STAGE HCI LEACH FILTRATION FEED TANK

1

310-SLP-001|101

1ST STAGE HCI LEACH FILTER #1 FEED PUMP

2

310-SLP-002|102

1ST STAGE HCI LEACH FILTER #2 FEED PUMP

2

315 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

310-SLP-003|103

1ST STAGE HCI LEACH FILTER #3 FEED PUMP

2

310-CAF-001|002|101

1ST STAHE HCl LEACH CANDLE FILTERS

3

310-AGI-002

1ST STAGE HCl LEACH FILTER WASH #1 TANK AGITATOR

1

310-TAK-002

1ST STAGE HCl LEACH FILTER WASH #1 TANK

1

310-SLP-002|102

1ST STAGE HCl LEACH FILTER WASH #1 PUMPS

2

310-AGI-003

1ST STAGE HCl LEACH FILTER WASH #2 TANK AGITATOR

1

310-TAK-003

1ST STAGE HCl LEACH FILTER WASH #2 TANK

1

310-SLP-003|103

1ST STAGE HCl LEACH FILTER WASH #2 PUMPS

2

310-AGI-004

1ST STAGE HCl LEACH FILTER WASH #3 TANK AGITATOR

1

310-TAK-004

1ST STAGE HCl LEACH FILTER WASH #3 TANK

1

310-SLP-004|104

1ST STAGE HCl LEACH FILTER WASH #3 PUMPS

2

310-SCC-001

1ST STAGE HCl LEACH RESIDUE SCREW CONVEYOR

1

310-AGI-005

HCl LEACH PLS FEED TANK AGITATOR

1

310-TAK-005

HCl LEACH PLS FEED TANK

1

310-AGI-105

HCl LEACH PLS FEED TANK AGITATOR

1

310-TAK-105

HCl LEACH PLS FEED TANK

1

310-AGI-205

HCl LEACH PLS FEED TANK AGITATOR

1

310-TAK-205

HCl LEACH PLS FEED TANK

1

310-AGI-305

HCl LEACH PLS FEED TANK AGITATOR

1

310-TAK-305

HCl LEACH PLS FEED TANK

1

310-SLP-005

HCl LEACH PLS FEED PUMP

1

310-SLP-105

HCl LEACH PLS FEED PUMP

1

310-SLP-205

HCl LEACH PLS FEED PUMP

1

UNIT 320

HCl - HCl LEACH RESIDUE DEWATERING

320-HYC-001|002 |003|101|102

DEWATERING STAGE 1 PRIMARY HYDROCYCLONE

5

320-AGI-001

DEWATERING STAGE 1 TANK AGITATOR

1

320-TAK-001

DEWATERING STAGE 1 TANK

1

320-SLP-001|101

DEWATERING STAGE 1 TRANSFER PUMP

2

320-SLP-201|301

DEWATERING STAGE 1 RECIRC. PUMP

2

320-HYC-004|005 |006|104|105

DEWATERING STAGE 2 PRIMARY HYDROCYCLONE

5

320-AGI-002

DEWATERING STAGE 2 TANK AGITATOR

1

320-TAK-002

DEWATERING STAGE 2 TANK

1

320-SLP-002|102

DEWATERING STAGE 2 TRANSFER PUMP

2

320-SLP-202|302

DEWATERING STAGE 2 RECIRC. PUMP

2

320-HYC-007|008 |009|010|107|108

DEWATERING STAGE 3 PRIMARY HYDROCYCLONE

6

320-AGI-003

CANDLE FILTER FEED TANK AGITATOR

1

320-TAK-003

CANDLE FILTER FEED TANK

1

320-SLP-003|103

CANDLE FILTER FEED PUMP

2

320-SLP-203|303

DEWATERING STAGE 3 RECIRC. PUMP

2

320-CAF-001|002|101

HCl LEACH RESIDUE DEWATERING CANDLE FILTERS

3

320-SCC-001

HCl LEACH RESIDUE SCREW CONVEYOR

1

UNIT 330

HCl - HCl LEACH RESIDUE DRYING

330-SCH-001

HCl LEACH RESIDUE PRE-HEATER

1

316 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

330-CBR-001

HCl LEACH RESIDUE LUMP BREAKER

1

330-SCC-001

HCl LEACH RESIDUE SCREW CONVEYOR

1

330-CNV-001

HCl LEACH RESIDUE BELT CONVEYOR

1

330-BIN-001

HCl LEACH RESIDUE BIN

1

330-LBF-001

HCl LEACH RESIDUE LIVE BOTTOM FEEDER

1

330-DRY-001

HCl LEACH RESIDUE ROTARY DRYER

1

330-FLT-001

HCl LEACH RESIDUE BURNER FILTER

1

330-BLO-001

HCl LEACH RESIDUE BURNER BLOWER

1

330-BLO-002

HCl LEACH RESIDUE 0/G BLOWER

1

330-ESK-001

HCl LEACH RESIDUE EXHAUST STACK

1

330-SCC-002

HCl LEACH RESIDUE SCREW CONVEYOR

1

Source: L3 2026

Area 400 – Sulfuric Acid

The summarized equipment list for Area 400 – Sulfuric Acid is presented as Table 14‑28.

Table 14‑28: Area 400 – Sulfuric Acid Summary Equipment List

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

UNIT 400

ABK-ACID BAKE

400-HOP-001

ACID BAKE FEED MATERIAL HOPPER

1

400-SWF-001

PUG MILL SCREW FEEDER

1

400-CNV-001

PUG MILL ACID FEED CONVEYOR

1

400-CHU-001

ACID BAKE MIXING CHUTE

1

400-PUG-001

ACID BAKE PUG MILL

1

400-AGI-001

H2SO4 FEED TANK AGITATOR

1

400-TAK-001

H2SO4 FEED TANK

1

400-SLP-001|101

H2SO4 FEED PUMP

2

400-KLN-001

ACID BAKE KILN

1

400-FLT-001

ACID BAKE KILN BURNER INLET FILTER

1

400-BLO-001

ACID BAKE KILN BURNER BLOWER

1

400-CNV-002

ACID BAKE RESIDUE TRANSFER CONVEYOR

1

400-HTX-001|101

REGEN H2SO4 COOLER

2

400-BLO-002

ACID BAKE KLIN COLLECTOR BLOWER

1

400-ESK-001

ACID BAKE KLIN EXHAUST STACK

1

400-SCR-001

H2SO4 PRIMARY STAGE CONDENSING VENTURI

1

400-AGI-002

H2SO4 PRIMARY STAGE RECOVERY TANK AGITATOR

1

400-TAK-002

H2SO4 PRIMARY STAGE RECOVERY TANK

1

400-SLP-002|102

H2SO4 PRIMARY STAGE RECOVERY RECIRC. PUMP

2

400-HTX-002|102

H2SO4 PRIMARY STAGE RECOVERY CONDENSER

2

400-SCR-002

H2SO4 SECONDARY STAGE CONDENSING COLUMN

1

400-AGI-003

H2SO4 SECONDARY STAGE RECOVERY TANK AGITATOR

1

400-TAK-003

H2SO4 SECONDARY STAGE RECOVERY TANK

1

400-SLP-003|103

H2SO4 SECONDARY STAGE RECOVERY RECIRC. PUMP

2

400-HTX-003|103

H2SO4 SECONDARY STAGE RECOVERY CONDENSER

2

317 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

400-CND-004|104

H2SO4 SECONDARY STAGE O/H CONDENSER

2

400-TAK-004

H2SO4 SCRUBBER O/H KNOCK OUT VESSEL

1

400-VAP-001

H2SO4 SCRUBBER VACUUM PUMP

1

UNIT 410

WTL-WATER LEACH

410-HOP-001

ACID BAKE RESIDUE HOPPER

1

410-CBR-001

ACID BAKE CAKE BREAKER

1

410-LBF-001

WATER LEACH LIVE-BOTTOM FEEDER

1

410-HTX-001

WATER LEACH HEATER

1

410-AGI-001

WATER LEACH MIXING TANK AGITATOR

1

410-TAK-001

WATER LEACH MIXING TANK

1

410-SLP-001|101

WATER LEACH REACTOR TRANSFER PUMP

2

410-SLP-201|301

WATER LEACH REACTOR RECIRC. PUMP

2

410-AGI-002

WATER LEACH REACTOR #1 AGITATOR

1

410-TAK-002

WATER LEACH REACTOR #1

1

410-SLP-002|102

WATER LEACH REACTOR #1 TRANSFER PUMP

2

410-HTX-002|102

WATER LEACH REACTOR #1 HEATER

2

410-SLP-202|302

WATER LEACH REACTOR #1 RECIRC. PUMP

2

410-AGI-003

WATER LEACH REACTOR #2 AGITATOR

1

410-TAK-003

WATER LEACH REACTOR #2

1

410-SLP-003|103

WATER LEACH REACTOR #2 TRANSFER PUMP

2

410-HTX-003

WATER LEACH REACTOR #2 HEATER

1

410-SLP-203

WATER LEACH REACTOR #2 RECIRC. PUMP

1

410-AGI-004

WATER LEACH REACTOR #3 AGITATOR

1

410-TAK-004

WATER LEACH REACTOR #3

1

410-SLP-004|104

WATER LEACH REACTOR #3 TRANSFER PUMP

2

410-HTX-004

WATER LEACH REACTOR #3 HEATER

1

410-SLP-204

WATER LEACH REACTOR #3 RECIRC. PUMP

1

410-AGI-005

WTL PLS FILTER TANK AGITATOR

1

410-TAK-005

WTL PLS FILTER TANK

1

410-SLP-005|105

WTL PLS FILTER FEED PUMP

2

410-SLP-205|305

WTL PLS FILTER FEED PUMP

2

410-CAF-001|002

WTL PLS CANDLE FILTERS

2

410-AGI-006

WTL PLS FILTER WASH #1 TANK AGITATOR

1

410-TAK-006

WTL PLS FILTER WASH #1 TANK

1

410-SLP-006|106

WTL PLS FILTER WASH #1 PUMPS

2

410-AGI-007

WTL PLS FILTER WASH #2 TANK AGITATOR

1

410-TAK-007

WTL PLS FILTER WASH #2 TANK

1

410-SLP-007|107

WTL PLS FILTER WASH #2 PUMPS

2

410-AGI-008

WTL PLS FILTER WASH #3 TANK AGITATOR

1

410-TAK-008

WTL PLS FILTER WASH #3 TANK

1

410-SLP-008|108

WTL PLS FILTER WASH #3 PUMPS

2

410-SCC-001

WATER LEACH RESIDUE DEWATERING SCREW CONVEYOR

1

UNIT 420

WTL-WATER LEACH FILTRATION

318 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

420-HYC-001|002 |003|101|102

DEWATERING STAGE 1 HYDROCYCLONE

5

420-AGI-001

WATER LEACH DEWATERING STAGE 1 TANK AGITATOR

1

420-TAK-001

WATER LEACH DEWATERING STAGE 1 TANK

1

420-SLP-001|101

WATER LEACH DEWATERING STAGE 1 TRANSFER PUMP

2

420-SLP-201|301

WATER LEACH DEWATERING STAGE 1 RECIRC. PUMP

2

420-HYC-004|005 |006|104|105

DEWATERING STAGE 2 HYDROCYCLONE

5

420-AGI-002

WATER LEACH DEWATERING STAGE 2 TANK AGITATOR

1

420-TAK-002

WATER LEACH DEWATERING STAGE 2 TANK

1

420-SLP-002|102

WATER LEACH DEWATERING STAGE 2 TRANSFER PUMP

2

420-SLP-202|302

WATER LEACH DEWATERING STAGE 2 RECIRC. PUMP

2

420-HYC-007|008 |009|010|107|108

DEWATERING STAGE 3 HYDROCYCLONE

6

420-AGI-003

WATER LEACH DEWATERING STAGE 3 TANK AGITATOR

1

420-TAK-003

WATER LEACH DEWATERING STAGE 3 TANK

1

420-SLP-003|103

WATER LEACH DEWATERING STAGE 3 TRANSFER PUMP

2

420-CAF-001|002|101

WATER LEACH RESIDUE DEWATERING CANDLE FILTERS

3

420-SCC-001

WATER LEACH RESIDUE DEWATERING SCREW CONVEYOR

1

UNIT 430

HYD-HYDROLYSIS

430-AGI-003

HYDROLYSIS FEED TANK AGITATOR

1

430-TAK-003

HYDROLYSIS FEED TANK

1

430-SLP-003|103|203

HYDROLYSIS FEED PUMP

3

430-HTX-001|101

STAGE 1 HYDROLYSIS PRE-HEATER

2

430-MIX-001

STG 1 HYDROLYSIS MIXER

1

430-AGI-001

STG 1 HYDROLYSIS REACTOR AGITATOR

1

430-TAK-001

STG 1 HYDROLYSIS REACTOR

1

430-SLP-001|101

STG 1 HYDROLYSIS TRANSFER PUMP

2

430-HTX-002|102

STG 1 HYDROLYSIS HEATER

2

430-MIX-002

STG 2 HYDROLYSIS MIXER

1

430-HTX-201|301

STG 2 HYDROLYSIS PRE-HEATER

2

430-AGI-002

STG 2 HYDROLYSIS REACTOR AGITATOR

1

430-TAK-002

STG 2 HYDROLYSIS REACTOR

1

430-SLP-002|102

STG 2 HYDROLYSIS TRANSFER PUMP

2

430-HTX-003|103

STG 2 HYDROLYSIS HEATER

2

430-AGI-004

HYDROLYSIS BARREN TANK AGITATOR

1

430-TAK-004

HYDROLYSIS TANK AGITATOR

1

430-SLP-004|104

HYDROLYSIS BARREN TRANSFERT PUMP

2

UNIT 440

HYD-HYDROLYSIS FILTRATION

440-CAF-001|002|003|101

BARREN FILTRATION CANDLE FILTER

4

440-SCC-003

HYDROLYSATE SCREW CONVEYOR

1

440-CNV-001

HYDROLYSATE CONVEYOR

1

440-TAK-002

BARREN HOLDING TANK

1

440-SLP-001|101

BARREN TRANSFER PUMP

2

UNIT 450

HYD - HYDROLYSATE CALCINATION

450-BIN-001

HYDROLYSIS CAKE BIN

1

319 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

450-LBF-001

HYDROLYSIS CAKE DRYING LIVE BOTTOM FEEDER

1

450-SCC-001

HYDROLYSIS CAKE DRYING FEED SCREW CONVEYOR

1

450-RCA-001

HYDROLYSIS CAKE CALCINER

1

450-FLT-001

HYDROLYSIS CAKE DRYING BURNER INLET FILTER

1

450-BLO-001

HYDROLYSIS DRYER BURNER BLOWER

1

450-HTX-001

HYDROLYSIS CAKE DRYING WASTE HEAT RECOVERY

1

450-BLO-002

HYDROLYSIS CAKE DRYING CALCINER COLLECTOR BLOWER

1

450-ESK-001

HYDROLYSIS CAKE DRYING CALCINER EXHAUST STACK

1

Source: L3 2026

Area 500 – Chlorination

The summarized equipment list for Area 500 – Chlorination is presented as Table 14‑29.

Table 14‑29: Area 500 – Chlorination Summary Equipment List

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

UNIT 500

CHLORINATION UNIT

500-BIN-001

HYDROLYSATE FEED BIN

1

500-BIN-002

PETROLEUM COKE FEED BIN

1

500-SCC-001

HYDROLYSATE SCREW CONVEYOR

1

500-SCC-002

PETROLEUM COKE SCREW CONVEYOR

1

500-CHU-001

CHLORINATION CHUTE

1

500-DIV-001

CHLORINATION DIVERTER VALVE

1

500-SWF-001|101

CHLORINATION SCREW FEEDER

2

500-CLN-001|101

CHLORINATOR

2

500-CYC-001|101

CYCLONE BANK

2

500-ROV-001|101

ROTARY VALVE

2

500-EFR-001

CHLORINATED MIX METALS ELECTROFILTER

1

500-SCR-001

Nb/Fe CONDENSER

1

500-SLP-001|101

Nb/Fe CONDENSER DISCHARGE PUMP

2

500-SLP-002|102

Nb/Fe CONDENSER CIRCULATION PUMP

2

500-HTX-001|101

Nb/Fe CONDENSER COOLER

2

500-SLP-003|103

Nb/Fe CONDENSER CRUDE TiCl4 DISCHARGE PUMP

2

500-SCR-002

TiCl4 PRIMARY CONDENSER

1

500-SLP-004|104

TiCl4 PRIMARY CONDENSER CIRCULATION PUMP

2

500-HTX-002|102

TiCl4 PRIMARY CONDENSER COOLER

2

500-SLP-005|105

TiCl4 PRIMARY CONDENSER CRUDE TiCl4 DISCHARGE PUMP

2

500-SCR-003

TiCl4 SECONDARY CONDENSER

1

500-SLP-007|107

TiCl4 SECONDARY CONDENSER CIRCULATION PUMP

2

500-HTX-004|104

TiCl4 SECONDARY CONDENSER COOLER

2

500-SLP-006|106

TiCl4 SECONDARY CONDENSER DISCHARGE PUMP

2

UNIT 510

TiCl4 TREATMENT UNIT

510-TAK-001

CRUDE TiCl4 BUFFER TANK

1

510-SLP-001|101

CRUDE TiCl4 FEED PUMP

2

510-TAK-002

TiCl4 DEGAS TANK

1

320 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

510-HTX-001

CRUDE TiCl4 FEED HEATER

1

510-CND-001

TiCl4 DEGAS TANK CONDENSER

1

510-VLS-001

TiCl4 DEGAS REFLUX DRUM V-L SEPARATOR

1

510-TAK-003

TiCl4 DEGAS REFLUX DRUM

1

510-SLP-002|102

TiCl4 DEGAS REFLUX DRUM PUMP

2

510-TAK-004

TiCl4 VAPORIZOR #1

1

510-HTX-004

TiCl4 VAPORIZOR #1 HEATER

1

510-SLP-003|103

TiCl4 VAPORIZOR #1 PUMP

2

510-CND-002

TiCl4 VAPORIZOR #1 CONDENSER

1

510-VLS-002

TiCl4 VAPORIZOR #1 REFLUX DRUM V-L SEPARATOR

1

510-TAK-005

TiCl4 VAPORIZOR #1 REFLUX DRUM

1

510-TAK-006

TiCl4 VAPORIZOR #2

1

510-HTX-006

TiCl4 VAPORIZOR #2 HEATER

1

510-SLP-004|104

TiCl4 VAPORIZOR #2 PUMP

2

510-CND-003

TiCl4 VAPORIZOR #2 CONDENSER

1

510-VLS-003

TiCl4 VAPORIZOR #2 REFLUX DRUM V-L SEPARATOR

1

510-TAK-007

TiCl4 VAPORIZOR #2 REFLUX DRUM

1

510-SLP-005|105

TiCl4 PUMP

2

UNIT 520

TI PURIFICATION

520-TAK-001

TREATED TiCl4 TANK

1

520-SLP-001|101

TiCl4 STRIPPER FEED PUMP

2

520-SCR-001

TiCl4 STRIPPER

1

520-CND-001

TiCl4 STRIPPER O/H CONDENSER

1

520-VLS-001

TiCl4 STRIPPER O/H V-L SEPARATOR

1

520-TAK-002

TiCl4 STRIPPER O/H SEPARATOR

1

520-SLP-002|102

TiCl4 STRIPPER O/H SEPARATOR REFLUX PUMP

2

520-SLP-003|103

TiCl4 PUMP

2

520-HTX-001

TiCl4 STRIPPER REBOILER

1

520-TAK-003

TiCl4 PURIFICATION COLUMN FEED TANK

1

520-SLP-004|104

TiCl4 PURIFICATION COLUMN FEED PUMP

2

520-COL-002

TiCl4 PURIFICATION COLUMN

1

520-CND-002

TiCl4 PRODUCT O/H CONDENSER

1

520-VLS-002

TiCl4 STRIPPER O/H V-L SEPARATOR

1

520-TAK-005

TiCl4 PURIFICATION REFLUX DRUM

1

520-SLP-006|106

TiCl4 PURIFICATION REFLUX PUMP

2

520-SLP-007|107

TiCl4 RODUCT PUMP

2

550-TAK-006 TO 015

TiCl4 PRODUCT STORAGE TANKS (QTY: 11)

11

520-SLP-008|108

TiCl4 PRODUCT PUMP

2

520-TAK-004

TiCl4 PURIFICATION COLUMN REBOILER TANK

1

520-HTX-004

TiCl4 PURIFICATION COLUMN REBOILER HEATER

1

520-SLP-005|105

TiCl4 PURIFICATION COLUMN REBOILER PUMP

2

UNIT 530

Nb CHLORIDE RECOVERY UNIT

530-SCH-001

Nb/Fe CHLORIDE DRYER

1

321 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

530-CNV-001

Nb/Fe CHLORIDE CONVEYOR

1

530-BIN-001

Nb/Fe CHLORIDE FEED BIN

1

530-ROV-001

Nb/Fe CHLORIDE FEED BIN ROTARY VALVE

1

530-SCR-001

Nb/Fe RECOVERY CONDENSER

1

530-SLP-001|101

Nb/Fe CHLORIDE RECOVERY CONDENSER PUMP

2

530-SLP-002|102

Nb/Fe CHLORIDE RECOVERY CONDENSER CIRCULATION PUMP

2

530-HTX-001|101

Nb/Fe CHLORIDE RECOVERY CONDENSER COOLER

2

 

 

 

UNIT 540

TiCl4 VAPOR RECOVEY UNIT

540-SCR-001

TiCl4 VENT CONDENSER

1

540-SLP-001|101

TiCl4 VENT CONDENSER BOTTOM PUMP

2

540-TAK-001

TiCl4 VENT CONDENSER RECIRC TANK

1

540-SLP-002|102

TiCl4 VENT CONDENSER RECIRC PUMP

2

540-HTX-001|101

TiCl4 VENT CONDENSER COOLER

2

540-SLP-003|103

TiCl4 VENT CONDENSER TiCl4 PUMP

2

540-SCR-002

TiCl4 VENT SCRUBBER

1

540-TAK-002

TiCl4 VENT SCRUBBER TANK

1

540-SLP-202|302

TiCl4 VENT SCRUBBER RECIRC PUMP

2

540-SLP-402|502

TiCl4 VENT SCRUBBER SPENT LIQUOR PUMP

2

540-BLO-001

TiCl4 VENT SCRUBBER BLOWER

1

540-ESK-001

TiCl4 VENT SCRUBBER EXHAUST STACK

1

UNIT 550

CHLORINATION OFF GAS MANAGEMENT UNIT

550-TOX-001

THERMAL OXIDIZER

1

550-HTX-001|101

THERMAL OXIDIZER WASTE HEAT EXCHANGER

2

550-BIN-001

CaCO3 BIN

1

550-ROV-001

CaCO3 BIN ROTARY VALVE

1

550-TAK-001

CaCO3 SLACKER

1

550-AGI-001

CaCO3 SLACKER AGITATOR

1

550-MEP-001|101

LIME FEED PUMP

2

550-SCR-001

CHLORINATION WET FGD SCRUBBER

1

550-SLP-001|101

CHLORINATION WET FGD SCRUBBER RECIRCULATION PUMP

2

550-SLP-002|102

FDG SCRUBBER GYPSUM DISCHARGE PUMPS

2

550-FLT-001

CHLORINATION WET FGD SCRUBBER BLOWER INLET FILTER

1

550-BLO-001

CHLORINATION WET FGD SCRUBBER BLOWER

1

550-BLO-002

CHLORINATION WET FGD SCRUBBER VENT BLOWER

1

550-ESK-001

CHLORINATION WET FGD SCRUBBER VENT STACK

1

UNIT 560

Nb CHLORIDE HYDROLYSIS UNIT

560-TAK-001

Nb/Fe STAGE #1 HYDROLYSIS TANK

1

560-AGI-001

Nb/Fe STAGE #1 HYDROLYSIS TANK AGITATOR

1

560-SLP-001|101

Nb/Fe STAGE #1 HYDROLYSIS PUMP

2

560-CND-001

Nb/Fe STAGE #1 HYDROLYSIS CONDENSER

1

560-STG-001|101

Nb/Fe HYDROLYSIS steam generator (VP)

1

560-TAK-002

Nb/Fe STAGE #2 HYDROLYSIS TANK

1

322 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

560-AGI-002

Nb/Fe STAGE #2 HYDROLYSIS TANK AGITATOR

1

560-SLP-002|102

Nb/Fe STAGE #2 HYDROLYSIS PUMP

2

560-CND-002

Nb/Fe STAGE #2 HYDROLYSIS CONDENSER

1

560-TAK-003

Nb/Fe STAGE #3 HYDROLYSIS TANK

1

560-AGI-003

Nb/Fe STAGE #3 HYDROLYSIS TANK AGITATOR

1

560-SLP-003|103

Nb/Fe STAGE #3 HYDROLYSIS PUMP

2

560-CND-003

Nb/Fe STAGE #3 HYDROLYSIS CONDENSER

1

560-THK-001

Nb/Fe HYDROLYSIS CLARIFIER

1

560-SLP-004

Nb/Fe HYDROLYSATE SLURRY PUMP

2

560-COA-001

MINERAL OIL COALESCER TANK

1

560-SLP-005|105

MINERAL OIL COALESCER O/F PUMP

2

560-SLP-006|106

MINERAL OIL COALESCER U/F PUMP

2

560-TAK-005

Nb/Fe HYDROLYSIS FILTER FEED TANK

1

560-AGI-005

Nb/Fe HYDROLYSIS FILTER FEED TANK AGITATOR

1

570-SLP-205|305

Nb/Fe HYDROLYSIS FILTER FEED PUMP

2

560-CAF-001|101

Nb/Fe HYDROLYSIS CANDLE FILTER

2

560-TAK-006

Nb/Fe HYDROLYSIS FILTRATE TANK

1

560-AGI-006

Nb/Fe HYDROLYSIS FILTRATE TANK AGITATOR

1

570-SLP-206|306

Nb/Fe HYDROLYSIS FILTRATE PUMP

2

560-TAK-007

Nb/Fe HYDROLYSIS WASH WATER TANK

1

560-AGI-007

Nb/Fe HYDROLYSIS WASH WATER TANK AGITATOR

1

570-SLP-207|307

Nb/Fe HYDROLYSIS WASH WATER PUMP

2

560-SCC-001

Nb/Fe HYDROLYSATE SCREW CONVEYOR

1

560-BIN-001

Nb HYDROLYSATE CALCINING FEED BIN

1

560-LBF-001

Nb HYDROLYSATE LIVE BOTTOM FEEDER

1

560-SWF-001

Nb HYDROLYSATE SCREW FEEDER

1

560-SCC-002

Nb FEED SCREW CONVEYOR

1

560-RCA-001

Nb CALCINER

1

560-FLT-001

Nb CALCINER BURNER AIR FILTER

1

560-BLO-001

Nb CALCINER BURNER BLOWER

1

560-HTX-001

Nb WASTE HEAT RECOVERY

1

560-BLO-002

Nb/Fe COLLECTOR BLOWER

1

560-ESK-001

Nb/Fe EXHAUST STACK

1

560-TAK-007

Nb/Fe STAGE #1 HYDROLYSIS CONDENSER SEPARATOR

1

560-TAK-008

Nb/Fe STAGE #2 HYDROLYSIS CONDENSER SEPARATOR

1

560-TAK-009

Nb/Fe STAGE #3 HYDROLYSIS CONDENSER SEPARATOR

1

UNIT 570

MINERAL OIL CONDITIONNING

570-HTX-001

MINERAL OIL STRIPPER

1

570-MEP-001|101

MINERAL OIL PUMP

2

Source: L3 2026

Area 600 – Solvent Extraction

The summarized equipment list for Area 600 – Solvent Extraction is presented as Table 14‑30.

323 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Table 14‑30: Area 600 – Solvent Extraction Summary Equipment List

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

UNIT 600

REE EXTRACTION

600-COL-001

DGA-6 EXTRACTION COLUMN

1

600-COL-002

DGA-6 SCRUB COLUMN

1

600-AGI-001

DGA-6 SCB COLUMN SOLUTION TANK AGITATOR

1

600-TAK-001

DGA-6 SCB COLUMN SOLUTION TANK

1

600-SLP-001|101

DGA-6 SCB COLUMN SOLUTION PUMP

2

600-AGI-002

DGA-6 LO TANK AGITATOR

1

600-TAK-002

DGA-6 LO TANK

1

600-SLP-002|102

DGA-6 LO PUMP

2

600-TAK-003

DGA-6 RAFF COALESCER TANK

1

600-SLP-003|103

DGA-6 RAFF COALESCER PUMP

2

600-TAK-016

DGA-6 ORG TANK

1

600-AGI-016

DGA-6 ORG TANK AGITATOR

1

600-SLP-016|116

DGA-6 ORG FEED PUMP

2

600-TAK-017

DGA-6 STR LIQUOR COALESCER

1

600-SLP-017|117

DGA-6 STR LIQUOR PUMP

2

UNIT 610

ACID SCRUB

610-TAK-004

DGA-6 ACID SCRUB FEED TANK

1

610-SLP-004|104

DGA-6 ACID SCRUB FEED PUMP

2

610-MSE-001|101

DGA-6 ACID SCRUB MIXER-SETTLER

2

610-TAK-005

DGA-6 ACID SCRUB COALESCER

1

610-SLP-005|105

DGA-6 ACID SCRUB LIQUOR PUMP

2

610-AGI-006

DGA-6 ACID SCRUB NEUT. REACTOR #1 AGITATOR

1

610-TAK-006

DGA-6 ACID SCRUB NEUT. REACTOR #1

1

610-AGI-007

DGA-6 ACID SCRUB NEUT. REACTOR #2 AGITATOR

1

610-TAK-007

DGA-6 ACID SCRUB NEUT. REACTOR #2

1

610-AGI-008

DGA-6 ACID SCRUB NEUT. REACTOR #3 AGITATOR

1

610-TAK-008

DGA-6 ACID SCRUB NEUT. REACTOR #3

1

610-SLP-008|108

DGA-6 ACID SCRUB NEUT. FILTRATION FEED PUMP

1

610-BIN-009

DGA-6 ACID SCRUB NEUT. MgCO3 DAY BIN

1

610-ROV-009

DGA-6 ACID SCRUB NEUT. MgCO3 ROTARY VALVE

1

610-SCC-009

DGA-6 ACID SCRUB NEUT. SCREW CONVEYOR

1

610-AGI-010

DGA-6 ACID SCRUB NEUT. FILTER FEED TANK AGITATOR

1

610-TAK-010

DGA-6 ACID SCRUB NEUT. FILTER FEED TANK

1

610-SLP-010|110

DGA-6 ACID SCRUB NEUT. FILTER #1 FEED PUMP

2

610-SLP-011|111

DGA-6 ACID SCRUB NEUT. FILTER #2 FEED PUMP

2

610-SLP-012|112

DGA-6 ACID SCRUB NEUT. FILTER #3 FEED PUMP

2

610-CAF-001|002|003

DGA-6 ACID SCRUB NEUT. RESIDUE FILTER #1 TO #3

3

610-SCC-001

DGA-6 ACID SCRUB NEUT. RESIDUE SCREW CONVEYOR

1

610-AGI-013

DGA-6 ACID SCRUB NEUT. FILTER WASH #1 TANK AGITATOR

1

610-TAK-013

DGA-6 ACID SCRUB NEUT. FILTER WASH #1 TANK

1

610-SLP-013|113

DGA-6 ACID SCRUB NEUT. FILTER WASH #1 PUMP

2

324 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

610-AGI-014

DGA-6 ACID SCRUB NEUT. FILTER WASH #2 TANK AGITATOR

1

610-TAK-014

DGA-6 ACID SCRUB NEUT. FILTER WASH #2 TANK

1

610-SLP-014|114

DGA-6 ACID SCRUB NEUT. FILTER WASH #2 PUMP

2

610-AGI-015

DGA-6 ACID SCRUB NEUT. FILTER WASH #3 TANK AGITATOR

1

610-TAK-015

DGA-6 ACID SCRUB NEUT. FILTER WASH #3 TANK

1

610-SLP-015|115

DGA-6 ACID SCRUB NEUT. FILTER WASH #3 PUMP

2

UNIT 620

REE STRIP

620-MSE-002

DGA-6 STR 1

1

620-MSE-003

DGA-6 STR 2

1

620-MSE-004

DGA-6 STR 3

1

620-MSE-005

DGA-6 STR 4

1

UNIT 630

IRON REMOVAL

630-BIN-001

DGA-6 STRIP LIQ. NEUT. MgCO3 DAY BIN

1

630-ROV-001

DGA-6 STRIP LIQ. NEUT. MgCO3 ROTARY VALVE

1

630-SCC-001

DGA-6 STRIP LIQ. NEUT. MgCO3 SCREW CONVEYOR

1

630-AGI-001

DGA-6 STRIP LIQ. NEUT. REACTOR #1 AGITATOR

1

630-TAK-001

DGA-6 STRIP LIQ. NEUT. REACTOR #1

1

630-AGI-002

DGA-6 STRIP LIQ. NEUT. REACTOR #2 AGITATOR

1

630-TAK-002

DGA-6 STRIP LIQ. NEUT. REACTOR #2

1

630-AGI-007

DGA-6 STRIP LIQ. NEUT. REACTOR #3 AGITATOR

1

630-TAK-007

DGA-6 STRIP LIQ. NEUT. REACTOR #3

1

630-SLP-007|107

DGA-6 STRIP LIQ. NEUT. FILTRATION FEED PUMP

2

630-AGI-004

DGA-6 STRIP LIQ. NEUT. FILTER FEED TANK AGITATOR

1

630-TAK-008

DGA-6 STRIP LIQ. NEUT. FILTER FEED TANK

1

630-SLP-001|101

DGA-6 STRIP LIQ. NEUT. FILTER #1 FEED PUMP

2

630-SLP-002|102

DGA-6 STRIP LIQ. NEUT. FILTER #2 FEED PUMP

2

630-SLP-003|103

DGA-6 STRIP LIQ. NEUT. FILTER #3 FEED PUMP

2

630-CAF-001|002|003

DGA-6 STRIP LIQ. NEUT. RESIDUE FILTER #1 to #3

3

630-SCC-002

DGA-6 STRIP LIQ. NEUT. RESIDUE SCREW CONVEYOR

1

630-AGI-008

DGA-6 STRIP LIQ. NEUT. FILTER WASH #1 TANK AGITATOR

1

630-TAK-004

DGA-6 STRIP LIQ. NEUT. FILTER WASH #1 TANK

1

630-SLP-004|104

DGA-6 STRIP LIQ. NEUT. FILTER WASH #1 PUMP

2

630-AGI-005

DGA-6 STRIP LIQ. NEUT. FILTER WASH #2 TANK AGITATOR

1

630-TAK-005

DGA-6 STRIP LIQ. NEUT. FILTER WASH #2 TANK

1

630-SLP-005|105

DGA-6 STRIP LIQ. NEUT. FILTER WASH #2 PUMP

2

630-AGI-006

DGA-6 STRIP LIQ. NEUT. FILTER WASH #3 TANK AGITATOR

1

630-TAK-006

DGA-6 STRIP LIQ. NEUT. FILTER WASH #3 TANK

1

630-SLP-006|106

DGA-6 STRIP LIQ. NEUT. FILTER WASH #3 PUMP

2

UNIT 640

DG6 MAKEUP AND SCRUBBER

640-TAK-005

DG6 TOTE

1

640-SLP-005

DG6 TOTE PUMP

1

640-TAK-006

EH ALCOHOL TOTE

1

640-SLP-006

EH ALCOHOL TOTE PUMP

1

325 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

640-TAK-007

DGA-6 ORG. MAKEUP TANK

1

640-AGI-007

DGA-6 ORG. MAKEUP TANK AGITATOR

1

640-SLP-007|107

DGA-6 ORG. MAKEUP PUMP

1

640-SCR-001

DG6 ORGANIC SCRUBBER

1

640-CEP-001

DG6 ORGANIC SCRUBBER DISCHARGE PUMP

1

640-THK-002

DG6 ORGANIC SCRUBBER LAMELLA THICKENER

1

640-TAK-014

DG6 ORGANIC SCRUBBER TOTE

1

640-SLP-020

DG6 ORGANIC SCRUBBER TOTE PUMP

1

640-CEP-002

DG6 ORGANIC SCRUBBER CIRCULATION PUMP

1

640-SCR-002

DG6 ORGANIC CAUSTIC SCRUBBER

1

640-TAK-015

DG6 ORGANIC CAUSTIC SCRUBBER MAKEUP TANK

1

640-CEP-003|103

DG6 ORGANIC CAUSTIC SCRUBBER MAKEUP PUMP

2

640-FLT-001|101

DG6 ORGANIC CAUSTIC SCRUBBER DUPLEX CARTRIDGE FILTER

2

640-HTX-001

DG6 ORGANIC CAUSTIC SCRUBBER MAKEUP COOLER

1

640-HX-001

DG6 ORGANIC CAUSTIC SCRUBBER MAKEUP CHILLER

1

640-BLO-001

DG6 ORGANIC CAUSTIC SCRUBBER INDUCED DRAFT FAN

1

640-ESK-001

DG6 ORGANIC CAUSTIC SCRUBBER EXHAUST STACK

1

Source: L3, 2026

Area 700 – Rare Earth Separation

The summarized equipment list for Area 700 – Rare Earth Separation is presented as Table 14‑31.

Table 14‑31: Area 700 – Rare Earth Separation Summary Equipment List

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

UNIT 700

PRIMARY CIRCUIT

700-TAK-001

PC ORG. CIRCULATION TANK

1

700-SLP-001|101

PC ORG. CIRCULATION PUMP

2

700-MSE-002|01-06

PC EXT MIXER-SETTLER (6)

6

700-TAK-003

PC EXT RAFF COALESCER

1

700-SLP-003|103

PC EXT RAFF PUMP

2

700-MSE-003|01-16

PC SCB MIXER-SETTLER (16)

16

700-MSE-004|01-24

PC STR1 CRUDE Tb MIXER-SETTLER (24)

24

700-TAK-004

PC STR1 CRUDE Tb COALESCER

1

700-SLP-004|104

PC STR1 CRUDE Tb PUMP

2

700-MSE-005|01-06

PC STR2 CRUDE Dy MIXER-SETTLER (6)

6

700-TAK-005

PC STR2 CRUDE Dy COALESCER

1

700-SLP-005|105

PC STR2 CRUDE Dy PUMP

2

UNIT 710

NdPr CIRCUIT

710-TAK-001

NdPr ORG. CIRCULATION TANK

1

710-SLP-001|101

NdPr ORG. CIRCULATION PUMP

2

710-MSE-001|01-02

NdPr SAP MIXER-SETTLER (2)

2

710-TAK-002

NdPr SAP EFFLUENT COALESCER

1

710-SLP-002|102

NdPr SAP EFFLUENT PUMP

2

710-MSE-002|01-12

NdPr EXT MIXER-SETTLER (12)

12

326 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

710-TAK-003

NdPr EXT COALESCER

1

710-SLP-003|103

NdPr EXT PUMP

2

710-MSE-003|01-24

NdPr SCB MIXER-SETTLER (24)

24

710-MSE-004|01-06

NdPr STR MIXER-SETTLER (6)

6

710-TAK-004

NdPr STR COALESCER

1

710-SLP-004|104

NdPr STR PUMP

2

UNIT 720

Tb CIRCUIT

720-TAK-001

Tb ORG. CIRCULATION TANK

1

720-SLP-001|101

Tb ORG. CIRCULATION PUMP

2

720-MSE-001|01-02

Tb SAP1 MIXER-SETTLER (2)

2

720-TAK-002

Tb SAP1 COALESCER

1

720-SLP-002|102

Tb SAP1 PUMP

2

720-MSE-002|01-16

Tb EXT MIXER-SETTLER (16)

16

720-TAK-003

Tb EXT COALESCER

1

720-SLP-003|103

Tb EXT PUMP

2

720-MSE-003|01-12

Tb SCB MIXER-SETTLER (12)

12

720-MSE-004|01-02

Tb SAP2 MIXER-SETTLER (2)

2

720-TAK-004

Tb SAP2 COALESCER

1

720-SLP-004|104

Tb SAP2 PUMP

2

720-MSE-005|01-32

Tb SCV MIXER-SETTLER (32)

32

720-TAK-005

Tb SCV COALESCER

1

720-SLP-005|105

Tb SCV PUMP

2

720-MSE-006|01-24

Tb STR MIXER-SETTLER (24)

24

UNIT 730

Dy CIRCUIT

730-TAK-001

Dy ORG. CIRCULATION TANK

1

730-SLP-001|101

Dy ORG. CIRCULATION PUMP

2

730-MSE-001|01-02

Dy SAP MIXER-SETTLER (2)

2

730-TAK-002

Dy SAP COALESCER

1

730-SLP-002|102

Dy SAP PUMP

2

730-MSE-002|01-12

Dy EXT MIXER-SETTLER (12)

12

730-TAK-003

Dy EXT COALESCER

1

730-SLP-003|103

Dy EXT PUMP

2

730-MSE-003|01-24

Dy SCB MIXER-SETTLER (24)

24

730-MSE-004|01-06

Dy STR MIXER-SETTLER (6)

6

730-TAK-004

Dy STR COALESCER

1

730-SLP-004|104

Dy STR PUMP

2

UNIT 740

SEG RECOVERY

740-TAK-001

SEG RAFFINATE MIXING TANK

1

740-AGI-001

SEG RAFFINATE MIXING TANK AGITATOR

1

740-SLP-001|101

SEG RAFFINATE MIXING PUMP

2

740-TAK-002

SEG CARBONATE PRECIP. TANK #1

1

740-AGI-002

SEG CARBONATE PRECIP. TANK #1 AGITATOR

1

740-SLP-002|102

SEG CARBONATE PRECIP. TANK #1 PUMP

2

327 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

740-TAK-003

SEG CARBONATE PRECIP. TANK #2

1

740-AGI-003

SEG CARBONATE PRECIP. TANK #2 AGITATOR

1

740-SLP-003|103

SEG CARBONATE PRECIP. TANK #2 PUMP

2

740-TAK-004

SEG CARBONATE PRECIP. TANK #3

1

740-AGI-004

SEG CARBONATE PRECIP. TANK #3 AGITATOR

1

740-SLP-004|104

SEG CARBONATE PRECIP. TANK #3 PUMP

2

740-CLR-001

SEG CARBONATE CLARIFIER

1

740-SLP-005|105

SEG CARBONATE SLURRY PUMP

2

740-TAK-005

SEG CARBONATE FEED TANK

1

740-AGI-005

SEG CARBONATE FEED TANK AGITATOR

1

740-SLP-006|106

SEG CARBONATE FEED PUMP

2

740-CAF-001|101

SEG CARBONATE CANDLE FILTER #1/#2

2

740-SCC-001

SEG CARBONATE DEWATERING SCREW CONVEYOR

1

740-TAK-006

SEG CARBONATE FILTRATE TANK

1

740-SLP-007|107

SEG CARBONATE FILTRATE TANK PUMP

2

740-FLT-001|101

SEG CARBONATE FILTRATE DULPEX CARTRIDGE FILTER

2

740-LIW-001

SEG CARBONATE LOSS-IN-WEIGHT FEEDER

1

740-RD-001

SEG CARBONATE ROTARY DRYER

1

740-CHU-001

SEG CARBONATE DRYER CHUTE

1

740-FLT-002

SEG CARBONATE INLET FILTER

1

740-BLO-001

SEG CARBONATE CONVEYOR BLOWER

1

740-PCN-001

SEG CARBONATE PNEUMATIC CONVEYOR

1

740-PIA-001

SEG CARBONATE STORAGE CONVEYOR RIGID FILTER

1

740-SVL-001

SEG CARBONATE STORAGE CONVEYOR DROP VALVE

1

740-SIL-001

SEG CARBONATE PRODUCT STORAGE SILO

1

740-ROV-001

SEG CARBONATE PRODUCT STORAGE SILO ROTARY VALVE

1

740-LCL-001

SEG CARBONATE LOAD CELL

1

740-DUC-001

SEG CARBONATE DUST COLLECTOR

1

740-ROV-002

SEG CARBONATE DUST COLLECTOR ROTARY VALVE

1

740-BLO-002

SEG CARBONATE EXHAUST BLOWER

1

740-ESK-001

SEG CARBONATE EXHAUST STACK

1

UNIT 750

HREY RECOVERY

750-TAK-001

HREY RAFFINATE MIXING TANK

1

750-AGI-001

HREY RAFFINATE MIXING TANK AGITATOR

1

750-SLP-001|101

HREY RAFFINATE MIXING PUMP

2

750-TAK-002

HREY CARBONATE PRECIP. TANK #1

1

750-AGI-002

HREY CARBONATE PRECIP. TANK #1 AGITATOR

1

750-SLP-002|102

HREY CARBONATE PRECIP. TANK #1 PUMP

2

750-TAK-003

HREY CARBONATE PRECIP. TANK #2

1

750-AGI-003

HREY CARBONATE PRECIP. TANK #2 AGITATOR

1

750-SLP-003|103

HREY CARBONATE PRECIP. TANK #2 PUMP

2

750-TAK-004

HREY CARBONATE PRECIP. TANK #3

1

750-AGI-004

HREY CARBONATE PRECIP. TANK #3 AGITATOR

1

328 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

750-SLP-004|104

HREY CARBONATE PRECIP. TANK #3 PUMP

2

750-CLR-001

HREY CARBONATE CLARIFIER

1

750-SLP-005|105

HREY CARBONATE SLURRY PUMP

2

750-TAK-005

HREY CARBONATE FEED TANK

1

750-AGI-005

HREY CARBONATE FEED TANK AGITATOR

1

750-SLP-006|106

HREY CARBONATE FEED PUMP

2

750-CAF-001|101

HREY CARBONATE CANDLE FILTER #1 / #2

2

750-SCC-001

HREY CARBONATE DEWATERING SCREW CONVEYOR

1

750-TAK-006

HREY CARBONATE FILTRATE TANK

1

750-SLP-007|107

HREY CARBONATE FILTRATE TANK PUMP

2

750-FLT-001|101

HREY CARBONATE FILTRATE DUPLEX CARTRIDGE FILTER

2

750-LIW-001

HREY CARBONATE LOSS-IN-WEIGHT FEEDER

1

750-RD-001

HREY CARBONATE ROTARY DRYER

1

750-CHU-001

HREY CARBONATE DRYER CHUTE

1

750-FLT-002

HREY CARBONATE INLET FILTER

1

750-BLO-001

HREY CARBONATE CONVEYOR BLOWER

1

750-PCN-001

HREY CARBONATE PNEUMATIC CONVEYOR

1

750-PIA-001

HREY CARBONATE STORAGE CONVEYOR RIGID FILTER

1

750-SVL-001

HREY CARBONATE STORAGE CONVEYOR DROP VALVE

1

750-SIL-001

HREY CARBONATE PRODUCT STORAGE SILO

1

750-ROV-001

HREY CARBONATE PRODUCT STORAGE SILO ROTARY VALVE

1

750-LCL-001

HREY CARBONATE LOAD CELL

1

750-DUC-001

HREY CARBONATE DUST COLLECTOR

1

750-ROV-002

HREY CARBONATE DUST COLLECTOR ROTARY VALVE

1

750-BLO-002

HREY CARBONATE EXHAUST BLOWER

1

750-ESK-001

HREY CARBONATE EXHAUST STACK

1

UNIT 760

NdPr RECOVERY

760-BAG-001

OXALIC ACID BAG UNLOADER

1

760-ROV-001

OXALIC ACID ROTARY VALVE

1

760-CHU-001

OXALIC ACID FEED CHUTE

1

760-LIW-001

NdPr OXALIC ACID LOSS-IN-WEIGHT FEEDER

1

760-TAK-002

NdPr OXALATE PRECIP. TANK #1

1

760-AGI-002

NdPr OXALATE PRECIP. TANK #1 AGITATOR

1

760-SLP-002|102

NdPr OXALATE PRECIP. TANK #1 PUMP

2

760-TAK-003

NdPr OXALATE PRECIP. TANK #2

1

760-AGI-003

NdPr OXALATE PRECIP. TANK #2 AGITATOR

1

760-SLP-003|103

NdPr OXALATE PRECIP. TANK #2 PUMP

2

760-TAK-004

NdPr OXALATE PRECIP. TANK #3

1

760-AGI-004

NdPr OXALATE PRECIP. TANK #3 AGITATOR

1

760-SLP-004|104

NdPr OXALATE PRECIP. TANK #3 PUMP

2

760-TAK-005

NdPr OXALATE FEED TANK

1

760-AGI-005

NdPr OXALATE FEED TANK AGITATOR

1

760-SLP-005|105

NdPr OXALATE FEED PUMP

2

329 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

760-CAF-001|101

NdPr OXALATE CANDLE FILTER #1 / #2

2

760-SCC-001

NdPr OXALATE DEWATERING SCREW CONVEYOR

1

760-TAK-006

NdPr OXALATE FILTRATE TANK

1

760-SLP-006|106

NdPr OXALATE FILTRATE TANK PUMP

2

760-FLT-001|101

NdPr OXALATE FILTRATE DUPLEX CARTRIDGE FILTER

2

760-LIW-002

NdPr OXALATE LOSS-IN-WEIGHT FEEDER

1

760-RCA-001

NdPr OXALATE ROTARY CALCINER

1

760-CHU-002

NdPr OXALATE CALCINER CHUTE

1

760-FLT-002

NdPr OXALATE INLET FILTER

1

760-BLO-001

NdPr OXALATE CONVEYOR BLOWER

1

760-PCN-001

NdPr OXALATE PNEUMATIC CONVEYOR

1

760-PIA-001

NdPr OXALATE STORAGE CONVEYOR RIGID FILTER

1

760-SVL-001

NdPr OXALATE STORAGE CONVEYOR DROP VALVE

1

760-SIL-001

NdPr OXALATE PRODUCT STORAGE SILO

1

760-ROV-003

NdPr OXALATE PRODUCT STORAGE SILO ROTARY VALVE

1

760-LCL-001

NdPr OXALATE LOAD CELL

1

760-DUC-001

NdPr OXALATE DUST COLLECTOR

1

760-ROV-002

NdPr OXALATE DUST COLLECTOR ROTARY VALVE

1

760-BLO-002

NdPr OXALATE EXHAUST BLOWER

1

760-ESK-001

NdPr OXALATE EXHAUST STACK

1

UNIT 770

Tb RECOVERY

770-BAG-001

OXALIC ACID BAG UNLOADER

1

770-ROV-001

OXALIC ACID ROTARY VALVE

1

770-CHU-001

OXALIC ACID FEED CHUTE

1

770-LIW-001

Tb OXALIC ACID LOSS-IN-WEIGHT FEEDER

1

770-TAK-002

Tb OXALATE PRECIP. TANK #1

1

770-AGI-002

Tb OXALATE PRECIP. TANK #1 AGITATOR

1

770-SLP-002|102

Tb OXALATE PRECIP. TANK #1 PUMP

2

770-TAK-003

Tb OXALATE PRECIP. TANK #2

1

770-AGI-003

Tb OXALATE PRECIP. TANK #2 AGITATOR

1

770-SLP-003|103

Tb OXALATE PRECIP. TANK #2 PUMP

2

770-TAK-004

Tb OXALATE PRECIP. TANK #3

1

770-AGI-004

Tb OXALATE PRECIP. TANK #3 AGITATOR

1

770-SLP-004|104

Tb OXALATE PRECIP. TANK #3 PUMP

2

770-TAK-005

Tb OXALATE FEED TANK

1

770-AGI-005

Tb OXALATE FEED TANK AGITATOR

1

770-SLP-005|105

Tb OXALATE FEED TANK PUMP

2

770-CAF-001|101

Tb OXALATE CANDLE FILTER #1 / #2

2

770-SCC-001

Tb OXALATE DEWATERING SCREW CONVEYOR

1

770-TAK-006

Tb OXALATE LIQOUR TANK

1

770-SLP-006|106

Tb OXALATE FILTRATE TANK PUMP

2

770-FLT-001|101

Tb OXALATE FILTRATE DUPLEX CARTRIDGE FILTER

2

770-LIW-002

Tb OXALATE LOSS-IN-WEIGHT FEEDER

1

330 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

770-RCA-001

Tb OXALATE ROTARY CALCINER

1

770-CHU-002

Tb OXALATE CALCINER CHUTE

1

770-FLT-002

Tb OXALATE INLET FILTER

1

770-BLO-001

Tb OXALATE CONVEYOR BLOWER

1

770-PCN-001

Tb OXALATE PNEUMATIC CONVEYOR

1

770-PIA-001

Tb OXALATE STORAGE CONVEYOR RIGID FILTER

1

770-SVL-001

Tb OXALATE STORAGE CONVEYOR DROP VALVE

1

770-SIL-001

Tb OXALATE PRODUCT STORAGE SILO

1

770-ROV-003

Tb OXALATE PRODUCT STORAGE SILO ROTARY VALVE

1

770-LCL-001

Tb OXALATE LOAD CELL

1

770-DUC-001

Tb OXALATE DUST COLLECTOR

1

770-ROV-002

Tb OXALATE DUST COLLECTOR ROTARY VALVE

1

770-BLO-002

Tb OXALATE EXHAUST BLOWER

1

770-ESK-001

Tb OXALATE EXHAUST STACK

1

UNIT 780

Dy RECOVERY

780-BAG-001

OXALIC ACID BAG UNLOADER

1

780-ROV-001

OXALIC ACID ROTARY VALVE

1

780-CHU-001

OXALIC ACID FEED CHUTE

1

780-LIW-001

Dy OXALIC ACID LOSS-IN-WEIGHT FEEDER

1

780-TAK-002

Dy OXALATE PRECIP. TANK #1

1

780-AGI-002

Dy OXALATE PRECIP. TANK #1 AGITATOR

1

780-SLP-002|102

Dy OXALATE PRECIP. TANK #1 PUMP

2

780-TAK-003

Dy OXALATE PRECIP. TANK #2

1

780-AGI-003

Dy OXALATE PRECIP. TANK #2 AGITATOR

1

780-SLP-003|103

Dy OXALATE PRECIP. TANK #2 PUMP

2

780-TAK-004

Dy OXALATE PRECIP. TANK #3

1

780-AGI-004

Dy OXALATE PRECIP. TANK #3 AGITATOR

1

780-SLP-004|104

Dy OXALATE PRECIP. TANK #3 PUMP

2

780-TAK-005

Dy OXALATE FEED TANK

1

780-AGI-005

Dy OXALATE FEED TANK AGITATOR

1

780-SLP-005|105

Dy OXALATE FEED TANK PUMP

2

780-CAF-001|101

Dy OXALATE CANDLE FILTER #1 / #2

2

780-SCC-001

Dy OXALATE DEWATERING SCREW CONVEYOR

1

780-TAK-006

Dy OXALATE FILTRATE TANK

1

780-SLP-006|106

Dy OXALATE FILTRATE TANK PUMP

2

780-FLT-001|101

Dy OXALATE FILTRATE DUPLEX CARTRIDGE FILTER

2

780-LIW-002

Dy OXALATE LOSS-IN-WEIGHT FEEDER

1

780-RCA-001

Dy OXALATE ROTARY CALCINER

1

780-CHU-002

Dy OXALATE CALCINER CHUTE

1

780-FLT-002

Dy OXALATE INLET FILTER

1

780-BLO-001

Dy OXALATE CONVEYOR BLOWER

1

780-PCN-001

Dy OXALATE PNEUMATIC CONVEYOR

1

780-PIA-001

Dy OXALATE STORAGE CONVEYOR RIGID FILTER

1

331 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

780-SVL-001

Dy OXALATE STORAGE CONVEYOR DROP VALVE

1

780-SIL-001

Dy OXALATE PRODUCT STORAGE SILO

1

780-ROV-003

Dy OXALATE PRODUCT STORAGE SILO ROTARY VALVE

1

780-LCL-001

Dy OXALATE LOAD CELL

1

780-DUC-001

Dy OXALATE DUST COLLECTOR

1

780-ROV-002

Dy OXALATE DUST COLLECTOR ROTARY VALVE

1

780-BLO-002

Dy OXALATE EXHAUST BLOWER

1

780-ESK-001

Dy OXALATE EXHAUST STACK

1

UNIT 790

SCANDIUM RECOVERY

790-TAK-001

NaOH ADJ. TANK

1

790-AGI-001

NaOH ADJ. TANK AGITATOR

1

790-SLP-006|106

PRESTRIPITATION NaOH PUMP

2

790-HTX-002|102

PRESTRIPITATION NaOH HEATER

2

790-TAK-002

Sc PRESTRIPITATION TANK #1

1

790-AGI-002

Sc PRESTRIPITATION TANK #1 AGITATOR

1

790-SLP-013|113

Sc PRESTRIPITATION TANK #1 PUMP

2

790-TAK-003

Sc PRESTRIPITATION TANK #2

1

790-AGI-003

Sc PRESTRIPITATION TANK #2 AGITATOR

1

790-SLP-014|114

Sc PRESTRIPITATION TANK #2 PUMP

2

790-THK-001

Sc PRESTRIPITATION THICKENER

1

790-SLP-007|107

Sc PRESTRIPITATION THK U/F PUMP

2

790-TAK-004

Sc BARREN ORG. TANK

1

790-AGI-004

Sc BARREN ORG. TANK AGITATOR

1

790-SLP-008|108

Sc BARREN ORG. PUMP

2

790-SLP-001|101

Sc BARREN ORG. CANDLE FILTER

2

790-TAK-010

Sc(OH)3 FILTER TANK

1

790-AGI-010

Sc(OH)3 FILTER TANK AGITATOR

1

790-SLP-015|115

Sc(OH)3 FILTER FEED PUMP

2

790-CAF-002

Sc(OH)3 CANDLE FILTER #1

1

790-CAF-003

Sc(OH)3 CANDLE FILTER #2

1

790-TAK-011

Sc(OH)3 FILTER WASH #1 TANK

1

790-AGI-011

Sc(OH)3 FILTER WASH #1 TANK AGITATOR

1

790-SLP-017|117

Sc(OH)3 FILTER WASH #1 PUMP

2

790-TAK-012

Sc(OH)3 FILTER WASH #2 TANK

1

790-AGI-012

Sc(OH)3 FILTER WASH #2 TANK AGITATOR

1

790-SLP-018|118

Sc(OH)3 FILTER WASH #2 PUMP

2

790-TAK-013

Sc(OH)3 FILTER FILTRATE TANK

1

790-AGI-013

Sc(OH)3 FILTER FILTRATE TANK AGITATOR

1

790-SLP-019|119

Sc(OH)3 FILTER FILTRATE PUMP

2

790-SCC-001

Sc(OH)3 RESIDUE DEWATERING SCREW CONVEYOR

1

UNIT 795

SCANDIUM PURIFICATION

795-TAK-001

Sc(OH)3 LEACH TANK

1

795-AGI-001

Sc(OH)3 LEACH TANK AGITATOR

1

332 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

795-SLP-001|101

Sc PLS PUMP

2

795-CAF-001

Sc PLS CANDLE FILTER #1

1

795-TAK-002

Sc FILTRATE TANK

1

795-SLP-002|102

Sc FILTRATE CENTRIFUGE PUMP

2

795-FLT-002|102

Sc FILTRATE DUPLEX CARTRIDGE FILTER

2

795-TAK-003

ScP EXT TANK

1

795-AGI-003

ScP EXT TANK AGITATOR

1

795-SLP-003|103

Sc LIQUOR PUMP

2

795-SLP-004|104

ScP LOADED ORG. PUMP

2

795-TAK-004

ScP LOADED ORG. TANK

1

795-AGI-004

ScP LOADED ORG. TANK AGITATOR

1

795-SLP-005|105

ScP STR LIQ PUMP

2

795-SLP-006|106

ScP BARREN ORG PUMP

2

795-TAK-005

ScP COND TANK

1

795-AGI-005

ScP COND TANK AGITATOR

1

795-SLP-007|107

ScP COND PUMP

2

795-TAK-006

ScP COND PHASE SEP. TANK

1

795-SLP-008|108

ScP COND ORG. PUMP

2

795-SLP-009|109

ScP EFFLUENT PUMP

2

795-BAG-001

OXALIC ACID BAG UNLOADER

1

795-CHU-001

OXALIC ACID FEED CHUTE

1

795-LIW-001

OXALIC ACID LOSS-IN-WEIGHT SCREW FEEDER

1

795-TAK-007

Sc OXALATE PRECIP. TANK

1

795-AGI-007

Sc OXALATE PRECIP. TANK AGITATOR

1

795-SLP-010|110

Sc OXALATE PRECIP. PUMP

2

795-BLF-001

Sc OXALATE VACUUM BELT FILTER

1

795-VAP-001

Sc OXALATE BELT FILTER VACUUM PUMP

1

795-TAK-008

Sc STRIP LIQUOR TANK

1

795-SLP-011|111

Sc STRIP LIQUOR PUMP

2

795-CHU-002

Sc OXALATE WET CAKE FILTER CHUTE

1

795-SCC-002

Sc OXALATE FILTER SCREW CONVEYOR

1

795-CBR-001

Sc OXALATE CAKE BREAKER

1

795-SCH-001

Sc OXALATE SCREW HEATER

1

795-CHU-003

Sc OXALATE LUMP BREAKER CHUTE

1

795-LB-001

Sc OXALATE LUMP BREAKER

1

795-SIL-001

Sc OXALATE LIVE BOTTOM FEEDER SILO

1

795-LBF-002

Sc OXALATE LIFE BOTTOM FEEDER

1

795-LIW-003

Sc OXALATE LOSS-IN-WEIGHT FEEDER

1

795-RCA-001

SCANDIUM OXIDE ROTARY CALCINER

1

795-SCC-004

SCANDIUM OXIDE SCREW CONVEYOR

1

795-SIL-002

SCANDIUM OXIDE PRODUCT SILO

1

795-ROV-001

SCANDIUM OXIDE ROTARY VALVE

1

795-LCL-001

SCANDIUM OXIDE LOAD CELL

1

333 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

795-FLT-003

SCANDIUM OXIDE DUST COLLECTOR INLET FILTER

1

795-DUC-001

SCANDIUM OXIDE DUST COLLECTOR

1

795-ROV-002

SCANDIUM OXIDE COLLECTOR ROTARY VALVE

1

795-BLO-001

SCANDIUM OXIDE EXHAUST BLOWER

1

795-ESK-001

SCANDIUM OXIDE EXHAUST STACK

1

795-TAK-009

D80 KEROSENE TOTE

1

795-SLP-012

D80 KEROSENE TOTE PUMP

1

795-TAK-010

ALAMINE 336 TOTE

1

795-SLP-013

ALAMINE 336 TOTE PUMP

1

795-TAK-011

ALIQUAT 336 TOTE

1

795-SLP-014

ALIQUAT 336 TOTE PUMP

1

795-TAK-012

TRIDECANOL TOTE

1

795-SLP-015

TRIDECANOL TOTE PUMP

1

795-TAK-013

ScP ORGANIC MAKEUP TANK

1

795-AGI-013

ScP ORGANIC MAKEUP TANK AGITATOR

1

795-SLP-016|116

ScP ORGANIC MAKEUP PUMP

2

795-SCR-001

ScP ORGANIC SCRUBBER

1

795-CEP-001

ScP ORGANIC SCRUBBER DISCHARGE PUMP

1

795-THK-002

ScP ORGANIC SCRUBBER LAMELLA THICKENER

1

795-TAK-014

ScP ORGANIC SCRUBBER TOTE

1

795-SLP-020

ScP ORGANIC SCRUBBER TOTE PUMP

1

795-CEP-002

ScP ORGANIC SCRUBBER CIRCULATION PUMP

1

795-SCR-002

ScP ORGANIC CAUSTIC SCRUBBER

1

795-TAK-015

ScP ORGANIC CAUSTIC SCRUBBER MAKEUP TANK

1

795-CEP-003|103

ScP ORGANIC CAUSTIC SCRUBBER MAKEUP PUMP

2

795-FLT-004|104

ScP ORGANIC CAUSTIC SCRUBBER DUPLEX CARTRIDGE FILTER

2

795-HTX-001

ScP ORGANIC CAUSTIC SCRUBBER MAKEUP COOLER

1

795-HX-001

ScP ORGANIC CAUSTIC SCRUBBER MAKEUP CHILLER

1

795-BLO-002

ScP ORGANIC CAUSTIC SCRUBBER INDUCED DRAFT FAN

1

795-ESK-002

ScP ORGANIC CAUSTIC SCRUBBER EXHAUST STACK

1

Source: L3 2026

Area 800 – Chloride Recovery

The summarized equipment list for Area 800 – Chloride Recovery is presented as Table 14‑32.

Table 14‑32: Area 800 – Chloride Recovery Summary Equipment List

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

UNIT 820

HCl RECOVERY

820-COL-001

HCl QUENCH TOWER

1

820-SLP-001|101

HCl QUENCH TOWER RECIRC. PUMP

2

820-HTX-001|101

HCl QUENCH COOLER

1

820-SLP-003|103

HCl QUENCH DISCHARGE PUMP

2

820-COL-002

HCl CONDENSER

1

334 | Page

 


SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

820-SLP-002|102

HCl CONDENSER RECIRC. PUMP

2

820-HTX-002|102

HCl CONDENSING CONDENSER

1

820-SLP-004|104

HCl CONDENSING DISCHRARGE PUMP

2

820-COL-011

HCl QUENCH TOWER

1

820-SLP-011|111

HCl QUENCH TOWER RECIRC. PUMP

2

820-HTX-011|111

HCl QUENCH COOLER

1

820-SLP-013|113

HCl QUENCH DISCHARGE PUMP

2

820-COL-012

HCl CONDENSER

1

820-SLP-012|112

HCl CONDENSER RECIRC. PUMP

2

820-HTX-012|112

HCl CONDENSING CONDENSER

1

820-SLP-014|114

HCl CONDENSER DISCHRARGE PUMP

2

820-AGI-005

REGENERATED HCl TANK AGITATOR

1

820-TAK-005

REGENERATED HCl TANK

1

820-SLP-005

REGENERATED HCl PUMP

2

UNIT 840

CHLORIDE PRE-EVAPORATION

840-AGI-001

CHLORIDE PRE-EVAPORATOR FEED TANK AGITATOR

1

840-TAK-001

CHLORIDE PRE-EVAPORATOR FEED TANK

1

840-SLP-001|101

CHLORIDE PRE-EVAPORATOR FEED PUMP

2

840-EVP-001

CHLORIDE PRE-EVAPORATOR

1

840-CND-001

CHLORIDE PRE-EVAPORATOR CONDENSER

1

840-AGI-001

CHLORIDE PRE-EVAPORATOR CONCENTRATE TANK AGITATOR

1

840-TAK-002

CHLORIDE PRE-EVAPORATOR CONCENTRATE TANK

1

840-SLP-002|102

CHLORIDE PRE-EVAPORATOR CONCENTRATE FEED PUMP

2

840-TAK-003

PRE EVAPORATOR O/H SEPARATOR

1

840-SLP-003|103

CHLORIDE PRE-EVAPORATOR RECIRC. PUMP

1

840-TAK-004

CHLORIDE PRE-EVAPORATOR CONDENSATE TANK

1

840-SLP-004|104

CHLORIDE CONDENSATE PUMP

2

UNIT 850

CHLORIDE SPRAY ROASTING

850-SPR-001

CHLORIDE PYROHYDROLYSIS SPRAY ROASTER

1

850-BUR-001

CHLORIDE PYROHYDROLYSIS SPRAY ROASTER BURNER

1

850-BUR-002

CHLORIDE PYROHYDROLYSIS SPRAY ROASTER BURNER

1

850-BLO-001

PYROHYDROLYSIS BURNER BLOWER

1

850-FIL-001

PYROHYDROLYSIS INLET FILTER

1

850-ROV-001

OXIDE RECOVERY ROTARY VALVE

1

850-FIL-002

OXIDE CONVEYOR INLET FILTER

1

850-PCN-001

OXIDE CONVEYOR PNEUMATIC CONVEYOR

1

850-CYC-001|002 |003|004|005|006|007|008

CHLORIDE PYROHYDROLYSIS CYCLONE

8

850-HTX-001

CHLORIDE PYROHYDROLYSIS WASTE HEAT RECOVERY

1

Source: L3 2026

Area 900 – Sulfate Effluent Treatment

The summarized equipment list for AREA 900 – Sulfate Effluent Treatment is presented as Table 14‑33.

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Table 14‑33: Area 900 – Sulfate Effluent Summary Equipment List

EQUIPMENT NUMBER

EQUIPMENT NAME

QTY

UNIT 950

SULFATE EFFLUENT NEUTRALIZATION

950-TAK-001

SULFATE EFFLUENT CaCO3 MIXING TANK

1

950-SLP-001|101

SULFATE EFFLUENT CaCO3 MIXING TANK PUMPS

2

950-LBF-001

SULFATE EFFLUENT WTL RESIDUE LIVE BOTTOM FEEDER

1

950-LBF-002

SULFATE EFFLUENT CaCO3 LIVE BOTTOM FEEDER

1

950-SCC-001

SULFATE EFFLUENT CaCO3 BY-PASS SCREW CONVEYOR

1

950-TAK-002

SULFATE EFFLUENT CaCO3 TANK #2

1

950-TAK-003

SULFATE EFFLUENT CaCO3 TANK #3

1

950-TAK-004

SULFATE EFFLUENT CaCO3 TANK #4

1

950-SLP-004|104

SULFATE EFFLUENT CaCO3 PUMPS

2

950-BIN-001

SULFATE EFFLUENT CaO FEED BIN

1

950-SCC-021

SULFATE EFFLUENT CaO FEED CONVEYOR

1

950-TAK-020

SULFATE EFFLUENT CaO MIXING TANK

1

950-SLP-020|120

SULFATE EFFLUENT CaO MIXING TANK PUMPS

2

950-CLR-020

SULFATE EFFLUENT CaO CLARIFIER

1

950-SLP-022|122

SULFATE EFFLUENT CaO SLURRY PUMPS

2

950-TAK-025

SULFATE EFFLUENT CaO PUMP BOX

1

950-SLP-023|123

SULFATE EFFLUENT CaO TRANSFER PUMPS

2

950-TAK-021

SULFATE EFFLUENT CaCO3 TANK #1

1

950-TAK-022

SULFATE EFFLUENT CaCO3 TANK #2

1

950-TAK-023

SULFATE EFFLUENT CaCO3 TANK #3

1

950-SLP-021|121

SULFATE EFFLUENT CaO PUMPS

2

950-BLF-030

SULFATE EFFLUENT CaO BELT FILTER #1

1

950-SCC-030

SULFATE EFFLUENT CaO BELFILTER #1 SCREW CONVEYOR

1

950-SLP-030|130

SULFATE EFFLUENT CaO FILTRATION TRANSFER PUMPS

2

950-BLF-031

SULFATE EFFLUENT CaO BELT FILTER #2

1

950-SCC-031

SULFATE EFFLUENT CaO BELFILTER #2 SCREW CONVEYOR

1

950-SLP-031|131

SULFATE EFFLUENT CaO FILTRATION TRANSFER PUMPS

2

950-SCC-032

SULFATE EFFLOUENT CaO CAKE SCREW CONVEYOR

1

950-BLF-040

SULFATE EFFLUENT CaO BELT FILTER #3

1

950-SCC-040

SULFATE EFFLUENT CaO BELFILTER #3 SCREW CONVEYOR

1

950-SLP-040|140

SULFATE EFFLUENT CaO FILTRATION TRANSFER PUMPS

2

950-BLF-041

SULFATE EFFLUENT CaO BELT FILTER #4

1

950-SCC-041

SULFATE EFFLUENT CaO BELFILTER #4 SCREW CONVEYOR

1

950-SLP-041|141

SULFATE EFFLUENT CaO FILTRATION TRANSFER PUMPS

2

Source: L3 2026

14.5.3 Pyrometallurgical Plant

Major Equipment Sizing and Cost Basis

Based on the established design criteria and mass balance results, major process equipment and selected minor equipment items were sized for the pyrometallurgical plant. Equipment sizing formed

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the basis for the capital and operating cost estimates presented in this study. Allowances were included for auxiliary systems, minor equipment, and supporting facilities required to provide a complete and operable installation.

The principal equipment items included in the capital cost estimate are listed in Table 14‑34.

Table 14‑34: Pyrometallurgical processing major equipment list.

Induction Furnace preparation Feed area

img170397038_131.jpg

 

Equipment Name

Qty

Description/Size/Model

FeNb Off Spec Operations Bin

1

1.37 m dia. x 2.28 m height

Disk Pelletizer

1

2.0m dia.

Rotative calciner

1

1.76m dia. X 3.91m long

FeNb Furnace

1

Electric Arc Furnace, - 6.00m3, 1000kW

FeNb Pelletizing Basin

1

1.5m x 1.5m x 1.5m

Rotary Dryer

1

1.21m dia. x 3.60m length

Slag Jaw Crusher

1

Screening System

1

Cooling Tower

1

Dust Collection

1

Source: MCS 2026

14.6 Power Requirements

14.6.1 Surface Crushing, Ore Storage & Mineral Processing Plant

The power requirements for the comminution circuit were developed based on the process design criteria established for the Project. The primary and ancillary equipment power requirements are summarized in Section 14.5.1, Table 14‑23 and Table 14‑24.

14.6.2 Hydrometallurgical Plant

The total installed power for the Hydrometallurgical process plant including areas 100 through 900 is 18,861 kVA. After applying the power factor and a 92% utilization rate, the installed operating

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power requirement is 17,352 kVA, which gives a total annual electrical energy consumption 149,379 MVAh/y. A summary unit breakdown is shown in Table 14‑35.

 

Table 14‑35: Installed power breakdown

Processing Unit

 

Units

Value

Hydrometallurgy

 

kVA

13,431

Solvent Extraction

 

kVA

739

Hydrochloric Acid Regen

 

kVA

4,691

Total

 

kVA

18,861

Source: L3 2026

14.6.3 Pyrometallurgical Plant

For the Pyrometallurgical process plant, the total installed power is 5,200 kVA (including the furnace). After applying the power factor and a 90% utilization rate, the installed operating power requirement is 3,500 kVA, which gives a total annual electrical energy consumption of 30,724 MVAh/y. The power requirement was estimated based on scoping test work and from calculations from previous FeNb test work (XPS, KPM, and Hazen). Furnace equipment / technology vendors also confirmed the estimated power requirement for the FeNb Furnace, as summarized in Table 14‑36.

Table 14‑36: FeNb Furnace Power Requirements

  Furnace Power Parameter

Units

Value

Electrical Power per ton Furnace Feed

kWh/t

334

Furnace Efficiency

%

60

Total Peak Power Input

kW

950

Furnace Design Power

kW

1,000

Source: Tetra Tech, 2017

14.7 Plant Layout

14.7.1 General

The site process facilities include the Mineral Processing Plant, Hydrometallurgical Plant and the Pyrometallurgical Plant (Figure 14‑14). These facilities, as well as other support and Infrastructure facilities, are located west of State Hwy 50, and south of County Road 721.

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img170397038_132.gif

Source: Dumas 2026

Figure 14‑14: Process Plant Layout

14.7.2 Mineral Processing Plant, Surface Crushing and Ore Storage

 

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14.7.3 Hydrometallurgical Plant

The Hydromet Plant building is a very large multi-level engineered steel structure with dimensions approximately 550 ft x 200 ft (167.64 m x 60.96 m) with a 100 ft (30.5 m) eave height. The building will house the equipment on two levels for the individual processes required to produce the scandium, rare earth and titanium products along with the niobium intermediate product that is then sent to the pyromet plant. The equipment has been placed to allow for ease of material movement and maintenance access. Some of the equipment, such as the calcinators and kilns, will be located outside on elevated steel support structures adjacent to the building. The electrical room is centrally located on the west side of the building. Personnel areas such as offices, break rooms, maintenance rooms and the Control Room are located near the electrical room. Longitudinally the building is split into three long bays to allow two separate 20-ton bridge cranes to service the east and west sides of the building. The center bay is open for vehicle and maintenance access.

img170397038_133.jpg

Figure 14‑15: Hydromet Plant

14.7.4 Pyrometallurgical Plant

Figure 14‑16 through Figure 14‑22 depict the pyromet plant. The pyromet building will house most of its equipment within a single building. This building will be an engineered steel structure with dimensions approximately 150 ft x 150 ft (45.7 m x 45.7 m ) with a 75 ft (22.9 m ) eave height. The open floor layout will allow for ease of material movement and maintenance of equipment.

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img170397038_134.jpg

Source: Tetra Tech, 2017

Figure 14‑16: Pyromet Building Southeast View

 

The bulk furnace feedstock storage and prep areas are located in the southwest quadrant of the building and utilize inclined sidewall conveyors to elevate the feed product into the storage bins.

 

img170397038_135.jpg

Source: Tetra Tech, 2017

Figure 14‑17: Bulk Feed and Storage

The furnace feed preparation is performed as a batch process with specified mass measurement of the niobium oxide and other reagents and fluxes done by the load cells fixed on each storage bins.

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Each ingredient, weighed accordingly to the recipe, is fed onto the furnace feed conveyor at the exact amount of quantity required for a batch.

 

img170397038_136.jpg

Source: Tetra Tech, 2017

Figure 14‑18: FeNb Furnace Feed System

 

The FeNb furnace, dryer, pelletization basin and product packaging are located on the east side of the building. The electrical room has been located close to the furnace to minimize the length of the high voltage water cooled cables for the furnace.

img170397038_137.jpg

Source: Tetra Tech, 2017

Figure 14‑19: FeNb Furnace, Pelletization Basin, Dryer and Packaging Equipment

 

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The personnel spaces such as offices, control room, restrooms and break room are located in the northwest quadrant of the building and utilize a two-level design to minimize the space requirements and to allow better communication.

img170397038_138.jpg

Source: Tetra Tech, 2017

Figure 14‑20: Office and Control Room

 

Several small building extensions are included to provide protection for reagent delivery equipment and the slag crusher equipment. A bridge crane shown in yellow below has been provided over the furnace equipment on the east side of the building to assist with maintenance and operation functions.

img170397038_139.jpg

Source: Tetra Tech, 2017

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Figure 14‑21: Pyromet Building Northwest View

 

The dust collection equipment which includes the baghouse, a fan and a stack is located outside of the building as are the cooling towers, pumps and water storage tanks containment area. All equipment is located close to its functional use point to minimize piping, ducting and energy consumption.

 

img170397038_140.jpg

Source: Tetra Tech, 2017

Figure 14‑22: Dust Collection and Cooling Systems

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15 Project Infrastructure

15.1 General Information Site Layout

There are several local communities near the Project site including Elk Creek, Syracuse, Tecumseh and Pawnee City that are capable of providing local housing for the Project construction and operating staff. There are several other communities within driving distance, and the large cities of Lincoln and Omaha are also within reasonable driving distance of the site. Both cities have substantial regional airports.

Presently, the site has no existing infrastructure except for access via the Nebraska state highway 50 and County Road 721 along with two core sheds to support field operations. The Project site will be accessed from County Road 721 through a guarded gatehouse into the Project property.

The site comprises an area of approximately 630 acres. Figure 15‑1 shows the layout. Note that tailings impoundments 5 and 6 are located east and south of the main plant site and are detailed in Section 15.11.

img170397038_141.jpg

Source: Dumas 2026

Figure 15‑1: Elk Creek Project Site Plan Layout

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15.2 Electrical Power

15.2.1 Microgrid

The local power utility (Omaha Public Power District) will provide approximately 200 kW of grid power to the site, using an existing connection to a powerline that runs on the east side of Highway 50.

A 6-acre parcel of land on the north side of the Property adjacent to County Road 721 has been set aside to host a third party microgrid to supply the majority of the power during construction and operations. This land area is adequate for the microgrid and will allow the micorogrid operator to access the microgrid directly from County Road 721.

The construction microgrid will consist of 6 x 2.5 MW natural gas fired generators, along the switchgear and transformers to provide power to surface and underground construction. The peak demand during construction is estimated to be 8 MW. The microgrid owner will construct, operate and maintain the microgrid, and the system has been designed with enough redundant generating capacity such that emergency backup generators will not be needed. The construction microgrid will be supplied with gas in two ways: via trucked LNG delivered to a storage and vaporization system located near the microgrid, and through a temporary gas pipeline connected to a distribution line located 5 miles east of the project site. The power demand for operations has been estimated to be 37 MW, and a larger, permanent microgrid will be deployed to service this need. This microgrid will be deployed by the same third party as the construction microgrid and will consist of 20 x 2.5 MW natural gas fired generators. Operation of this large microgrid will require the installation of a larger gas supply line from a local utility. This larger gas line will connect to a main distribution line located approximately 30 miles west of the project site and will be ready for service at the end of the second year of construction. The third-party owner of the microgrid will construct, operate and maintain the system over the life of the operation.

15.2.2 Electrical Power Distribution - Plant and Facilities

The microgrid will feed 13.8 kV power distribution lines for distribution to the surface plant, supporting infrastructure and mine.

15.2.3 Electrical Power Distribution – Underground

Underground electrical power is supplied at 13.8 kV from the Underground Electrical Maintenance Substation and Compressor Facility (Facility 23), which receives power from the main surface electrical distribution system. Redundant feeders routed through both the service and production ramps provide reliable power distribution to underground substations, where voltage is stepped down for mine infrastructure and operational loads. The system has been designed to provide reliable power to critical underground services, including ventilation, dewatering, communications, and refuge stations, while supporting the planned mining equipment and production requirements. As a greenfield project, all underground electrical infrastructure will be newly constructed

15.2.4 Emergency Power Generation

As both the construction and operational microgrids will have built-in redundancy, there will be no need for additional emergency generators at the project site.

 

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15.3 Control & Communications

15.3.1 Process Control System

Distributed processing will be implemented throughout the processing facilities. The Allen Bradley Control Logix 5000 PLC/PAC family of processors or equivalent will be used. Several networks will be utilized to maintain security, throughput and functionality.

15.3.2 Site Communications

Site communications are handled via phone service, radio communications and email communications. Internet service will be provided through a connection to an existing high speed fiber internet line that runs along the west side of the main property.

15.3.3 Access and Security System

The entire site will be enclosed with a barbed wire fence. Site access will be permitted through a manned security gate for vehicles, or through employee turnstiles operated electronically by card key. A security network will be installed, allowing for control of gate access and security camera control. Locked gates will be located around the facility perimeter to facilitate access for maintenance or areas that are not actively being used to support the project, as well as to provide access over the life of the project for additional construction activities such as those associated with future tailings impoundments.

15.4 Natural Gas

15.4.1 Natural Gas Pipeline to Site

Natural gas will be used throughout the Elk Creek during the construction and operation phases of the project. The initial supply for construction will be from either trucked LNG or from a temporary gas pipeline connected to a gas distribution pipeline located 5 miles east of the project site. As gas demand will be much higher during operations, a larger gas pipeline connected to a gas distribution pipeline located approximately 30 miles west of the facility will be constructed with an in-service date at the end of the second year of construction. The natural gas will be used to generate power using the on-site microgrid and is also essential to provide heat for surface building and the mine along with heat for the numerous high temperature operations contained in the surface production process.

15.4.2 Natural Gas Distribution on Site

Natural gas will be distributed to all on-site facilities utilizing HDPE natural gas distribution pipe. Natural gas piping located inside of facilities will consist predominately of carbon steel pipe. Maximum on-site pipeline distribution pressure will be 100 psi. Natural gas will be used for facility heating, water heating, and for natural gas-fired process equipment.

15.5 Plant Water

15.5.1 Water Treatment Plant

Water used for all on-site for all process needs and activities will be supplied from mine dewatering activities, recycling and from a local water utility (City of Tecumseh). Approximately 1,000 gpm of fresh water is needed to maintain a site water balance, and the supply from the City of Tecumseh will supply 1,500 gpm. Water from the mine and the surface water plant will be treated in a water

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treatment plant, which will produce a clean water stream for re-use in site operations as well as a solid salt that will be sent to the salt impoundment on the north side of the project site.

The Water Treatment System is designed to reduce the hardness, metals, and dissolved solids of the process wastewater, cooling tower blowdown, well/utility and mine water streams. The system consists of precipitation softening, clarification, pH adjustment, multimedia filtration (MMF), and reverse osmosis (RO). Concentrated brine from the RO system will be sent to a thermal evaporator and crystallizer to produce a salt cake for disposal with the distillate being returned and combined with RO permeate for reuse.

The Process Water Treatment System includes the following major equipment units:

(1)
Process Water Influent Equalization Tank
(2)
Softening Reactor
(3)
Clarifiers
(4)
pH Adjustment Reactor
(5)
Multimedia Filters
(6)
Reverse Osmosis Units
(7)
Sludge Holding Tank
(8)
Filter Presses (shared with CTMU system)
(9)
Evaporator/Crystallizer System
(10)
Crystallizer Solids Dewatering System
(11)
Chemical Feed Systems

The following Table 15‑1 was used as the design basis.

Table 15‑1: Design Requirements

Parameter

Quantity (gpm)

Notes

Plant Source Water

1,188

City of Tecumseh supply, mine formation water, water entrained in ore, water in reagents

Pyromet Feed Make-up

10

From RO Units

Hydromet Feed

2,231

Supplied from RO system, fresh water, water in reagents, water entrained in ore

Mine Operations

200

Supplied from fresh water

Cooling Towers

811

Supplied from RO system

Source: NioCorp 2019

 

The following is a summary description of the Proposed Water Treatment Plant.

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15.5.1.1 Flow Equalization

Process wastewater and underground mine water from NioCorp will be pumped into an equalization tank. Cooling Tower Blow Down (CTBD) will also be added to this tank since it will contain elevated total dissolved solids and hardness. The tank will also receive intermittent return flows from MMF backwash and the sludge dewatering system. The equalization tank will allow for storage during a shutdown and to sustain consistent flow to the system. The combined process wastewater and mine water will be pumped from the equalization tank to the softening reactor at a controlled rate. In the case of a system shutdown, it was assumed there would be enough storage capacity to accommodate reduced or no flow of mine water to the treatment system.

15.5.1.2 Softening Clarification

The combined streams will enter a Turbomix® softening reactor where chemicals will be added for precipitation softening. The advantage of the Turbomix design is that it promotes precipitation/crystallization of the dissolved particles to maximize their size and density. This results in faster settling rates, improved sludge handling characteristics, and improved sludge thickening and dewatering rates. To enhance the crystallization reaction kinetics and to maximize the density of the settled sludge, a portion of the precipitated sludge collected in the downstream clarification process will be recycled back to the Turbomix draft tube. Hydrated lime and soda ash will be fed to the Turbomix based on the flow rate, hardness, and alkalinity of the incoming water. A coagulant also will be added.

TheTurbomix reactor will overflow to two flocculating clarifiers to provide redundancy to allow one unit to be taken down for short durations for maintenance. A polymer will be added to the clarifier center well to promote flocculant growth and improve the settling characteristics of the precipitated solids. A rotating rake assembly including two long rake arms will move the settled solids to a center sludge discharge sump. The clarifier rake drive will be equipped with a high torque alarm and an automatic rake lift to raise the rotating rake mechanism should a torque overload condition occur.

The settled sludge will be withdrawn from the bottom of the clarifiers continuously by underflow pumps. The settled softening sludge is expected to have a solids concentration of close to 10%.

The clarifier effluent will be collected in a launder and will exit the clarifier through a drop box and be conveyed to the pH adjustment reactor tank ahead of the multimedia filters. The pH will be reduced to near neutral. This will allow any residual aluminum to precipitate for subsequent removal in the Multimedia Filter (MMF). An oxidant will also be added to this tank for ammonia removal. Water will be pumped from this tank to the MMF to further reduce the suspended solids prior to RO.

15.5.1.3 Multimedia Filtration

The effluent from the pH Adjustment Reactor (MMF Feedtank) is pumped to the MMF System. The goal of the filtration system is to reduce the inlet suspended solids concentration prior to RO. The vessels contain three separate layers of filtration media and a gravel support bed. The gravel supports the top three active filter layers consisting of anthracite, sand and fine garnet. This layered media profile provides a high sediment holding capacity as compared to conventional dual media/sand filters. The larger incoming particles are trapped on the upper layer of the media allowing the smaller particles to continue through the bed where they are trapped in the lower layers, producing a high-quality effluent. A filter aid will be added to the inlet of the MMF to enhance solids-liquid separation process and achieve deep bed filtration versus conventional surface filtration.

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During operation, the softened water enters the multimedia filter vessel under pressure at the top and is distributed uniformly over the top layer of the media bed. After passing through the media bed, the filtered service water exits the vessel through the under-drain assembly at the bottom. As the water flows through the media bed, the suspended solids and turbidity present in the feed water will be removed. The filter media bed slowly exhausts from top to bottom. When the turbidity and/or the differential pressure from the media bed approaches a predetermined set point, the media bed is exhausted and is subjected to cleaning/backwash cycle.

15.5.1.4 Reverse Osmosis (RO) System

Filtered water from the MMF is collected in the RO Feed Tank and will be pressurized through a single pass RO system for removal of total dissolved solids. A small portion of the filtered water will be utilized for Multimedia Filter backwash purposes.

The RO process separates dissolved contaminants from the feed water by passing through a semipermeable thin film composite membrane. These membranes remove 95 ~ 99% of the dissolved solids present in the feed water and essentially perform a complete removal of all particulate matter.

During operation, the filtered water from the RO feed tank is pumped to the cartridge filter vessels. The water pressure forces the feed water through the filter elements while leaving any residual impurities behind on the filter element surface. The cartridge slowly exhausts, and when they are clogged with impurities, the pressure drop across the cartridge filter system exceeds the desired limit, and the dirty filter elements are taken out of service for replacement. An antiscalant will be added at the RO cartridge filter inlet to prevent any potential scaling issues across the downstream RO system.

The filtered water from the cartridge filter is then pressurized using the RO booster pump and is fed to the first stage membranes in the RO system. The concentrate from the RO system is routed to the RO Reject Tank prior to being discharged. The concentrate will be sent to the evaporation / crystallization process for further concentration. The permeate stream from the system is collected in the RO Product tank where it blends with the distillate from the evaporator and crystallizer and is pumped to the Hydromet process, cooling tower and other water users.

Over a period of time, the RO membrane elements will be subjected to potential fouling by suspended material or sparingly soluble material that may be present in the feed water. Upon an increase of the feed pressure or decline of permeate quantity/quality, the RO system will be taken offline, and the membranes will be cleaned.

15.5.1.5 Sludge Handling

Sludge from the PW will be collected in a sludge storage tank.

Intermittently the sludge from the storage tank will be pumped to the filter presses for dewatering. Pumps are provided to feed the filter presses. Filter press filtrate will flow by gravity to the building sump and then pumped to the Process Water Equalization Tank using sump pumps. The building sump will also receive filter backwash from the MMFs.

15.5.1.6 Evaporation and Crystallization System

Evaporator Brine Flow

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The RO concentrate will be processed through an Evaporator/Crystallizer system to produce a salt cake for disposal. The RO concentrate contains a certain amount of alkalinity. In order to prevent calcium carbonate fouling of the Evaporator heat exchanger, it is important to eliminate all the carbonate alkalinity in the feed stream. This is accomplished in a three-stage process: feed acidification with sulphuric acid, feed preheating and feed deaeration / decarbonation. Feed acidification (via metered sulphuric acid addition) is performed within the Evaporator Feed Tank. The sulphuric acid converts the carbonate and bicarbonate ions to CO2. The CO2 is subsequently stripped out of the feed stream in the Feed Deaerator following heat recovery in the Feed Preheater. Brine from the Evaporator Feed Tank is pumped to the Feed Preheater where the temperature is increased by exchanging heat with the Evaporator and Crystallizer condensate. The feed then enters the Feed Deaerator where vapor and non-condensable gasses (NCGs) vented from the shell side of the Evaporator, heats the feed and allows for the release of CO2 to the atmosphere. The feed then enters the Evaporator.

The purpose of the Evaporator is to remove the majority of the water in the most energy and cost-efficient manner prior to the crystallization system. The feed flow enters the vapour body and is pumped up through the center of the heater via Evaporator Recirculation Pump. The recirculating brine stream is introduced into a vertical heat exchanger tube bundle utilizing a vendor double distributor plate design. The brine falls down the inside of the heater tubes where it is heated by vapors condensing on the outside of the tubes, causing the brine to boil. The concentrated brine gathers in the vapor body below the heater, where it is recirculated again.

Antifoam can be added to the Evaporator on an as needed basis to ensure that no liquid is carried over through the mist eliminators. Caustic is added to the Evaporator to maintain the pH between 8.0 and 8.5 to ensure the system will not be susceptible to corrosion.

The concentrated brine leaves the Evaporator via a purge line off the discharge of the Evaporator Recirculation Pump and is pumped to the Crystallizer Feed Tank for further concentration.

Low-pressure steam is created by the auxiliary boiler. This steam is utilized for start-up purposes and as supplemental heat for the system when required.

Crystallizer Brine Flow

The concentrated brine from the Evaporator is pumped to the Crystallizer Feed Tank. Caustic is again added to the system at the Crystallizer Feed Tank. Caustic is needed at this point to make up for metal hydroxides that precipitate as the brine is concentrated. The target pH in the Crystallizer is 8.0-8.5. The Crystallizer is a forced circulation unit meaning the recirculation pump circulates the concentrated brine through the Crystallizer Heater, where heat is transferred through the tubes. The hydrostatic head from the level in the Crystallizer Vapor Body suppresses boiling in the tubes. This prevents scaling that may occur if dry spots form on the heater tubes (which can be the case if boiling occurs in the tubes).

Brine entering the Crystallizer Vapor Body from the heater flash boils and releases heat in the form of water vapor. The concentrated brine collects in the vapor body and is re-circulated through the heater again. As the evaporation process continues, the concentration of the brine contained in the vapour body increases. As the concentration increases, the solution becomes supersaturated, and salts precipitate from solution resulting in a brine slurry.

Antifoam can be added to the Crystallizer on an as-needed basis to ensure that no liquid is carried over through the mist eliminators into the Crystallizer First Stage Fan during upset conditions.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Slurry from the Crystallizer is removed from the vapor body and is pumped through a recirculation loop to the Crystallizer Centrifuges by the Slurry Pump. The feed flow to each centrifuge is controlled to maintain the proper slurry density, ~25 wt% suspended solids, in the recirculating brine. The slurry is pumped from the vapour body, and a slipstream is diverted to each centrifuge for dewatering while the remaining portion recirculates back to the Crystallizer. This recirculating slurry highway is utilized to maintain a relatively high fluid velocity to avoid any solids settling and plugging in the piping.

The centrifuges process the Crystallizer product slurry. The resultant wet-cake is discharged for on-site disposal. The centrate is sent to the Centrate Tank and returned to the Crystallizer.

Make-up steam can be added as necessary but is normally only needed during start-up. Figure 15‑2 is the block flow diagram of the proposed Process Water Treatment Plant.

img170397038_142.jpg

Source: NioCorp 2019

Figure 15‑2: Process Water Treatment Plant Block Flow Diagram

 

15.5.2 Process Water

Process water will be produced at the Water Treatment Plant. Plant process water will be required in the Hydromet Plant, Paste Backfill Plant and the Pyromet Plant. Additional treated water will be required for both the Mine, as well as for site potable and fire water systems.

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The vast majority of process water will be required in the Hydromet Plant. The Paste Backfill Plant will utilize RO permeate for backfill, as will the mine for underground operations. The remaining plants identified will require small quantities of make-up water primarily for cooling and chilling purposes.

The overall water balance is shown in Figure 15‑3.

img170397038_143.gif

Source: NioCorp 2026

Figure 15‑3: Overall Water Balance

15.5.3 Fire Water

The firewater system will be comprised of two 225,000 gallon insulated fire water tanks and two independent firewater pumps capable of delivering 2,000 gpm for a minimum period of four hours. Both pumps will be powered by the facility microgrid, which has enough redundant generating capacity such that a dedicated emergency generator or diesel-powered pump is not needed. A fire water distribution system will be installed throughout the site. Dry and wet sprinkler systems, hydrants, hose reels and fire extinguishers will be utilized per the design.

All infrastructure facilities on the surface, except for the gate house, will include fire suppression systems. Process building fire suppression systems will include wet sprinklers in all office spaces and control rooms. Dry sprinkler systems will be utilized in the hydrometallurgical buildings within specified high hazard areas. The remaining open process/factory areas of these two process facilities, as well as the open areas of the mineral processing building, will utilize fire hose protection from outside hydrants, as well as interior located fire hose reels. The pyromet operation will have a separate fire protection system appropriate for use with molten metal.

15.5.4 Potable Water

Potable water will be supplied at an operational flow rate of 1500 gpm to dedicated potable water tankage. The supply will be furnished by the City of Tecumseh (1,500 gpm). Potable water will be distributed to all site facilities via a dedicated pumping system with redundancy at 50 psig pressure.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

The nominal flow rate will be 100 gpm for the entire facility, with a peak flow rate of 750 gpm during shower usage at shift change.

15.6 Auxiliary Buildings and Facilities

15.6.1 Mining Infrastructure

The Elk Creek Project includes several purpose-built surface facilities to support underground development and full-production operations. These facilities are strategically located in close proximity to the box-cut area and mine portals for operational efficiency and are illustrated on the General Site Plan (Drawing 4498-G-010).

Mine Dry, Underground Control Centre and First Aid Facility (Facility 31A)

Facility 31A houses the mine dry (change rooms, showers, lockers, and laundry facilities), the Underground Mine Control Centre for monitoring and remote operation of underground systems, the first-aid and emergency-response station, offices, lunchroom, muster room, and medical bay. The facility is located near the mine access box-cut area.

Railveyor Railcar Maintenance Facility (Facility 31B)

Facility 31B provides dedicated maintenance and service for the Railveyor train sets. The building is equipped with an overhead crane and a maintenance track loop that allows complete trains to be moved through the facility for inspection, repair, and component replacement.

Surface Vehicle Maintenance and Battery Charging Facility (Facility 31C)

Facility 31C serves as the surface maintenance shop for mobile equipment and the primary battery charging and swap station for the battery-electric vehicle fleet. The facility is sized to support initial development operations as well as complex repairs that are more efficiently performed on surface.

Mine Ventilation Plant (Facility 31D)

Facility 31D houses the main mine ventilation plant, including fans, heaters, and bulk air coolers. It is located in close proximity to the North Ramp portal. The ventilation plant design and capacity are detailed in Section 13.7.

Compressed Air and Electrical Substation Facility (Facility 23)

Facility 23 combines the surface compressed-air plant with the primary underground electrical distribution substation. It houses the main air compressors, dryers, receivers, and the 13.8 kV switchgear lineup that distributes power to surface facilities and the underground mine via redundant feeders in both the service ramp (Ramp 1) and production ramp (Ramp 2).

All facilities are new construction for this greenfield project and are integrated with the site utilities, stormwater management, and emergency power systems. Detailed general arrangements and elevations are provided in Drawings 4498-G-060 through 4498-G-076 and the associated Basis of Design documents.

The mining infrastructure described supports the full Life-of-Mine production schedule. Final facility layouts, equipment specifications, and architectural details will be completed during detailed engineering.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_144.jpg

Source: Dumas 2026

Figure 15‑4: Building 31 A – General Mine Admin, First Aid, Dry, and Underground Central Control

img170397038_145.jpg

Source: Dumas 2026

Figure 15‑5: Building 31C - Shop and Battery Charging

15.6.2 Supporting Infrastructure

Administration & Service Building

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

The Administration Building will consist of modular units or a long-term leased building that will house offices for support staff and site management. Dimensions will be 160 ft x 24 ft.

Maintenance Shop

The Maintenance Shop and the Warehouse will both be located in a single-story, steel-framed structure, 240 ft x 61 ft located centrally within the site. The Maintenance shop will include a wash bay and a Maintenance Shop area. The Warehouse will be the primary hub for receiving all parts and materials for the mine and processing facilities and shipping of all products.

Mobile Maintenance Shop

The Mobile Maintenance Shop will be equipped to service and maintain the surface vehicle fleet. It will consist of a single story, steel framed building measuring 180 ft x 70 ft.

Process Plant and Maintenance Modular Offices

Additional office space for processing area and maintenance personnel will be provided in modular units located in the vicinity of the Hydrometallurgical Building

Assay Laboratory

The Process Analysis Laboratory will be housed in a single story, steel-framed building located near the main processing facilities with dimensions of 80 ft x 48 ft.

Gate House

A Gate House, a portable lease building of 30 ft x 16 ft (9.1m x 4.9 m), will be located at the main site access point. The Gate House will host the security personnel controlling access into the site.

Geology Building

The Geology Building will supplement the existing two core shacks on site and serve as base of operations for the site geology team. It will include areas for drill core logging and processing as well as sample preparation. It will consist of a single story, steel-framed building measuring 100 ft x 40 ft.

Site Drainage

Stormwater will be collected on-site by a stormwater collection system that will consist of a combination of buried HDPE pipe and surface swales and ditches. Surface water from disturbed areas will be collected in a stormwater retention basin prior to its release into the local stream.

Stormwater that is collected from areas of potential contamination from hazardous material from process areas will be collected separately from other surface water sources and analyzed prior to discharge to the stormwater collection system. The fuel island, as well as the retention pond pipe inlet, will include oily water separators to ensure any petroleum that is in the surface water is not discharged to local waters and is collected for off-site disposal.

Sanitary Wastewater System

Sanitary wastewater will be collected in an underground PVC SR35 sewer piping network combining manholes and sewage lift stations. The system is designed for a peak flow rate of 750 gpm during peak shower usage and 27,300 gpd daily nominal volume. The sanitary wastewater will be routed to a sewage treated lagoon. The lagoon area will also include two buildings – the Aeration Blower shack (30 ft x 20 ft) and the NitrOx Blower shack (30’x20’). Treated water will be discharged to Elk Creek.

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First Aid Facilities

The Administration building, as well as the Mine Change building, will each have a first aid station for treatable on-site injuries. There will be an on-site emergency mine rescue vehicle and a rescue trailer.

Laydown Area / Cold Storage

During normal operation of the mine and processing facilities, there will be minimal need for laydown areas or additional, covered or enclosed storage. The spacing between buildings as well as the area for future tailings storage facilities has been chosen to provide adequate clearances for construction, and space for staging equipment and replacement parts for maintenance and plant turnarounds.

Reagent Storage

Reagents will be used in the Hydromet, Pyromet, Acid Plant, HCI Regeneration Plant and the Paste Backfill Plant. Liquid reagents will be stored in the reagent or raw material tank farm located adjacent to the Hydromet Plant. The tank farm will include truck unloading stations and transfer pumps to transfer reagent to their required process. All tanks of specific reagents will be isolated from other reagents and located within their own diked containment areas.

Products Storage, Packaging, Shipping

Process facilities will also store reagent tanks, bunkers, bins and silos. Additional plant reagents will be stored in the process buildings.

Packaging of the products will take place at the outlet of the respective final processing equipment, as a continuation of the process flow. Packaged products that won’t be immediately shipped to customers will be stored in the on-site warehouse.

The anticipated production rates of niobium and titanium products will warrant multiple shipments per week of each product via over-the-road vehicles. The anticipated production rate of scandium and rare earth products will yield much smaller volumes. Frequency of shipments of scandium and rare earth products will be less frequent, and the small volume of these containers will be stored inside the Maintenance / Warehouse Building until shipment.

The types and locations of loading and unloading facilities will be specific to the material or products being received and shipped.

Waste Storage

This storage area will include a concreted diked containment area for the storage of wastes, including any hazardous wastes generated at the facility prior to offsite disposal. The storage area will include a perimeter fence and a locked access gate.

Truck Scale

A truck scale will be located near the primary site access.

Fuel Storage - Surface Fuel Station

Fueling facility for surface vehicles will be provided.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

15.7 Roads

15.7.1 Main Access Road to Site

The primary access to the site will be from County Road 721. Access into the site will be controlled by security personnel stationed at the Guard Gate. The site access road will provide access to the mine, the administration building, reagent / supply unloading areas and all other locations at the main project site.

15.7.2 Secondary Site Access Roads

A second, emergency access to the site will be connecting to Nebraska State Route 50 approximately 0.75 miles south of the main access road. The secondary access will be used to access the core shed, geology building, mine, stormwater infrastructure and the sewage lagoon.

15.7.3 Secondary Site Roads

Secondary roads on site include access roads connecting the plant site to the tailings storge facilities and light vehicle access roads connecting infrastructure throughout the site. Light vehicles include light-duty pickups and service vehicles supporting infrastructure.

15.8 Carbonatite Rock Stockpile

The Carbonatite Stockpile has been designed to store approximately 1.4 million tons (Mtons) of Carbonatite and will be developed using a sequential approach involving site preparation, drainage collection system installation, waste rock material placement, and construction of the adjacent collection pond. The final Stockpile configuration is planned to have a maximum stack height of approximately 110 feet and an overall slope of 2.5H:1V (horizontal: vertical) (Figure 15‑6).

Tierra Group/BBA classified the Stockpile in accordance with the industry-accepted guidelines (Hawley and Cunning, 2017) for mine waste dumps and stockpiles. Based on site conditions (regional settings, foundation, and material quality) and design performance (geometry, physical stability, construction, and stability performance), the Stockpile was classified as a moderate (waste hazard class III) hazard. This classification process allows assignment of geotechnical design criteria for the facility based on potential consequences and does not reflect probability of failure.

The design basis was also defined in accordance with the Nebraska Administrative Code (NAC) Title 132 – Integrated Solid Waste Management Regulations. Where appropriate, additional design criteria were included based on professional judgment, standard engineering practices, and site-specific conditions.

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_146.jpg

Source: Tierra Group/BBA 2026

Figure 15‑6: Carbonatite Stockpile Layout

Given the current understanding of the characteristics of the stockpile material, it is reasonable to anticipate potential for constituents of concern in the material to have the potential to mobilize due to interaction with precipitation over the life of the project and in closure. Therefore, the containment design for the stockpile includes a composite liner system comprising (from bottom to top):

•
Prepared subgrade constructed by moisture conditioning and compacting native or fill materials to obtain a minimum Standard Proctor (ASTM D-698) density of 95%;
•
Geosynthetic Clay Liner (GCL);
•
60-mil (1.5mm) Linear Low Density Poly-Ethylene (LLDPE) double-sided textured geomembrane; and
•
A minimum 2-foot thick crushed, clean, and free-draining gravel fill placed in a single uncompacted lift above the geomembrane to provide drainage and protect the geomembrane during stockpile material placement.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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The GCL is equivalent or better than the prescribed low permeability soil liner and achieves a better degree of engineering control.

15.9 Surface Water Management for TSF and Temporary Stockpile Areas

15.9.1 Stockpile

The stockpile’s water management strategy separates non-contact and contact water. Non-contact water (surface runoff) will be diverted through diversion ditches outside the stockpile, while contact water will be conveyed through the drainage collection channel and stored in the Collection Pond. The collection pond is designed to contain the 100-year, 24-hour storm event.

The drainage collection system was designed to limit hydraulic head on the geomembrane and consists of primary pipes (250 mm, 10 inches), secondary pipes (150 mm, 6 inches), and tertiary pipes (100 mm, 4 inches) installed above the geomembrane within the drain fill (clean gravel). Tertiary pipes will convey flows to secondary pipes, which then convey flows to primary pipes, leading to the lined collection pond. The corrugated and perforated pipes collect infiltrated water for conveyance by gravity to the collection pond.

15.9.2 Tailings Storage Facility (“TSF”)

The surface water management plan aims to deliver technically and environmentally efficient water management infrastructure. The primary water management plan goals include:

•
Keep non-contact water separate from contact water by diverting runoff from undisturbed basins whenever possible and controlling the discharge to the natural drainage ways;
•
Categorize the contact water sources and manage them accordingly; and
•
Apply sedimentation and erosion best management practices (BMPs) when applicable.

The TSF internal water management is based on the low free water content of the tailings paste, which is expected to “bleed” only minimal water once deposited. Within the facility, each cell is designed with adequate freeboard to safely contain direct precipitation and stormwater runoff without the need for operational discharge. Any accumulated water will be pumped to the site water treatment system for recycling and reuse. The operational criteria for the TSF cells include provision for storage of extreme rainfall events without overflow through the spillway during normal operational conditions. However, during final cell filling and grading to achieve closure configuration, the spillway will act as an emergency outlet to prevent overtopping of the embankments and will become the primary outlet for post-closure surface water flows.

The water management strategy consists of capturing, collecting, conveying, and diverting surface runoff within the TSF area (TSF West Cells and TSF East Cells). Table 15‑2 summarizes the surface water management infrastructure within the TSF area, while Figure 15‑7 and Figure 15‑8 illustrate the conceptual water management system

Table 15‑2: TSF Infrastructure Description

Infrastructure

Description

Non-Contact Water Diversion

The non-contact water diversion channel will convey runoff from undisturbed watershed basins surrounding the facility and safely divert it to natural drainage channels. The TSF diversion channel has been designed for this purpose. The channel is designed for the

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Infrastructure

Description

 

100-year return-period storm event, while incorporating a configuration that facilitates future upgrading to accommodate the 500-year return-period closure design event.

Stormwater Pond (West Cells)

This structure was designed to collect and store surface water runoff generated from the box cut disturbance area and the watershed basin located immediately upstream of the stormwater pond. The pond has been designed to provide storage for the 10-year return-period storm event, while the spillway has been sized to convey flows associated with the 100-year return-period storm event.

Stormwater Pond (East Cells)

Contact Water Diversions

Contact water diversion systems will collect and convey contact water generated on the dam embankment slopes through drainage ditches to check dams. Runoff discharged from the check dams may be safely released to the natural drainage system. The drainage ditches have been designed to convey runoff from the 100‑year return-period storm event.

Culverts

Culvert structures will be provided at road crossings, as required. The culverts will be designed to safely convey flows associated with the 100-year return-period storm event while maintaining sufficient freeboard to prevent roadway overtopping and ensure safe operation of the access roads.

Spillways

Post-closure spillways are inclined open-channel structures constructed along the dam slopes to provide a safe conveyance path for runoff generated during extreme hydrological events. The spillways associated with TSF Cells 2, 3, and 4 discharge into the TSF diversion channel, while those associated with TSF Cells 1, 5, and 6 discharge directly to the natural drainage system. The spillways have been designed to convey runoff generated by the Probable Maximum Precipitation (PMP).

Underdrain

A subdrain system is designed within the former natural drainage channel underlying TSF Cells 3 and 4 to intercept and safely convey any incident groundwater or subsurface flow that may occur beneath the foundations of these facilities.

Leak Detection Sump

The Leak Detection Sump is designed to collect any potential leakage that may migrate through the primary TSF liner. Water collected within the Leak Detection Sumps will be conveyed and removed by a dedicated pumping system for appropriate management.

Tailings Deposition and Excess Water Reclaim Systems (by others)

Tailings paste pumped in pipelines and deposited into the TSF cells at points along the embankment crest. Excess fluid pumped from the tailings cells for use in the process plant.

Source: Tierra Group/BBA 2026

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_147.gif

Source: Tierra Group/BBA 2026

Figure 15‑7: TSF West Cells Water Management

 

 

img170397038_148.gif

Source: Tierra Group/BBA 2026

Figure 15‑8: TSF East Cells Water Management

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

15.10 Tailings Surface Logistics

The tailings will be transported by conveyor from the Hydromet building to the paste plant area. When the paste plant is running, all of the tailings will be introduced into the paste production process and either pumped underground as structural backfill or pumped to one of the six surface TSFs. The paste plant will be equipped with a concrete containment equipped with a discharge conveyor, to allow for stockpiling of tailings during periods where the paste plant is not operating. A hopper and transfer conveyor will allow the reintroduction of stockpiled tailings back into the paste production process using a wheel loader. Slag will be transported from the Pyromet building by truck or skid loader to the concrete containment adjacent to the paste plant

15.11 Tailings Storage and Associated Facilities

15.11.1 Overview and Capacity

The Tailings Storage Facility (“TSF”) consists of six discrete cells that will be developed in phases over the life of the project. The cells have varying storage capacities based on site conditions and facility geometry, providing a flexible and scalable approach to tailings management. This phased configuration allows storage capacity to be expanded as operational requirements evolve while optimizing construction sequencing and facility utilization. Table 15‑3 summarizes the TSF capacity and lifespan by cell, and Figure 15‑9 presents the facility arrangement. The design will accommodate the anticipated tailings and waste scheduled for disposal in the TSF. Based on the current mine plan, the tailings production rate of 2,290 tonnes per day will be split with approximately 78% delivered to the TSF at 60% solids content and 2% binder (by weight), with the remainder of the tailings utilized for mine backfill. Combined with approximately 4.09 million tonnes (Mt) of mine waste scheduled to the TSF, the total required capacity over the LOM is approximately 31 Mt. The lifespan of each cell ranges from 3 years to over 10 years. Some additional capacity is available in Cell 6 beyond the currently defined LOM.

Table 15‑3: TSF Capacity Summary

Cell

Storage Volume
(m
3) [1]

Cumulative Volume (m3)

Cumulative Tonnage [2]

Cell Lifespan

1

1,024,431

1,024,431

1,577,624

3 years

2

4,044,039

5,068,470

7,805,444

6 years & 2 months

3

3,604,375

8,672,845

13,356,181

7 years & 4 months

4

4,246,850

12,919,695

19,896,330

8 years & 10 months

5

5,042,938

17,962,633

27,662,455

10 years & 8 months

6

3,911,341

21,873,974

33,685,920

6 years [3]

Source: Tierra Group/BBA 2026

Notes:

[1] Storage volume considering a 3-foot freeboard.
[2] Based on in-place tailings density of 1.54 t/m3 (T Engineering, 2026).
[3] Cell 6 has more capacity than required for the LOM.

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

img170397038_149.gif

Source: Tierra Group/BBA 2026

Figure 15‑9: TSF General Arrangement

15.11.2 Design Basis

Design criteria for the TSF was assigned in compliance with Nebraska Administrative Code (“NAC”) Title 132 Integrated Solid Waste Management Regulations (NDEQ, 2016) and Title 458 Rules for the Safety of Dams and Reservoirs, overseen by the Department of Environment and Energy (“NDEE”) and the Nebraska Department of Natural Resources (NDNR), respectively. Internationally recognized guidance for tailings facilities and dams was also utilized, as appropriate (ICOLD, 2025) and (GISTM, 2020).

15.11.3 Embankment Configuration

The TSF embankment will be constructed of compacted glacial till derived from required site excavations and is designed to provide stable, long-term containment of tailings during operations, closure, and post-closure. Embankment heights range from approximately 55 to 87 ft (downstream toe to crest), depending on site topography and storage requirements. The embankments include a 30-foot-wide crest, upstream slopes of 2.5H:1V (horizontal: vertical), and downstream slopes of 3H:1V to promote stability and facilitate construction. Compacted glacial till will be used due to its low permeability, adequate shear strength, and local availability. Placement and compaction of engineered fills will be verified through quality assurance and quality control programs to ensure compliance with design requirements and long-term performance objectives.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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15.11.4 Liner System

The TSF liner is a composite containment system designed to control seepage, provide redundant containment with provision for leak detection and collection to limit hydraulic head on the liner. The system incorporates multiple engineered layers that work together to protect groundwater and maintain the facility’s long-term environmental performance.

The liner system consists of the following components (from the top down):

•
Primary liner: A 60-mil (1.5-millimeter [mm]) double-sided textured high-density polyethylene (HDPE) geomembrane that serves as the primary seepage barrier;
•
Geocomposite drainage layer: Drainage and leak-detection layer between the primary and secondary liners designed to collect and convey potential seepage for monitoring and management.
•
Secondary liner: A 60-mil (1.5-mm) double-sided textured HDPE geomembrane that provides redundant containment beneath the primary liner;
•
Geosynthetic clay liner (GCL) A low-permeability, bentonite-based barrier to enhance seepage control and containment performance; and
•
Prepared subgrade.

15.11.5 Instrumentation

The TSF instrumentation and monitoring program is designed to evaluate embankment performance, monitor seepage conditions, and verify that the facility is performing in accordance with design expectations throughout construction, operation, and closure. Instrumentation provides critical data on pore water pressures, groundwater conditions, deformation, and settlement, supporting ongoing performance assessment and informed operational decision-making:

•
Vibrating wire piezometers monitor pore water pressures within the embankment and foundation to assess seepage conditions and embankment performance;
•
Open standpipe piezometers measure groundwater and phreatic surface elevations to support seepage monitoring and verification of drainage performance;
•
Dataloggers automatically collect, store, and transmit instrumentation data, enabling continuous monitoring and trend evaluation;
•
Survey monuments provide reference points for monitoring embankment movement, deformation, and long-term stability;
•
Inclinometers measure lateral displacement within the embankment and foundation materials to detect potential instability or ground movement; and
•
Settlement plates monitor vertical settlement of embankment and foundation materials during construction and operation.

15.11.6 Conceptual Closure

The conceptual closure plan for the TSF includes progressive closure of individual TSF cells as they reach final capacity, providing for phased reclamation rather than end-of-life closure of the facility as

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

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a whole. Each completed cell would be regraded to promote positive drainage toward the outer slopes and designated spillway, consistent with the overall closure landform objectives. A composite closure cover system is proposed as part of this conceptual approach, beginning with installation of a geomembrane liner across the surface of each closed cell. The liner would be overlain by approximately 36 inches of engineered overliner material to provide protection and long-term stability. A final cover system consisting of 12 inches of cover material and 12 inches of growth media would then be placed over the TSF surface and embankment areas to support vegetation establishment and long-term erosion control. This multilayer system, applied in a progressive, cell-by-cell manner, is intended to enhance geotechnical stability, minimize infiltration, and promote long-term environmental closure performance while enabling reclamation activities to advance concurrently with ongoing TSF operations. A complete description of the closure and reclamation approach is provided in Section 17.5.

15.12 Salt Management Cells

The Mine Water Holding Pond and Wastewater Treatment Solids Impoundment (hereafter referred to as ‘salt cell’, as the primary solids from wastewater treatment will be residual salt from the hydrometallurgical operation) will be a surface impoundment located in the northern portion of the site. The salt cell is designed to hold brackish water from the mine during construction as well as salt cake (and other waste solids) from the process wastewater treatment system during normal mine operation.

15.12.1 Mine Water Holding Function

Formation water during construction is expected to be brackish and unsuitable for direct discharge from the site. During normal operation, this formation water will be sent to the process water treatment plant and reused in the process. During construction and before the surface plant is complete, this water will be sent to the salt cell for storage until it can be treated. Treatment in this instance will be through the use of turbomisters, spray evaporators that will maintain a manageable level in the pond through forced evaporation of the unwanted excess water. The remaining salt ‘brine’ will remain in the salt cell, which will then act as the final disposal location for this material.

Potential formation water flow is expected between 100 - 400 gpm, with 400 gpm the average value during operation. The turbomisters have a capacity of 57 GPM and there will be eight (8) turbomisters as part of the assembly. The pond itself is designed to act as a surge basin for episodes of high flow or rain events for mine dewatering.

The quality of the brackish water from the formation is shown in Table 15‑4:

Table 15‑4: Expected Quality of Formation Water to WWT

Parameters

Units

Mine

 

Parameters

Units

Mine

Flow

gpm

1000

 

Ni

mg/L

0

Ca

mg/L

522

 

Se

mg/L

0.024

Mg

mg/L

128

 

Ag

mg/L

0

Na

mg/L

5998

 

Tl

mg/L

0

K

mg/L

79

 

V

mg/L

0

Al

mg/L

0.8

 

U

mg/L

0.001

Ba

mg/L

0.14

 

Zn

mg/L

0.01

Sr

mg/L

41

 

SO4

mg/L

1260

NH3

mg/L

1.8

 

Cl

mg/L

9580

Fe

mg/L

6.2

 

PO4

mg/L

1.13

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Parameters

Units

Mine

 

Parameters

Units

Mine

Mn

mg/L

0.33

 

NO3

mg/L

0

As

mg/L

0.012

 

SiO2

mg/L

23

Be

mg/L

0

 

B

mg/L

3.15

Cd

mg/L

0

 

Total Alkalinity

mg/L

230

Cr

mg/L

0

 

Total Hardness Calc

mg/L

1830

Co

mg/L

0

 

TOC

mg/L

4.4

Cu

mg/L

0.02

 

pH

SU

7.85

Pb

mg/L

0

 

Temp

F

70

Li

mg/L

1.25

 

TDS

mg/L

17926

Hg

mg/L

0

 

Cond

us/cm

26755

Mo

mg/L

0

 

Source: (Veolia Water Technologies, Inc., 2019)

15.12.2 Wastewater Treatment Solids Disposal

Once the process wastewater treatment plant is operational it will receive the mine water (instead of the salt cell/mine water holding pond). It will then be treated and reused in the hydrometallurgical operation. The wastewater treatment plant is designed to recover all available water from the process and the mine dewatering. It will send all recoverable water back into the hydrometallurgical process and pull out all the solids from the wastewater. These solids will be sent to the salt cell for disposal. The only water sent to the salt cell will be in the form of bound water, either entrained within the solid matrix or existing as hydrates in the salt cake (where the additional energy expenditure to drive off the bound moisture would be inefficient).

These solids will primarily be salts (and a large portion of these will be chloride salts). The expected flows to the salt cell of the primary constituents from the wastewater treatment is shown below in Table 15‑5. Note there may be traces of other salts – chlorides, carbonates, and sulfates – as well as residual tailing material from the hydrometallurgical process. However, no hazardous constituents will be sent to the salt cell based on generator knowledge.

Table 15‑5: Primary Expected Solid Flows to Salt Cell from Process Water Treatment

Component

Flow (kg/hr)

Calcium Chloride

2130

Potassium Chloride

1499

Sodium Chloride

736

Calcium Sulfate

345

Magnesium Chloride

45

Source: Tetra Tech 2026

Based on the volume of the cell of 16 MM c.f. and the flows shown above, it will take approximately 15 years to meet the nominal storage capacity of the salt cell (with a 15% safety factor). To ensure the salt cell is not filled to capacity, part of the operational strategy of the plant will be to find avenues to reduce and reuse the salt from the wastewater treatment process. In addition, contracts will be set up with local landfills to accept a portion of this waste as needed.

Because the salt cell will be used as a temporary storage pond for mine dewatering activities and will contain sludge from wastewater treatment (the saltcake), it meets the definition of a wastewater

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works and will need to have a synthetic liner per Nebraska Title 123, ‘Rules and Regulations for the Design, Operation, and Maintenance of Wastewater Works’. The construction and materials of the pond will meet these regulatory criteria.

15.13 Paste Backfill System and Underground Distribution

15.13.1 Paste Backfill Plant

The Elk Creek Paste Backfill System will receive the full stream of process waste produced by the Hydrometallurgical Plant to produce backfill for both underground backfilling and surface storage at the TSF. Approximately 22% of process waste by mass of the ore mined will be returned underground as paste backfill. The remaining process waste will be directed to the TSF as paste backfill. In terms of annual quantities, the Paste Backfill System will accept approximately 950,000 tons of process waste per year to produce an average of 1,120 yd3/d of paste backfill to underground and 2,475 yd3/d of paste backfill to the TSF.

The Paste Backfill System will consist of the Paste Backfill Plant with the adjacent Surge Storage Facility (SSF) for process waste storage, and a Paste Distribution System (PDS) to deliver paste backfill to either the TSF on surface or mine workings underground.

The process waste will be delivered to the Paste Backfill System via a belt conveyor. A system of belt conveyors will direct the process waste to the Paste Backfill Plant during paste backfill production, or to the SSF when paste backfill is not being produced.

The Paste Backfill Plant will blend the process waste from the Hydrometallurgical Plant with binder and water to produce paste backfill. The paste mix design will vary depending on the intended use, with the primary variable being the binder content. Based on laboratory test work and hydraulic modelling, paste backfill delivered to the TSF and to UG stopes will have a solids content of 60%, with binder contents of 2% and 20%, respectively.

15.13.1.1 Basis of Design

All process waste from the Hydrometallurgical Plant will be converted to paste, whether for UG All process waste from the Hydrometallurgical Plant will be converted to paste, whether for UG backfilling or deposition at the TSF. As such, the Paste Backfill Plant will be a critical and non-circumventable component of managing process waste.

Since the Hydrometallurgical Plant will operate continuously, the Paste Backfill Plant must also be designed for continuous operation and be capable of producing paste at a rate consistent with the Hydrometallurgical Plant’s production of process waste. Therefore, the Paste Backfill Plant is designed with adequate redundancy. This will allow the system to have a high rate of availability (85%).

The Paste Backfill Plant must be able to store surplus process waste during operational interruptions at the Paste Backfill Plant. The SSF will allow temporary decoupling of the Paste Backfill Plant from the Hydrometallurgical Plant. The SSF may also provide additional feed material to the Paste Backfill Plant during periods of higher-than-normal UG paste backfill demand. The SSF will be designed to store an amount of material equivalent to 24 hours of process waste output from the Hydrometallurgical Plant, approximately 2,600 yd³.

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The Paste Backfill Plant will be located near the Hydrometallurgical Plant to minimize the conveyance distance of process waste. This location is also roughly in the center of the mine and TSF cells, reducing the maximum lengths of the PDS.

15.13.1.2 Key Design Parameters

A summary of key design parameters used for the design of the Paste Backfill System is detailed in Table 15‑6 below.

Table 15‑6: Paste Backfill System Key Design Parameters

Description

Value

Unit

Average Annual Ore Production

1,171,756

st/yr

Average Daily Ore Production

3,210

st/d

Average Annual Mined Voids

454,363

yd3/yr

Average Annual Paste Demand

408,927

yd3/yr

Average Daily Paste Demand

1,120

yd3/d

Replacement Ratio

22.1%

-

Hourly Process Waste Streams Production Rate

108.4

stph

Ratio of Carbonates to Process Waste

51%

wt%

Ratio of Iron Oxides to Process Waste

18%

wt%

Ratio of Leach Residue to Process Waste

31%

wt%

Average Ore SG

3.06

-

Carbonates SG

1.91

-

Iron Oxides SG

4.52

-

Leach Residue SG

2.81

-

Combined Tailings SG

2.40

-

Combined Process Waste Solids Content

83%

wt%

Paste Backfill Solids Content

60%

wt%

UG Paste Backfill UCS Requirement

58.0

psi

UG Paste Backfill Binder Content

20%

wt% (solids)

TSF Paste Backfill Binder Content

2%

wt% (solids)

Source: T Engineering 2026

15.13.1.3 Process Description

The Paste Backfill Plant will receive a combined stream of process waste from the Hydrometallurgical Plant, including carbonates, iron oxides, and leach residue, with the combined material containing

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approximately 83% solids by weight. The process waste will be mixed with binder and water to produce a homogeneous, non-segregating paste at 60% solids that can be pumped to UG or the TSF.

At the Paste Backfill Plant, process waste from the Hydrometallurgical Plant will be discharged to a live-bottom feeder equipped with a hopper, steadily feeding onto a two-way belt conveyor. The two-way belt conveyor will direct process waste to either the Paste Backfill Plant or to the SSF.

A front-end loader will manage material within the SSF. When the material is reclaimed for paste production, the front-end loader will feed process waste to a live-bottom feeder equipped with a hopper, with process waste discharging onto the incline conveyor that feeds the paste plant. This reclaim conveyor will be equipped with a belt scale to measure and monitor the rate of process waste added to the paste mixer. The primary incline conveyor that feeds the Paste Backfill Plant will also be equipped with a belt scale to measure the total feed to the plant.

The binder system of the Paste Backfill Plant will consist of two binder storage silos, one dedicated to GU cement and another to fly ash. These silos will be loaded by cement trucks equipped with onboard blowers. At the base of each silo, the binder will be fluidized by air and discharged through a rotary valve. A mass flow meter will measure the binder feed rate to adjust the flow rate through the rotary valve. Both storage silos will supply binder to a shared day-use binder silo through pneumatic conveying, wherein the binder types will mix. The day-use binder silo will dispense binder via a rotary valve and will be equipped with a mass flow meter, allowing binder addition based on the binder requirements in the selected paste mix design. A two-way screw conveyor will direct the binder to one of two paste mixers.

In the Paste Backfill Plant, the process waste will be mixed with binder and water in a continuous twin-shaft-type mixer. The rate of water added to the mixer will be based on the power drawn by the paste mixer. This control will maintain the flow properties of the paste. The paste mixer will discharge paste through a hatch to connect to a paste hopper below, with each hopper connected to a piston-type paste pump. The paste pumps will pump the paste backfill to the TSF or UG via the Paste Distribution System.

Because the Paste Backfill Plant is an independent structure, it will have its own clean water, compressed air, and wastewater collection system.

The Paste Backfill Plant will have a clean water system that is supplied by the site’s clean water source and stored in a clean water tank. This water will be distributed to high-pressure washers, the Paste Distribution System for flushing, and to the paste mixers.

A compressed air system will be included to supply both plant air and instrument air. The instrument air will have a dedicated receiver that serves sensitive components, such as valve actuators, dust collectors, and the binder fluidizer.

An agitated wastewater tank will collect wastewater from the sumps. Under emergency conditions, the sumps may also receive paste discharge from the paste mixers and hoppers. Wastewater may be used as trim water for paste production, but will otherwise be sent to the mine’s water management system.

The process flow diagram for the Paste Backfill Plant is provided in Figure 15‑10 and Figure 15‑11.

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img170397038_150.jpg

Source: T Engineering 2026

Figure 15‑10: Process Flow Diagram of Paste Backfill Plant - Page 1

 

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img170397038_151.jpg

Source: T Engineering 2026

Figure 15‑11: Process Flow Diagram of Paste Backfill Plant - Page 2

15.13.1.4 Paste Backfill Plant Design

The Paste Backfill Plant building has a footprint of approximately 62 ft by 60 ft, with a height of 52 ft. The plant layout was developed to follow the flow of paste production, with process waste received at the uppermost level, feeding to the paste mixers. The Paste Backfill Plant is to be enclosed to control the indoor environment. The adjacent SSF will be hosted within a domed enclosure, approximately 73 ft in diameter and 39 ft in height.

Plan and elevation views of the paste backfill plant and SSF are shown in Figure 15‑12 and Figure 15‑13, respectively.

 

 

 

 

 

 

 

 

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img170397038_152.jpg

Source: T Engineering 2026

Figure 15‑12: Plan View of the Paste Backfill Plant and SSF

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img170397038_153.jpg

Source: T Engineering 2026

Figure 15‑13: Elevation View of the Paste Backfill Plant and SS

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15.13.1.5 Power Requirements

The Paste Backfill Plant has a total connected load of 4,253.6 kW and an estimated maximum demand of 1,477.0 kW. Emergency power will be sourced from the site’s electrical distribution system.

15.13.2 Paste Distribution System

Paste backfill will be pumped to underground mine workings or to the TSF on surface via a network of pipelines called the Paste Distribution System (“PDS”). The underground portion of the PDS is called the Underground Distribution System (“UDS”).

15.13.2.1 Throughput

Four throughput cases were considered for sizing the PDS: Minimum, Nominal to UG, Nominal to TSF, and Maximum. The Nominal Rate represents the rate of paste production required to process waste from the Hydrometallurgical Plant at the same rate it is generated.

The Nominal Rates of paste flow are 478 GPM (109 m³/h) to the TSF and 575 GPM (131 m³/h) to UG. These rates fall within the recommended operating range for an 8-inch PDS, which ranges from 467 GPM (106 m³/h) to 660 GPM (150 m³/h). The lower value represents the recommended lower limit of the optimal backfilling range for an 8-inch system, while the higher value reflects the practical pump size limit before the paste pump becomes oversized. A summary of these rates is provided in Table 15‑7.

Table 15‑7: Backfill Throughput Rates

Rate

Paste Throughput

Basis

GPM

m3/h

Nominal Rate (TSF)

478

109

The backfill rate at which all process waste from the hydrometallurgical plant is converted into paste backfill, to the TSF.

Nominal Rate (UG)

575

131

The backfill rate at which all process waste from the hydrometallurgical plant is converted into paste backfill, to UG.

Minimum Design Rate

467

106

The recommended lower limit of the optimal backfilling range for an 8-inch distribution system.

Maximum Design Rate

660

150

Practical upper limit of selected paste pump capacity before larger pumping equipment would be required.

Source: T Engineering 2026

15.13.2.2 Hydraulic Modelling

To design the PDS, steady-state hydraulic modelling was performed. Modelling incorporated data from rheology test work and proposed pipeline paths from the plant to a variety of mine levels and TSF cells. Modelling assessed the hydraulic grade line, operating pressure during typical paste backfilling, as well as the maximum hydrostatic pressure under no-flow (e.g. during pipeline blockage) scenarios. These scenarios assessed the most extreme operating conditions the PDS may experience to support the selection of pipeline pressure requirements, pipe sizing, pump requirements, and overpressure protection provisions.

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Source: T Engineering 2026

Figure 15‑14 shows paths of the Paste Distribution System used for hydraulic modelling.

img170397038_154.jpg

Source: T Engineering 2026

Figure 15‑14: Paths of the Paste Distribution System Modelled

15.13.2.3 Paste Distribution System Process Description

Because paste will be pumped across a long lateral distance to reach both stopes and the TSF, the paste pump will be a 120-bar continuous positive-displacement pump, with a maximum flow rate of 660 GPM (150 m3/h).

The PDS will begin at the paste pump discharge. A diverter valve downstream of the paste pump will direct paste backfill to either the UDS or the TSF. Piping is specified in accordance with ASME B31.3. Most of the distribution system will use carbon steel piping, with final sections near stopes or the TSF to be constructed from HDPE piping. Surface piping will either be heat-traced or trenched below the frost line to prevent freezing in the winter. The pipeline will be sloped to promote self-drainage.

The underground portion of the PDS, the UDS, will consist of approximately 2,900 ft of surface piping to reach the portal, where the UDS will travel via the ramp piping to access levels. Likewise, to reach the TSF, the PDS will run at the surface from the Paste Backfill Plant to the TSF. The length of piping to reach TSF Cell 1 is approximately 2,400 ft.

The PDS will be designed with appropriate safeguards to prevent over-pressurization. Flushing will be performed to reduce solids accumulation in the pipeline. Flush water volumes will be based on the length and configuration of each PDS segment to optimize water use. A pre-flush will still be applied to slick the pipeline before use and verify that the PDS has been correctly configured. Emergency dump valves will also be installed at strategic locations to prevent loss of boreholes in the event of a blockage.

15.13.3 Paste Backfill Test Work

Test work on paste backfill and associated process wastes was performed to inform the design of the paste backfill and the Paste Backfill Plant. Test work involved characterization and UCS testing on a variety of paste backfill types.

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15.13.3.1 Characterization

Characterization included analyses of particle size distribution (“PSD”), mineralogy, chemical composition, and specific gravity (SG) for all process waste types assessed in the paste mix design program. Sand used in the test work was assessed for PSD and SG.

•
PSD analysis was performed either by T Engineering’s laboratory in Sudbury, Ontario, using wet laser diffraction and/or sieve analysis, or by the XPS laboratory in Falconbridge, Ontario, using dry laser diffraction.
•
Mineralogy was performed by QEMSCAN testing by the XPS laboratory in Falconbridge, Ontario.
•
Chemical characterization was performed by Inductively Coupled Plasma (“ICP”) testing by the AGAT laboratory in Mississauga, Ontario.
•
SG testing was performed by pycnometer by the XPS laboratory in Falconbridge, Ontario.

15.13.3.2 Paste Mix Design

A laboratory program was undertaken to assess whether process waste generated by the Hydrometallurgical Plant could be used to produce a paste backfill with sufficient pumpability and unconfined compressive strength (UCS) of 400 kPa, and to determine the solids content and binder content required to achieve these properties. Eleven blends of process waste were assessed as part of the program, identified as Blend A and Blends 1 through 10. Blend 1 is the base case for the study, as it most closely represents the properties and proportions of process wastes expected to be produced by the Hydrometallurgical Plant under the current design. Some blends modified the proportions of the process waste types, eliminated a process waste type, or incorporated sand. These cases were investigated to inform future optimization but were not adopted as the basis of design for this study.

For each blend, the solids content of the paste was adjusted to target a static yield stress of approximately 200 Pa, providing a consistent basis across batches for assessing pumpability from the Paste Backfill Plant to the stopes or the TSF.

Each blend was tested across a range of binder contents to assess the effect on UCS, with binder contents ranging from 5% to 20%. Although the Paste Backfill Plant is expected to use a blend of GU cement and fly ash, only GU cement was used for the test work due to limited fly ash availability, except for Batch 2.

Several blends exhibited low strength development, with some batches showing limited or no improvement in UCS with increased curing time or binder content. This low strength may be caused by chemical reactions between process waste types or between process waste and binder, inhibiting binder hydration and UCS development. Although some blends with sand added were able to reach the target UCS at a relatively reduced binder content, it was determined that sand addition is not optimal, as it negatively impacts the replacement ratio. In other words, less process waste can return underground, increasing the size of the TSF. Blend 1, the base case, was able to reach the target strength at 20% binder content at a solids content of 61.6%. Blend 1 exhibited improved UCS compared to Blend A, which had the same mix design except for using unwashed carbonates instead of washed carbonates.

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16 Market Studies

The market section of this Report constitutes a review of both current and historical market reports and offtake agreements as relevant for niobium, scandium, titanium and rare earth elements (REEs) in support of the 2026 Elk Creek Study.

16.1 Market Studies

NioCorp has commissioned market reports for each commodity upon which project revenue is derived. These market reports include:

•
Niobium: CMP Group Market Report, 2025
•
Scandium: OnG Market Report, 2025
•
Titanium: TZMI Market Report and Pricing Estimate, 2025
•
Magnetic Rare Earths: Adamas Intelligence Q2/25 outlook, base case
•
SEG and Heavy Rare Earths: Adamas forecast 2025, base case

16.1.1 Niobium Market Overview

Niobium has a wide range of applications and is extremely versatile. Niobium improves the material properties that often lead to increased efficiencies, performance and enhances the properties of advanced steels, batteries and electronics. Specifically, ferroniobium is used as a microalloy and accounts for approximately 90% of the total niobium consumption (CPM Group, 2025). The remaining 10% is consumed in various markets at a much smaller volume such as superconductors, high-performance alloys, carbides, electronics, lithium-ion battery components, and functional ceramics.

The commercial trade is dominantly ferroniobium, which is typically described in metric tonnes as a gross weight (FeNb) and has a niobium content of approximately 65% with some variations and has applications in non-ferrous metallurgy in the form of vacuum-grade FeNb (CPM Group, 2025).

The niobium market is dominated by three major producers:

•
Companhia Brasileria de Metalurgia e Mineração (CBMM)
•
Magris Resources
•
China Molybdenum Co. Ltd (CMOC)

Even though there are three major producers of niobium the market operates as a monopoly with CBMM setting the market price and the other operators acting as the price takers. CBMM also performs its own research and development activities to evaluate the additional/increasing usage of niobium that has a positive impact for other market participants. For the past several decades, CBMM has become the reliable supplier/producer which has significantly reduced supply disruptions and which has effectively returned an increased supply to accommodate market demand growth. While supply into the market from China and its available capacity is unknown (and is expected to be minimal), the principal producers have a combined annual capacity of 117kt Nb (CPM Group, 2025).

Table 16‑1 provides the reported annual production capacity from the three significant producers.

Table 16‑1: Niobium Producers

Mine/Project

Owner

Country

Resources (Est.)

Annual Ferroniobium
Production Capacity (Est.)

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Araxa (OP)

CBMM

Brazil

829 Mt @ 2.4% Nb2O5 (weathered)

110 kt/y

 

936 Mt @ 1.57% Nb2O5 (fresh)

 

Niobec (UG)

Magris Resources

Canada

95 Mt @ 0.54% Nb2O5

7.1 kt/y

Catalao (OP)

CMOC

Brazil

Area I 143 Mt at 1.01% Nb2O5

10 kt/y

Area II 169 Mt at 0.34% Nb2O5

Source: NioCorp, 2026, updated from CMP Group, 2025

Due to niobium not being a publicly traded commodity, transactions typically occur directly between producers and consumers. Trading firms do play a small role as market intermediaries and quoted prices for various ferroniobium and niobium oxide products are established based on the traders transactions.

Niobium Demand

Global ferroniobium demand in 2024 is estimated at approximately 69kt of contained Nb, based on international trade volumes and assumptions about consumption in key markets. Looking ahead, the base case forecast projects demand growing to around 90kt Nb by 2035 (CAGR of 2.6%), roughly in line with GDP growth and assuming stable intensity of use in steel production — a level consistent with the 2019 peak in Brazilian and Canadian exports. A more pessimistic scenario, driven by a bearish outlook for Chinese steel production, projects slower growth to around 80kt by 2035 (CAGR of 1.5%) (CPM Group, 2025). Figure 16‑1 represents the ferroniobium demand forecast from 2025 to 2035.

img170397038_155.jpg

Source: CMP Group, 2025

Figure 16‑1: Ferroniobium Demand 2025-2035 (kt Nb)

Niobium Pricing

Ferroniobium prices have been historically stable. However, future prices are highly dependent upon CBMM, as CBMM could flood the market with low-cost production, decreasing the average price and

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driving out competition. To date, CBMM has shown tolerance for additional producers and has controlled their own production levels to maintain stable pricing.

CPM Group, Niobium Review and Outlook (CPM Group, 2025), has further indicated that ferroniobium pricing has a long history of being stable. Starting from a 2024 baseline of US$46/kg contained Nb, CPM's two price forecast scenarios project modest growth: a high case tied to global inflation expectations and a low case assuming steady 2% annual growth (Figure 16‑2). Significant deviations from this range are considered unlikely absent major supply disruptions, with prolonged price declines also not anticipated (CPM Group, 2025).

Using CPM’s forecast, a price of $52/kg for ferroniobium was selected for the economic analysis of the Elk Creek Project.

img170397038_156.jpg

Source: CMP Group, 2025

Figure 16‑2: Ferroniobium Price Forecast 2025-2035 (US$/kg)

16.1.2 Titanium Tetrachloride (TiCl4) Market Overview

Titanium tetrachloride (TiCl₄) is a dense, colourless, volatile liquid (density 1.72–1.73 g/cm³ at 68°F (20°C); boiling point 277.5°F (136.4°C); freezing point -11.38°F (−24.1°C)) that serves as the primary intermediate in the production of both titanium dioxide (TiO₂) pigment via the chloride process and metallic titanium via the Kroll sponge process. It is produced by the high-temperature carbochlorination of titaniferous feedstocks, typically rutile, synthetic rutile, upgraded slag, or chloride-grade slag, in the presence of petroleum coke as reductant.

NioCorp will produce TiCl₄ as a co-product from the proposed Elk Creek Project. The hydrolysate generated during niobium and scandium processing at Elk Creek contains a significant titanium content (generally 3.5 parts Ti to 1-part Nb, along with minor Fe) that is amenable to chlorination. This section summarises the TiCl₄ market context, key demand segments, pricing dynamics, and North American production cost benchmarks that are material to the Project’s commercial assessment. The market analysis presented herein was prepared by TZMI (TZMI, 2025) and forms the basis of the discussion below.

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The TiCl₄ value chain originates at mine sites where titanium-bearing minerals are extracted and beneficiated into marketable feedstocks. These feedstocks are chlorinated to yield crude TiCl₄, which is subsequently purified by condensation, distillation, and chemical treatment before being directed to either (i) chloride-process TiO₂ pigment manufacture, (ii) titanium sponge production (via the Kroll or Hunter process), or (iii) a range of specialty chemical end uses. TiO₂ pigment manufacture accounts for the overwhelming majority of global TiCl₄ consumption; titanium metal and the specialty chemical segments represent a comparatively small but commercially important portion of the merchant market. The largest volume end market, by far, is titanium pigment and all other end uses are much smaller by comparison.

Titanium Tetrachloride Supply

Currently, North America hosts eight major TiCl₄ production sites, all operated as captive units integral to chloride-process TiO₂ pigment plants. Four companies—Chemours, INEOS, Tronox, and Kronos—account for all North American chloride pigment and associated TiCl₄ production. Together these facilities produce over 4.1 million tonnes of TiCl₄ per year on a captive basis, as estimated by TZMI, are summarised in Table 16‑2 below.

Table 16‑2: North American TiCl₄ Producers (2024)

Site

Location

Estimated TiCl₄ Production (t)

Altamira

Tampico, Mexico

803,415

Ashtabula 1

Ohio, USA

300,287

Ashtabula 2

Ohio, USA

288,047

De Lisle

Mississippi, USA

817,770

Hamilton

Mississippi, USA

549,839

Lake Charles

Louisiana, USA

389,897

New Johnsonville

Tennessee, USA

799,142

Varennes C

Quebec, Canada

217,617

 

Source: TZMI Project 12176 (July 2025).

 

Titanium Tetrachloride Demand

TiCl₄ is consumed in two distinct market arenas. First, and by far the largest in absolute volume, is captive TiCl₄ produced and consumed internally by chloride-process TiO₂ pigment manufacturers; this stream does not enter the merchant market. Second, a much smaller merchant market exists comprising titanium sponge production and a suite of specialty chemical applications. The analysis below addresses the merchant market, as this is the relevant commercial context for the Elk Creek Project.

Within the merchant market, titanium metal (sponge) accounts for approximately 98% of total TiCl₄ consumption. The remaining 2% is distributed across specialty applications including ultrafine TiO₂, pearlescent pigments, Ziegler-Natta (ZN) catalysts, organo-titanates, barium titanates, and laboratory/pharmaceutical uses. Despite their small absolute volume, the specialty segments command significantly higher unit prices than sponge-grade supply, creating potential revenue uplift opportunities for a new merchant entrant.

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Table 16‑3: TiCl4 Demand by End-Use Application (Excl. TiO2 Pigment)

Application

Market Share*

Est. Volume (t/yr)

Indicative Price

Purity Requirements

Pearlescent Pigments

35%

15,000 – 30,000

US$0.75 – 1.50/lb

Similar to finished TiO₂; moderate

Ultrafine TiO₂

39%

Included above

Variable

Moderate

Ziegler-Natta Catalyst

10%

3,500 – 5,000

US$1.30 – 2.60/lb

Very high (Al, Si critical)

Organo-titanates

9%

750 – 7,500

US$0.60 – 1.50/lb

Less stringent

Barium Titanates

4%

750 – 3,000

US$1.15 – 2.00/lb

Very high (conductivity metals)

Laboratories / Pharma

3%

750 – 1,500

US$2.00 – 40.00/lb

Very stringent

Notes:

*Share of non-TiO₂ merchant TiCl₄ demand. Prices are at long-term Cl₂ pricing

Source: TZMI Project 12176 (July 2025).

Titanium Tetrachloride Pricing

As noted in Table 16‑3 above, there are various price ranges for titanium tetrachloride based on the end use application and product purity. Currently China hosts the only broadly traded spot market for TiCl4 of significant volume which is sold to mainly titanium sponge manufactures. These Chinese market prices peaked in mid-2022 with an approximate price of US$1,242-1,380 per tonne prior to declining approximately 41% by early 2025 (Figure 16‑3). The price correction was largely driven by lower merchant chlorine gas prices and weakening downstream sponge and pearlescent pigment demand. These prices are likely to remain under downward pressure (TZMI, 2025).

img170397038_157.jpg

Note: Prices are based on TiCl4 prices in Liaoning Province, ex-works inclusive of VAT.

Source: TZMI Project 12176 (July 2025), www.cnfeol.com.

Figure 16‑3: Chinese Indicative TiCl4 Pricing

The US merchant TiCl₄ market is thin, opaque, and dominated by bilateral long-term contracts between pigment producers and sponge manufacturers. Historically, US merchant TiCl₄ prices have broadly tracked a range of US$1,300–2,000/t in nominal terms (approximately US$1,500–2,700/t in real 2024 USD terms), with cyclical peaks coinciding with tight sponge market conditions in 2012 and 2022.

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US TiCl₄ production costs are materially more sensitive to merchant chlorine prices than other global regions. Between early 2021 and mid-2023, US merchant liquid chlorine prices approximately doubled from US$0.23/lb Cl₂ to US$0.60/lb Cl₂, driven by retirement of older diaphragm-cell capacity and constrained membrane-cell replacement. As a consequence, chlorine’s contribution to TiCl₄ production costs rose from 13–18% of total costs in 2021 to 37–45% at the 2023 peak, before moderating to 28–34% by 2024. This volatility has motivated US pigment producers, including Chemours and Ineos, to invest in captive chlor-alkali capacity to reduce exposure to merchant chlorine price cycles.

TZMI’s base-case forecast for US TiCl₄ prices (ex-works, nominal) anticipates a modest recovery from the 2025–2026 trough, with prices gradually recovering toward US$1,600–1,800/t by 2030, supported by growing sponge demand and potential ATI Rowley restart activity. The high-case scenario reaches approximately US$1,900–2,000/t by 2030, reflecting accelerated aerospace demand recovery and domestic sourcing premiums. The low-case scenario maintains prices near US$1,300–1,400/t through 2028 before modest recovery, reflecting persistent Chinese oversupply and demand softness. In real 2024 US dollar terms, the base-case trajectory remains flat to modestly positive, reflecting structural improvements in demand relative to the 2024 trough.

A cost-plus pricing arrangement with a major TiO₂ pigment producer (structured on the basis of production cost recovery plus a defined margin) represents a commercially viable and lower-risk off-take structure for a new entrant such as Elk Creek. Under such an arrangement, a TiO₂ plant receiving one tonne of merchant TiCl₄ effectively recovers approximately 0.75 tonnes of chlorine for internal recycle within its chlorination circuit, providing a direct cost offset that enhances the economics of the purchase relative to captive production. Figure 16‑4 outlines the titanium tetrachloride historical and forecast pricing in the US.

img170397038_158.jpg

Source: TZMI Project 12176 (July 2025).

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Figure 16‑4: Historical and Forecast TiCl4 Pricing

TZMI developed an indicative cost model for TiCl4 production using a new entrant whose feedstock is high-grade, as titanium feedstock remains the largest cost driver that accounts for approximately 37-38% of total production costs at standard chlorine pricing. The cost model presented in Table 16‑4, presents two different scenarios which reflect both base and peak chorine pricing (US$350/t Cls and US$800/t Cl2 respectively).

Table 16‑4: Indicative TiCl4 Production Cost Breakdown (TZMI Model)

Cost Component

Consumption Rate

Unit Cost (US$)

Total (US$/t TiCl₄)

Raw Materials

 Ore

0.50

800

400

 Chlorine Gas (base Cl₂ price)

0.78

350

273

 Chlorine Gas (peak Cl₂ price)

0.78

800

624

 Petroleum Coke

0.15

400

60

 Calcium Hydroxide

0.09

200

18

Utilities

 Gas

2.20 GJ/t

7.5

16.5

 Electricity

237 kWh/t

0.075

17.77

 Water

0.60

0.3

0.18

Labor

—

—

55

Others (steam, fixed costs)

—

—

100

Maintenance

—

—

120

Total (Base Cl₂ @ US$350/t)

~US$1,063/t

Total (Peak Cl₂ @ US$800/t)

~US$1,414/t

Source: TZMI 2025

Note: Feedstock conversion cost excludes ore input costs

 

 

 

At base chlorine pricing (US$350/t), total production cost is estimated at approximately US$1,063/t TiCl₄ with a feedstock conversion cost of US$663/t. At the 2023 peak chlorine price of US$800/t, total costs increase to approximately US$1,414/t Comparing these costs against the 2024 North American captive producer range of US$626–798/t illustrates that a new standalone TiCl₄ facility would be structurally higher cost than integrated pigment-plant producers, who benefit from economies of scale, existing infrastructure, and recycled chlorine streams. Any viable business case for Elk Creek TiCl₄ production therefore depends critically on securing a price premium via (i) strategic supply of sponge-grade TiCl₄ to a domestic sponge restart (e.g., ATI Rowley), (ii) a cost-plus supply agreement with an existing pigment producer, or (iii) selective targeting of higher-value specialty chemical segments.

As part of this Technical Report Summary, the economic analysis assumes a constant long-term price of US$1.86/kg, based on TMZI market report and benchmark on pricing estimate and assumes no discounts on the recycled Cl2 reuse.

16.1.3 Scandium Trioxide Market Overview

Scandium production remains dominated by China as a by-product of iron ore and rare earth production. Based on Altinsel el. al, paper in 2018 on “Extraction of Scandium from Lateritic Nickle-Cobalt Ore Leach Solution by Ion Exchange” scandium is generally produced as a co-product of

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primary metals processes, wastes and reprocessed tailings. Scandium is the 50th most abundant element with an average crustal abundance of 20-30 ppm, but current does not have an identified single deposit type due to its natural occurrence as a dispersed state. Scandium has been identified as a critical mineral and has utilization potential in key areas such as solid fuel cells, aerospace and other electronic industries.

The scandium market still remains fairly obscure, and NioCorp has engaged OnG Commodities LLC (OnG) to produce an independent market assessment report. The market analysis presented in detail below was prepared by OnG and forms the basis of the discussion below.

16.1.3.1 Scandium Trioxide Market Supply

As of September 2025, OnG notes that all of the scandium supply in 2025 was a byproduct of various streams with the primary producers noted in Table 16‑5 totalling approximately 59 tonnes of scandium trioxide (Sc2O3).

Table 16‑5: Known Scandium Oxide Producers, Feedstock and Status

Producer

Country

Feedstock / Process

Nameplate Capacity
(tpy Sc₂O₃)
1

Est. 2025 Output
(tpy Sc₂O₃)
2

Primary Market / Notes

 

 

Hunan Oriental Scandium

China

Titanium dioxide sulphate process acid waste streams

50 (~40 effective)

~40

Primary supplier to Bloom Energy. Expansion to ~100 tpy Sc₂O₃ possible from existing sulphate plant feedstock.

 

 

China MinMetals / MCC

China

Nickel laterite; Ramu mine concentrate (Papua New Guinea)

Unknown

~10–15 (estimated)

Two production lines commissioned; merchant supply volume uncertain. Likely strategic / captive use.

 

 

Rio Tinto

Canada

Titanium dioxide acid waste streams (TiO₂ refinery)

3 (pilot scale)

0 (not operating)

Planned expansion to 12 tpy on hold. DoD purchase agreement secured (up to 6.4 t through 2030, ~US$ 40M).

 

 

Sumitomo Metal Mining

Philippines

Nickel laterite HPAL circuit residues

7.5

~4–5 (oxalate equivalent)

Established long-term supply relationship with Bloom Energy at ~US$ 2,000/kg Sc₂O₃. Export data sporadic; circuit consistently underperforms nameplate.

 

 

Rusal3

Russia

Red mud lagoon treatment (alumina refinery waste)

1.5 (claims 20–25 tpy potential)

~1.5

Rusal claims scalability to 20–25 tpy. Excluded from Western market supply projections due to geopolitical constraints (Russia–Ukraine conflict).

 

 

Rosatom3

Russia

Uranium solvent extraction acid streams

~1–3 (historical estimate)

Unknown

Information flows halted since 2022. Excluded from Western market supply projections.

 

 

Source: OnG Commodities LLC

Notes:

(1)
Nameplate capacity figures represent reported or estimated installed capacity; effective operating capacity may differ materially

 

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(2)
Output represents OnG Commodities LLC estimates based on trade data, export records and industry sources

 

(3)
Russian supply included for completeness, but excluded from Western Market supply/demand and pricing projections

 

China remains the primary producer of scandium globally, even with new production coming online and available to the market. A key aspect of western supply is the production of scandium from Rio Tinto, which is currently under strategic review by that company and represents the most consequential near-term uncertainty on western supply.

In September, the Defense Logistics Agency announced plans to procure more than 6,000 kilograms of scandium oxide for the National Defense Stockpile from Rio Tinto’s operations in Sorel-Tracy, Quebec, Canada; this procurement would take place over a 5-year period with a minimum commitment of $2 million and a potential total value of as much as $40 million. In October, the Canada Growth Fund committed $18 million to the Sorel-Tracey operation to expand scandium oxide production capacity to 9 tonnes per year; this commitment was accompanied by an offtake agreement with the Government of Canada (USGS, 2026). These strategic investments by various governments indicates specific intent on securing a western supply chain, however, the implied price of approximately US$6,250/kg is not a realistic market price and likely represents the economics of production including high capital costs, small-scale outputs, labor intensive processes and low recoveries from pilot scale operations.

16.1.3.2 Scandium Trioxide Market Demands

The current global scandium trioxide demand is estimated at approximately 37 tonnes in 2025 and is projected to reach 711 tonnes by 2035 across all market segments (OnG, 2025). Primary market drivers for scandium trioxide can be summarized into the following markets: solid oxide fuel cells and electrolysers, electronics, titanium replacement alloys, aerospace and automotive.

Solid Oxide Fuel Cells and Electrolysis Cells

OnG provided an overview of scandium use in the SOFC market and notes that Bloom Energy (Bloom) is reliant on scandium to ensure delivery of high reliability and ability to operate the SOFCs at a much lower temperature than competing markets. Bloom has pioneered the use of scandium-cerium-doped zirconia (CeScSZ) as the solid ceramic electrolyte in its SOFC stacks and is considered the largest single consumer of scandium. While there are no official public numbers, OnG estimates that approximately 75-100kgs of Sc2O3 are needed per MW of installed SOFC capacity and represents approximately 5% of product cost per MW. Each SOFC stack has a usage duration of approximately 10 years with spent ceramic wafers recycled at approximately 85% efficiency and estimates 20-25% of gross scandium from recycled material.

Between the late 2010s through 2023 Bloom experienced an estimated revenue growth of ~20% per year with power sales growth of up to 25% per year. These revenue growths did stall in 2024 for unknown reasons, Revenue growth appears to have resumed at an estimated 25% per year trajectory and is expected to continue through the mid-2030s which is driven by AI data center power demands. To date, Bloom has supplied 300 MW of data center power and OnG projects a 30% CAGR in data center fuel center installs which is driven by the US power supply shortfall of 25-30 GW by 2030 related to AI and data processing facilities. Bloom is also expanding their maritime and hydrogen electrolysis business units. OnG estimates that Bloom is nearing the practical capacity of Hunan Oriental and will need to secure additional non-Chinese supply.

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OnG notes that Bloom is also expanding it SOEC (solid oxide electrolysis cells). These SOEC systems use the same scandium bearing CeScSz ceramics but in reverse. SOEC splits steam into hydrogen and oxygen at high efficiencies and Bloom claims ~38 kWh per kg of hydrogen versus ~40-45 kWh for alkaline systems. Large scale green hydrogen programs are underway in the EU and Asia, and the SOEC market is expected to grow from ~1% today to 3% by 2030 and 8% by 2035. The total combined SOEC/SOFC demand not supplied by Bloom is projected at 319 tpy Sc2O3 by 2035.

Electronics

OnG’s scandium report notes that currently there is widespread commercial use of scandium in radio frequency filters which allow devices to transmit data on allocated networks and an emerging use in micro-electromechanical systems (MEMS) and semiconductors by utilizing scandium with gallium nitrides (GaN). All of these applications use scandium aluminum nitrides (ScAIN) at an approximate weight percent of 30% Sc as part of the established ceramic choice for 5G radio frequency band-pass filters. While the amount of Sc required per device is extremely small (~50μg) an approximate input of 20-25kg of Sc2O3 is required for every 1kg of finished product due to fabrication losses. OnG estimates that electronics demand is estimated at 5 tpy in 2025 and expanding to 26 typ by 2030 and 55 typ by 2035.

Specialty Alloys

Scandium was evaluated in the early 2010s by the US Department of Defense as an alloying agent to create a range of high temperature alloys able to substitute for titanium in military (mainly aerospace) applications, more for weight than cost and also for manufacturability. The project reportedly met its technical goals yet foundered due to concerns over the scandium supply chain. However, alloys that showed the potential to maintain adequate strength at 300 C (a key operating threshold) were developed and the project did not completely disappear (OnG, 2025). Following the initial evaluation of titanium, evaluation began on aluminum-cerium alloys for high temperature casting, combined with low levels of scandium. The addition of scandium to the alloy, the alloys are able to approach and potentially meet the 572°F (300°C) threshold.

Aluminium-cerium-scandium (AlCeSc) alloys continue to be under development as low-cost, lightweight alternatives to titanium in applications requiring corrosion resistance and moderate elevated-temperature performance. The addressable titanium market in heat exchangers, desalination tubing, offshore and marine structures, and non-structural aerospace components is estimated at 40,000–50,000 tonnes of titanium today, with approximately 8–9% annual growth projected through 2035. The indifference price for AlCeSc alloys (at 0.2 weight percent Sc) versus the lowest-value titanium applications is estimated at approximately USD 10,000/kg Sc2O3, making price a non-binding constraint on adoption.

Despite favorable economics, adoption is expected to be slow due to material qualification timelines and institutional resistance to change in safety-critical and cost-insensitive industries. The market analysis applies a 50% demand derating factor to capture this sentiment. Scandium demand from titanium substitution is projected at approximately 14 tonnes Sc2O3 by 2030 and 55 tonnes by 2035.

Aerospace

Commercial passenger aircraft represent a technically attractive but practically inaccessible near-term market for scandium-aluminium alloys, constrained by supply chain qualification requirements, recycling obligations, and competition from engine efficiency improvements. Other

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than limited use on Russian narrow-body aircraft, demand from commercial aviation is negligible and is expected to remain so through 2035.

Drones — including commercial delivery drones, civilian surveillance platforms, and military/heavy-lift systems — are identified as a more accessible and high-value market. High-scandium alloys such as Scalmalloy (registered trademark of Airbus) can reduce drone aluminium structure weight by 15–20%, translating to significant payload benefits. The indifference price for scandium in drone applications at current payload values is estimated at USD 20,000 or more per kg Sc2O3 on a one-year payback basis. Demand is forecast at approximately 20 tonnes Sc2O3 by 2030 and 40 tonnes by 2035.

Automotive

The global automotive aluminium market consumes approximately 15 million tonnes per year. While the potential demand for scandium-bearing alloys in electric vehicle (EV) battery enclosures and structural castings is theoretically large, the economics are considered unfavourable through 2035. At a minimum viable Western World scandium oxide price of approximately USD 2,000/kg, an AlCeSc alloy at 0.2% Sc would add approximately USD 4–6/kg alloy cost relative to standard automotive aluminium. Mass market adoption requires either significantly lower scandium prices (incompatible with new capital investment) or dramatic reductions in scandium alloy intensity below 0.05 weight percent with demonstrated equivalent or superior performance. The market analysis projects zero attributable automotive demand through 2035 for planning purposes.

Overall, the base case supply-demand OnG projects indicates that the scandium market will move into structural deficit during 2029, based on projected demand growth across the SOFC/SOEC, electronics, titanium substitution and drone sectors outpacing supply. Supply additions from NioCorp (2030), Rio Tinto expansion (2028–2030), and EU ScaVanger (2030) are projected to return the market to surplus in 2030–2031, with a tightening trend resuming toward 2035 as demand continues to accelerate.

The following integrated supply-demand comparison identifies key market inflection points in Figure 16‑5 and Table 16‑6 below.

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img170397038_159.jpg

Source: OnG 2025

Figure 16‑5: Sc2O3 tonnes Supply and Demand; Established Demand Segments Only

 

Table 16‑6: Scandium Oxide Supply vs. Demand by Year

2025

2026

2027

2028

2029

2030

2031

2032

2033

2034

2035

Total Demand (t)

37

51

84

117

171

228

300

379

478

583

711

Total Supply (t)

59

79

115

141

170

291

427

529

589

661

671

Surplus / (Deficit) (t)

22

28

31

24

(-1)

63

127

150

111

78

(-40)

Source: OnG, 2025

Notes: Figures in tonnes Sc2O3; negative values denote market deficit assumes no accelerated Chinese supply

 

OnG highlighted key observations below based on the supply-demand analysis:

•
The 2029 market deficit is most likely to be mitigated by accelerated capacity additions at Hunan Oriental, which has demonstrated willingness to invest ahead of demand. Spot prices are expected to firm in 2027–2029 in anticipation of tightening.
•
The projected 2030–2032 supply surplus reflects simultaneous commissioning of NioCorp, Rio Tinto expansion, and EU ScaVanger, alongside continued Chinese supply growth. This surplus is expected to moderate rather than collapse pricing, given the bifurcated Western / Chinese price structure.
•
The global supply and demand projections encompass both Chinese and non-Chinese supply. In practice, a bifurcated market means Western World consumers will experience the tighter

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supply-demand balance of non-Chinese supply, supporting elevated non-China prices throughout the forecast period.
•
Commissioning delays, which are common in new hydrometallurgical operations, would materially tighten the Western World market in the 2030–2032 period.

16.1.3.3 Scandium Trioxide Pricing

OnG discussed that Scandium oxide prices in 2025 are estimated at approximately USD 800/kg Sc2O3 (3N purity, tonne quantities, ex-China). This price reflects a global market capacity utilisation of approximately 67%, consistent with short-run marginal cost pricing well below reinvestment-level economics. The independent market analyst identifies the threshold for sustained price appreciation at approximately 85% capacity utilization. A central conclusion of the OnG’s market analysis is that the global scandium market will bifurcate into Chinese and non-Chinese pricing regimes through the forecast period. This bifurcation is driven by:

•
China's imposition of export controls on scandium, aligning it with strategic critical minerals subject to state direction;
•
Bloom Energy's strategic imperative to diversify supply outside China within 2–3 years, driving committed offtake agreements at prices above Chinese market levels;
•
The inability of non-Chinese producers to justify capital investment at current Chinese price levels (estimated minimum viable price of USD 2,000/kg for byproduct recovery operations and approximately USD 3,000/kg for dedicated mining projects such as Burra); and
•
Demonstrated US government willingness to provide pricing support and capital for critical minerals supply (MP Materials rare earth contract; DoD purchase from Rio Tinto; ExIm Bank engagement with NioCorp and Sunrise).

As a result, Chinese spot prices are expected to remain in the range of USD 800–1,200/kg Sc2O3 through 2035, while non-Chinese average prices are projected to trade in the range of approximately USD 1,900–2,700/kg Sc2O3, with peak pricing in 2029–2030 and 2034–2035 corresponding to market tightness periods. OnG Pricing estimates are noted in Source: OnG, 2025

Figure 16‑6 and Table 16‑7 below.

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img170397038_160.jpg

Source: OnG, 2025

Figure 16‑6: Projected Sc2O3 Price per Kg through 2035

Table 16‑7: Price Forecast by Region 2025 through 2035

Source / Region

2025

2026

2027

2028

2029

2030

2031

2032

2033

2034

2035

China (avg.)

 $ 800

 $ 800

 $ 1,000

 $ 1,000

 $ 1,200

 $ 1,000

 $ 950

 $ 850

 $ 900

 $ 950

 $ 1,200

World Average

 $ 902

 $ 876

 $ 1,113

 $ 1,099

 $ 1,398

 $ 1,429

 $ 1,330

 $ 1,255

 $ 1,384

 $ 1,637

 $ 1,826

Non-China Average

 $ 2,000

 $ 2,000

 $ 2,300

 $ 2,273

 $ 2,444

 $ 2,412

 $ 2,056

 $ 1,929

 $ 2,144

 $ 2,508

 $ 2,652

Sumitomo

 $ 2,000

 $ 2,000

 $ 2,000

 $ 2,000

 $ 2,000

 $ 2,000

 $ 2,000

 $ 2,000

 $ 2,000

 $ 2,000

 $ 2,000

Rio Tinto

—

—

 $ 3,000

 $ 3,000

 $ 3,000

 $ 3,000

 $ 3,000

 $ 3,000

 $ 3,000

 $ 3,000

 $ 3,000

NioCorp (Elk Creek)

—

—

—

—

—

 $ 2,000

 $ 1,750

 $ 1,500

 $ 1,800

 $ 2,250

 $ 2,500

Source: OnG, 2025

Notes:

(1)
All prices in USD per kg Sc2O3: Non-China average reflects weighted average of all non-Chinese supply sources.
NioCorp and other Western sources subject to supply-demand cycle pricing between US$1,500 (floor) and US$2,500 (ceiling) through 2035

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OnG also evaluated scandium pricing specific to NioCorp and noted the following as important factors on pricing projections:

•
Prices in China and the rest of the world will bifurcate, with China likely enjoying excess supply and soft pricing while the western world sees tight supply and elevated prices. OnG do not expect this to be as abrupt a change as, say, the gallium market but OnG believes things are well down this path and will not soon turn back.
•
Bloom is already close to the point at which a second non-Chinese source of scalable scandium supply is necessary. Since Bloom's balance sheet cannot support a non-recourse financing, Bloom will have to turn to Rio (for which there are no financial contingencies) or else turn to a partner (such as SK, or perhaps the US Government) to provide loan guarantees.
•
Near term (pre-2030) only Rio and Syerston are realistic candidates to supply Bloom and Bloom will need only one of them. OnG expect Rio (more likely) and Syerston (if Rio exits the market) to expand. In either case, the project will require firm prices and OnG estimates $3,000 per Kg scandium oxide as the price needed to justify capital investment here.
•
OnG expects secondary recovery in the EU, some red mud recovery in the US, and NioCorp all to enter production in the period 2029-2032. None of these companies possess the market power of Rio and none of them can take the risk of a committed supply, thus OnG expects all these emerging suppliers to obtain prices between the China price and Rio's price, with the actual price per Kg determined by industry utilization lagged by 6-12 months (because prices will tend to be sticky). OnG also expects Sumitomo to continue to supply product to Bloom at around $2,000 per Kg scandium oxide although we see this business as limited in volume.

OnGs expectation is that western producers (other than Rio) will experience price fluctuations based on supply-demand imbalances but will likely enjoy substantially higher prices than Chinese producers. OnG noted difficulty in differentiating between NioCorp and EU/US recovery operations from red mud and titanium pigment operations and expect all these sources to experience the same price volatility over time.

As part of the Projects economics, a base price through LOM is estimated to be $1,966/kg of Sc2O3 averaged throughout the Project life.

16.1.4 Rare Earth Market Overview

In the mineral exploration and mining industry, the rare earth elements (“REEs”) are commonly defined as the lanthanide series, together with yttrium (“Y”). These include lanthanum (“La”), cerium (“Ce”), praseodymium (“Pr”), neodymium (“Nd”), samarium (“Sm”), europium (“Eu”), gadolinium (“Gd”), terbium (“Tb”), dysprosium (“Dy”), holmium (“Ho”), erbium (“Er”), thulium (“Tm”), ytterbium (“Yb”), lutetium (“Lu”), and yttrium.

Rare earth elements are not termed “rare” because they are necessarily scarce in the Earth’s crust. For example, cerium has a crustal abundance broadly comparable to copper. Rather, the term reflects the difficulty of identifying REE mineralization in concentrations, mineralogical forms, and geological settings that can be economically mined, processed, and refined. REEs typically occur together in mineral assemblages and are generally recovered into an intermediate product, such as a mixed rare earth carbonate, mixed rare earth oxide, or concentrate, before being separated into individual rare earth oxide products for use in downstream supply chains.

 

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img170397038_161.jpg

Source: Van Gosen 2014

Figure 16‑7: Lanthanide Series for REE's modified after Van Gosen 2014.

The REE market comprises of a range of sectors. Principal uses of REEs include battery alloys, catalysts, ceramics, pigments and glazes, glass polishing powders and additives, metallurgy and alloys, permanent magnets, phosphors, and other applications in chemicals, communications, healthcare, defence, and advanced technologies.

Although REEs are used across a broad range of applications, the market is commonly assessed with reference to the distribution of the individual rare earth oxides within a project’s total rare earth oxide (“TREO”) basket.

The magnetic rare earths (Nd, Pr, Tb and Dy) account for roughly 90% of the value of the overall rare earth market consumption (Adamas Intelligence, 2019). As such, these four REEs dominate the REE value within essentially all REE mineral projects, including Elk Creek (SRK, 2022).

The economic significance of an REE mineral project is therefore commonly influenced by several interrelated factors, including:

•
total rare earth oxide (TREO) grade;
•
the relative distribution of individual rare earth oxides;
•
the proportion of magnet rare earth oxides, particularly Nd, Pr, Dy, and Tb;
•
mineralogy and liberation characteristics;
•
metallurgical recoveries and processing requirements;

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•
levels of deleterious or radioactive elements, particularly uranium and thorium;
•
ability to produce a saleable concentrate, carbonate, or oxide product;
•
access to downstream separation and refining capacity;
•
jurisdiction, infrastructure, permitting, and environmental considerations; and
•
potential strategic interest from governments, and downstream users.

The REE market is increasingly driven by demand for permanent magnets used in defence, electric vehicles, wind turbines, high-efficiency motors, aerospace and advanced electronics. Magnetic REEs (Nd, Pr, Dy, Tb), are expected to remain the primary value drivers. Projects located outside China with favourable mineralogy, and a credible downstream processing pathway are likely to attract increasing strategic interest.

16.1.4.1 Market Demand

Demand for the magnet feed magnetic REEs (Nd, Pr, Tb, and Dy) make up the vast majority of global REE value today and, in the years ahead, demand growth for these four REEs is expected to exceed demand growth for all other rare earth elements, challenging the ability of the supply-side to keep up.

Adamas Intelligence forecasts that global demand for NdPr oxide will increase at a compound annual growth rate (“CAGR”) of 8.2% from 2025 through 2040. As nearly all PrNd oxide consumed globally is used in the production of NdPr alloy and subsequently NdFeB permanent magnets, this forecast supports continued demand growth for the principal light magnet-feed rare earths.

Looking ahead, further U.S. domestic rare earth and magnet supply-chain participants are expected to emerge as federal funding, equity investment, and strategic partnerships continue to support projects that link mining, processing, separation, metal and alloy production, and magnet manufacturing. Heavy rare earth supply and rare earth metal-making capacity are expected to remain potential bottlenecks for the expansion of the U.S. magnet industry and other non-China supply chains. As a result, these segments may attract increased investment, strategic partnerships, and merger and acquisition activity (Adamas Intelligence, 2025).

Rare earth permanent magnet consumption was temporarily disrupted during the COVID-19 period; however, the market has since moved beyond the immediate recovery phase and is now driven by structural growth in electrification, renewable energy, high-efficiency motors, robotics, defence, aerospace, and advanced electronics. The International Energy Agency (“IEA”) reported that demand for magnetic rare earth elements has doubled since 2015 and is projected to increase by a further one-third by 2030 under current policy settings. The USGS also identifies magnets as the leading global end use for rare earths, confirming the importance of the permanent magnet sector as a major driver of REE demand (IEA, 2026).

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img170397038_162.jpg

Source: Adamas 2020

Figure 16‑8: Historical global consumption and forecasted demand for NdFeB magnets by end-use category

In addition to dominating demand, China also dominates the production of REEs. The largest source of rare earths globally is the Bayan Obo mine, in the Baotou region of China, and has historically been the dominate global producer of REEs since the 1990s (SRK, 2022) Rare earths are also produced from the Maoniuping mine and several other mines in China. Recently, within the last decade, additional production has been brought online, most notably from Myanmar (South Asian clays), Australia (Mt. Weld), and the United States (MP Materials).

MP Material halted export to China in April 2025 as the US-China trade wars heated up. In April 2025 exports from Mynamar to China spiked as press agencies reported that the Kachin independence army had taken control of key mine sites key for critical exports to China choking the supply chain (Adamas Intelligence, 2025). To counter this China moved into the Shan state to counter the losses from the Kachin state. This has been effective but illustrated the need for global alternative sources of REE to alleviate pressure on these volatile supply sources.

U.S. government policy has become an increasingly important driver of rare earth market demand, particularly for magnetic rare earths used in neodymium-iron-boron (“NdFeB”) permanent magnets. Not only has mining enjoyed this improved support, but also downstream processing, metal and alloy production, and magnet manufacturing. These are strategic focus areas specifically within the domestic mine-to-magnet supply chains.

In 2025, MP Materials and Vulcan Elements, together with its partner ReElement Technologies, received significant investment support from the U.S. government. In January 2026, the U.S. Department of Commerce announced a non-binding letter of intent to provide USA Rare Earth with up to US$277 million in direct funding and up to US$1.3 billion in senior secured debt under the CHIPS and Science Act to support domestic rare earth processing and NdFeB magnet production (USA Rare Earth Inc., 2026). This investment reflects a common strategic theme for the support of vertically integrated rare earth supply chains, near-term or existing production capability, scalable development potential, and stated ambitions to establish domestic NdFeB permanent magnet manufacturing capacity of approximately 10,000 tonnes per annum (SRK, 2026).

 

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The White House has also identified rare earth permanent magnets as derivative products of processed critical minerals that are vital to electronics, vehicles, defence systems, and broader national-security supply chains.

These policy measures aim to support increased demand for Nd, Pr, Dy, and Tb by encouraging domestic magnet manufacturing capacity. Supported by offtake agreements, stockpiling initiatives, and strategic investment in non-China rare earth supply chains the market show that this support will improve the entire value chain. Similarly, Adamas Intelligence also identified that this type of policy support will improve production capacity and limit potential near term bottlenecks and grow the supply chain.

16.1.4.2 Pricing

Adamas 2025, reported that following the Q1 2025 performance average magnet rare earth oxides prices were starting to trend higher into Q2 2025 in line with previous BASE Case expectations they had reported. Overall magnet rare earth prices trended higher due to the tightening concentrate supplies to China amidst the export restrictions.

The anticipated tightening in heavy rare earth supply conditions broadly materialised later 2025, particularly outside China, following Chinese export controls and continued dependence on Chinese heavy rare earth separation capacity (Adamas Intelligence, 2025). However, the price movements were uneven across elements and regions. Tb remained strongly supported by supply-chain concerns, while Dy pricing showed signs of correction in the Chinese domestic market as export restrictions and licensing delays contributed to material being retained domestically. As such, the late-2025 market was characterised less by a uniform HREO price increase and more by element-specific price divergence and widening regional price bifurcation.

Pricing forecasts by Adamas Intelligence for Nd oxide, Pr oxide, Tb oxide, and Dy oxide are presented in Figure 16‑9 to Figure 16‑11 below (Adamas Intelligence, 2022). These pricing forecasts support the inclusion of REEs in the Mineral Resource for the Elk Creek Project.

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img170397038_163.jpg

Source: Adamas 2022

Figure 16‑9: Forecasted China domestic price of dysprosium oxide

 

img170397038_164.jpg

Source: Adamas 2022

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Figure 16‑10: Forecasted China domestic price of terbium oxide

 

img170397038_165.jpg

Source: Adamas 2022

Figure 16‑11: Forecasted China price of neodymium oxide, praseodymium oxide and didymium oxide.

Publicly available rare earth price benchmarks in early May 2026 indicated NdPr oxide pricing up to $115.00/kg DDP USA, Tb oxide pricing of approximately US$1,130/kg FOB China and US$4,250/kg DDP USA, and Dy oxide pricing of US$280/kg FOB China and US$1,200/kg DDP USA (Argus Media (2026). These prices should be considered indicative only and are inclusive of estimated shipping terms. Mixed intermediate products, including SEG carbonate, SEG+ precipitate and heavy rare earth carbonate, are less transparent than separated oxides and are commonly valued by reference to contained rare earth value, with Dy and Tb content being particularly important. The 2026 Mountain Pass TRS (SRK, 2026), using Adamas analysis, applies a long-term SEG+ precipitate benchmark of US$51.30/kg REO equivalent for MP Materials specifications, while noting that mixed precipitate pricing remains relatively opaque.

Table 16‑8: Comparison of NioCorp Pricing to publicly available information.

Report Comparisons

Product

NioCorp Price

Adamas Q3 2025

Argus 2026 DDP USA

Mountain Pass 2025

Price

Recovery

Units

Price

Units

Price

Units

Price

Units

NdPr Oxide, 99.5%

$125

92%

$/kg

$62.50

$/kg

$115

$/kg

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Report Comparisons

Product

NioCorp Price

Adamas Q3 2025

Argus 2026 DDP USA

Mountain Pass 2025

Price

Recovery

Units

Price

Units

Price

Units

Price

Units

Tb2O3, 99.99%

$1,845

92%

$/kg

$977.50

$/kg

$4,250

$/kg

Dy2O3, 99.5%

$410

92%

$/kg

$240.00

$/kg

$1,200

$/kg

SEG Carbonate

$8.97

92%

$/kg

$51.30

$/kg

Heavies Carbonate

$5.05

92%

$/kg

Source: NioCorp 2026

 

For the purposes of U.S.-focused market analysis, China domestic spot prices should be treated as indicative reference prices only. U.S.-delivered rare earth oxide prices may differ materially due to supply-chain qualification, logistics, tariffs, export controls, contract terms, and ex-China premiums, particularly for heavy rare earths such as Dy and Tb. In December 2025, Argus report U.S.-delivered price assessments for NdPr oxide, Nd oxide, Pr oxide, Dy oxide, Tb oxide, Y oxide, and Gd oxide, reflecting the need for more transparent pricing benchmarks in the U.S. market. The U.S. Department of Defense’s 2025 agreement with MP Materials, which included a US$110/kg NdPr price floor, also provides a relevant policy-supported benchmark for domestic rare earth supply-chain development.

Current market conditions support the use of NioCorp pricing in this technical report.

16.2 Contracts and Status

The Company has entered into one executed offtake agreement covering ferroniobium produced from the Project, and has advanced a second offtake agreement, covering ferroniobium together with the balance of the Project’s saleable commodities, to a draft definitive stage. The two agreements together form the contractual framework that underpins the marketing assumptions used elsewhere in this Report. The summaries below describe the material commercial terms of each agreement and are qualified in their entirety by reference to the complete text of the relevant agreement. The executed agreement has been filed by the Company on SEDAR+. The draft agreement remains under negotiation as at the effective date of this Report and would be filed if and when executed in substantially the form described below.

16.2.1 Ferroniobium Offtake Agreement with Thyssen Krupp Metallurgical Products GmbH

On November 10, 2014, NioCorp entered into an offtake agreement with Thyssen Krupp Metallurgical Products GmbH (the “TK Agreement”), a company organized under the laws of Germany. The TK Agreement remains in force as at the effective date of this Report and has been filed by the Company on SEDAR+. The agreement grants Thyssen Krupp the exclusive right to purchase a Committed Product Amount of ferroniobium from the Project for sale within a defined Territory, being Europe and such other countries as the parties may agree from time to time in writing. The Committed Product Amount is 50% of annual ferroniobium production from the Project, capped at

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3,750 tonnes per year. The recitals to the TK Agreement record the parties’ expectation that the Project will produce approximately 7,500 tonnes of ferroniobium per annum, against which the cap was set. In any single month the Buyer is entitled to order up to 150% of one-twelfth of the Committed Product Amount, subject to the annual cap. Ferroniobium production in excess of the Committed Product Amount may be sold by the Company to other customers, provided that such other customers are not permitted to on-sell into the Territory. The agreement also contemplates a third-party investment scenario in which an investor in the Project may be permitted to participate provided that the investor does not distribute the product within the Territory.

Pricing under the TK Agreement is referenced to the low quotation for ferroniobium published in the Metal Pages “Ferro-niobium 65% Nb (EU)” Index for the week prior to delivery (or such other price as the parties may agree in writing for a particular order). The settlement calculation, in sequence, applies any agreed customer discount or premium to produce a Market Price 1, deducts the Buyer’s actual logistics, financing and handling costs (freight, marine insurance, port and warehouse handling, customs clearance, import duties, storage, and inland freight) to produce a Market Price 2, and deducts a commission of 3.75% calculated on the Market Price 2 to arrive at the Settlement Price payable to the Company. The Buyer pays 85% of the Provisional Price within ten days of shipment against the Seller’s invoice, bill of lading or equivalent waybill, certificate of origin and certificate of quality and quantity, with a true-up at the end of the month following delivery once actual logistics costs are fixed. Deliveries are generally made FCA or FOB Port of Shipment under Incoterms 2010. The term of the TK Agreement commences within 30 days of the first commercial production of ferroniobium and continues for 10 years from that date, extendable by mutual written agreement of the parties. The agreement is governed by the substantive laws of Switzerland (excluding the United Nations Convention on Contracts for the International Sale of Goods) and provides for binding arbitration under the Rules of the International Chamber of Commerce, seated in Paris, France, conducted in the English language.

16.2.2 Definitive Offtake Agreement with Traxys North America LLC

NioCorp and Traxys North America LLC (“Traxys”), a Delaware limited liability company, have advanced a draft definitive offtake agreement (the “Traxys Agreement”) that, upon execution, will supersede and replace the parties’ prior arrangements in their entirety, being (i) the ferroniobium offtake agreement originally entered into between NioCorp and CMC Cometals on June 13, 2016 (subsequently assigned to Traxys, as amended), and (ii) the scandium offtake agreement between NioCorp and Traxys dated October 3, 2018. The draft of the Traxys Agreement reviewed for the purposes of this disclosure is dated April 13, 2026. The Traxys Agreement has not been executed as at the effective date of this Report. Certain commercial terms in the draft, including the reference pricing publication and quotation period applicable to ferroniobium, the per-order and aggregate caps on deductible marketing costs, the agreed commission rates applicable to the products other than ferroniobium, and the form of credit support to be provided by the Buyer, remain to be agreed between the parties prior to execution. There can be no assurance that the Traxys Agreement will be executed on the terms summarized below, or that it will be executed at all.

The draft Traxys Agreement covers two product categories. The first is ferroniobium produced from the Project, in respect of which the Committed Product Amount is 50% of annual ferroniobium production. The second is the balance of the Project’s saleable commodities (the “Other Products”), comprising niobium pentoxide, scandium oxide, scandium metal, scandium-aluminum master alloy, titanium dioxide, titanium chloride and the rare earth elements identified in the schedule to the

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agreement. Traxys has been granted the exclusive right to market and sell 100% of the Other Products produced from the Project on a best-efforts basis, subject to small quantities reserved by NioCorp for sampling, quality control and regulatory requirements. The Territory for ferroniobium is global, excluding the territory reserved to Thyssen Krupp under the TK Agreement for so long as the TK Agreement remains in effect; the Territory for the Other Products is worldwide. The draft Traxys Agreement also includes a Strategic Transaction mechanism, under which NioCorp may identify and negotiate commercial arrangements with third parties relating to the marketing and sale of any Product, with all such sales (other than sales pursuant to the TK Agreement) executed through Traxys as marketing and sales intermediary. Where a Strategic Transaction results in economics more favourable than would otherwise be realized under the standard pricing structure, the incremental economics are allocated 75% to NioCorp and 25% to Traxys.

Pricing under the draft Traxys Agreement is structured around a Provisional Price for ferroniobium (referenced to a Pricing Publication and Quotation Period to be specified prior to execution) and, for each Other Product, a Market Price to be mutually agreed in writing prior to each shipment. In each case the settlement calculation deducts from the reference price (i) any agreed customer discount or premium, (ii) the Buyer’s actual logistics costs, at cost and without mark-up, (iii) the Buyer’s actual marketing costs, subject to per-order and annual aggregate caps to be specified, (iv) finance charges of U.S. Prime multiplied by 1.3333 in respect of any agreed customer credit terms in excess of net 30 days, and (v) a commission of 3.5% calculated on the net amount resulting from the foregoing deductions (or, for each Other Product, the commission rate agreed in writing between the parties in the relevant exhibit to the agreement, with a default rate of 3.5% applying in the absence of such agreement). The Buyer is required to pay the Provisional Price in full within ten days of shipment, with a settlement true-up at the end of the month following delivery once actual logistics costs are fixed. Deliveries are generally made FCA Seller’s plant under Incoterms 2020. The Buyer is required to maintain detailed records of all costs and deductions taken under the pricing clauses and is subject to an annual right of audit by an independent accounting firm.

The term of the draft Traxys Agreement commences on the Commercial Production Date, defined as the first day of the month during which the Project’s output of the applicable Product over the three preceding calendar months equals or exceeds 80% of Planned Production on an annualized basis, and continues for an initial term of 10 years, with automatic renewals for successive one-year periods unless either party provides 12 months’ written notice of non-renewal. If the Commercial Production Date has not occurred on or before the date that is 60 months after execution, either party may unilaterally terminate the agreement within the 90 days following that date; force majeure events do not suspend or extend that 60-month sunset. The Buyer is required to provide customary credit support for its obligations in forms acceptable to NioCorp and its lenders, the form of which remains to be agreed. The agreement is governed by the laws of the State of New York (without regard to choice of law principles) and provides for binding arbitration under the Rules of the International Chamber of Commerce, seated in New York, New York, conducted in the English language by a single arbitrator.

Other than the two agreements described above, the Company has not entered into any binding offtake or marketing arrangements covering production from the Project as at the effective date of this Report. Marketing of the balance of ferroniobium production not committed under the TK Agreement (and, following its execution, the Traxys Agreement), and of the Other Products, will be subject to commercial arrangements to be concluded in the ordinary course, including any Strategic Transactions implemented through Traxys under the framework of the draft Traxys Agreement once

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executed. The TK Agreement constitutes, and the Traxys Agreement upon execution is expected to constitute, a material contract for the purposes of applicable Canadian securities disclosure obligations.

16.3 Market Dynamics

Since the commissioning of the market reports that support the Elk Creek Project’s Mineral Resource and Mineral Reserve, there have been changes of substance to the market prices for dysprosium, terbium and scandium. All three of these elements are an important part of the project’s economics and are produced predominantly in China. China began to implement market export controls in April 2025. In June 2026, China added specific US rare-earth producers and defense-linked manufacturers to its extraterritorial export control list. The net impact of these changes has been a bifurcation of the market for the dysprosium, terbium and scandium into two pieces: A Chinese market, and a market for the rest of the world. The practical impact of this bifurcation is a dramatic difference in price for these products in China versus the rest of the world; in general, prices outside of China are 3 to 4 times the price inside China at the time of writing. The light rare earths, niobium and titanium are not impacted by these changes.

In considering the impact of these price changes, this report presents conservative prices in Section 19.1 of this report as the long-term basis for the project’s Mineral Resource and Mineral Reserve. However, to account for the economic impacts of the current high price environment (which does not show any signs of abating), higher prices for terbium, dysprosium and scandium are used in the Project’s economic model. Additional information for each of these products is presented in Sections 19.3.1 and 19.3.2 below.

16.3.1 Scandium

The text below is adapted from OnG’s reassessment of Scandium pricing in June 2026:

“We have reassessed our scandium pricing forecast since August of 2025. There are a range of reasons, some unchanged and some new, and we summarize the logic below.

First, unchanged from 2025, we believe prices in China and the rest of the world will bifurcate, with China likely enjoying excess supply and soft pricing while the western world sees tight supply and elevated prices. As of late June 2026, prices in China appear to be in the range of $850-900/Kg oxide (for a 3N oxide) while western world prices are perhaps 4x higher in the commercial market and almost 6x higher as paid by the US DLA to Rio.

Prices for scandium oxide in China appear to have risen modestly in recent months, according to The Rare Earth Observer. We believe these prices are reasonably representative of domestic China prices but, thanks to export control and dual use legislation in China, are currently unmoored from global pricing.

Second, Bloom is one of the beneficiaries of the enormous capital investment surge in AI, potentially set to reach $650 billion in 2026 if company announcements are to be believed. Within the US, both Goldman and JP Morgan estimate very large medium-term power shortages due to congested grids, shortage of interconnect plant, and long lead times for new gas turbines. JP Morgan estimates a shortfall in available AI power in the US of about 50GW in 2028. This explains why many data centres are turning to fast-to-deploy power (solar plus storage) and islanded (no grid reliance) power infrastructure to help accelerate time to market.

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Bloom has several headline AI related agreements, including Brookfield (up to $5 billion), Oracle (master agreement for 2.8 GW), AEP (up to 1 GW), and Nebius (328MW for 2026 installation). At an estimated 75 Kg/MW scandium intensity, Nebius alone represents almost 25 tons of scandium oxide demand. The four announced agreements together represent likely over 400 tons of incremental scandium oxide demand.

While growth in the hydrogen market appears to be slowing and being pushed out, the next 5 years were not anticipated to represent meaningful scandium demand and we do not see a slowdown in electrolysis demand as having a meaningful impact on Bloom's business in the next 5 years.

Bloom may defer or decline opportunities in its core business and may slow down its work on maritime power - in fact, we think both these outcomes are probably inescapable - however the scale of AI demand and probable further growth in orders imply Bloom likely has to expend dramatically, and quickly, its scandium supply. This could come from China, from laterite secondary recovery, and from emerging Western World projects such as Rio and Sunrise.

Third, Bloom's revenue and demand growth in the past twelve months, plus the risk of reliance on Chinese scandium, mean Bloom likely has to move aggressively to develop alternative sources of supply outside of China. The company has never disclosed any perceived risk of scandium supply but it is widely understood Bloom is heavily dependent on Chinese scandium oxide and (less clear but widely understood to be the case) ceramic elecrodes. Scandium itself is categorised in China as a dual use material and we believe continued supply cannot be taken for granted. Thus Bloom will have to commit to expand supply and without a currently bankable balance sheet will need to pay a premium for supply.

Fourth, in the near term (pre-2030) there are limited options for Bloom. Rio is developing a 12-ton per year plant but whether it goes beyond this is an open question for a tiny unit within a $5 billion-range business unit (Rio Tinto Fer et Titan) that is currently an asset held for sale. We understand there are plans to expand recovery at Sumitomo's operations in the Philippines, however the plant appears from export data never to have produced more than about 75% of nameplate capacity (7.5 tpy scandium oxide). Syerston (Sunrise's primary scandium project) is approaching a final investment decision probably subject to adequate debt finance, but we doubt an agreement with Bloom could backstop debt meaning Sunrise will need either Government guarantees or a willing lender, for which margin-based covenants will be important. This means higher prices, of course.

There is no doubt that the laterite nickel-cobalt operations in Indonesia, the Philippines and Papua New Guinea contain thousands of tons of scandium in their ores. Actual recovery is minuscule in contrast (Sumitomo in Tagano Bay) and probably China MinMet via the Ramu project in Papua New Guinea, currently perhaps 10-20 tpy of scandium oxide although with large uncertainties.

We could imagine small pilot plants at other laterite operations in the medium term, but doubt the risk of affecting a large part of the material flow at any of these plants, to recover scandium for Bloom, would represent an acceptable commercial risk for any laterite operator.

Fifth, there appears to be strongly increasing interest in scandium-aluminium alloys and additive manufacturing, especially in aerospace where scalmalloy powders (on average around 1 weight percent contained scandium) are showing striking benefits in aluminium additive printing. The MoUs between Traxys and Niocorp and Sunrise and Lockheed make the point that additive manufacturing alloys are likely a near term demand source for scandium, albeit that neither offtaker is willing (both are able) to provide bankable financing.

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Additive parts offer several benefits, including the ability to achieve complex shapes for parts inaccessible via more established metal making, the ability to reduce material intensity and frequently by double-digit percentages over standard metallurgy parts, the ability to prototype and iterate rapidly, and a buy-to-fly bill of materials close to one.

For aerospace, a bona fide weight reduction for a civilian aircraft is estimated to be worth $4,000 per Kg. Hence if scalmalloy allows a 1% weight reduction for a 1% addition of scandium metal, crudely put the part can tolerate a scandium price of $4,000. Of course, there is more to the matter but this very naive arithmetic illustrates the possible value of scandium alloys in aerospace.

One final data point here is the emergingevidence (private communications from industry actors) that Scalmalloy enables aluminium additive printing in ways other aluminium alloys cannot, especially in achieving desired as-built alloy strength. We understand the focus of the Lockheed-Sunrise deal is Scalmalloy, for instance.

We expect industrial applications of scandium to grow faster than our prior projections once a supply is established (probably from Sunrise), creating price competition for Bloom as aluminium additive and wider use of scandium in industrial alloys starts to grow.

Our former projections from August 2025 are reproduced below in Table 16‑9:

Table 16‑9: Price projections, current US$, scandium oxide per Kg by source, 2025-35.

 

2025

2026

2027

2028

2029

2030

2031

2032

2033

2034

2035

China

800

800

1000

1000

1200

1000

950

850

900

950

1200

Sumitomo

2000

2000

2000

2000

2000

2000

2000

2000

2000

2000

2000

Rio

0

0

3000

3000

3000

3000

3000

3000

3000

3000

3000

NioCorp

0

0

0

0

0

2000

1750

1500

1800

2250

2500

Other

0

0

0

0

0

2000

1750

1500

1800

2250

2500

Average

902

876

1113

1099

1398

1429

1330

1255

1384

1637

1826

Source: OnG Estimates & Analysis, August 2025

 

Today things look very different. We no longer believe that China prices can be relied upon by Western consumers. Thus, low-capacity utilisation in China, something we expect to persist while also maintaining low prices and driving net demand there, is unlikely to operate so as to exert significant downward leverage on Western market pricing. Ultimately, the Government of China's goal is to export end products rather than raw materials hence access to refined minerals, or components such as solid oxide electrolytes, risk becoming much harder to source from China.

Moreover, western firms are certain to be aware of supply constraints. Scandium is currently (a) essential for certain cell phone 5G components and (b) largely unobtainable outside China. This is sure to engender a loss of trust in China's ability to supply that will be hard to overcome even if Chinese policies changed today. All in all, this means that western firms will be forced to buy what they can from non-Chinese sources, what they must from China, and hope the supply meets their needs for their businesses.

So, where does this leave prices? The current Rio price, based on market rumours, is close to $5,000/Kg of scandium oxide (probably a 3N product). Rumours also suggest prices from Taganito have picked up from a low around $1,000/Kg scandium oxide in 2023 (using Philippines export data)

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to closer to $1,500/Kg for a similar quality oxide. The Sunrise data that is public suggests an oxide price of $1,500/Kg would be sufficient, however this is before significant capital has been expensed and our view is costs and pricing are optimistic. Moreover, whatever Sunrise's initial price (which we expect to be $2,000/Kg or higher), further expansions ought to see higher pricing.

We do not expect other emerging miners (Scandium International, Scandium Canada, Australian Mines etc) to be able quickly to raise capital in the event Sunrise is actually able to reach financial close (still a moot point at time of writing). There are no bankable offtakes in sight and as we discuss below, there are several risks to our forecast.

The impact of AI is decisive in our model of supply and demand. Eliminating everything except Bloom, electronics demand and half of aerospace/drone demand, the scandium market (even with our former China projections) is expected to be short supply until 2031 and to remain above 90% utilisation except in 2034. Hence prices will in our view trade well above our August 2025 projections. Prices will have to rise enough (a) to stimulate extra supply; (b) perhaps to enable some additional Chinese exports; and (c) to depress demand in lower value segments (some metal alloy markets, possibly some existing Bloom business). Revised Sc pricing projection is shown below in Table 16‑10.

Table 16‑10: Revised Price projections, current US$, scandium oxide per Kg by source, 2025-36

 

2025

2026

2027

2028

2029

2030

2031

2032

2033

2034

2035

2036

China

800

800

1000

1200

1200

1000

950

850

900

950

1200

1200

Sumitomo

1250

1500

2500

3000

3000

3000

3000

3000

3000

3000

3000

3000

Rio

3000

4900

4500

3500

3500

3500

3500

3500

3250

3500

3500

3500

NioCorp

 

 

 

 

 

3250

3250

3250

2900

3250

3250

3250

Sunrise

 

 

 

2000

2500

3000

3000

3000

2500

3000

3000

3000

Other

 

 

 

 

 

3250

3250

3250

2900

3250

3250

3250

Average

963

1106

1736

2105

2051

2144

2287

2333

2082

2360

2433

2433

Non-China average

1750

2427

3500

3350

3350

3308

3282

3293

3001

3324

3324

3324

Source: OnG Estimates & Analysis, June 2026

We expect current non-China prices to rise rapidly through 2027, then to dip somewhat as Sunrise starts up and offers (we estimate) $2,000/Kg for oxide initially. We do not expect this to last.

Our view is that prices will have to reach and remain in the $3,000/Kg range for oxides to permit adequate scandium supply. We expect small volumes of red mud and EU Scavanger-type supply through our planning period, however (a) these are not low-cost operations and (b) the heterogeneity of these resources means their contribution to overall supply will be measured.

We do not expect a positive price environment to help the sundry scandium juniors to enter the market quickly. Capital will in our opinion remain short for pure scandium operations, Sunrise aside thanks to the shareholding of Robert Friedland.

There are several risks to our forecast.

1.
The AI boom may turn out to be a bubble. We do not believe current levels of capital investment are sustainable and the revenue model is unproven, but there is a plausible argument that AI represents the long-delayed returns to innovation that followed mass

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electrification. Still, a large downturn in near-term AI capital spending would drastically reduce scandium demand and therefore our price outlook.
2.
Trade war may turn into trade peace. Were this to happen (we think it highly improbable over our forecast horizon) Chinese raw materials would immediately undercut western demand across a host of critical industries. For this reason and regardless of what China wants, we see growth in domestic and bloc-style critical material supply as a long-term global shift.
3.
Large scale reclamation of scandium from laterites may start. Whether this would redound to the benefit of western firms is open to doubt, not least since many projects operate using Chinese technology and this will impose export controls on scandium.
4.
Demand may quickly exceed our projections in metal markets. The value of scandium is likely to be extremely high in additive-printed aluminium and even a modest share will push prices higher for all other consumers.
5.
Broader application in electronics (such as power electronics) could rapidly grow demand in semiconductors. This, too, would pressure supply into Bloom.
6.
Finally, if Chinese scandium exports are substantially curtailed at any time during the balance of this decade, all bets are off. There is not enough scandium to meet market needs and the economic damage will be widespread unless Bloom can dramatically (by a factor of 3-10 depending on timing) reduce scandium intensity per MW. We have no reason to believe the company is even close to this capability.

Our base case is what it is. We believe all the above variations are relatively low probability and while they do not cancel out, our price outlook provides a reasonable view of the current landscape for scandium pricing evolution.”

16.3.2 Dysprosium and Terbium

The market dynamics for dysprosium and terbium closely mirror those for scandium. Reputable rare earth market services are now reporting in China and outside China pricing. The demand for these two elements outside of China has not abated, and the available supplies are commanding a price that is 3 to 4 times the in China price. A compilation of pricing reported by Argus in the second quarter 2026 appears below in Table 16‑11.

Table 16‑11: Argus Non-Ferrous Market Pricing for Dy and Tb

2Q26 Average

 

 

 

 

 

 

Dy

$1,308

 

 

 

 

 

 

Tb

$4,523

 

 

 

 

 

 

 

 

 

 

 

 

 

 

Issue

Date

Dysprosium Oxide min 99.5% ddp US, $/kg

Terbium Oxide min 99.99% ddp US, $/kg

Low

High

Average

Low

High

Average

26-66

7-Apr-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 3,800

 $ 4,250

 $ 4,025

26-68

9-Apr-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 3,800

 $ 4,250

 $ 4,025

26-70

13-Apr-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 3,800

 $ 4,250

 $ 4,025

26-71

14-Apr-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 3,800

 $ 4,250

 $ 4,025

26-72

15-Apr-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 3,800

 $ 4,250

 $ 4,025

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26-73

16-Apr-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 3,800

 $ 4,250

 $ 4,025

26-74

17-Apr-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 3,800

 $ 4,250

 $ 4,025

26-82

29-Apr-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 3,800

 $ 4,250

 $ 4,025

26-83

30-Apr-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 4,000

 $ 4,250

 $ 4,125

26-86

6-May-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 4,000

 $ 4,250

 $ 4,125

26-87

7-May-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 4,000

 $ 4,250

 $ 4,125

26-88

8-May-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 4,000

 $ 4,250

 $ 4,125

26-90

12-May-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 4,000

 $ 4,250

 $ 4,125

26-91

13-May-26

 $ 1,050

 $ 1,200

 $ 1,125

 $ 4,000

 $ 4,250

 $ 4,125

26-92

14-May-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-93

15-May-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-94

18-May-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-96

20-May-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-97

21-May-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-98

22-May-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-99

26-May-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-101

28-May-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-102

29-May-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-103

1-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-104

2-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-105

3-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-106

4-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-107

5-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-108

8-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-109

9-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-110

10-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-111

11-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-112

12-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-113

15-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-114

16-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-115

17-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-116

18-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-117

19-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-118

22-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-119

23-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-121

25-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

26-122

26-Jun-26

 $ 1,200

 $ 1,600

 $ 1,400

 $ 4,500

 $ 5,000

 $ 4,750

Source: (Argus, 2026)

16.3.3 Economic Model Pricing

Based on the information presented in Sections 16.3.1 and 16.3.2, Table 16‑12 below presents a comparison between the pricing used for the resources and reserves presented in this report, along with the pricing utilized in the project’s economic model. Note that the scandium pricing presented in Section 16.3.1 is averaged over the forecast period.

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Table 16‑12: Pricing Comparison – Resource/Reserve versus Economic Model

Product

2026 Pricing

For Resources/Reserves

2026 Pricing

For Economic Model

Ferroniobium

$23.59/lb Nb

$52.00/kg Nb

$23.59/lb Nb

$52.01/kg Nb

Scandium Trioxide

$892/lb

$1,966/kg

$1,562.90/lb

$3,443.61/kg

Titanium Tetrachloride

$0.84/lb

$1.86/kg

$0.84/lb

$1.86/kg

Nd/Pr oxide

$56.7/lb

$125/kg

$62.78/lb

$138.40/kg

Dy oxide

$186/lb

$410/kg

$593.30/lb

$1,308/kg

Tb oxide

$837/lb

$1,845/kg

$2,048.21/lb

$4,515.52/kg

SEG Carbonate

$4.07/lb

$8.97/kg

$4.07/lb

$8.97/kg

Heavies Carbonate

$2.29/lb

$5.05/kg

$2.29/lb

$5.05lg

Source: NioCorp 2026

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

17 Environmental Studies, Permitting & Plans, Negotiations, or Agreements with Local Individuals or Groups

17.1 Environmental Studies

17.1.1 Soils

As outlined in the previous technical report summary (Batty et al. 2022), the Natural Resources Conservation Service identifies soils in the area as primarily comprised of clay, silty clay, silt loam, and clay loam; the ecological site is typified as “rangeland”. Infiltration is generally “slow” to “very slow”, and the depth to any restrictive layer in all soil types is more than 200 cm below ground surface (bgs). The area’s soils range in slope from 2% to 30% with the majority having slopes between 6% and 11% and are generally eroded (NRCS, 2015).

17.1.2 Climate/Meteorology/Air Quality

A dedicated meteorological station was installed at the Elk Creek site in July 2014. The instrument package included devices for: wind speed; wind direction; temperature; temperature difference (3 feet to 30 feet); dew point temperature; precipitation; pressure; and solar radiation. These meteorological data were continuously monitored until 2022, periodically audited by a third party, and are available for use in air dispersion modeling and air quality permitting.

Upon meeting with the Nebraska Department of Environment and Energy (NDEE, now DWEE) in 2016 regarding the on-site air monitoring program and air quality permitting needs, it was determined that the ambient monitoring program must include PM2.5 data collection. At that time, this parameter was under review by the U.S. Environmental Protection Agency (EPA). Thus, monitoring for PM2.5 was initiated in February 2017; PM10 monitoring was added in March 2017, along with CO, NOx, SOx, and ozone.

The Elk Creek site obtained an air quality construction permit in 2020, which remains active. Follow-up meetings with DWEE in late 2025 to update the agency on the status of and changes to the project resulted in determination that a modification to the air quality construction permit would be necessary due to a change in the PM2.5 air quality standard. In January 2026, it was also determined that a second air quality construction permit would be required as on-site power generation would be necessary due to the Company’s decision to use an on-site microgrid to provide power during construction and operations. Coordination with the microgrid provider is ongoing at this time, with initiation of air quality permitting for this additional source to follow.

17.1.3 Cultural and Archaeological Resources

As outlined in the previous technical report summary (Batty et al. 2022), there are no significant archaeological resources which will be impacted by construction of the Project, including the mine and processing area, evaporation pond and tailings impoundment area.

The Project will be subject to the provisions of the Nebraska Unmarked Human Skeletal Remains and Burial Goods Protection Act (Neb. Rev. Stat. §28-1301) during construction.

17.1.4 Vegetation

As outlined in the previous technical report summary (Batty et al., 2022), cultivated cropland makes up the predominant surface land cover within the project boundary, with native and non-agricultural

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vegetation found along field margins and in riparian areas associated with surface water drainages. NRCS (2015) ecosite descriptions note that areas in proximity to the project have predominantly annual and perennial weedy forbs and less desirable grasses which resulted from the abandonment of adjacent farmland. NioCorp has committed to best management practices which include project development predominantly on previously disturbed land.

17.1.5 Wildlife

As outlined in the previous technical report summary (Batty et al., 2022), the project is located within the Tallgrass Prairie Ecoregion of Nebraska (Schneider et al., 2011). This ecoregion is home to more than 300 species of resident and migratory birds and 55 mammal species, most of which are also found in central and western Nebraska.

17.1.6 Threatened, Endangered, and Special Status Species

As listed in the previous technical report summary (Batty et al., 2022), the following “Tier I at-risk species” for the state of Nebraska may occur in the vicinity of the project:

Birds:

•
Greater Prairie-Chicken (Tympanuchus cupido);
•
Henslow’s Sparrow (Ammodramus henslowii);
•
Loggerhead Shrike (Lanius ludovicianus); and
•
Wood Thrush (Hylocichla mustelina)

 

Reptiles:

•
Massasauga (Sistrurus catenatus); and
•
Timber Rattlesnake (Crotalus horridus)

 

Insects:

•
Iowa Skipper (Atrytone arogos iowa);
•
Regal Fritillary (Speyeria idaliaI);
•
Married Underwing (Catocala nuptialis); and
•
Whitney Underwing (Catocala whitneyi)

Mollusks:

•
Pimpleback (Quadrula pustulosa);
•
Pistolgrip (Tritogonia verrucosa); and
•
Plains Pocketbook (Lampsilis cardium)

Mammals:

•
Plains Harvest Mouse (Reithrodontomys montanus griseus)

The U.S. Fish and Wildlife Service (USFWS) Information for Planning and Consultation (IPaC) tool and the Nebraska Game and Parks Commission (NGPC) Conservation and Environmental Review

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Tool (CERT) were used to review the project for risks to threatened and endangered species. NioCorp and Olsson also coordinated with NGPC via two conference calls in December 2025. Olsson completed a biological assessment at the request of NGPC, which included effects determinations for the northern long-eared bat (Myotis septentrionalis) and western massasauga (Sistrurus tergeminus). Because these determinations were “no effect” and “may affect, but not likely to adversely affect”, respectively, NGPC gave its approval for state-level permitting. NioCorp committed to make every effort practicable to only remove trees from the site within the inactive period for the bat (September 15 – March 31), and to use downward-facing lighting on the project site whenever possible and practicable.

Based on a review of the USFWS IPaC and NGPC CERT results, there is no designated critical habitat for threatened, endangered, or proposed species within the project area. The USFWS IPaC identified three proposed species as potentially occurring within the project site: monarch butterfly (Danaus plexippus), Suckley’s cuckoo bumble bee (Bombus suckleyi), and western regal fritillary (Argynnis idalia occidentalis). As there is no federal nexus for the project, these three species were not further considered. USFWS IPaC did not identify any currently listed species with the potential to occur within the project area.

17.1.7 Land Use

As outlined in the previous technical report summary (Batty et al., 2022), farming for livestock, crops, and pasture have been the most important land uses within Johnson County. Land use in the vicinity of the project is most suitable for rangeland and hay or corn, sorghum, or soybeans if irrigated (USDA, 1984).

17.1.8 Hydrogeology (Groundwater)

As outlined in the previous technical report summary (Batty et al., 2022), a hydrogeological characterization of the deposit was conducted in 2014. The data collected here was used to establish prospective mine water inflow. The hydrogeological issues associated with preliminary findings were significant enough to warrant a second investigation in 2015. The results of this testing were used to develop a preliminary conceptual model.

The data was re-analyzed in 2017 by Adrian Brown, a mining geohydrological consultant. Based on his review, Brown concluded that mine inflow control could be achieved using ground freezing and grouting for the shafts and grouting in the mine development. Additional work in 2025 by Adrian Brown determined that improved control of formation water inflow to the mine could be achieved through grouting. Water treatment of the mine dewatering flow can be handled by reverse osmosis (RO), and the RO permeate can then be used in the surface plant. The salts/brines from the RO will be evaporated or crystallized into a solid salt, which can then be disposed of in engineered and lined salt management cells or disposed offsite (Batty et al., 2022).

While sampling from 2014 and 2015 indicated similar water quality, results varied across the site. Deep groundwater test samples identified dissolved solids sometimes over 18,000 ppm (with major contributors of sodium and chloride) as well as maximum contaminant load (MCL) exceedances of arsenic, gross alpha, and Ra-226 + Ra-228. These deep groundwater samples also documented exceedances of secondary MCLs for chloride, fluoride, iron, manganese, sulphate, and total dissolved solids (Batty et al., 2022). The deep groundwater quality is a pre-exiting condition, and suggests that the water is remnant of the shallow sea the existed around the time the Pennsylvanian marine sediments formed.

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It is noted that the project will include a grouting program to minimize seepage of deep groundwater into the mine and that any seepage will be treated as described above.

17.1.9 Hydrology (Surface Water)

As outlined in the previous technical report summary (Batty et al., 2022), surface water sampling has been conducted at the site periodically since early 2014 to establish baseline monitoring results for upstream and downstream areas of the project. The preliminary results identified: (1) minor water quality impairments; (2) average stream TDS concentrations that fluctuated, although this is likely the result of post-harvest runoff; (3) circum-neutral stream pH; and (4) gross alpha, beta, Ra-226 and Ra-228 detection in some water samples, although below MCLs

•
Wetlands / Riparian Zones

Olsson Associates (now Olsson) completed a wetland delineation for the project in 2015. Olsson identified 45 wetlands totaling 4.3 hectares (10.64 acres). In 2016, Olsson submitted a request for an Approved Jurisdictional Determination (AJD) from the U.S. Army Corps of Engineers; this AJD identified 11 stream reaches and associated wetlands as jurisdictional waters of the U.S. (Batty et al., 2022). It is noted that federal law governing jurisdictional waters has changed significantly since this determination.

Olsson completed another wetland delineation for the project in 2022, which included overlap with the original area delineated in 2015 and a small additional area to the southeast at the corner of Highway 50 and County Road 720. This delineation also reduced the area of delineation to only east of County Road 620 and south of County Road 721. This delineation identified 29 wetlands totaling 1.67 hectares (4.13 acres) and four stream channels totaling 15,981 linear feet (4,871 meters) . An AJD request was submitted in 2025 based on this updated wetland delineation; this AJD identified two jurisdictional linear features (Elk Creek and an associated intermittent tributary running west-to-east across the site) and two wetlands associated with these linear features. This more recent AJD will be valid until February of 2031.

17.1.10 Environmental Geochemistry

NioCorp has developed a comprehensive environmental geochemistry characterization program for tailings, ore, and waste rock. Ore and waste rock were thoroughly characterized during the 2017 study (SRK, 2017). Tailings quantities have been limited, and geochemical characterization has lagged other test work that is critical for production, such as geotechnical analyses and paste strength testing. Consequently, characterization work on tailings materials recently produced from metallurgical testing is in progress at the time of writing this report. Geochemical characterization results received to date are described in the following sections.

Niobium Mineralized Material

NioCorp plans to temporarily stockpile limited quantities of ore on ground surface before processing. Laboratory testing indicates that the ore has the potential to leach various constituents upon exposure to meteoric precipitation. Leach testing of a composite sample of this material from drill hole NEC11-001 was completed using the Meteoric Water Mobility Procedure (MWMP), and indicates that, at a minimum, fluoride and nitrate are likely to be mobilized during surface stockpiling. It is worth noting that fluoride is the only analyte in the test leachate that exceeds the Environmental Protection Agency’s Primary Maximum Contaminant Level (MCL). Nitrate and several metals are detectable, but not at concentrations exceeding their respective MCL for drinking water

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The mineralized material contains naturally occurring uranium and thorium. Drilling data indicate that the average thorium and uranium contents in the mineral resource are 0.011% and 0.0033%, respectively (DGC, written communication, 2026).

Laboratory leach testing of potential waste rock has not produced concentrations of radionuclides above regulatory limits, although concentrations in the rock are relatively elevated (SRK, 2017):

•
Uranium = 22 ppm
•
Thorium = 153 ppm
•
Gross alpha = 83 pCi/g
•
Gross beta = 67 pCi/g
•
Radium 226 = 28 pCi/g
•
Radium 228 = 8 pCi/g

The current assay database for the Elk Creek Project contains 22,153 samples for which uranium and thorium were analyzed and detected. Of this dataset, 1,713 samples had a combined uranium + thorium concentration greater than 500 ppm. The mean and median concentration of uranium + thorium was 146 ppm and 50 ppm, respectively.

Waste Rock and Overburden

There are two basic types of waste rock associated with the deposit. These include:

(1)
Pennsylvanian limestones and mudstones – The upper 100 ft (30 m) of lithology consists of unconsolidated glacial till, underlain by 560 to 590 ft (170 to 180 m) of low-permeability, Pennsylvanian-aged mudstone and limestone. The Pennsylvanian is reportedly continuous across the state of Nebraska, and locally it behaves as a very effective aquitard. This material is acid-neutralizing due to its high carbonate content. In terms of metal leaching characteristics, MWMP testing suggests that the Pennsylvanian has the potential to leach antimony and selenium at concentrations above general surface water standards. Additionally, the Pennsylvanian exhibits a propensity to leach gross alpha and radium above regulatory limits. This lithology is the primary source for construction aggregate in Nebraska.
(2)
Non-ore grade carbonatite – Assessment of the host rock identified visual sulfide content of up to 1% based on observations by core loggers. Laboratory analyses confirmed the sulfide content at around 1.34%. This sulfide consists mainly of pyrite, chalcopyrite, bornite, galena, sphalerite, and possibly pyrrhotite. However, even with detectable sulfide content, the carbonatite waste rock is still net neutralizing given the high carbonate content.

Of the 94 rock samples collected over an 837 ft (255 m) vertical length of the waste rock and mineralized zone, eight samples registered a reading of >25 µRads/hour. These levels are not considered to be hazardous but may be used as a diagnostic tool to identify elevated concentrations of uranium and thorium.

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Temporary surface disposal of waste rock will be predicated on minimizing meteoric infiltration and leaching of this material. NioCorp has conservatively elected to line the waste rock and low-grade mineralized material stockpiles, and actively manage any runoff derived from these materials until such time as that, and residual ore and low-grade mineralized materials can be processed, and the surface waste rock transferred to the TSF for final disposal.

NioCorp will use Pennsylvanian waste rock as construction fill in the mine area and will selectively favor the limestone unit for this purpose. Among the various waste rock lithologies, limestone is the most environmentally favorable and therefore the best option for fill. The unit’s radionuclide content is significantly lower than the other Pennsylvanian lithologies, and MWMP testing indicates low concentrations of metals in the leachate (SRK, 2017).

Tailings

The geochemical characterization program relies on representative samples of the five materials planned for disposal in the TSF, which include the three post-processing tailings products from the metallurgical testing program (Water Leach Tailings, Fe-Oxide, and Mg/Ca Carbonate), waste rock, and low-grade ore.

At the time of writing this report, geochemical characterization of tailings is still in progress. Results from geochemical analyses of tailings that have been completed are described below.

Short term leach testing was completed on tailings using the Toxicity Characterization Leaching Procedure (EPA method 1311) and the Synthetic Precipitation Leaching Procedure (EPA method 1312), which are designed to determine the mobility of both organic and inorganic analytes present in the liquid, solid, and multiphasic wastes, and assist in the proper classification of waste materials. The tailings material tested under the TCLP protocol showed negligible mobility of regulated constituents, indicating a non-hazardous classification.

Other test work completed on tailings include whole rock analyses by L3 Process Development, and detailed mineralogical analyses by SGS Laboratory. Results from these analyses will help in evaluating geochemical characterization data that will be generated from the tests currently in progress.

A testing program in progress at ACZ Laboratory includes the following:

•
Humidity cell test (HCT). The humidity cell will test the leachate chemistry of a composite sample blended from the five materials described above, in the proportions at which they will be deposited in the TSF, as follows:
o
Water Leach Residue: 35%
o
Fe-Oxide: 21%
o
Mg/Ca Carb: 24%
o
Waste rock: 10%
o
Low-grade ore: 10%
o
Multi-element analysis of the HCT leachate and solids
o
Radiochemical analysis of the HCT leachate and solids

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NioCorp Developments Ltd.

17.1.11 Known Environmental Issues

At this time, there are no known environmental concerns that would materially impact NioCorp’s ability to extract the mineral reserves or mineral resources near Elk Creek. Environmental permitting timelines at the state level require up to six months for processing of most individual permits, with roughly 18 months needed for solid waste permitting for tailings impoundments. Broadly speaking, general permits can be active within seven to 10 days of providing a full and complete application package.

17.2 Waste Management & Disposal

17.2.1 Mine Overburden

Excavated marine sediments and will be crushed and used as construction fill/material.

17.2.2 Tailings/Waste Rock/Process Waste (Onsite)

Waste rock sourced from the carbonatite will be placed in a lined impoundment on the surface or co-disposed with the tailings in lined impoundments. Tailings and process waste streams will be combined with water, cement, and fly ash and either pumped underground as structural fill in the underground mine or pumped to engineered and lined surface disposal impoundments. Pyrometallurgical slag will be hauled to the same engineered and lined surface disposal impoundments.

Due to the presence of naturally occurring radioactive materials (NORMs) in the ore and waste materials, including the RO water treatment salts and the final process waste streams that will make up the bulk of the tailings mass, there is potential for limited reaction to contact with water. Previous regulatory testing of these materials indicated they are classified as non-hazardous. As such, sitewide non-contact stormwater will be routed to a detention pond with periodic discharge as needed. Following closure, it is not anticipated that any of the mine development or waste rock would remain exposed on the surface.

As previously mentioned, reject brine from the proposed RO process will be evaporated/crystallized into a solid salt. This solid salt will then be disposed of in engineered and lined salt management cells (Batty et al., 2022).

17.2.3 Project Waste Disposal (Offsite)

Solid Waste

Sanitary solid waste (other than waste rock, tailings, and other process-related solid waste) will be disposed of through contract with a local solid waste hauler.

Hazardous Waste

Any hazardous waste generated by the project will be transported by a licensed hazardous waste operator to the Clean Harbors Environmental Services Facility in Deer Trail, Colorado, which is approximately 470 miles (756 km) from the project site. This will be done in accordance with all applicable state and federal regulations (Batty et al., 2022).

17.2.4 Site Monitoring

The baseline surface water and groundwater monitoring will continue during the life of the project, with monitoring areas added as deemed necessary during the regulatory process. Monitoring efforts

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will include, but may not be limited to, groundwater monitoring upgradient and downgradient of the tailings storage facilities. With the solid waste disposal permit, geotechnical monitoring of the tailings storage facilities will also be completed on a regular basis (Batty et al., 2022).

Ambient air quality monitoring (including emission control monitoring during operations if necessary) will be conducted in accordance with corresponding air permits (Batty et al., 2022).

17.2.5 Water Management

Construction Water Management

The advancement of the underground workings is anticipated to require dewatering for the first several years of construction. Dewatered shallow groundwater and stormwater within the footprint of the portal excavation will be directed to a stormwater detention pond and discharged intermittently as needed to an intermittent tributary of Elk Creek. NioCorp has obtained both required DWEE permits (Dewatering and Construction Stormwater Permit), as well as the floodplain development permit needed from Johnson County for the construction of the stormwater pond.

Operational Water Management

NioCorp anticipates a shortfall of operational and processing water when using the water from dewatering for mine facilities. As outlined in the previous technical report summary (Batty et al. 2022), NioCorp anticipates receiving an adequate supply of water for operations from the Tecumseh Board of Public Works water supply.

Internal contact water from tailings being deposited within the TSF cells will also need to be managed during operations. This internal contact water will be collected and treated in the facility wastewater treatment system, which includes softening/precipitation and reverse osmosis (RO) treatment steps. The reverse osmosis permeate water can then be reused in the process plant; RO reject water will be crystalized and the salt deposited in a Salt Management Cell.

Post-Closure Management

Groundwater and stormwater management and monitoring may continue past the closure for verification/sustainability monitoring. TSF contact water streams will need to be evaluated during the final years of operation.

17.2.6 Chemical and Reagents Handling

As outlined in the previous technical report summary (Batty et al. 2022), process reagents and chemicals will be transported to the site and stored in specially designed and constructed containers located within appropriate secondary containment set-ups (concreted and concrete-bermed areas). For liquid chemicals and reagents, the bermed storage area will be designed to hold a minimum of 110% capacity of the largest storage tank or series of tanks within the containment.

Other liquids such as fuel, antifreeze, petroleum oils, and solvents will be delivered in tanker trucks, totes, and barrels and transferred to appropriate onsite storage tanks. These storage tanks will also be stored in bermed areas designed to hold a minimum of 110% capacity of the largest storage tank or series of tanks within the containment (Batty et al. 2022). Spill Prevention, Controls and Countermeasures (SPCC) are required during construction and operational phases, and initiation of SPCC inspections and planning has begun.

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Explosive materials including blasting agents and initiation devices will be stored in both surface and underground magazines, with explosive magazines stored separately from other components. The magazines in conformance with U.S. Bureau of Alcohol, Tobacco and Firearms, MSHA, and other applicable state and local regulations (Batty et al., 2022).

17.3 Project Permitting Requirements

Engagement of local and state regulators is currently in progress. While the formal operational permitting program for the Project is dependent upon the completion of the mine plan, preliminary permitting and consultation as necessary in anticipation of construction has commenced. At this time, NioCorp had completed the following:

(1)
Nebraska Department of Water, Energy, and Environment (DWEE) Mineral Exploration Permit for exploration drilling;
(2)
DWEE air quality construction permit;
(3)
DWEE authorization for Class V underground injection well for the hydrogeological portion of the exploration drilling;
(4)
Johnson County road use and maintenance agreement;
(5)
Johnson County special use permit;
(6)
DWEE construction stormwater permit;
(7)
DWEE construction dewatering discharge permit;
(8)
Notification of Commencement of Operations with the Mine Safety and Health Administration (MHSA); and
(9)
Johnson County floodplain development permit.

These permits and authorizations have allowed for mine portal construction activities, and other construction and operations permits as needed have been scheduled for initiation as needed to support remaining stages of construction and commencement of operation. These are further summarized in Section 17.3.5.

Additional permitting requirements may include those from: Johnson County, the State of Nebraska, and U.S. Environmental Protection Agency (EPA) and U.S. Army Corps of Engineers (USACE). The full list of potentially applicable permits and authorizations are included in Table 17‑1 below, including current status as relevant.

Table 17‑1: Project Permits

Permit/Approval

Issuing Authority

Permit Purpose

Status

Federal Permits, Approvals, and Registrations

Explosives Permit

U.S. Bureau of Alcohol, Tobacco, and Firearms (BATF)

Storage and use of explosives

Required – Explosives will be used and stored on site during portal excavation.

EPA Hazardous Waste Registration

U.S. Environmental Protection Agency (EPA)

Registration as a Conditionally Exempt Small Quantity

May Be Required – NioCorp facilities are

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Permit/Approval

Issuing Authority

Permit Purpose

Status

 

 

Generator (CESQG) or a Small Quantity Generator (SQG) of waste

likely to generate small quantities of hazardous waste.

Spill Prevention, Control, and Countermeasure (SPCC) Plan

EPA

Regulation of facilities having an aggregate aboveground oil storage capacity greater than 1,320 gallons or an underground storage capacity greater than 42,000 gallons

Required – There will be onsite fuel storage during construction (in process).

Notification of Commencement of Operations

Mine Safety and Health Administration (MSHA)

Mine safety inspections, safety training plan, mine registration

Completed and obtained.

Obstruction Evaluation/Airport Airspace Analysis (OE/AAA)

Federal Aviation Administration (FAA)

Regulations requiring notification for any construction or alteration exceed 200 feet above ground level

Required – If any structures will exceed 200 feet above ground level.

Federal Communications Commission Permit

Federal Communications Commission (FCC)

Frequency registrations for radio/microwave communication facilities

Required – If NioCorp intends to use business radios to transmit their own frequency.

Clean Water Act Section 404

U.S. Army Corps of Engineers

If impacts to jurisdictional water features exceed regulatory thresholds

May be required – If any impacts to jurisdictional features are anticipated.

State Permits, Authorizations, and Registrations

Explosives Permit

Nebraska State Patrol

Regulates the use, storage, or manufacturing of explosive materials

Required – Explosives will be used on site; also regulated by MSHA, DHS, and BATF.

Permit to Discharge under the National Pollutant Discharge Elimination System (NPDES) – Construction Dewatering

DWEE

Permits groundwater dewatering on industrial sites

Completed and obtained.

NPDES – Construction Stormwater

DWEE

Regulates construction activity that cause a land disturbance of more than one acre and provide guidelines for stormwater control

Completed and obtained.

NPDES – Industrial Stormwater

DWEE

Regulates discharge of stormwater from industrial sites

Required – NioCorp will need this permit for operations.

NPDES – Sanitary Wastewater Discharge

DWEE

Regulates discharge of wastewater

Required – NioCorp will need this permit for discharge of sanitary wastewater during operation.

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Permit/Approval

Issuing Authority

Permit Purpose

Status

Operation of Wastewater Works

DWEE

Regulates design, operation, and maintenance of wastewater works

Possibly required – Early discussions with DWEE indicate permitting for Salt Management Cell may be required under Title 123

Mineral Exploration Permit

DWEE

Regulates the exploration for minerals by boring, drilling, diving, or digging

Complete and obtained.

Air Construction Permit

DWEE

Regulates emissions during construction activities

One permit completed and obtained; modification required due to changes in regulations and additional source(s) due to on-site power generation for construction and operations.

Air Operating Permit

DWEE

Regulates emissions during operation

Required – The project will have emissions which may impact ambient air quality. Application no sooner than after the completion of 1 year of operations

Authorization for Class V Well Underground Injection; Other Underground Injection TBD

DWEE

All activities conducted pursuant to Title 122 – Rules and Regulations for Underground Injection and Mineral Production Wells

 May be required for placement of tailings/treated wastewater in mining voids.

Boiler Inspection Certificate

Nebraska Department of Labor

Inspection and approval for boilers

Required – For any boiler installations for the project.

Section 401 Water Quality Certification

DWEE

Evaluation of federal permits and licenses which involve discharge to waters of the state and determine whether or not the activity complies with Title 117 – Nebraska Surface Water Quality Standards.

May Be Required – If Section 404 permitting requirements are triggered.

Fire and Life Safety Permit

Nebraska State Fire Marshal

Review of non-structural features for safety purposes

Required – NioCorp will need to submit operations and building plans for approval.

State Business License

Nebraska Secretary of State

License to operate in the state of Nebraska

Complete and obtained.

Retail Sales Permit or Exemption Certificate

Nebraska State Tax Commissioner

Permit to by wholesale or sell retail

May Be Required – If NioCorp intends to do direct sales of products.

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Permit/Approval

Issuing Authority

Permit Purpose

Status

Solid Waste Management Permit

DWEE

Regulates construction and operation of solid waste management facilities

Required – NioCorp intends to create an onsite solid waste management facility (i.e. tailings).

Hazardous Waste Management

DWEE

Management and recycling of hazardous waste

Required – This entails reporting hazardous waste generated and/or transported from facility.

Dam Safety Approval

DWEE

Regulates design and construction of any dam

May Be Required – If artificial barriers with the ability to impound water or liquid-borne materials (includes tailings) will be utilized at any onsite impoundment

Permit to Impound Water

DWEE

Regulates any water impoundment that has a normal operating water volume of at least 15 AF below the spillway

May be Required – If any impoundment will impound greater than 15 AF below the spillway.

Groundwater Well Registration

DWEE

Registers groundwater wells in a statewide database

Obtained; required if NioCorp constructs additional groundwater wells.

Permit to Operate a Public (Non-transient, Non-Community) Water System

DWEE

Regulates water systems regularly serving at least 25 people not living in a community.

Required if NioCorp owns the service line and connection from the City of Tecumseh and operates the water system within the boundaries of the project site.

Groundwater Transfer Permit

DWEE

Permits the transfer of groundwater off of land from which it is extracted.

Required (City of Tecumseh as permit holder) if Tecumseh provides water to NioCorp.

Local Permits for Nemaha Natural Resources District, Johnson County, and Pawnee County

Permit to Construct a Water Well

Nemaha Natural Resources District

Permits the construction of high-capacity groundwater wells and withdrawal of groundwater.

Required if operations dictate need for extraction of groundwater beyond that provided by the City of Tecumseh.

Building and Construction Permit

Johnson County Zoning Administrator

Ensure compliance with local building standards/requirements

Required – This is required of all development in Johnson County.

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Permit/Approval

Issuing Authority

Permit Purpose

Status

County Road Use and Maintenance Permit/Agreement

Johnson County

Sets terms and conditions for use and maintenance of county roads

Completed and in effect.

County Law Enforcement Agreement

Johnson County

NioCorp will pay for a sherrif’s deputy during construction

Completed and in effect

Special Use Permit

Johnson County Zoning Administrator

Authorizes permitted use in a zoning district and sets conditions for operations

Completed and obtained.

Permitted Use Zoning Permit

Johnson County Zoning Administrator

Regulates construction of new buildings

Required – This is required of all development in Johnson County.

Floodplain Development Permit

Johnson County Zoning Administrator

Regulatory requirements for structures being constructed within a floodplain

Completed and obtained.

Building and Construction Permit

Pawnee County Zoning Administrator

Ensure compliance with local building standards/requirements

May be required if operations extend into Pawnee County in the future.

County Road Use and Maintenance Permit/Agreement

Pawnee County Zoning Administrator

Sets terms and conditions for use and maintenance of county roads

May be required if operations extend into Pawnee County in the future.

Special Use Permit

Pawnee County Zoning Administrator

Authorizes permitted use in a zoning district and sets conditions for operations

May be required If operations extend into Pawnee County in the future.

Permitted Use Zoning Permit

Pawnee County Zoning Administrator

Regulates construction of new buildings

May be required if operations extend into Pawnee County in the future.

Floodplain Development Permit

Pawnee County Zoning Administrator

Regulatory requirements for structures being constructed within a floodplain

May be required if operations extend into Pawnee County in the future.

Source: Olsson, 2026

The following is a brief discussion of some permits which were or are considered likely to be required for the project.

17.3.1 Nebraska Underground Injection Control

NioCorp may reinject reject waters from the RO process versus crystallization, should crystallization be determined to be impractical. If reinjection is pursued, this permit will be required. The UIC Program at DWEE issues and reviews permits, conducts inspections and performs compliance reviews for wells used to inject fluids into the subsurface, to ensure compliance with state and federal regulations. DWEE has authority and manages Class I, III, and V wells; Class II wells are associated with oil and gas production and are regulated by the Nebraska Oil and Gas Conservation Commission.

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This water treatment system brine re-injection well would likely classify as a Class V well, as it would not be used to inject industrial or municipal wastewater or for the purpose of extracting minerals.

Additionally, DWEE may require UIC permitting for placement of tailings mixed with treated process wastewater into mining voids. However, indications are that such a permit is not a concern to obtain and likely would not be needed as this material may qualify as beneficial fill and would not behave as a waste material.

Additional guidelines related to groundwater protections include following rules and regulations identified in the Nemaha Natural Resources District’s Groundwater Management Plan.

As noted, this is included only as an alternative to the current planned treatment and disposal of water.

17.3.2 DHHS Radioactive Materials Program and Licensing

As previously noted, the post-processing tailings from the project will contain trace amounts of NORMs (specifically uranium and thorium). Preliminary conversations with the State of Nebraska (December 2018), as discussed in the previous technical report summary (Batty et al. 2022), indicated that a Specific License of Broad Scope Radioactive Materials would be necessary. However, upon further communication with the State in 2026, it was determined that no licensing was expected to be needed as concentrations of uranium and thorium were below regulatory thresholds. Should additional testing yield different results, additional discussion with the State would be needed and licensing may be required.

17.3.3 Nebraska Air Quality Permitting

The Nebraska air quality regulations are primarily based on regulations developed by the EPA to address the Clean Air Act. DWEE’s Air Quality Program facilitates air permitting to implement the Clean Air Act for the state of Nebraska. Facilities which anticipate potential air emissions above specified levels are required to obtain a construction permit and/or operating permit.

For construction, generally, a facility must obtain a state-level construction permit before constructing, reconstructing, or modifying any air contaminant source or emission unit where there is an increase in the potential emissions above regulatory thresholds. At the federal level, there are two types of permits: a Prevention of Significant Deterioration (PSD) permit, which applies to areas with pollution levels below the national ambient air quality standards (NAAQS; i.e. attainment zones), and New Source Review permits, which apply to areas with pollution levels above the NAAQS (i.e. nonattainment zones). EPA has provided guidance to states to implement these permitting programs under the Clean Air Act. Nebraska is currently in attainment for all ambient air quality standards. The emissions thresholds for either of these construction permitting pathways generally are higher than the state-designated thresholds that trigger a state construction permit. Given the potential emissions profile of the project, a state construction permit was obtained on June 2, 2020. In follow-up discussion with DWEE in late 2025, it was determined that this permit would require modification due to changes in the PM2.5 standard. Additionally, NioCorp elected to obtain construction and operational power from an on-site microgrid operated by a third party. The on-site generators associated with the microgrid will also require air quality permitting; it is likely that the modification of the existing air quality construction permit will encompass both the changes due to PM2.5 standards and the on-site power generation.

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DWEE also issues operating permits based on a facility’s level of emissions. Operating permits incorporate all of a facility’s requirements into one permit, including those identified in the construction permit limitations and associated federal regulations. An operating permit usually comes with additional monitoring, reporting, and recordkeeping requirements. There are two types of operating permits: Major Source (Class I or Title V) and Minor Source (Class II). The federal major source program regulates Class I sources, which have potential to emit quantities greater than:

•
100 tons per year (tpy) of any criteria air pollutant excluding lead
•
10 tpy of any single hazardous air pollutant (HAP) or 25 tpy of a combination of HAPs
•
5 tpy of lead

Class II facilities can be classified as synthetic minor sources or natural minor sources based on the following:

•
Synthetic minor – potential emissions above Class I emissions but federally enforceable limits are taken to keep emissions below Class I emission levels
•
Natural minor – potential emissions below Class I emissions; actual emissions above 50% of Class I emissions

These potential emissions are based on operating the unit/source 24 hours per day at maximum capacity.

This facility is likely to qualify as a Class II facility and will need an operating permit, the application for which must be submitted to DWEE within 12 months of the emission unit(s) beginning operations.

17.3.4 Nebraska Dam Permitting

Per DWEE, a dam is defined as any artificial barrier with the ability to impound water or liquid-borne materials. DWEE approval is required when the dam has a total height of 25 feet or more, or the dam has an impounding capacity at the top of the dam of 50 acre-feet or more. Before constructing, reconstructing, altering, breaching, removing, or abandoning a dam in Nebraska, approval from DWEE must be obtained. All approved dams are also subject to the Safety of Dams and Reservoirs Act.

To receive DWEE approval for the dam, an application for approval of plans for dams must be submitted including dam design plans stamped by a licensed engineer. Upon construction of the dam, a construction certification form must be submitted which states that the dam was constructed in accordance with the approved plans and specifications submitted to DWEE for approval.

In addition to dam approval, if the reservoir will impound more than 15 acre-feet below the lowest open overflow, a permit to impound water will also be required. Requirements for submittal will vary depending on the reservoir classification and corresponding Nebraska Administrative Code Title; this project would likely fall under Title 458 if the water impoundment has a dam associated with it.

Generally, these permits may be required for the project if artificial barriers with the ability to impound water or liquid-borne materials (includes tailings) will be utilized at any of the on-site impoundments.

17.3.5 Permitting Status

As outlined in the previous technical report summary, initial permitting activities for the project began in January 2015 with the submittal of a Jurisdictional Delineation report to USACE. In the years following, additional meetings with federal, state, and local agencies were held in order to introduce

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the project and discuss potential regulatory requirements (Batty et al., 2022). Permits received thus far are:

(1)
DWEE Mineral Exploration Permit – Initially issued April 19, 2011 and renewed thereafter, for the exploration drilling program for the project.
(2)
DWEE Authorization for Class V Well Underground Injection – This was initially issued for the project June 19, 2014, for the hydrogeological portion of the exploration drilling program, and will also be required for future disposal of tailings and/or crystallized brine gels.
(3)
Johnson County Special Use Permit – Issued to NioCorp on December 24, 2019.
(4)
DWEE Air Quality Construction Permit – Issued June 2, 2020 for the project. A permit modification application will need to be submitted for the project given changes to project plans, including on-site power generation, since initial submittal.
(5)
Johnson County Road Use and Maintenance Agreement/Permit – Issued December 29, 2025 for the project and covers all project use and constructed access to county roads in Johnson County.
(6)
DWEE NPDES Dewatering Discharges – The Notice of Intent was approved February 3, 2026 and the project was authorized to conduct dewatering discharges under the terms and conditions of NPDES General Permit NEG71000 2017. This permit establishes daily flow and PCE monitoring, and Discharge Monitoring Reports are required to be submitted quarterly to remain in compliance with the authorization.
(7)
DWEE NPDES Construction Stormwater Permit – The Notice of Intent was approved on February 10, 2026 and the project was authorized to discharge storm water under the terms and conditions of NPDES General Permit NER 210000. A separate stormwater permit will be required for discharge during operations.
(8)
MSHA Notification of Commencement of Operations – MSHA approved this in February 2026, and the mine is now listed as an operational mine under MSHA.
(9)
Johnson County Floodplain Development Permit – Issued to NioCorp on March 6, 2026.

17.3.6 Post-Performance and Reclamation Bonding

There are limited requirements in terms of post-performance and reclamation bonding for hardrock mining in Nebraska given the lack of a general regulatory framework specific to hardrock mining activities in the state. An exception to this would be if the facility is required to apply for a Special License for radioactive material (as described in Section 20.3.2), as this comes with specific decommissioning planning and funding requirements. At present, the state of Nebraska has determined that a Radioactive Materials License is not required. NioCorp has taken a conservative approach and assumed that the licensure program and financial surety requirements will apply. Of note, financial surety is required for both Specific Licenses of Broad Scope and for Specific Licenses, but the financial surety avenues differ between the two. For Specific Licenses of Broad Scope, the following methods are acceptable for financial surety (180 TAC 3-011.02(A)):

•
Surety bond

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•
Cash deposit
•
Certificate of deposit
•
Deposit of government securities
•
Letters or lines of credit
•
Any combination of the above

Specific Licenses have more specific long-term reporting requirements and offer a more limited set of options for financial surety (180 TAC 3-018.06(B)):

•
Prepayment (trust fund)
•
Surety bond
•
Insurance
•
Letter of credit
•
Parent company guarantee of funds (based on a financial test)
•
External sinking fund

Financial surety will also apply to the TSFs, which are regulated under Integrated Solid Waste Management Regulations (DWEE Title 132). These regulations include requirements related to provision of a third-party closure cost estimate, a plan for proper disposal of all materials and waste, and post-closure care plan for the solid waste disposal area. These regulations allow for the following financial assurance methods:

•
Trust fund
•
Surety bond guaranteeing payment or performance
•
Letter of credit
•
Insurance
•
Corporate financial test
•
Local government financial test
•
Corporate guarantee
•
Local government guarantee
•
Other method approved by the state

At this time, the estimated cost of closure of the Project is US$106 million, but the type and phased amount of financial surety have not yet been determined. The specific requirements for closure, decommissioning, and financial surety will be refined through coordination with the relevant state regulatory agency staff members and submission of the appropriate documentation.

17.4 Community Relations and Social Responsibilities

As outlined in the previous technical report summary (Batty et al. 2022), NioCorp has pursued a multitude of engagement opportunities with local communities, including town halls (most recently in December 2025) as well as individual meetings with landowners. NioCorp has also met with local leadership, including county commissioners, as well as the Southwest Nebraska Development District. Regulatory agencies have also been actively engaged as of this Technical Report Summary, and a number of permits and authorizations have been received for the project (as discussed in Section 17.3.5).

NioCorp continues to be committed to garnering a Social License to Operate from the local community for this project. While overall feedback towards the project has been generally positive, there are local opponents as well as non-government organizations which oppose the project. NioCorp previously engaged with one of these local opposition groups, Bold Nebraska, on May 23,

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2016, to discuss the project while it was still in early stages. NioCorp has continued to engage with the group and keep them informed of major developments (Batty et al., 2022).

17.4.1 Safety and Health

MSHA is the predominant regulatory agency over occupational health and safety for the underground mine elements of the project, under 30 CFR 1-199. 30 CFR 46-49 provides specific guidelines for training requirements for mine operations. Given the presence of U and Th in the ore, MSHA will likely require a radon exposure and monitoring program for all underground workers (in accordance with 30 CFR 57.5039 -57.5047).

Nebraska has not enacted any state workplace safety rules or regulations; therefore, regulations set by the Occupational Safety and Health Act (OSH Act) will be the predominant regulatory framework for general workplace health and safety for the surface portion of the project. Nebraska does have the Nebraska Occupational Health Surveillance Program, which tracks injuries, illnesses, and hazards to help monitor workplace trends and guide prevention efforts. In addition, the Nebraska Department of Labor (DOL) is responsible for health and safety through enforcement of the Nebraska Boiler Inspection Act. If the project will have any boilers or pressure vessels on site, DOL staff will need to inspect to ensure proper installation and maintenance.

17.5 Reclamation & Closure

As previously mentioned, there are limited state statutes, regulations, or obligatory requirements for reclamation and closure of mine properties in Nebraska. Within other regulatory statutes which apply to the project, however, there are specific provisions which are likely to be applied to the project during permitting and licensing. The following sections provide a summary of key elements that form the basis for the closure cost estimate also provided in this report.

17.5.1 Surface Disturbance

Surface reclamation will predominantly focus on returning lands disturbed by mining and associated operations to a productive post-mine land use. Baseline information has been collected for soils, vegetation, wildlife, and radiological conditions and this will be used as guidelines for reclamation post-closure. Reclamation will also include returning the site to similar topography and slope and will be designed to prevent soil erosion and re-establish natural drainage patterns.

17.5.2 Buildings and Equipment

All surface structures and equipment will be evaluated prior to closure to determine the appropriate end of life scenario, whether this be re-use or disposal. All equipment and structures will be decommissioned, decontaminated to the extent possible as deemed necessary, dismantled, and then either salvaged or disposed of properly. All wells, regardless of use, will be properly abandoned following the appropriate Nebraska Department of Health and Human Services (DHHS) regulations as well as any conditions set during permitting and licensing.

17.5.3 Tailings Disposal Facility

The TSF and salt management cells for the project will be subject to DWEE Title 132 (Integrated Solid Waste Management Regulations) and possibly Title 123 (Design, Operation, and Maintenance of Wastewater Works Regulations), which includes specific requirements for closure and decommissioning. The design of the TSF cells do allow for concurrent reclamation in order to reduce the amount of precipitation contact water that will require active management, and once a cell has

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reached design capacity, it will be closed (Batty et al. 2022). The closure costs provided in this Technical Report Summary assume that only one cell will be active at any given time for which reclamation may be required. TSF construction and material placement will also be approached in such a way to allow the operator to concurrently close portions of each cell as they reach capacity.

As outlined in the previous technical report summary (Batty et al. 2022), at initial closure, a geomembrane liner will be placed over the tailings, which will be surface graded. This liner will have an over-liner drainage system that will discharge to the outer slope of the embankment for each TSF cell. The liner will also be of adequate thickness of cover to facilitate vegetative growth but may require a root barrier to prevent rooting into the tailings. Regulations require that solid waste disposal area operators must maintain post-closure care for at least 30 years. Currently, there are no plans for post-closure solution/drain down management given the nature of the materials in the tailings and the anticipated closure approach. There is the potential for other, additional technologies and/or approaches which may also provide the level of effectiveness as the method proposed here developed prior to actual reclamation of the site, but this presents the current, conservative approach to closure of the TSF cells. The salt management cells will be closed in a similar manner.

17.5.4 Closure Cost Estimate

Closure costs were estimated using current site design information and developed using the Standardized Reclamation Cost Estimator 2.0 (SRCE), available for download at www.nvbond.org, along with a user-defined cost data file (CDF).

Reclamation and closure cost for the Project includes concurrent reclamation of the TSF cells, scheduled prior to closure where appropriate, along with activities that will occur during the three-year closure and 30-year post closure periods. Decontamination of site facilities is included, however, select items may be decommissioned and disposed of on-site in the last open TSF rather than decontaminated and disposed of offsite. A cost of US$106 million has been estimated to cover reclamation activities and accounts for the earthwork associated with reclaiming surface disturbance areas, decontamination of facilities, demolition of surface facilities and features, closure of underground mine workings, re-establishing native vegetation, and closure/post-closure monitoring and maintenance activities.

17.6 International Standards & Guidelines

The United States is a Designated Country under the Equator Principles. Designated Countries are those countries deemed to have robust environmental and social governance, legislation systems, and institutional capacity designed to protect their people and the natural environment (Equator Principles Association, 2020).

The current version of the Equator Principles (EP4) was launched in July 2020 and came into effect on October 1, 2020. This version of the Equator Principles requires the same assessment and management structures for projects whether they are in Designated or Non-Designated Countries. As identified in the previous technical report summary, the project is in compliance with the 2020 EP4 requirements.

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18 Capital and Operating Costs

Capital and operating cost estimates were prepared by Ausenco, Dumas, T Engineering, SRK and Tierra Group/BBA with contributions from NioCorp and were reviewed and adopted by Scott Honan, M.Sc., SME-RM, of NioCorp as the Qualified Person.

18.1 Capital Cost Estimate

18.1.1 Basis of Estimate

The estimate is suitable for the preparation of the 2026 Elk Creek Study and is reported in Q2 2026 U.S. constant dollars. The capital cost estimate reflects a detailed bottom-up approach that is based on key engineering deliverables that define the Project scope. This scope was described and quantified within material take-offs (MTOs) in a series of line items for the surface features of the project, and on a unit rate basis for the underground features. Capital costs are divided among the areas of underground mining, processing, infrastructure, water management, tailings management, indirect costs, owner’s costs and contingency. Sustaining capital costs are related to underground mining development, underground mine replacement equipment, process plant maintenance, infrastructure maintenance, tailings management and mine closure.

The maturity of the estimate supports a 10% contingency on all Project elements except for the surface plant. As the surface estimate is at a slightly less mature stage of design, the applied contingency for surface plant costs is 20%.

18.1.1.1 Mining, Process, and Infrastructure Capital Cost

The mining capital costs were developed, including a combination of vendor and contractor quotations, first principles buildup, allowances, and historical database costs. The estimates include Labor, materials, fixed equipment purchase and operation cost, rental equipment, supplies and freight. Energy is excluded, as it will be provided by the site microgrid and is carried in Owner’s costs. The costs developed include direct and indirect costs and included separate contingencies on both.

18.1.1.2 Tailings and Tailings Water Management Capital Costs

The capital cost for tailings facility construction was based on engineering and contractor estimates for earthworks and liner installation. Tierra Group/BBA’s estimates were developed from recent and relevant costs on other projects or developed from first principles.

18.2 Capital Cost Summary

Table 18‑1 shows the breakout in of initial and sustaining capital estimates, which total US$ 4,019 million over the project life. An overall 14 % contingency factor has been applied to the initial capital estimate, as described above. The pre-production period is defined as the first 35 months of construction, after which the mine and plant reach commercial production. The initial capital estimate is US$ 1,849 million which reflects the capitalized portion of the construction period.

Table 18‑1: Capital Costs Summary (US$ 000’s)

Description

Initial

Sustaining

Total

Capitalized Preproduction Expenses

$2,506

 

$2,506

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Description

Initial

Sustaining

Total

Site Preparation and Infrastructure

$24,722

$42,032

$66,754

Processing Plant

$870,468

$309,322

$1,179,790

Water Management & Treatment

$13,000

 

$13,000

Mining Infrastructure

$144,938

$382,347

$527,285

Tailings Management

$56,874

$168,930

$225,804

Site Wide Indirects

$3,894

 

$3,894

Processing Indirects

$33,620

 

$33,620

Mining Indirects

$169,167

$999,917

$1,169,084

Owner's Costs Indirects

$296,437

$2,522

$298,959

Closure and Reclamation

$0

$95,930

$95,930

Contingency

$233,409

$169,168

$402,577

Total Capital Costs

$1,849,036

$2,170,168

$4,019,204

Source: NioCorp 2026

18.2.1 Capitalized Pre-production Costs

Pre-production costs are defined as production operating expenses that are incurred in the pre-production period before the declaration of Commercial Production phase. For this study, costs were categorized as capital for taxation purposes. The mine and plant are expected to quickly ramp to full production, so only a very small proportion of mine development costs fall into this category, totalling US$2.506 million.

18.2.2 Mining Capital Costs

Mining capital costs primarily comprise the following areas: decline development, lateral mine development, and stationary/fixed mine infrastructure. It has been assumed that a mining contractor would be operating at the site from the beginning of the Project to the end of mine life. In addition, is assumed that the mine portal and box cut which commenced construction in February 2026 is complete for the purposes of this estimate. The mine contractor would be responsible for decline development, developing the underground drifts including the internal ramp, footwall and hanging wall access drifts, other underground mine infrastructure, the ventilation system and full production activities. The contractor would also develop all internal vertical development (ventilation raises, ore and waste passes).

The direct mining capital cost contribution is summarized in Table 18‑2. The indirect mining cost is summarized in Table 18‑3.

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Table 18‑2: Mine Direct Initial Capital Cost Breakdown

Item

US$000s

Permanent Mine Plant Infrastructure

$20,867

Site Preparation & Infrastructure

$3,854

Vertical Development

$1,941

Underground Development

$105,995

Underground Other

$37,002

Subtotal

$169,660

Contingency (10%)

$16,966

Total

$186,626

Source: Dumas 2026

 

Table 18‑3: Mine Indirect Capital Cost Breakdown

Item

US$000s

Contractor Indirects

$125,378

Owner Indirects

$43,788

Subtotal Mining

$169,166

Contingency (10%)

$16,916

Total Mining Indirect

$186,083

Source: Dumas 2026

18.2.3 Processing Plant Capital Costs

The surface processing plant capital summarized in Table 21-1 is further broken down in Table 18‑4.

Table 18‑4: Process Plant Costs Summary

Item

US$000s

Process Plant

$649,437

Process Plant Additional Areas

$35,665

Process Plant Services & Facilities

$95,512

On-site Infrastructure

$89,854

Total

$870,468

Source: Ausenco 2026

 

The table above includes the surface crusher, mineral processing plant, hydromet plant, pyromet plant, water treatment plant and supporting infrastructure.

 

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18.2.3.1 Processing Indirects

The processing indirect capital cost summarized in Table 18‑1 is further broken down in Table 18‑5.

Table 18‑5: Processing Indirects Cost Summary

Item

US$000s

Field Indirects

$23,028

Project Delivery

$139,275

Commissioning and Operations Readiness

$1,223

Vendor Representatives

$1,223

Spares

$3,620

First Fills

$4,525

Contingency

$38,331

Total

$211,226

Source: Ausenco 2026

18.2.3.2 Process Commissioning

The mine and plant are expected to ramp up quickly, and the plant is expected to go through 3 months of initial commissioning during which time the costs are primarily labor, followed by 2 months of commissioning with ore and one month of commissioning with ore when saleable product is expected to be produced. Total direct costs during the commissioning period are US$51,437 million.

18.2.4 Tailings, Stockpile, Salt Management and Paste Tailings Costs

During the initial capital build period, the initial tailings impoundment (TSF 1), the carbonatite stockpile and the salt management cell will be constructed. Costs for these features were estimated by Tierra Group/BBA and T Engineering based on equipment quotations and local contractor quotes. The cost for constructing these facilities is presented in Table 18‑6.

Table 18‑6: Pre-production Facilities

Item

US$000s

Earthworks

$21,985

Piping

$261

Geosynthetics (Supply and Installation)

$6,397

Instrumentation

$248

Water Management Channel

$15

Water Management Structures

$84

CQA Services

$1,944

Paste Backfill System

$24,658

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Item

US$000s

Subtotal

$55,593

Contingency

$5,687

Total

$61,281

Source: Tierra Group/BBA, T Engineering 2026

18.2.5 Water Management and Infrastructure

The cost for the on-site zero discharge water treatment plant is included in Table 18‑6. Water supply for the project will be provided by the City of Tecumseh, and the capital for this aspect of the project will be paid partially by NioCorp, with the remainder of the capital paid by the City of Tecumseh and recovered through the rate paid by NioCorp for the delivered water. NioCorp’s share of the capital is $13 million.

18.2.6 Site Preparation and Infrastructure Capital Costs

Site preparation and infrastructure capital costs total US$ 24.722 million. A contingency of 10% is applied to these costs, for a total of US$27.194 million. Theses costs include temporary surface infrastructure to support mine development, permanent mine infrastructure, infrastructure related to the Railveyor® and the mine fleet during the construction period.

18.2.7 Owner’s Costs

Table 18‑7 shows the Owner’s cost detail for the project. NioCorp owns the land needed for the initial construction of the project, and the remaining land acquisition costs are carried in sustaining capital late in the mine life to support land needed for TSF 5 and TSF 6.

 

Table 18‑7: Owner’s Costs

Item

USD$000s

Permitting, Environmental, & Social Resp.

$523

Total Land Acquisition

$16,648

Construction Power

$16,284

Temporary Gas Line

$4,905

Gas Line

$62,000

Compressors/ LNG Gas Back Up Supply

$1,736

Grouting

$48,945

Operations Readiness

$2,522

Construction Umbrella Insurance

$3,600

EPCM Site-Wide Premium

$139,275

Subtotal Owners Costs

$296,437

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Contingency

$39,268

Total Owners Costs

$335,705

Source: NioCorp 2026

18.2.8 Closure and Reclamation

Closure Cost Basis

The closure cost estimate for the Project was developed using the Standardized Reclamation Cost Estimator (SRCE) (available at www.nvbond.org) and a user-defined cost data file (CDF). The inputs to the CDF were obtained from the following sources:

•
Equipment costs have been obtained from Gana Trucking, a local Nebraska contractor. These include all-in operator rates, fuel consumption, consumables, and preventive maintenance.
•
The operator rates are included in the equipment hire costs. The Labor rates are input separately for non-operator rates only.
•
Material costs have been obtained from current quotes, where available.

Plant and Mine Facilities

Facilities and equipment associated with the underground mine and processing plant will be reclaimed as follows:

•
Plant site buildings will be decontaminated, the buildings will be demolished, and the debris hauled off-site.
•
Ponds no longer in use will have sediment and liners removed and hauled to the underground mine for disposal.
•
Residual wastes (solid and/or hazardous), will be hauled to appropriate off-site disposal facilities or to the tailings impoundments.
•
Groundwater wells will be no longer required at the end of operations and will be plugged and abandoned.
•
Underground access will be plugged to prevent public access post-closure.
•
On-site water pipelines will be removed.
•
General disturbances will be covered with soil and vegetated.
•
Tailings impoundments will be regraded, capped and vegetated. Reclamation will be carried out concurrently as each impoundment reaches the end of its operating life.

Post-Closure Monitoring

Monitoring is assumed to continue for 30 years after the end of operations and includes baseline and radiochemical profiles. Monitoring around the tailings and salt management cells will be conducted at three points. Long-term management costs include fence maintenance and repairs to covers and vegetated areas.

The total closure and reclamation cost is US$106 million, including contingency.

18.2.9 Sustaining Capital Costs

The sustaining capital for the mine includes lateral and vertical waste development and mine fixed equipment. The sustaining capital captures all costs related to supporting mining activities and includes fixed equipment purchase prices over the life of mine. The sustaining capital for the surface processing plant is a factored estimate based on the initial capital cost of the surface plant. Sustaining

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capital also includes the construction of tailings impoundments TSF-2 through TSF-6 over the life of the project. These costs are detailed in Table 18‑1.

18.2.10 Contingency

The maturity of the estimate supports a 10% contingency on all project elements except for the surface plant. As the surface estimate is at a slightly less mature stage of design, the applied contingency for surface plant costs is 20%. The total direct cost contingency is US$171.383 million, the indirect cost contingency is US$ 62.259 million and the sustaining capital contingency is US$169.168 million.

18.3 Operating Costs

18.3.1 Basis of Estimate (BoE)

Operating cost estimates were developed to show annual costs for production. All unit costs are expressed as US $/short ton ($/ton) of ore feed to the hydrometallurgical plant and are based on Q2 2026 US$. This report includes the final products of Ferroniobium (FeNb), Scandium Oxide (Sc2O3), the rare earth products Neodymium/Praesodymium (NdPr), Dysprosium Oxide (Dy2O32) and Terbium Oxide (Tb2O3).

Operating costs are primarily divided between the underground mining, and the surface Operating costs are primarily divided between the underground mining and the surface facilities. The costing data for the surface facilities is consistent with an industrial chemical processing facility and categorizes costs by labor, reagent consumption, energy usage (fuel, electricity, natural gas), water consumption, other consumables, ongoing maintenance and repair costs, costs associated with quality assurance at each step (ie laboratory testing and quality control), and overhead costs associated with both managing the surface facilities and providing continued technical support to the facility. The costing data for mining is similarly derived, with the added costs associated with mining-specific activities.

All costing is derived from best estimates as applicable to the level of this report. Costs for reagents are derived from both industry averages and vendor quotes. This provides an estimate that is both directly relevant to the facility location and available suppliers while incorporating the larger market analysis that would mitigate against fluctuations and cost spikes. Natural gas costing is the best estimate for the delivered cost of the utility at the time of the report and incorporating the impact of both the cost of gas itself and the operation the natural gas pipeline.

18.3.1.1 Mining Operating Costs BoE

Mining operating costs for the Elk Creek Project have been developed based on a combination of first principles estimating, benchmarking, and input from equipment vendors, mining contractors, and industry sources.

The underground mining operation is planned to be executed under a hybrid owner operator model, whereby owner personnel provide management, technical oversight, and key support functions, while mining contractors perform the majority of underground development and production activities. Operating cost assumptions reflect this execution strategy.

Operating costs were developed using:

•
Production and development quantities derived from the mine plan;

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•
Equipment fleet selection and utilization assumptions described in Section 16.9.17;
•
Labor requirements based on the planned workforce structure;
•
Productivity rates established from first principles calculations and benchmarked against comparable operations;
•
Unit costs for consumables, materials, and services based on vendor quotations and industry data, including freight where applicable.

Maintenance Labor and materials for mobile and fixed equipment, as well as supervision, technical services, and administrative functions, are included in the mining operating cost estimate consistent with the workforce assumptions presented in Section 13.9.16.

Backfill operating costs are included in the estimate consistent with the mine production schedule and backfill strategy. Cost assumptions reflect the integration of backfill within the overall mining sequence; however, detailed backfill design and mix parameters are defined separately as described in Section 13.6.4.

Operating costs vary annually in accordance with development requirements, production rates, and haulage distances as defined in the mine schedule. Haulage profiles and travel distances have been explicitly considered in estimating equipment productivity, fuel consumption, and maintenance requirements.

Scope boundaries between underground mining, backfill infrastructure, and surface facilities have been defined to ensure consistency with the overall Project cost estimate. A contingency allowance has been applied to mining operating costs consistent with the level of engineering definition at this study stage.

18.3.1.2 Process Plant Operating Costs BoE

The operation of the processing facilities is directly related to mineral processing and production will be carried out by the mine owner. The annual process operating costs were divided into the primary cost categories referenced above, then aggregated by process area. These include mineral processing, hydrometallurgy, pyrometallurgy, water treatment and the paste plant.

The primary methodology was to use a throughput derived from the most recent mass and energy balance. Both the details for the mass and energy balance and the cost per unit basis are provided for the individual sections of the report. The mass and energy consumption for a year of operation were then multiplied by the unit cost rates to determine annual operating cost. Additional costs associated with labor, maintenance and repair activities and quality assurance activities (such as laboratory testing and quality control) were estimated for one year of operation and aggregated with the total.

Packaging costs are considered separately and represent an overall minor contribution to the whole.

18.3.1.3 Tailings Management Costs

The tailings from the process plant will be sent either to the underground mine as structural backfill or to the Tailings Surface Facilities (TSF’s). The paste will be in a pumpable form and the primary method of transportation will be through a piping arrangement that will be contingent on the current active TSF and the volume sent to the active cell. There is consideration for hauling tailings material to the TSF’s via surface equipment to account for situations when the tailings material will not be

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sent to the Paste Plant. Additionally, the estimate considers costs associated with hauling water treatment plant residuals to the salt pond. These costs were incorporated into the Infrastructure category in the form of both equipment operation, maintenance, fuel, and labor.

18.3.1.4 General and Administrative (G&A) Costs BoE

The annual general and administrative (G&A) costs were divided into two parts, Infrastructure Costs and Fixed Manufacturing Costs. Infrastructure costs are not dependent on production but are directly associated with production activities. These reflect the requirements to directly support day-to-day operation and include the costs to manage the tailings facilities and maintain the associated equipment. Fixed Manufacturing Costs are, for the most part, independent of production and reflect the indirect costs that will have very little fluctuation with respect to production.

18.3.1.5 Water Supply Operating Costs BoE

The annual costs associated with water supply were obtained from the most recent rate schedule from the City of Tecumseh dated 3/13/2026, which is expected to supply the entirety of the water required for the plant based on the latest estimate of water consumption.

Costs associated with process water treatment and reclamation were obtained via the budgetary proposal from Veolia dated 4/11/2019 and updated with 2026 dollars. The quality and flow of the water to the treatment plant, on which the proposal was based, is not expected to change substantially and as such remains a reasonable estimate for the operational cost associated with the water treatment plant.

18.3.1.6 Closure and Reclamation

The closure cost estimate for the Project was developed using the Standardized Reclamation Cost Estimator (SRCE) (available at www.nvbond.org) and a user-defined cost data file (CDF).

The most recent site layout was used to determine the buildings footprint and estimated demolition material amount to inform both decontamination and waste disposal costs.

The most recent design of the tailings surface facilities from Tierra Group/BBA was used to determine both material and labor costs associated with the closure of the tailings and other surface impoundments (stockpiles, salt cell, stormwater pond, sanitary lagoon).

The most recent design of the mine portal from Dumas/Tiley was used to estimate costs associated with demolition of the Railveyor and filling in and sealing the entrance to the mine.

Equipment rates are based on information from Gana Trucking (including labor) and the annual NDEP cost data file with data provided by Cashman Equipment Company (July 2025). Even though the onsite Elk Creek equipment fleet will be utilized, rental rates for equipment are used in order to generate a complete rate, which includes preventative maintenance, wear items, and tire costs as appropriate.

18.3.2 Operating Cost Summary

Table 18‑8 summarizes the operating costs by area, which equals 268.78 $/ton ore. These unit rates are stated on a LOM basis, where the costs are estimated from the beginning of construction to the end of the mine life. LOM operating costs include the pre-production and first/last years of production.

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Table 18‑8: LOM Operating Cost Unit Rate Summary

Description

LOM $/ton ore

Hydromet

128.01

Mining

71.34

Pyromet

17.69

Water Management

14.44

Site G&A

13.26

Infrastructure

8.60

Paste Plant

7.34

Mineral Processing

7.12

Product Packaging

0.97

Subtotal

268.78

Source: NioCorp 2026

18.3.2.1 Mining Operating Costs

Mining operating costs for the Elk Creek Project over the life of mine (LOM), when considering steady-state production (Years 4 to 42), average US$71.34 per ton mined. Table 18‑9 presents a detailed breakdown of unit costs by mining activity, including both production and supporting services.

The operating cost includes all activities required to sustain underground mining operations, namely:

•
production drilling and blasting,
•
ground support installation and shotcrete application,
•
loading, hauling, crushing, and material handling to surface,
•
ventilation and pumping,
•
underground and surface maintenance,
•
technical services and mine engineering,
•
backfill operations, and
•
mine supervision and general administration (G&A).

General services, infrastructure support, and labor costs are allocated across total ore production during steady-state operations.

While annual costs vary based on production sequencing, mine location, and activity levels, the total mining operating cost averages approximately US$79.2 million per year over the LOM steady-state period.

The unit costs presented are based on a Q1 2026 cost basis.

Years 0 to 3 are classified as pre-production. The final two years (Years 43 and 44) correspond to a planned ramp-down phase, during which production falls below nameplate capacity; accordingly, these years are excluded from the operating cost per ton calculation to maintain consistency with steady-state assumptions.

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Table 18‑9: Steady State Mining Operating Unit Cost

Mining Activity Category

Total Cost ($000) over 39-Year Steady-State Production

Cost per Short Ton of Ore (US$)

Production Drill & Blast

730,420

16.87

Development

256,015

5.91

Material Handling (LHD, Railveyor)

242,001

5.59

Energy – Mining

357,354

8.26

Underground Services and G&A

1,502,313

34.71

Total Operating Cost

3,088,102

71.34

 

 

 

 

 

 

Sustaining production rate

1,109,900

Short Tons/year

Average sustaining operating cost

$79,182,110

US$/year

Source: NioCorp 2026

18.3.2.2 Process Plants Operating Costs

The annual LOM operating costs for the Process and Infrastructure portion of the facility (which will encompass the bulk of the surface facilities) is summarized below in Table 18‑10 and is estimated at 197.44 $/ton of ore process. This estimate includes six (6) primary areas of the of the surface plant: Mineral Processing, Hydrometallurgy, Pyrometallurgy, Water Management and Treatment, Paste Plant, and Infrastructure. Product packaging is incorporated into this cost as well.

The estimate for each process area was developed by determining the required quantities of workforce (encompassing hourly, supervisory, technical, and support functions), energy (electrical, natural gas, and vehicle fuels), reagent consumption (based on the most recent mass balance for the facility), maintenance and repair costs (determined as a portion of the total operating cost), quality assurance costs (determined as a portion of the operating labor, as the basis is consistent with general guidelines costs associated with quality assurance activities), and other general costs required for one year of operation. When applicable, the estimate basis was multiplied by the unit cost to obtain the annual operating cost.

The operating costs for this project were based on processing 3,040 short tons per day of ore (3040 stpd) or 1,109,900 short tons per year.

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Table 18‑10: ROM Processing Operating Cost Unit Rate Breakdown

img170397038_166.gif

Source: NioCorp 2026

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Operating costs for the surface facilities were systematically reviewed to ensure the requisite accuracy for this level of estimate and reflect the most up to date information of the mineral and metallurgical processing facilities.

The two largest items in the operating cost are the hydromet reagent consumption and hydromet natural gas consumption. Both the mass and energy balance for the hydromet facility were reviewed and updated to ensure the most accurate information utilized for the estimate.

Figure 18‑1 illustrates the relative proportion of the reagent consumption cost in the hydromet facility. Two (2) reagents represent about 70% of the reagent cost for the facility – Sulfuric Acid, and Liquid Chlorine. Acids are heavily utilized for leaching operations and chlorine is used to generate one of the primary products from the facility, titanium tetrachloride (TiCl4).

Reagent cost data was derived from both industry averages and vendor quotes. Vendor quotes were utilized to ensure costing data specific to the region and incorporated the delivered cost of the materials. Industry averages were also utilized to mitigate against pricing swings and the variability inherent in quotes from multiple vendors. The costing formula used a weighted average between the two.

img170397038_167.jpg

Source: NioCorp 2026

Figure 18‑1: Reagent Consumption Percentages for the Hydrometallurgical facility

Natural gas consumption for the hydrometallurgical facility (approximately 76.8 Megatherms/yr) is heavily influenced by the chloride recovery circuit. The chloride recovery circuit is essential for recycling the hydrochloric acid in the process vs. consuming the entirety of the hydrochloric acid. Of the 6.66 MM lbs/day of 32% hydrochloric acid used in the process, 6.52 MM lbs/day is recovered and recycled back to the process (the balance, ~2.1%, is what is delivered to site). This represents a

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substantial environmental benefit from the current process and would not only be costly but would generate significantly more waste if the entirety of this acid was consumed.

Figure 18‑2 illustrates the relative breakdown of the natural gas between the different unit operations.

img170397038_168.jpg

Source: NioCorp 2026

Figure 18‑2: Natural Gas Consumption per Process area in Hydrometallurgy

18.3.2.3 Tailings and Salt Management Operating Costs

All costs associated with tailings and the management of the surface ponds (salt cell, stormwater pond, sanitary lagoon) are incorporated into the infrastructure section shown above.

18.3.2.4 Site G&A Operating Costs

Site general and administrative costs were divided between salary labor and non-labor overhead costs. These represent the fixed costs of operation that are invariant with respect to production and encompass multiple support activities (site management, technical services, health, safety, and environmental functions, human resources, supply chain management, information technology (IT), finance, and general support)

Salary workforce costs were determined by estimating the requisite organizational roles that would provide technical and supervisory support for the both the surface facilities and the hourly workforce. These are representative of similar industrial chemical processing facilities. Annual compensation costs for these roles were estimated from the Bureau of Labor and Statistics Labor Codes and scaled to 2026 dollars. The estimated salary workforce is shown below in Table 18‑11.

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Table 18‑11: Support Roles for Facility Operations

Category

Job Description

Positions

US Labor Code

2026 Salary

Bonus

Cumulative Compensation

Management

Plant Manager

1

420700

$185,300

$203,830

$185,300

HES Manager

1

420700

$118,931

$130,824

$118,931

HR Manager

1

446267

$143,115

$157,427

$143,115

Controller

1

413395

$160,375

$176,413

$160,375

IT Manager

1

409743

$151,978

$167,176

$151,978

Purchasing/Logistics Manager

1

424353

$133,384

$146,722

$133,384

Engineering Manager

1

2608503

$149,521

$164,473

$149,521

Reliability Manager

1

2608503

$149,521

$164,473

$149,521

Operations Manager

1

420700

$118,931

$130,824

$118,931

Maint Superintendent

1

420700

$118,931

$130,824

$118,931

Mine Superintendent

0

420700

$118,931

$130,824

-

Chief Geologist

1

420700

$118,931

$130,824

$118,931

QA/Lab Manager

1

420700

$118,931

$130,824

$118,931

Engineering

I&E Engineer

3

17-2071

$107,908

$118,699

$323,724

Controls Engineer

2

17-2071

$107,908

$118,699

$215,816

Mechanical (Fixed/Rotating) Engineer

4

17-2141

$94,977

$104,475

$379,908

Environmental Engineer

1

17-2081

$100,550

$110,605

$100,550

Mining Engineer

0

17-2141

$94,977

$104,475

-

Chemical Engineer

3

17-2041

$121,762

$133,938

$365,286

Geologist

1

19-2042

$90,779

$99,857

$90,779

Lab Supervisor

1

19-2031

$81,700

$89,870

$81,700

Supervision

Mine Planner

0

51-1011

$72,780

$80,058

-

Mine Supervisor

0

51-1011

$80,089

$88,098

-

Maint Supervisor

8

51-1011

$65,835

$72,418

$526,677

Operations Supervisor

5

51-1011

$80,089

$88,098

$400,445

Safety/Mine Rescue/ Training Supervisor

4

51-1011

$80,089

$88,098

$320,356

Safety Supervisor

2

51-1011

$80,089

$88,098

$160,178

Support

Trainer

2

51-1011

$72,780

$80,058

$145,560

Safety

4

43-5071

$63,446

$69,791

$253,784

Maint Planner - Mine

0

51-1011

$72,780

$80,058

-

Maint Planner - Surface

3

51-1011

$72,780

$80,058

$218,340

Shipping Receiving Warehouse Tech

4

43-5071

$45,671

$50,238

$182,684

10 Lab Techs, in 4 or 5 work stations

8

19-4031

$62,713

$68,984

$501,702

Geology Technician

1

17-3022

$71,876

$79,064

$71,876

Tech Writer

2

17-3023

$57,727

$63,500

$115,454

Admin Assistant

2

43-6014

$47,828

$52,610

$95,655

Clerk

2

43-3099

$44,814

$49,295

$89,628

HR Recruiters/Generalists

5

13-1071

$66,855

$73,541

$334,275

IT technician

2

15-1231

$72,401

$79,641

$144,802

Purchasing Agent

2

13-1020

$77,350

$85,084

$154,699

Customer Service Rep

2

41-4012

$80,877

$88,965

$161,754

Drafter/Document Control

2

17-3013

$61,621

$67,783

$123,242

SUBTOTAL Salary

87

$7,226,723

Source: NioCorp 2026

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Non-labor overhead costs were estimated as a portion of both the manpower requirements of the facility and the capital cost of the facility itself. The estimate was derived from best practices consistent with the level of design in the current study for chemical process facilities (Turton, 2012).

18.3.3 Mine Operating Costs

Mining operating costs for the Elk Creek Project over the life of mine (LOM), when considering steady-state production (Years 4 to 42), average US$71.34 per ton mined.

Table 18‑12 presents a detailed breakdown of unit costs by mining activity, including both production and supporting services. The operating cost includes all activities required to sustain underground mining operations, namely:

•
Production drilling and blasting,
•
Ground support installation and shotcrete application,
•
Loading, hauling, crushing, and material handling to surface,
•
Ventilation and pumping,
•
Underground and surface maintenance,
•
Technical services and mine engineering,
•
Backfill operations, and
•
Mine supervision and general administration (G&A).

General services, infrastructure support, and labor costs are allocated across total ore production during steady-state operations.

While annual costs vary based on production sequencing, mine location, and activity levels, the total mining operating cost averages approximately US$79.2 million per year over the LOM steady-state period.

The unit costs presented are based on a Q1 2026 cost basis.

Years 0 to 3 are classified as pre-production. The final two years (Years 43 and 44) correspond to a planned ramp-down phase, during which production falls below nameplate capacity; accordingly, these years are excluded from the operating cost per ton calculation to maintain consistency with steady-state assumptions.

Table 18‑12: Steady State Mining Operating Unit Cost

Mining Activity Category

Total Cost ($x1000) over 39 yr Steady-State Production

Cost per Short Ton Ore US$

Production Drill & Blast

730,420

16.87

Development

256,015

5.91

Material Handling (LHD, Railveyor)

242,001

5.59

Energy mining

357,354

8.26

Underground Services and G&A

1,502,313

34.71

Total Operating Cost

3,088,102

71.34

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Sustaining production rate

1,109,900

Short Tons/year

Average sustaining Operation cost $/year

$ 79,182,110

 $/year

Source: NioCorp 2026

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19 Economic Analysis

19.1 Cautionary Statement

The results of the economic analysis represent forward-looking information that is subject to a number of known and unknown risks, uncertainties and other factors that may cause actual results to differ materially from those presented here. Forward-looking statements in this Report include, but are not limited to, statements with respect to future niobium, scandium, titanium and rare earth prices, the estimation of Mineral Resources and Mineral Reserves, the estimated mine production and niobium, scandium, titanium and rare earths recovered, the estimated capital and operating costs, and the estimated cash flows generated from the planned mine production. Actual results may be affected by:

•
Unexpected variations in the quantity of ore, grade or recovery rates, or presence of deleterious elements that would affect the process plant or waste disposal
•
Unexpected geotechnical and hydrogeological conditions from what was assumed in the mine designs, including water management during construction, mine operations, and post mine closure
•
Differences in the timing and amount of estimated future niobium, scandium and titanium production, costs of future niobium, scandium and titanium production, sustaining capital requirements, future operating costs, requirements for additional capital, unexpected failure of plant, equipment or processes not operating as anticipated.
•
Changes in government regulation of mining operations, environment, and taxes.
•
Unexpected social risks, higher closure costs and unanticipated closure requirements, mineral title disputes or delays to obtaining surface access to the property.
•
The production schedules and financial analysis annualized cash flow table are presented with conceptual years shown. Years shown in these tables are for illustrative purposes only. If additional mining, technical, and engineering studies are conducted, these may alter the Project assumptions as discussed in this Report and may result in changes to the calendar timelines presented and the information and statements contained in this Report. No development approval action has yet been taken by the NioCorp Board as the funds for project execution are still in the process of being raised at the time of writing. While permits are in hand for construction and construction has commenced as of February 2026, operating permits, are required to be granted prior to the commencement of operations

19.2 Methodology Used

The Project has been evaluated using discounted cash flow analysis. Cash inflows consist of annual revenue projections. Cash outflows consist of initial capital expenditures, sustaining capital costs, operating costs, taxes, royalties, and commitments to other stakeholders. These are subtracted from revenues to arrive at the annual cash flow projections. Cash flows are taken to occur at the end of each period. To reflect the time value of money, annual cash flow projections are discounted back to the Project valuation date using the yearly discount rate. The discount rate appropriate to a specific

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project can depend on many factors, including the type of product, the cost of capital to the Project, and the level of Project risks (i.e., market risk, environmental risk, technical risk and political risk) in comparison to the expected return from the equity and money markets. The base case discount rate for the 2026 Elk Creek Study is 8%. The discounted present values of the cash flows are summed to arrive at the Project’s NPV (Net Present Value). In addition to the NPV, the IRR (Internal Rate of Return) and the payback period are also calculated. The IRR is defined as the discount rate that results in an NPV equal to zero. The payback period is calculated as the time required to achieve positive cumulative cash flow for the Project from the start of production.

19.3 Financial Model Parameters and Assumptions

The indicative economic results summarized in this section are based upon work performed by NioCorp in 2026. They have been prepared on both a periodic monthly format and an annual format. The metrics reported in this section are based on the annual cash flow model results. The metrics are on both a pre-tax and after-tax basis; a 100% equity basis with no Project financing inputs; and are in Q1 2027 U.S. constant dollars.

Key criteria used in the analysis are discussed in detail throughout this section. Principal Project assumptions used are shown summarized in Table 19‑1.

Table 19‑1: General Assumptions

Description

Value

Pre-Production Period

35 months

Process Plant Life

40 years

Mine Operating Days per Year

365

Mill Operating Days per Year

365

Discount Rate

EOP @ 8%

Commercial Production Year

Y2M34

Source: NioCorp, 2026

All costs incurred prior to June 2026 are considered sunk with respect to this analysis.

The selected Project discount rate is 8% as directed by NioCorp, and the valuation uses standard end-of-period discounting. A sensitivity analysis of the discount rate is discussed later in this section.

Foreign exchange impacts were deemed negligible as most, if not all costs and revenues are denominated in US dollars.

The major criteria adopted to define when the Project enters into Commercial Production include the following: (1) all major capital expenditures to bring the mine to nameplate capacity have been completed; (2) the process plant, and other facilities have been transferred to the control of the Operations team from the Commissioning team; (3) the plant has reached at least 80% of initial design capacity following an adequate ramp-up period; (4) product recoveries are at or near expected levels; (5) the mine has the ability to sustain ongoing production of ore at the required CoG (Cut-off Grade); and (6) costs are under control or within expectations.

Mineral Resource, Mineral Reserve and Mine Life

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The Mineral Resource discussed in Section 14 was converted to the Mineral Reserve outlined in Section 12. The estimated Mineral Reserve will support a 40-year production life, using the mine plan as provided in Section 13.

Metallurgical Recoveries

The basis for the process recoveries is included in Section 13, and the process design is outlined in Section 14.

Product Prices

The product price basis is discussed in Section 19.

Capital and Operating Costs.

The capital and operating cost estimates are detailed in Section 18.

Closure Costs and Salvage Value.

Reclamation costs were included with the capital cost estimate and are detailed in Chapter 0.

Financing

The economic analysis assumes 100% equity financing and is reported on a 100% project ownership basis.

Inflation

The economic analysis assumes constant prices with no inflationary adjustments.

19.3.1 Physicals

Mining

Table 19‑2 is a summary of the estimated mine production over the 43-year LOM. Ore mined refers to Probable Mineral Reserves.

Table 19‑2: Mining Physicals

Description

Value

Ore Mined (st)

45,929

Target Production Rate (st/d)

3047

Niobium Grade

0.76%

Scandium Grade (ppm)

69.3

TiO2 Grade

2.68

TREO Grade

0.34

Contained Nb (st)

205

Contained Sc (st)

4,585

Contained TiCl4 (st)

2,341,367

Contained TREO (st)

53,309

Source: Amplify 2026, NioCorp 2026

Processing

A summary of the estimated process plant production for the Project is contained in Table 19‑3 for a 40-year operating life at an average capacity of 3047 st/d. Table 22-4 shows more detail of process

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recovery rates for each product in the three plants. Ore processed refers to Probable Mineral Reserves.

Table 19‑3: Processing Physicals

Description

Value

Total Ore Processed (st 000s)

45,929

Recovery, Nb

84.70%

Recovery Sc

94.30%

Recovery Ti

80.50%

Recovery NdPr

93.04%

Recovery Tb

94.40%

Recovery Dy

94.60%

Contained Nb (st)

205,464

Contained Sc2O3 (st)

4,585

Contained TiCl4 (st)

2,341,367

Contained NdPr oxide (st)

25,923

Contained Tb oxide (st)

690

Contained Dy oxide (st)

2,649

Source: NioCorp and Amplify 2026

19.3.2 Revenue

Based on data discussed in Section 19, Table 19‑4 and Table 19‑5 show benchmark product pricing assumptions used in the economic analysis. The following criteria apply to the calculation of revenue:

•
Niobium measured in the resource and reserve as Nb2O5 but is produced as commercial ferroniobium, which is a mixture containing 65% Nb and 35% Fe. Ferroniobium pricing is based solely on its Nb content.
•
Ti is measured as TiO2 in the resource and reserve and is produced as TiCl4.
•
Scandium is measured as Sc in the resource and reserve and is produced and sold as the compound Sc2O3.
•
Rare earths are measured as oxides and are produced as oxides.

Table 19‑4: Pricing Assumptions

Description

Short Tons Saleable Product

LOM Benchmark Price US$/lb product

Payable Nb

202,407

 $ 23.59

Payable Sc2O3

4,518

 See Table 19-5

Payable TiCl4

2,305,195

 $ 0.84

Payable TREO

44,354

 See Table 19-6

Source: Amplify, OnG, Argus, and NioCorp 2026

 

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Table 19‑5: Scandium Trioxide Pricing Assumptions

Year

US$/lb

Y1

$1,474

Y2

$1,474

Y3

$1,474

Y4

$1,474

Y5

$1,474

Y6

$1,474

Y7

$1,315

Y8

$1,474

Y9

$1,474

Y10

$1,474

Y11

$1,474

Y12

$1,474

Y13 and on

$1,588

Source: OnG 2025 and 2026; NioCorp 2026

 

Table 19‑6: TREO Pricing Assumptions

Description

US$/lb

NdPr Oxide

$62.78

Tb2O3

$2,048.21

Dy2O3

$593.30

SEG Carbonate

$4.07

Heavies Carbonate

$2.29

Source: NioCorp, Argus and OnG 2026

 

The following is a breakdown of netback pricing assumptions for each product:

Niobium

•
Ferroniobium (65% Nb) product (FeNb product) with constant price of US$ 23.59/lb Nb.
•
All settlement Nb prices have a 3.75% discount to the netback price of benchmark price minus Buyers Logistics Costs (BLC) except with customers buying on spot pricing.
•
It is assumed that all FeNb product purchases have a 10 Net Days Outstanding (NDO) A/R term. At the time of this report, the Project had two committed offtake customers signed up for 10- year terms with all remaining annual FeNb production sold on a spot basis:
o
Buyer #1 - US-based metals trader with mill operations located in the southern half of the US:
▪
10-year commitment to purchase 25% of annual offtake production to a maximum of 2067 st/y.
o
Buyer #2 - European-based manufacturer with global mill operations:
▪
10-year commitment to purchase 50% of annual offtake production to a maximum of 4134 st/y.

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o
Spot Buyer - It is assumed that all annual FeNb production not sold under an offtake agreement is sold at spot (or benchmark) pricing of constant US$ 23.59/lb Nb on an ex-mine gate basis with a 10-day NDO A/R term.

Titanium Tetrachloride

•
Offtake is subject to a Memorandum of Understanding with Traxys.
•
It is assumed that all annual TiCl4 production is sold at spot (or benchmark) pricing of constant US$ 0.84/lb on an ex-mine gate basis with a 10-day NDO A/R term.

Scandium Trioxide

•
Offtake is subject to a Memorandum of Understanding with Traxys.
•
Scandium Trioxide (Sc2O3) product with an average realized LOM price of US$ 1,562.90/lb.
•
It is assumed that all Sc2O3 product purchases have a 10-day NDO A/R term.

TREOs

•
Offtake is subject to a Memorandum of Understanding with Traxys.
•
It is assumed that all annual NdPr production is sold at spot (or benchmark) pricing of constant US$ 62.78/lb on an ex-mine gate basis with a 10-day NDO A/R term.
•
It is assumed that all annual Tb2O3 production is sold at spot (or benchmark) pricing of constant US$ 2,048.21/lb on an ex-mine gate basis with a 10-day NDO A/R term.
•
It is assumed that all annual Dy2O3 production is sold at spot (or benchmark) pricing of constant US$ 593.30/lb on an ex-mine gate basis with a 10-day NDO A/R term.
•
It is assumed that all annual SEG production is sold at spot (or benchmark) pricing of constant US$ 4.07/lb on an ex-mine gate basis with a 10-day NDO A/R term.
•
It is assumed that all annual Heavies Carbonate production is sold at spot (or benchmark) pricing of constant US$ 2.29/lb on an ex-mine gate basis with a 10-day NDO A/R term.

19.3.3 Operating

Operating cost metrics in the technical, economic model are reported on a LOM basis meaning that all of these unit rates are stated on a LOM basis where the costs are estimated from the beginning of construction to the end of mine life. LOM operating costs include the pre-production and first/last years of production.

The total LOM operating cost unit rate of US$ 265.94/ton processed is summarized in Table 19‑7.

 

Table 19‑7: Operating Cost Summary

Description

LoM US$/short ton ore

Mining Cost

70.95

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Process Cost

151.96

Water Mgmt

13.72

Tailings

8.08

Other Infrastructure

9.52

Site G&A

0.32

Subtotal

254.56

Royalties/Bond Premium

11.38

Total LOM Operating Cost

265.94

Source: NioCorp, 2026

19.3.4 Capital Costs

Total capital costs totaling US$ 3,923 billion, not including US$ 96 million of final closure/reclamation costs are summarized in Table 19‑8.

Table 19‑8: Capital Cost Summary (US$ 000’s)

Description

Initial

Sustaining

Total

Capitalized Preproduction Expenses

3

3

Site Preparation and Infrastructure

25

42

67

Processing Plant

870

309

1,180

Water Management & Treatment

13

13

Mining Infrastructure

145

382

527

Tailings Management

57

169

226

Site Wide Indirects

4

4

Processing Indirects

34

34

Mining Indirects

169

1,000

1,169

Owner's Costs Indirects

296

3

299

Contingency

233

169

403

Total Capital Costs

$1,849

$2,074

$3,923

Source: NioCorp 2026, Dumas, Ausenco, Tierra Group/BBA, SRK, and T Engineering 2026

 

Further details of the initial capital estimate are presented in Table 19‑9.

Table 19‑9: Initial Capital Costs Summary (US$ 000’s)

Description

Initial

% of Total

Capitalized Pre-Production Costs

$3

0%

Subtotal Preproduction Costs

$3

0%

Site Preparation and Infrastructure

$25

1%

Processing Plant

$870

47%

Water Management & Treatment

$13

1%

Mining Infrastructure

$145

8%

Tailings Management

$57

3%

Subtotal Direct Costs

$1,110

60%

Site Wide

$4

0%

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Description

Initial

% of Total

Processing

$34

2%

Mining

$169

9%

Owner's Costs

$296

16%

Subtotal Indirect Costs

$503

27%

Project Total Before Contingency

$1,616

86%

Contingency

$233

14%

Project Total

$1,849

100%

Source: NioCorp 2026, Dumas, Ausenco, Tierra Group/BBA, SRK, and T Engineering 2026.

19.4 Cashflow Forecasts & Annual Production Forecasts

Cashflow Forecasts are summarized on a LOM basis in this section.

The technical, economic model metrics are prepared on an annual pre-tax and after-tax basis, the results of which are summarized in Table 19‑10. Based on current assumptions and design listed in this report, the Project returns a pre-tax NPV 8% of US$ 4,111 million and an IRR of 24.0 % along with an after-tax NPV 8% of US$ 3,441 million and IRR of 22.8%.

Table 19‑10: Indicative Economic Results (US$ 000’s)

Pre-Tax NPV8% ($M)

$4,111

Pre-Tax IRR

24.0%

After-Tax NPV8% ($M)

$3,441

After-Tax IRR

22.8%

After-Tax Payback Period (years)

2.93

Total Upfront CAPEX ($M)

$1,849

Mine Life (years)

40

LoM Gross Revenue ($M)

$37,435

Niobium

$9,781

Scandium

$14,331

Titanium

$3,946

Rare Earths

$9,378

NdPr Oxide

$3,254

Dy Oxide

$3,137

Tb Oxide

$2,827

SEG Carbonate

$113

Heavy Rare Earth Carbonate

$46

Average Annual EBITDA over Full Production Years ($M)

$608

Average EBITDA Margin (EBITDA as % of total revenue)

67%

Average Annual Operating Cash Flow ($M)

$519

Revenue Per Ton, (US$/ton)

$815

Average Annual Operating Cost (OPEX) (US$/ton)

($255)

Effective Tax Rate

14.3%

Development Timeline (months)

35

Source: NioCorp 2026

 

 

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19.5 Taxes, Royalties & Other Interests

Due to the Project’s location in a rural area of Nebraska with little industrial activity, taxes and depreciation for the Project were modelled based upon input from NioCorp, as well as a review of various guidelines such as the Nebraska Advantage Act, Nebraska tax credit and Federal tax rates. As such, a detailed tax methodology was developed for the technical, economic model to model the impacts of various government tax incentives.

The assumptions used in the methodology are described in this section and assumptions are as follows:

•
Taxes calculation is on an annual basis.
•
Corporate Income Tax (CIT) rates are 21% for Federal and 3.99% for Nebraska.
•
County property tax based on the end of year value of Project, net of capital improvements and depreciation taken, multiplied by 0.0136. A 10-year tax abatement has also been established based on the Company’s successful application for tax benefits under the Nebraska Advantage Act.
•
Net Operating Losses (NOL) is carried forward indefinitely and can be used up to 100% of annual positive taxable income per period.
•
Federal Depletion allowance is calculated using the co-product percentage depletion method as it was determined that the cost depletion method would be too small compared to the former method. The percentage of depletion rates applied against Gross Income from Mining (subject to 50% of Net Income from Mining limit) are:
o
Nb – 22%
o
TiO2 – 22%
o
Sc2O3 – 14%
o
TREO – 14%
•
Tax Depreciation allowance is calculated each year by the following methods:
o
Mining Development/Capitalized Pre-production Costs: 70% of cost expensed in the year incurred and remaining 30% amortized over 5 years.
o
Mine Fleet Equipment: 7 year Modified Accelerated Cost Recovery System (MACRS) depreciation starting in the year when the cost is incurred.
o
Plant: 7-year MACRS depreciation starting in the first year of commercial production.
o
Infrastructure: 10-year MACRS depreciation starting in the first year of commercial production.
•
Tax credits available to the Project include:
o
Nebraska Investment Tax Credit (ITC) is applied against NE state income tax payable from a beginning balance of US$ 144.1 million based on a formula incorporating development capital spent in area to date.

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The calculated effective income tax rate for the Project is 14.3% (CIT Payable/Adjusted EBITDA).

The Project is subject to a private third party NSR royalty of 2%. For the purposes of this economic analysis, this royalty is better defined as a “Net Proceeds” royalty as annual operating costs are deducted along with freight/insurance costs.

There is a US$ 9.63 million reclamation bond premium payable on the Project to be paid quarterly in a five-year period from 2025 through 2029, at which point the Project will be eligible based on its financial statements to provide other means of financial assurance to the State of Nebraska.

19.6 Sensitivity Analysis

The sensitivity of NPV and IRR to a range of project metrics is presented in Figure 19‑1 through Figure 19‑3.

 

dsimg170397038_169.gif

Source: NioCorp 2026

Figure 19‑1: Pre-Tax NPV Sensitivity Analysis

 

 

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img170397038_170.gif

Source: NioCorp 2026

Figure 19‑2: Pre-Tax IRR Sensitivity Analysis

 

img170397038_171.gif

Source: NioCorp 2026

Figure 19‑3: After-Tax NPV Sensitivity Analysis

 

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img170397038_172.gif

Source: NioCorp 2026

Figure 19‑4: After-Tax IRR Sensitivity Analysis

 

The economic model was tested for sensitivity to variances in head grades and recoveries for the major pay metals. Figure 19‑5 through Figure 19‑8 illustrate the results of pre/post tax basis with respect to these variables.

 

img170397038_173.gif

Source: NioCorp 2026

Figure 19‑5: Pre-Tax NPV Sensitivity to Grade and Recovery

 

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img170397038_174.gif

Source: NioCorp 2026

Figure 19‑6: After Tax NPV Sensitivity to Grade and Recovery

 

img170397038_175.gif

Source: NioCorp 2026

Figure 19‑7: Pre-Tax IRR Sensitivity to Grade and Recovery

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img170397038_176.gif

Source: NioCorp 2026

Figure 19‑8: After Tax IRR Sensitivity to Grade and Recovery

 

Discount rate sensitivity is always important in a project valuation, and with respect to this Project, there is a complex process plant flow sheet and market uncertainty to account for. NPV profile charts are presented in Figure 19‑9 and Figure 19‑10, which shows pre- and after-tax NPV results for 100 basis point increments between 0% and 20%.

 

img170397038_177.gif

Source: NioCorp 2026

Figure 19‑9: Before-Tax NPV Profile

 

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img170397038_178.gif

Source: NioCorp 2026

 Figure 19‑10: After-Tax NPV Profile

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20 Adjacent Properties

Apex Critical Metals Corp. (“Apex”) has entered into option agreements on additional properties surrounding the Elk Creek Project properties (Figure 20‑1). Apex commenced a diamond drilling program on these properties in late January 2026, and the program remains ongoing as of the Effective Date of this Report. Exploration is focused on evaluating the potential for rare earth element mineralization associated with the eastern portion of the Elk Creek Carbonatite Complex.

The QPs have not independently verified the adjacent Property where applicable and mineralization or exploration results on adjacent properties are not necessarily indicative of mineralization on the Elk Creek Project.

img170397038_179.jpg

Source: DGC 2026

Figure 20‑1: Adjacent Properties

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21 Other Relevant Data and Information

21.1 Project Implementation Plan

The key project objectives are as follows:

(1)
Deliver the Elk Creek Mine Project on time and on budget.
(2)
Ensure - the project maintains environmental compliance.
(3)
Ensure the safety of all Project stakeholders.
(4)
Ensure compliance with all applicable laws and regulations, at the local, state and federal levels.
(5)
Ensure positive economic impacts for SE Nebraska, including the use of local businesses wherever feasible, the employment of local residents and tax benefits for local governments.
(6)
Maintain a high level of engagement and communication with all stakeholders.
(7)
Ensure the Project meets design objectives including throughput, product quality, and operating budget objectives.

The Project Implementation Plan (PIP) execution is based on the use of two main contractors: one for underground and one for surface. The underground scope will be structured using an incentivized reimbursable model and the surface scope will be structured along EPCM lines. The approach is reflected in the capital cost estimate for the Project.

21.1.1 Project Cost Objectives

Section 18 of this report presents the capital cost of the Project. The cost objective of the Project is to reach 100% of production capacity within the total initial capex of US$ 1,850 million. Numbers are rounded to the nearest thousand.

21.1.2 Project Schedule Objectives

The scheduling objective is to deliver a fully constructed and commissioned facility within 35 months. The mine and surface plant will be constructed in parallel.

The schedule highlights are as follows:

•
The total duration of the project is 35 months from Authorization to Proceed to the end of the ramp-up period.
•
The schedule contemplates that the starting point for mine development is from the completed sockets in the mine portal. The establishment of the mine portal is underway at the time of writing of this report and the sockets are expected to be in place by the end of 2026.
•
An aggressive five-month commissioning and ramp-up period is included in the overall schedule in the last three months of the capital build period. During this time, the surface plant will be commissioned using approximately 148,000 tons of stockpiled ore which is generated during mine development.

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•
The Project timeline is linked to both the mining-related activities and the surface operations in both sequencing and duration. The construction of the main surface plant buildings and supporting infrastructure is not on the critical path.

The critical path activities are the development of the underground mine and the establishment of the first producing stopes.

The Project construction schedule is reflected in the economic model for the Project.

21.1.3 Early Works

Project Execution requires key early work that includes the following:

•
Finalize contracts for the underground and surface scopes
•
Initiate operational environmental permitting, such that permits are in hand for the start of operations at the end of the construction period.
•
Complete the surface grouting program for the mine, and ensure that work does not conflict with underground mine development activities
•
Perform detailed engineering and procurement of long lead time items.
•
Complete contracting and deploy the third party microgrid power plant that will provide construction power
•
Complete contracting tied to the supply of natural gas to the project, for both construction and operational use
•
Complete the construction of the mine portal and the establishment of the decline sockets, which is underway at the time of writing.
•
Initiate work with the City of Tecumseh to supply fresh water to the project site

21.1.4 Project Team

The underground and surface contractors will report to NioCorp as the Project Sponsor. NioCorp will provide the following key functions as part of the Owner’s team: HES, legal, permitting, communications, finance and controls and project oversight. The NioCorp corporate team will remain in Denver, CO with a Project Team located both on the Elk Creek Mine site and in the Company's offices in nearby Tecumseh, NE. The project contractors will provide engineering, procurement, construction and commissioning services.

21.1.5 Project and Document Control

NioCorp will utilize a project controls system for monitoring, reporting, and controlling the Project schedule, the cost, and the scope of work (change management).

•
The NioCorp Project Team will be responsible for establishing project controls procedures and assuring its consistent application throughout the Project timeline.
•
The Project team will also develop a control budget to aid in managing the overall effort and will develop an appropriate Project accounting system.

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•
The accounting system will be used to baseline the Project cost and aid in forecasting cash flow needs. The system will aid in the creation of Earned Value Reporting (EVR) for the Project.
•
The Project team will maintain the Project schedule with the use of scheduling software such as Primavera P6 or equivalent. The schedule will be updated on a regular basis to track Project progress, noting any deviations.
•
Change management will also be a function of the Project controls system and will be used to identify and track changes in the scope of work throughout the course of the Project.
•
The Project controls system will provide Project KPIs (Key Performance Indicators) through dashboards, monthly reports, and management reports. KPIs will be determined by management in conjunction with the contractors to measure Project success.

21.1.6 Engineering

Following the completion of the 2026 Elk Creek Study, detailed design and engineering activities will be undertaken by engineering teams at the surface and underground construction contractors.

21.1.7 Supply Chain and Procurement

The supply chain management responsibilities will reside with the construction Contractors. These duties include procurement, subcontracting, site material management, and development and management of work packages. The contractors will perform procurement work consisting of:

•
Development of the Long Lead Equipment list.
•
Development of site-wide procurement needs and packages.
•
Development of Equipment Procurement Packages.
•
Procurement of goods and services as required.
•
Administration of purchase orders.
•
Expediting of deliveries.
•
Quality Control of Fabrications.
•
Logistics.

The key long lead-time equipment currently identified are as follows:

•
Major building transformers and power distribution centers (PDCs)
•
The High Pressure Grinding Rolls (HPGR)
•
Hydromet CO2 compressors / blowers
•
Hydromet calciners and rotary dryers
•
Pyromet electric arc furnace

21.1.8 Construction Management

The construction contractors will perform construction management functions, including planning, organizing, and resolving issues involving subcontractors. They will be responsible for ensuring their work and the work of any subcontractors is performed according to the Project's safety, quality, schedule, and cost requirements. Additionally, the construction contractors are required to provide

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the facilities and services, including security, to support construction activities. This practice will ensure that quality standards are maintained and will improve the use of shared resources and equipment. The primary construction management functions include planning and coordination, subcontractor management, quality assurance, resolving design engineering issues, quantity measurement, and materials management.

21.1.9 Commissioning, Operational Readiness, and Early Operations

Commissioning

The Owner's team, in conjunction with the construction contractors, will be responsible for commissioning activities. The team will develop a detailed commissioning plan during the course of detailed design that will address the following:

•
Lists of Handover Packages & Commissioning Systems.
•
Transition process.
•
Commissioning Sequence.
•
Alignment of Boundaries between Handover Packages and Construction Work Packages.
•
Commissioning Schedule.
•
Roles and Responsibilities.
•
Scope of Work Alignment.
•
HES Management for Commissioning.
•
Handover Documentation.
•
Vendor Management.
•
Monitoring of Inspection and Testing performed by work Contractors.
•
Commissioning deficiencies management.
•
Acceptance process.
•
Reporting.
•
Management of County of Origin for materials purchased

The team will also partner with other key stakeholders (vendors and suppliers) to complete the commissioning effort to hand over the Project to operating personnel for early operations and ramp up.

Operational Readiness and Ramp-up

Two Operations Readiness Plans will be prepared: the first Plan will be specific to the operation of the mine; the second Plan will be specific to the surface plant.

Training on equipment (both factory-based and on-site) will be provided by vendors. Request for quotations will require all vendors to supply Operation and Maintenance manuals, lists of spare parts for the first year of operation, list of commissioning spare parts, and training manuals. Vendors may

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be requested to perform on-site training based on the complexity of the equipment and/or its controls.

Ramp-up consists of bringing the plant production from First Metal, achieved by commissioning of the plant, up to 100% of commercial capacity. For the purpose of ramp-up, commercial capacity involves the production of the planned product suite at facility nameplate capacity, in salable quality.

NioCorp internal resources will execute the ramp-up for the surface plant. The underground contractor will be responsible for the ramp-up of the mine.

21.2 Risk Assessment

The Project’s 2022 Risk Assessment was reviewed by NioCorp. The process used in the 2022 Risk Assessment was as follows: Each QP was provided with a semi-quantitative risk matrix where the likelihoods and consequences were assigned numbered levels that were multiplied to generate a numerical description of risk ratings. The values that were assigned to the likelihoods and consequences were not related to their actual magnitude, but to the numerical value that was derived for risk (Figure 21‑1). This approach provided for a standardized grouping and generation of indicated risk ratings. Each QP worked independently and reported their findings which were then compiled and summarized.

img170397038_180.jpg

Source: NioCorp, 2022

Figure 21‑1: Likelihood and Consequence Matrix

21.2.1 2022 Risk and Current Status

The major risks identified in 2022 and their current status are outlined below. This Technical Report Summary has been built to address risks identified in 2022 and to generally improve and derisk the mine and surface plant. Each major risk identified in 2022 is followed by a status report indicating the progress that NioCorp has made in addressing the risk.

Mine Operational Risks

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•
Shaft Location - Drilling pilot holes for shaft locations to determine local geological, geotechnical and hydrological characteristics and conditions that would be encountered during shaft sinking.

Status: The shafts have been replaced by ramp access. Geomechancial holes were drilled at each ramp location to characterize local geological, geomechanical and hydrogeologic conditions during the 2025 field program.

•
Resource/Reserve and Mine Design - Significant infill definition drilling is required during construction and operations phases to determine local geological, geotechnical and hydrological characteristics and conditions in conjunction.

Status: An additional 17 diamond drill holes were completed in 2025 with the objective of increasing confidence in the resource and reserve and increasing knowledge of the conditions that will be encountered underground. This program was successful and established measured resources and proven reserves, along with a plan for grouting the orebody.

•
Grade Control - A daily grade control monitoring program is required to maximize the value of ore mined and fed to the surface plant. The grade control process involves the predictive delineation of the tonnes and grade of ore that will be recovered by the mining team. The program will involve incorporating the results from the infill drilling program in conjunction with an underground chip sampling program to define the boundaries of mineable ore blocks and determine the daily/weekly feed grades to the plant.

Status: The daily grade control monitoring program will be deployed.

•
UG Ground Support/Hydrogeology – an ongoing probe hole drill program/grout program needs to be established to support mining activities and not create significant production delays. The need to develop and deploy a high-pressure grout injection system is required to protect the mine from excess inflow to safeguard the project from injury, property damage and loss of life or equipment.

Status: During the 2025 field program, extensive grouting tests were conducted, confirming that grouting is both feasible and effective. A surface grouting program covering both the underground production and underground infrastructure areas has been developed and integrated into the project’s schedule and budget. In addition, a probe hole and dental grouting program has been developed and integrated into the mine development plan.

•
An additional risk was identified subsequent to the 2019 formal risk assessment. In reviewing the 2015-2017 geotechnical drilling campaign, SRK noted both good and poor-quality rock. There is thus a concern about the ramp-up rate given that regions of poor ground conditions might be encountered early in the development schedule. This could result in a risk that shaft sinking could be delayed due to the combination of ground conditions and seepage inflows (even though the ground should be frozen). There is also the risk that the first development rates could be slowed by the need to install more ground support than anticipated without having room for drill jumbos.

Status: A2GC has reviewed prior geomechanical data and mandated extensive additional data collection during the 2025 field program. A2GC has developed an updated geomechanical model

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for the mine and had identified both good ground conditions (75%) and poor ground conditions (25%). A2GC’s recommendations for ground support in both ground condition cases have been integrated into the mine plan contained in this report.

Ventilation

•
Air Requirement – Further detailed review of the ventilation design and specifically the air quantity required, are needed to ensure all aspects of potential pollutants, radon daughters, and environmental conditions, including those relating to heat stress, are adequately addressed.

Status: An updated ventilation model incorporating measurements of the ground temperature gradient has been developed for the mine by Dumas and Jodouin for this report. The ventilation system designed by Jodouin incorporates both heating in the winter and cooling in the summer and considered prospective contaminants in the air stream. As the mine has been designed around an electric fleet, the risk from combustion products has been eliminated.

Hydrometallurgical Process Risks

A summary of the recommended test work is presented below to reduce further the risks associated with the Hydromet process design. It is expected that the work would proceed in parallel with detailed engineering for the project and would take an estimated 4 months to complete. At the time of writing, the Company has contracted with L3 process development to construct a small-scale demonstration plant to complete the recommended test work and to also investigate the potential to recovery rare earths into commercial-grade products. This demonstration plant is scheduled to become operational in 2022.

HCl Leach

•
Optimize leaching of iron (Fe) to correlate with optimum niobium (Nb) precipitation and Fe/Nb ratios– aiming for the highest recovery of Nb while preventing titanium (Ti) co-precipitation. Validate the method used in the aging of the HCl Leach liquor prior to scandium (Sc) Solvent Extraction.

Status: The demonstration plant was operated using a 3- tonne sample of drill core from 2022 through 2025. Flowsheet improvements negated the need to optimise Fe/Nb ratios and improved both Nb and Ti recovery. Aging of the HCl leach liquor was incorporated into demonstration plant operations.

Acid Bake – Water Leach

•
Perform vendor testing and optimization of Acid Bake operations and equipment. Validate process control and equipment capabilities – optimizing mixing time, temperature, acid to residue ratio. Optimize water to residue ratio in Water Leach.

Status: The acid bake and water leach unit operations were constructed and operated during as part of the demonstration plant. Continuous operation of both units was achieved and water consumption in the water leach was minimized.

Iron Reduction

•
Verify reaction kinetics and the use of briquettes.

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Status: The iron reduction unit operation has been eliminated from the flowsheet.

Nb Precipitation

•
Optimize FeNb ratio. Optimize Precipitant (dilution water) acidity to maximize Nb precipitation and Ti selectivity. Optimize Final Free Acid (FAT) to maximize selectivity against Ti.

Status: The demonstration plant optimized Nb/Ti through a bulk hydrolysate precipitation followed by chlorination to separate Nb and Ti. This combination of unit operations achieved a very good separation between Nb and Ti while minimizing water consumption in hydrolysis.

Ti Precipitation

•
Further test work required to maximize the removal of uranium and thorium from the Titanium dioxide product to increase its value.

Status: The demonstration plant was based on bulk hydrolysis followed by chlorination to achieve a good separation of Nb and Ti, while effectively eliminating U and Th from the Ti product.

Sc Precipitation

•
Optimize the H3PO4 addition. Optimize the Fe addition. Perform locked cycle tests on the Calcium loop.

Status: The demonstration plant integrated Sc separation and recovery with rare earth separation and recovery in a single integrated solvent extraction operation. The unit operations noted above are no longer part of the production flowsheet.

Sc Refining

•
Optimize and further evaluate Zr/Nb removal using mixed organics – stripping acid. Optimize conditions to minimize Sc losses.

Status: As noted above, scandium separation, recovery and refining operations were optimized during the demonstration plant.

Sc oxalate Precipitation

•
Verify precipitation using solid oxalic acid – optimal amount for optimal recovery. Optimize acidity, temperature, and g/l with solid oxalic acid. Optimize the washing of Sc oxalate for calcining equipment integrity.

Status: This optimization work will be addressed during detailed engineering and plant commissioning. While the demonstration plant confirmed the flowsheet for separating and recovering scandium, optimization exercises such as those described above require larger quantities of scandium than the demonstration plant can deliver.

Acid Regeneration

•
Optimize the filtration – evaluate equipment and filtration media.

Status: This aspect of the flowsheet was eliminated as a result of demonstration plant testwork.

Sulfate Calcining

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•
Optimize residence time. Vendor testing of different equipment and assembly.

Status: This unit operation preceded the sulphuric acid plant in the prior flowsheet. It has subsequently been eliminated.

General

•
Equipment selection, material of construction and vendor guarantee testing.

Status: These considerations will be addressed during detailed engineering.

•
Consider a fully integrated pilot testing to be operated onsite during construction of a full-size plant to make final adjustments and equipment selection.

Status: The demonstration plant was operated from 2022 to 2025, and included bench, pilot and fully integrated continuous operations of the project’s flowsheet.

•
Further perform process engineering during the detailed design phase.

Status: Extensive process engineering was completed concurrently with the development of the demonstration plant; this process will continue during detailed design.

•
Perform process simulation of the yearly or monthly elemental feed composition using the METSIM model and the compositions from the mine plan.

Status: The monthly, annual and life of mine plans were provided to L3 for modeling purposes as part of the development of this Technical Report Summary.

Scandium Market Risks and Sales Plan

At the time of this report, NioCorp had entered into one offtake agreement covering scandium trioxide production from the Project.

The scandium trioxide offtake agreement is structured similarly to the Niobium contracts. The agreement has a ten-year term and a minimum of 12 t/y. At that rate, approximately 10 – 15% of the projected annual production is contracted. Further, the customer may elect to take more material in any given year above the prescribed minimum quantity.

NioCorp is also working with other potential customers at the time of writing and discussions with these potential customers are proceeding under the provisions of Non-Disclosure Agreements (NDAs). These potential customers can be separated into the following categories or end products:

•
Scandium/Aluminum alloys used in aerospace, automotive, and other applications to increase strength and allow for a reduction of weight. Interested customers are situated at various points in the supply chains for aerospace manufacturing and operation; specialty alloy manufacturing; and specialty minerals and metal brokers/distributors.
•
Solid Oxide Fuel Cells. Scandium is used in the electrolyte of solid oxide fuel cells to increase the conductivity at lower temperatures, allowing for higher efficiency and longer life. Discussions with interested customers in this industry and its supply chains are continuing.

NioCorp has produced a small quantity of 99.9% pure scandium trioxide during lab pilot testing, which meets or exceeds the purity needed for virtually all mainstream commercial applications. This material has been sent and will continue to be sent to interested customers for their analysis.

Rare Earth Market Risks

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•
At the time of this report, a steady increase in demand magnet feed REEs (Nd, Pr, Tb, and Dy) is forecast. NioCorp does not have any off-take agreements at present but is investigating potential customers. 

Status: On April 9, 2026, NioCorp announced that it had entered into a non-binding agreement (the “Term Sheet”) with Traxys North America LLC (“Traxys”) outlining a long-term marketing and offtake arrangement for NioCorp’s remaining planned critical minerals products from its Elk Creek Critical Minerals Project. This includes the magnetic rare earth elements.

Pyrometallurgy Process Risks

Based on the XPS test results and the associated assessment of industrial operating conditions, the titanium-bearing Hydromet product should not be considered as it represents an operation risk for the Pyromet process. The titanium reports predominantly to the slag and provides no metallurgical benefit to the aluminothermic reduction. Its presence significantly increases the quantity of slag generated, asks more energy from the furnace, and requires a high frequency of slag tapping. At the projected production scale, this additional slag burden could interfere with normal furnace operation, restrict the time available for ferroniobium tapping, adversely affect metal–slag separation, and increase the risk of niobium losses.

The complex sodium-bearing product generated by the Hydromet process should not, however, be rejected solely because of its sodium content or mineralogical complexity. The test work indicates that this material may remain suitable for ferroniobium production, however the Hydromet circuit must consistently produce a feed showing the same chemical composition and mineralogical characteristics. The continued development of this feed should therefore focus on establishing a reproducible product composition and defining acceptable operating ranges for the constituents that materially affect the aluminothermic reaction, slag formation, metal–slag separation, niobium recovery, and final alloy quality.

As a fundamental design requirement, the composition of the Hydromet product and the Pyromet operating conditions should be established to maintain a metal/(metal + slag) mass ratio greater than 40%. Maintaining this ratio is considered necessary to limit the slag burden to an operationally manageable level, support effective metal–slag separation, and minimize the potential for niobium losses to the slag.

Attention must also be given to phosphorus. The last XPS test work confirmed that phosphorus contained in the titanium Hydromet feed can report to the ferroniobium alloy. Because phosphorus is tightly controlled in steelmaking due to its potentially adverse effects on steel ductility and toughness, a phosphorus-control strategy must be incorporated into the Hydromet process design.

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22 Interpretations and Conclusions

22.1 Geology & Mineral Resource

The Elk Creek deposit is a carbonatite hosted, multi element system defined entirely by diamond drilling and geophysical interpretation, with no surface outcrop due to approximately 656 ft (200 m) of overlying Pennsylvanian marine sediments. Geological domain, informed by lithological logging of 65 drill holes, has established three estimation domains (MCARB, DOL_CARB, and LAMP) with hard boundaries supported by statistically significant grade populations among the three domains. The MCARB domain hosts most Measured and Indicated resources and exhibits the strongest grade continuity and lowest variability of the three domains, supporting confidence in the resource classification assigned to this domain.

The Mineral Resource Estimate, effective June 30, 2026, is prepared in accordance with the Regulation S-K 1300, and totals 209.1 Mtons of Measured + Indicated and 169.2 Mtons Inferred at a cut-off of NSR > US$218 per ton. The estimate incorporates a domain specific variography and Ordinary Kriging approach, validated through global mean comparison, swath plot analysis, and grade-tonnage curve reconciliation, with all analytes confirmed within 5% of the declustered composite mean. The Qualified Person considers the Mineral Resource estimate to be unbiased, geologically reasonable, and suitable for public disclosure under Regulation S-K 1300.

The following factors are considered material to the interpretation and reliability of the Mineral Resource Estimate:

•
Geological uncertainty at depth and domain margins: The absence of surface exposures means the geological model is reliant on drill hole density and geophysical interpretation. Uncertainty is elevated in the peripheral DOL_CARB domain, where wider drill spacing and higher grade variability result in a larger proportion of Inferred classification.
•
Classification and data density: The Inferred resource (169.2 Mt) is large relative to the combined Measured and Indicated resource (209.1 Mt), reflecting the extent of DOL_CARB drilled at wider spacing. Upgrading Inferred resources to Indicated classifications would require additional infill drilling in the peripheral domain.
•
Multi Element Estimation: The resource incorporates four reported analytes (Nb₂O₅, TiO₂, Sc, TREO) plus three additional NSR only streams (Tb₂O₃, NdPr Oxide, SEG Carbonate) not independently reported as resource attributes. The NSR cut-off used to define reasonable prospects of eventual economic extraction is therefore sensitive to metallurgical recovery and commodity price assumptions across all seven products, particularly niobium and scandium, which dominate the NSR value.

The Qualified Person is of the opinion that the geological model, database, and resource estimation methodology are appropriate and adequate to support the classification and reporting of Mineral Resources under Regulation S-K 1300. No factors have been identified that would materially affect the reliability of the Mineral Resource estimate as reported.

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22.2 Mining & Mineral Reserve

Longhole stoping is seen as the appropriate mining method for the deposit geometry. The large stope sizes minimize the mining cost. The increased dilution due to large stopes sizes is not particularly material to the mine plan as dilution has some grade.

An NSR approach was used focused on targeted amounts of Nb2O5 and considers revenue for four product streams (Nb2O5, TiO2, Sc and rare earths). Stope optimization was completed to identify economic mining areas. The 3D mine design was completed on an elevated CoG, which achieved over 2.7 times the actual calculated cut-off. Three main mining blocks were designed, giving a 43-year LOM, although additional material, classified as indicated, exists in addition to the mine plan presented here.

The underground mine is accessed through a dual access ramp system from the surface box cut excavation to each of the mine working levels. The primary air intake ramp will also serve as the access ramp into the mine workings for all labor, materials, services, power, equipment, and supplies. The haulage ramp serves as the mine air exhaust, a second means of access, and a second mechanical emergency egress. Both ramps are excavated using conventional drifting. A short vertical ventilation shaft will be excavated near the surface exit of the ramp to allow the mine supply fans to be located on the surface and reduce the tendency for potential recirculation.

If upon review, it is found that the overall air volume requirement increases or decreases, it is currently assumed that current ramp sizing will not change. However, an increase in air volume may require additional considerations with respect to ramp or fan infrastructure aerodynamics and conveyance stability.

Tonnage and grades presented in the reserve include dilution and recovery and are benchmarked to other similar operations. Productivities were generated from first principles with inputs from mining contractors, blasting suppliers, and equipment vendors where appropriate. The productivities were also benchmarked to similar operations. Equipment used in this study is specified as battery electric equipment.

Monthly and yearly production schedules were generated using Deswik© scheduling software. The steady-state mine production schedule of 3,100 t/d ore was based on targeting mine production to match the mill processing throughput of 3,050 t/d. The mine design targeted 8,267 tons of annual ferroniobium production during full production, which resulted in an average annual production rate of 8,282 tons per year over the full production period of the mine life.

22.3 Recovery Methods

Hydrometallurgical Plant

The recovery methods described in Section 17 are based directly on the results of the test work presented in Section 13. Design criteria for all areas have been established at a level of definition appropriate for the 2026 Elk Creek Study. Where continuous operation and recycle streams are critical (for example in Area 200 – Ammonium Chloride cycle and Area 400 – Sulfuric Acid), the test work has been used to evaluate impurity buildup and required bleed ratios.

The recovery methods for Area 500 – Chlorination is based on the results of test work for the chlorination and for the recovery of niobium. The titanium tetrachloride purification circuit was

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designed based on SMH/L3’s expertise and experience with such systems. SMH/L3’s engineers have been involved in various projects for the production of titanium tetrachloride used both in TiO2 pigment and in titanium metal.

The recovery methods for Area 800 – Chloride recovery is based on the results of test work for the pyro hydrolysis and for the recovery of hydrochloric acid. The hydrochloric acid tower circuit was designed based on SMH/L3’s expertise and experience with such systems. SMH/L3’s engineers have been involved in various projects for the synthesis and recovery of hydrochloric acid.

Pyrometallurgical Plant

Even if the Pyromet test program successfully demonstrated the production of ferroniobium alloy through aluminothermic reduction, the small-scale tests were not sufficient to establish a definitive industrial niobium recovery or to fully quantify the distribution of niobium between the metal, slag, dust, and residual metallic particles.

The Pyromet plant design should include provisions for collecting and recycling niobium-bearing dust and metallic fines generated during feed preparation, furnace operation, tapping, alloy handling, and crushing. Slag should also be evaluated for entrained ferroniobium particles and residual niobium-bearing phases to determine whether a dedicated slag-metal recovery step is technically and economically justified.

Further representative-scale testing is recommended to close the niobium mass balance and confirm the achievable overall recovery. The testing should quantify niobium reporting to the alloy, slag, dust, and other process residues and establish the recycle streams required for the final process design. Slag reprocessing should be considered a secondary recovery measure and should not be used to compensate for inadequate metal–slag separation in the primary Pyromet operation.

22.4 Processing & Metallurgical Testing

The hydrometallurgical test work program completed in support of the 2026 Elk Creek Study is considered adequate in scope, scale, and representativeness to support process design criteria, Mineral Reserve estimation, and the economic analysis presented in this Technical Report Summary.

Samples used for metallurgical testing were selected by Niocorp to represent the material included in the Mineral Reserves. Demonstration scale test work is on-going with regards to Ore variability with some results included in Section 13. The demonstration Plant operation indicates that the selected process route is technically viable for the range of feed materials expected during the life of mine.

The overall Hydromet recovery of the primary payable element products using the selected flowsheet is presented as Table 22‑1 .

Table 22‑1: Hydromet Elemental Recovery Summary

Element

Recovery

Nb

84.7%

Ti

80.5%

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Element

Recovery

Sc

94.3%

NdPr

88.7-94.4%

Tb

94.4%

Dy

94.6%

Source: L3 2026

 

Optimization test work is on-going with a focus on the process energy efficiency optimization as well as in the production of commercial samples for all products.

Further test work around the Chlorination will confirm the operating design and will optimize the niobium and titanium recoveries.

The Pyromet test program successfully demonstrated the technical feasibility of producing a ferroniobium alloy from the Hydromet feed through aluminothermic reduction. The fundamental reaction pathway has therefore been established, and the remaining development work should focus on improving and validating the supporting Pyromet design parameters required for reliable industrial operation.

Further testing should specifically address slag composition and fluidity to ensure effective metal–slag separation and practical slag tapping. The Hydromet feed must also be further developed to provide consistent chemical and mineralogical characteristics, since feed variability can directly affect reaction behaviour, slag formation, niobium recovery, and alloy quality. In parallel, refractory selection should be investigated to confirm chemical compatibility with the metal and slag phases, minimize refractory degradation and alloy contamination, and provide an acceptable service life.

The next phase of testing should therefore be conducted at a larger and more representative scale to optimize these parameters and establish the final process design criteria. The objective is no longer to demonstrate that ferroniobium can be produced, but to confirm that it can be produced consistently, efficiently, and at the required commercial quality under industrial operating conditions.

22.5 Infrastructure

Onsite and Offsite Infrastructure

Based upon the most current operating and process design information and expectations, the on-site and off-site infrastructure and services will meet each of the required needs of this entire facility.

Infrastructure buildings, office space, locker facilities and showers were sized and designed based upon current workforce projections for the site, as well as a tentative work schedule of 12-hr shifts for shift personnel, and standard 8-hr shifts for non-shift staff. A change in the number of shifts and/or shift durations may have an impact on the requirements of these facilities.

Likewise, both potable water and wastewater distribution systems were sized based upon the above shift criteria. Changes in the number of personnel, and/or changes in numbers of shifts and shift durations may have an impact on the potable and wastewater demands which must be addressed during the detail phase of this design.

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Off-site infrastructure in the form of natural gas and electrical power services provided by others are readily available, and well within the current demand requirements of the facility. Potable water sources yielding approximately 1,500 gpm are available from the local municipality (City of Tecumseh). The public water source would require a service extension from the existing system.

Foundation designs for large loads and structures, as well as roadway designs, were based upon the most current geotechnical reports and best engineering practices for the local site conditions.

The most current geotechnical report partially addressed the recommended designs for deep foundations or foundations for large loads; building columns, columns with bridge crane loads, large process equipment or structures. It will be important that the geotechnical reports completed during detailed engineering address these types of loads and provide specific recommendations, but that the final geotechnical site evaluation includes test borings in the final locations of buildings, process equipment and major structures. An extensive site geotechnical investigation was completed in the second quarter 2026, including geotechnical borings at the major building locations.

22.5.1 Tailings Storage Facility

The tailings storage facilities (“TSFs”) are designed for storage of paste tailings solids in lined facilities permitted under State of Nebraska Industrial Solid Waste regulations. Based on the parameters and assumptions outlined in Section 15.11, the TSFs have been designed with adequate containment and capacity to manage the planned production of waste streams over the life of the mine.

22.6 Environmental, Permitting & Social or Community Considerations

NioCorp has developed information and conducted environmental studies for the purpose of baseline site characterization. Hydrogeology and geochemistry studies are included in this, to characterize the production rate and dewatering water quality, which will dictate critical factors for onsite water balance and management practices that may be required.

There are low levels of naturally occurring radioactive materials (NORMs) in this ore body. Therefore, waste materials (e.g., RO treatment salts and process waste/tailings) and wastewater have the potential for low radioactivity levels. Gross alpha, gross beta, and radioactivity of nine isotopes indicated that fugitive dust and external radiation exposure are potential concerns for the site. Four of these radionuclides (gross alpha, gross beta, Ra-226, and Ra-228) exceeded the screening levels but were below respective MCLs. These results indicate that the site materials are non-hazardous and will be permitted/managed as non-hazardous.

There are limited requirements for reclamation and closure of mine properties in Nebraska due to the lack of specific hardrock mining regulations. Within the applicable regulatory frameworks for the project, however, there are provisions which will be applied to the project during the permitting and licensing process. The current estimate for closure and reclamation is US$106 million.

Engagement of local and state regulators is currently in progress. While the formal operational permitting program for the project is dependent upon the completion of the mine plan, preliminary permitting and consultation which can be applied for prior to finalized mine plans have commenced. At this time, NioCorp had completed the following:

(1)
Nebraska Department of Water, Energy, and Environment (DWEE) Mineral Exploration Permit for exploration drilling;

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(2)
DWEE air quality construction permit;
(3)
DWEE authorization for Class V underground injection well for the hydrogeological portion of the exploration drilling;
(4)
Johnson County road use and maintenance agreement;
(5)
Johnson County special use permit;
(6)
DWEE construction stormwater permit;
(7)
DWEE construction dewatering discharge permit;
(8)
notification of Commencement of Operations with the Mine Safety and Health Administration (MHSA); and
(9)
Johnson County floodplain development permit. These permits and authorizations have allowed for the commencement of mine portal excavation and construction, and other construction and operations permits as needed have been scheduled for initiation as needed to support remaining stages of construction and commencement of operation.

At this time, there are no known environmental concerns that would materially impact NioCorp’s ability to extract the mineral reserves or mineral resources near Elk Creek. Environmental permitting timelines at the state level require up to six months for processing of most individual permits, with roughly 18 months needed for solid waste permitting for tailings impoundments. Broadly speaking, general permits can be active within 7 to 10 days of providing a full and complete application package.

Overall, the project has continued to advance at a pace which will initiate submittal of additional permitting for construction and operation as well as document practices for mine closure. Coordination with state regulatory agencies has assisted in providing regulatory officials with familiarity of this type of mining; however, it is important to acknowledge that risks still remain within the permitting process that could slow project development given the nascency of this type of mining in Nebraska and general lack of familiarity.

22.7 Market Studies & Contracts

Market studies were completed for all four of the major product groups that will be produced from the Elk Creek project: niobium, titanium, scandium and rare earths. Each of these products provides a meaningful contribution to revenue. The marketing studies used in this report are as follows:

•
Ferroniobium: Niobium Review and Outlook First Half 2025 (CPM Group 2025)
•
Scandium: A Market Appraisal (OnG Commodities LLC 2025, 2026)
•
Titanium: TiCl4 Market Analysis (TZMI, 2025)
•
Magnetic Rare Earths: Adamas Intelligence Q2/25 outlook (Adamas 2025) along with Argus Non-Ferrous Markets Rare Earth Pricing (Argus 2026)
•
SEG and Heavies carbonates: NioCorp Carbonates Value Forecasts (Adamas 2025)

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NioCorp currently has two offtake agreements covering 75% of niobium production for the first 10 years of operation and an MOU covering the balance of the project’s product suite. NioCorp is in the process of converting the MOU to a definitive offtake agreement.

22.8 Projected Economic Outcomes

Total LOM capital costs, including initial, sustaining and reclamation costs, are US$ 4,019 million. The initial capital estimate of US$ 1,849 million is incurred during a 35-month construction period. An overall 14 % contingency factor has been applied to the initial capital estimate

Operating cost estimates were developed to show monthly and annual costs for production. All unit costs are expressed as US$/ton processed and are based on Q2 2026 US$. Operating cost metrics in the technical economic model are developed on a unit rate basis and applied to the 40-year operating period of the project, from the end of construction to the end of the mine life.

The total operating cost unit rate is US$ 268.78/ton processed.

This Technical Report Summary is based on processing of 45,929,462 short tons of ore over a 40-year operational life to produce 205,464 tons of Nb in the form of ferroniobium, 4,585 tons of scandium oxide, 2,341,367 tons of TiCl4, 25,923 tons of NdPr oxide, 690 tons of Tb oxide, 2,649 tons of Dy oxide, 13,886 tons of SEG carbonate and 10,161 tons of heavies carbonate.

On a pre-tax basis, the NPV (8% discount) is US$ 4,111 million, the IRR is 24.0%, and the payback period is 2.93 years.

On a post-tax basis, the NPV (8% discount) is US$ 3,441 million, the IRR is 22.8%.

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23 Recommendations

23.1 Geology and Resources

During all drilling programs completed on the Project, further confidence in the geological continuity coupled with mineralization has expanded, resulting in further increasing the confidence in the Mineral Resource Estimation.

DGC recommends that during the drilling being completed as part of the grouting program as outlined in Section 13.3.2.4 by ABC, be incorporated into a resource infill program to further increase the confidence of the Mineral Resource Estimation as defined in this Report. By completing all grouting drill holes using coring methods, the same protocols and procedures can be used, and an additional 33 drill holes planned in the Mineral Resource Estimate can utilized for geological logging and analyses. These drill holes as defined by ABC in Section 13.3.2 of this Report and Figure 13‑8 align well with resource infill program. Costs to complete the data capture and sample analysis are outlined in Section 23.9 below.

23.2 Hydrometallurgical Plant

Test work has identified that carbonates generated by the Hydrometallurgical Plant have a negative impact on the unconfined compressive strength (UCS) of paste backfill. Therefore, it is recommended that future studies of the Hydrometallurgical Plant evaluate methods of reducing or eliminating carbonate content in waste streams directed to the Paste Backfill Plant, including by calcination of carbonates.

It is recommended that a comprehensive paste backfill testing program be conducted to further optimize the paste mix design. This program should evaluate paste produced from a revised hydrometallurgical plant waste stream with reduced carbonate content, whether achieved through carbonate removal or calcining, to determine the effect on UCS. This program should also identify opportunities to increase solids content and reduce binder content. The testing program should also assess the effect of fly ash on UCS.

Additionally, a more complete rheological testing program, including cemented rheology, should be performed on the resulting paste mixes to characterize pumpability. This work would support reducing the OPEX of the Paste Backfill System by reducing the binder requirement and reducing the size of the TSF by increasing the ratio of tailings returned to underground.

It is recommended that the on-going hydrometallurgical plant optimization test work be continued. For instance, significant gains in energy efficiency are likely to be realized with further optimization of the ammonium chloride circuit and the optimization of chloride pyrohydrolysis unit.

In addition, the piloting of the chlorination unit through commercial samples of niobium and titanium is likely to result in a reduction of capital cost through the reduction in engineering design factors in the titanium distillation process. Additional larger-scale piloting work in the chlorination unit is required to minimize phosphorus reporting to the ferroniobium product.

Finally, the QP recommends operating the chloride demonstration circuit through commercial samples of scandium, didymium, terbium and dysprosium oxides to perform the final calibration of the circuit steady state model and allow for subsequent reagent optimization and for the preparation

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of a commercial plant circuit start-up strategy through the validation of the separation circuit dynamic model (digital twin) developed by L3 Process Development.

23.3 Geomechnical

It is recommended that underground observations be completed during mine development and early production to confirm the assumptions used in the geomechanical analyses and mine design.

•
Particular attention should be given to validating the in-situ stress regime, including both stress orientation and magnitude, as these parameters have an important influence on stope stability, dilution, and ground support requirements.
•
The presence, location and rock mass conditions of the degraded rock mass quality areas should be investigated. As such, it will be important to validate the location and thickness of the interpreted property-scale structures. A better definition and 3D understanding of the zones with lower quality (weathered areas) is needed for the detailed and reliable planning of the stoping area.
•
A Ground Control Management Plan (GCMP) should be developed. This plan will need to be regularly updated and audited during the mine life.
•
The dilution assumptions used in the 2026 Elk Creek Study should be validated against actual operating performance during initial mining.

23.4 Mining & Reserves

Ventilation design

Following the QP review, it is recommended that a more in depth and broader review be undertaken on the ventilation design and its optimization specifically addressing:

•
Thermal conditions that could be encountered underground during the summer,
•
Any need to manage radiation exposure requiring consistent ventilation though open areas,
•
A more detailed study of clean engine technologies and battery electric equipment to control diesel particulate matter,
•
The load diversity during concurrent development and production stages,
•
The shift load diversity and the capacity for it to be managed through ventilation on demand.
•
Production (haulage) ramp velocities and the influence of conveyances on airflows.

Other recommendations:

•
Infill Drilling during the pre-production period is recommended to help identify final locations for primary and infrastructure development locations.
•
Geotechnical review of active drifting and infill drilling is recommended to further refine final stope lengths by ground type.

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•
Hydrogeological drilling and review is recommended to be conducted in conjunction with pre-production development to confirm surface grouting success and to reduce risk of un-planned water inundation.

Paste Backfill Underground Distribution System (“UDS”)

It is recommended that future study phases investigate the potential to route the paste backfill UDS via dedicated boreholes rather than via the ramp. This configuration would reduce the lateral distance of the UDS, reducing friction losses and thus increasing the solids content of the paste backfill to reach equivalent stopes. Routing the UDS outside of the ramp would also reduce potential interference that inspection, maintenance, or repair of the UDS may have on ramp traffic and operations. Lastly, because routing via boreholes would reduce the length of the UDS, it could potentially have a lower CAPEX and OPEX compared with routing via the ramp.

23.5 Pyrometallurgical Plant

Test work has successfully demonstrated that ferroniobium alloy can be produced from the Hydromet feed through aluminothermic reduction. Therefore, it is recommended that a larger-scale Pyromet testing program be conducted to further develop and confirm the operating and design parameters required for consistent industrial production. Additionally, a refractory evaluation program should be conducted to identify materials compatible with the expected metal and slag compositions, minimize alloy contamination, and provide an acceptable operating life. Representative metal, slag, dust, and residual materials should be fully characterized to close the elemental mass balance and confirm niobium recovery. Attention should be given to phosphorus, as testing has confirmed that phosphorus contained in the feed can report to the ferroniobium alloy. Feed and product limits should therefore be established to ensure that the final alloy consistently meets the applicable commercial specification. This program should focus on optimizing slag composition and fluidity, improving metal–slag separation, confirming tapping behavior, and maximizing niobium recovery to the alloy.

23.6 Recovery Methods

It is recommended that a full-scale heat integration and optimization analysis (Pinch Analysis) be undertaken on the Hydromet flowsheet to optimize energy recovery.

23.7 Infrastructure

General Infrastructure

Additional geotechnical investigation is recommended based upon the detail design requirements addressed in Section 22.5. This would include borings in the selected building and large equipment locations, high load and deep foundation recommendations, as well as pavement design recommendations based upon the type and frequency of vehicle traffic.

Any additional work required is included in the detailed engineering scope of work and included in the cost.

Tailings

With respect to tailings Tierra Group/BBA provides the following recommendations:

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•
Complete a comprehensive tailings laboratory testing program to characterize the material and provide geomechanical properties to support detailed design of the TSF. The program should include index testing (grain size, specific gravity, Atterberg limits, Proctor density), slump, strength, settling and drying, permeability and consolidation tests.
•
Conduct a site specific seismic hazard assessment (“SHA”). This is a specialized engineering study used to define the exact earthquake shaking and ground failure risks for a particular project location. It replaces standard building code estimates with precise, localized data to optimize structural design and ensure safety.
•
Identify suitable locations for the storage of topsoil and any excess excavated material.
•
Conduct additional geotechnical investigations to further characterize foundation soils and assess potential borrow sources to support detailed design and construction planning across the Project site. Additional boreholes should be completed in the footprint of each TSF cell prior to final design and should include installation of additional piezometers to further define the groundwater conditions. Laboratory testing of collected samples should include index testing, permeability, consolidation and shear strength testing.
•
Update design parameters and optimize designs based on the results of the geotechnical and hydrogeological investigations. The primary parameters include seismicity, foundation and structural fill shear strength, consolidation and pore pressure response.
•
Utilize observations and lessons learned during early cell construction to refine design details and construction methods for subsequent cells. The primary considerations include the suitability of the materials from required excavations for use as structural fill, behavior of the foundation soils upon loading, and construction controls required to achieve the specifications.

Salt Management

The final salt product will be characterized for solubility, runoff chemistry, and geotechnical characteristics to aid in the detailed design of the proposed salt management cells.

Paste Backfill

Additional testing for the optimum paste backfill mixture during the next phase of the project is recommended. Additional testing could help further optimize the cement content, maximize early strength gain and minimize the paste backfill plant operating cost. By doing so early, the design for the paste backfill plant can be modified to allow for the addition of the relatively cheap, locally available fly ash as a binder, and for the paste backfill recipe to be perfected prior to detailed design or construction.

23.8 Environmental & Social

Olsson provides the following environmental, permitting, and social/community related recommendations to NioCorp:

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•
Continue engagement and transparency with all relevant stakeholders which have been identified throughout the development process. This helps to reduce opposition to development and ensures genuine regulatory buy-in to the project.
•
Continue engagement with state and local regulatory bodies to ensure an up-to-date and ongoing understanding of the mine plan, including processing of materials and disposal of wastes. This will help to ensure that lead times for permitting are known in advance and will prevent delays in both the permitting and construction processes.

 

23.9 Summary of Costs for Recommended Work

Area

Program

Cost Estimate (US$)

Geology & Resource

Couple Proposed grouting plan with resource infill program to increase confidence in the Mineral Resource. Of the 68 planned surface grout holes, use 33 as resource infill. Costs include onsite geological support and expenses, analytical costs and shipping, and update to the Mineral Resource Estimate.

$7,500,000

Processing & Metallurgical Testing

 Paste backfill test program, chlorination testwork, optimization, Pinch Analysis

$5,000,000

Mining Reserves

 Additional infill drilling (will be accomplished through execution of the grouting program)

$0

Ventilation Design

 Additional Ventilation Studies

$250,000

Geomechanical

 Ground Control Management Plan

$200,000

Salt Management

Salt characterization program

$50,000

Pyrometallurgical Plant

 Additional pyromet testing program

$150,000

Tailings

 Tailings laboratory Testing Program, site specific hazard analysis, geotechnical investigations

$200,000

Paste Backfill

 Covered above under Process

$0

TOTAL:

$13,350,000

 

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24 References

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A2GC. (2026b). Elk Creek Project - Rock Engineering in Support of the Mine Design for the 2026 Feasibility Study [Technical Report under preparation] Andrieux & Associates Geomechanics Consulting, June 2026.

ABC. (2026). Groutability of the Elk Creek Mine Orebody. Adrian Brown Consultants.

Adamas Intelligence. (2019). Rare Earth Elements: Market Issues and Outlook (Q2 2019). 1–10.

Adamas Intelligence. (2022). Rare Earth Magnet Market Outlook to 2035. Online Abstract. (May 23, 2022). https://www.adamasintel.com/report/rare-earth-magnet-market-outlook-to-2035/

Adamas Intelligence. (2025). Rare Earth Magnet Market Outlook to 2040: Top Predictions for 2026. Toronto, Canada.

Anzman, J. R. (1976). Interpretation of Gravity and Magnetic Data, Elk Creek Anomaly, Johnson and Pawnee Counties, Nebraska. Molycorp Inc.

Argus. (2026). Argus Non-Ferrous Markets. Argus Media Group.

Barton, N. R., Lien, R., & Lunde, J. (1974). Engineering classification of rock masses for the design of tunnel support. Rock Mechanics, 6(4), 189–236.

Batty, M., Everett, B., Broili, A., Brown, A., Doundarov, G., Gorham, J., Hales, M., Harton, S., Jundis, R., Khwaja, M., Larochelle, E., Lepage, M., Marx, W., McKenzie, I., Sames, J., Smith, D., Tinucci, J., Willow, M., & Winters, D. (2022). NI 43-101 Technical Report Feasibility Study, Elk Creek Project, Nebraska [NI 43-101].

Berendsen, P., & Weis, T. (2001). New Kimberlite Discoveries in Kansas: Magnetic Expression and Structural Setting. 104(3–4), 223–236.

Birkett, T. C., & Simandl, G. J. (1999). Carbonatite Associated Deposits: Magmatic, Replacement and Residual. 3.

Brookins, D. G., Treves, S. B., & Bolivar, S. L. (1975). Elk Creek, Nebraska Carbonatite: Strontium Geochemistry. Earth and Planetary Science Letters, 28, 79–82.

Burchett, R. R. (1982). Thickness and structure maps of the Pennsylvanian and Permian rocks across Southern Nebraska (Report of Investigations No. 7). Nebraska Geological Survey.

Burchett, R. R., & Reed, E. C. (1967). Centennial Guidebook to the Geology of southeastern Nebraska. Lincoln, NE: University of Nebraska, Conservation and Survey Division.

Carlson, M. P. (1992). Tectonic implications and influence of the Midcontinent. Rift System in Nebraska and adjoining areas. In: (Richard W. Ojakangas, Albert B. Dickas, John C. Green, Eds. Proceedings of the Tenth International Conference on Basement Tectonics.

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Carlson, M. P., & Treves, S. B. (2005). The Elk Creek Carbonatite, Southeast Nebraska—An Overview. Natural Resource Research, Vol. 14(No.1), 39–45.

Carmichael, M. J., & Arulraj, G. P. (2017). Strength and Permeability Studies on Concrete with Nano-Cement. International Journal of Civil Engineering and Technology, 8(1), 132–139.

CIM. (2014). CIM Definition Standards on Mineral Resources and Mineral Reserves. Canadian Institute of Mining, Metallurgy and Petroleum, May 19, 2014.

CIM. (2019). CIM Estimation of Mineral Resources and Mineral Reserves Best Practice Guidelines [CIM Estimation of Mineral Resources & Mineral Reserves Best Practice Guidelines, November 29, 2019]. Canadian Institute of Mining, Metallurgy and Petroleum.

Clark, L. M. (1998). Minimizing dilution in open stope mining with a focus on stope design and narrow vein longhole blasting (p. 357 p.) [(Master Thesis). University of British Columbia]. Mining & Mineral Process Engineering.

Cook, W. B., & Shearer, R. L. (1986). Proposed Land Retention for 1986, Elk Creek, Nebraska. Internal Molycorp Memo, February 5, 1986.

Cordell, L. (1979). Gravimetric Expression of Graben Faulting in Santa Fe Country and the Espanola Basin, New Mexico. In: Ingersoll, R.V., Ed., Guidebook to Santa Fe Country. 59–64.

Cordell, L., & Grauch, V. J. S. (1985). Mapping Basement Magnetization Zones from Aeromagnetic Data in the San Juan Basin, New Mexico. In: Hinze, W.J., Ed., The Utility of Regional Gravity and Magnetic Anomaly Maps. Society of Exploration Geophysicists, 181–197.

CPM Group. (2025). Niobium Review and Outlook, A comprehensive study of the global niobium market including 10-year projections of niobium supply, demand by end use, and prices. (May 2025).

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Erdosh, G. (1979). The Ontario Carbonatite Province and Its Phosphate Potential. Economic Geology, 74, 331–338.

Farmer, J. D., Chamberlain, K. R., & Babcock, S. M. (2013). Final Technical Report for “Collaborative Research with the University of Nebraska and University of Colorado on the Age and Origin of the REE-Rich Elk Creek Carbonatite, Southeast Nebraska, USA. USGS Award Number G12AP20052.

GISTM. (2020). Global Tailings Review, Global Industry Standard on Tailings Management. (August 2020).

Grimstad, E., & Barton, N. (2014). Q-System—An Illustrated Guide Following 40 Years in Tunnelling (p. 43 p.) [Technical Report].

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Hoek, E. (1994). Strength of rock and rock masses. International Society for Rock Mechanics (ISRM) News Journal, I(2), 4–16.

Hoek, E., & Bray, E. T. (1974). Rock Slope Engineering. Institution of Mining and Metallurgy.

ICOLD. (2025). International Committee on Large Dams (ICOLD). Bulletin 194 on Tailings Dam Safety(April 28, 2025).

IEA. (2026). Rare Earth Elements: Pathways to Secure and Diversified Supply Chains. International Energy Agency, (8 April 2026).

Jodouin. (2025). NioCorp Elk Creek Technical Report Update Ventilation Design Criteria REV B. June 20, 2025.

Jodouin. (2026). Mine Ventilation Design Report.

King, P. B. (1969). The Tectonics of Middle North America.

Larochelle, T., Larochelle, E., Dissem, N., Sixberry, R., & Honan, S. (2024). A new paradigm for the recovery of rare earth elements: The high activity flowsheet as applied to the Elk Creek deposit.

Mathews, K. E., Hoek, E., Stewart, S. B. V., & Wyllie, D. C. (1980). Prediction of Stable Excavation Spans for Mining at Depths Below 1000 meters in Hard Rock, [CANMET Technical Report].

McBee, W. (2003). Nemaha Strike-Slip Fault Zone. Search and Discovery Article #10055.

Mitchell, R. H. (2005). Carbonatites and Carbonatites and Carbonatites. The Canadian Mineralogist, 43(6), 2049–2068.

Naugle, R. C. (2018). A Brief History of Nebraska. https://doi.org/ISBN%20978-0-933307-39-1

NDEQ. (2016). Nebraska Department of Environmental Quality (NDEQ), Nebraska Administrative Code. Title 132 – Integrated Solid Waste Management Regulations.

NGI. (2022). Using the Q-system—Rock mass classification and support design. Revised handbook edition.

Nickson, S. D. (1992). Cable support guidelines for underground hard rock mine operations. [(Master Thesis). University of British Columbia].

Nordmin. (2019). NI 43-101 Technical Report, Feasibility Study, Elk Creek Superalloy Materials Project, Nebraska [NI 43-101 (Effective Date: April 16th, 2019, Report Date: May 29, 2019). Prepared for NioCorp Developments Ltd.].

NRCS. (2015). United States Department of Agricultural Natural Resources Conservation Service Web Soil Survey. http://websoilsurvey.sc.egov.usda.gov/App/HomePage.html

OnG. (2025). Scandium: A Market Appraisal, prepared for NioCorp Ltd., by OnG Commodities LLC. (September 2025).

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Woolley, A. R. (1989). The Spatial and Temporal Distribution of Carbonatites. In: Carbonatites, Genesis, and Evolution (K. Bell, Ed.), 15–37.

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24.1 Definition of Terms

Table 24‑1: Summary of general mining terms potentially used in this Technical Report Summary.

Term

Definition

Assay

The chemical analysis of mineral samples to determine the metal content.

Capital Expenditure

All other expenditures not classified as operating costs.

Composite

Combining more than one sample result to give an average result over a larger distance.

Concentrate

A metal-rich product resulting from a mineral enrichment process such as gravity concentration or flotation, in which most of the desired mineral has been separated from the waste material in the ore.

Crushing

The initial process of reducing the ore particle size to render it more amenable for further processing.

Cut-Off Grade (CoG)

The grade of mineralized rock, which determines as to whether or not it is economical to recover its gold content by further concentration.

Dilution

Waste, which is unavoidably mined with ore.

Dip

The angle of inclination of a geological feature/rock from the horizontal.

Fault

The surface of a fracture along which movement has occurred.

Footwall

The underlying side of an orebody or stope.

Gangue

Non-valuable components of the ore.

Grade

The measure of the concentration of gold within the mineralized rock.

Hanging wall

The overlying side of an orebody or slope.

Haulage

A horizontal underground excavation which is used to transport mined ore

Hydrocyclone

A process whereby material is graded according to size by exploiting

Igneous

Primary crystalline rock formed by the solidification of magma.

Kriging

An interpolation method of assigning values from samples to blocks that minimize the estimation error.

Level

A horizontal tunnel, the primary purpose is the transportation of personnel and materials.

Lithological

Geological description pertaining to different rock types.

LRP

Long Range Plan.

Milling

A general term used to describe the process in which the ore is crushed and ground and subjected to physical or chemical treatment to extract the valuable metals to concentrate or finished product.

Mineral/Mining Lease

A lease area for which mineral rights are held.

Mining Assets

The Material Properties and Significant Exploration Properties.

Ongoing Capital

Capital estimates of a routine nature, which is necessary for sustaining operations.

Ore Reserve

See Mineral Reserve.

Ore reserve Pillar

Rock left behind to help support the excavations in an underground mine.

Sedimentary

Pertaining to rocks formed by the accumulation of sediments, formed by the erosion of other rocks.

Shaft

An opening cut downwards from the surface for transporting personnel, equipment, supplies, ore and waste.

Sill

A thin, tabular, horizontal to sub-horizontal body of igneous rock formed by the injection of magma into planar zones of weakness.

Smelting

A high temperature pyrometallurgical operation conducted in a furnace, in which the valuable metal is collected to a molten matte or dolt phase and separated from the gangue components that accumulate in a less dense molten slag phase.

Stope

The underground void created by mining.

Stratigraphy

The study of stratified rocks in terms of time and space.

Strike

The direction of the line formed by the intersection of strata surfaces with the horizontal plane, always perpendicular to the dip direction.

Sulphide

A sulphur-bearing mineral.

Tailings

Finely ground waste rock from which valuable minerals or metals have been extracted.

Thickening

The process of concentrating solid particles in suspension.

Total Expenditure

All expenditures, including those of an operating and capital nature.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Term

Definition

Waste Rock

Rock excavated during mining that is not processed as ore. The term is a standard mining term and does not, by itself, determine regulatory status, environmental classification, or beneficial-use potential; those determinations depend on material characteristics, proposed use or management, and applicable regulations.

Variogram

A statistical representation of the characteristics (usually grade).

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

24.2 Abbreviations

Abbreviation

Unit or Term

Abbreviation

Unit or Term

%

percent

LOI

loss on ignition

%w/w

percent mass fraction for percent mass

LOM

life of mine

<

less than

LREO

Light Rare Earth Oxide (Lanthanium through Neodymium)

>

greater than m2)

M

million

°

degree (degrees)

m

meter

°C

degrees Celcius

m.y.

million years

µm

micrometer per micron

m2

square meter

µRads/hour

microradian/hour

m3

cubic meter

A

ampere

m3/h

cubic meter per hour

AA

atomic absorption

Ma

mega-annum (1 million years)

Airn2

amperes per square meter

masl

meters above sea level

AMS

Air Monitoring Stations

MCL

maximum contaminant levels

ANFO

ammonium nitrate fuel oil

MDA

Mine Development Associates

AQS

Air Quality Stations

mg/L

Milligrams per liter

Au

gold

MgCO3

Magnesium Carbonate

BATF

U.S. Bureau of Alcohol, Tobacco and Firearms

MJ

megajoules

bgs

below ground surface

mm

millimeter

BoE

Basis of Estimate

mm2

square millimeter

CAA

Clean Air Act

mm3

cubic millimeter

CaCO3

Calcium Carbonate

MME

mine & mill engineering

CaF2

calcium fluoride

MMF

Multimedia Filter

CaO

Calcium Oxide

Mpa

megapascal

CAPEX

capital expenditure

MSHA

Mine Safety and Health Administration

CCTV

Closed-circuit video

Mt

million tonnes

CDF

cost data file

Mtpa

Million tonnes per annum

cfm

cubic feet per minute

MTW

measured true width

CIM

Canadian Institute of Mining, Metallurgy, and Petroleum

MW

million watts

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Abbreviation

Unit or Term

Abbreviation

Unit or Term

cm

centimeter

MWMP

meteoric water mobility procedure

cm2

square centimeter

NaNbO3

sodium niobate

cm3

cubic centimeter

Nb2O5

Niobium Pentoxide

CoG

cut-off grade

NCG

non-condensable gas

ConfC

confidence code

NDEE

Nebraska Department of Environmental and Energy

CoNSR

Cut-Off Net Smelter Return

NdPr

Neodymium/Praseodymium

CRC

Cultural Resources Consulting

NGO

non-governmental organization

CRec

core recovery

NH4

Ammonium

CRM

certified reference material

NH4Cl

Ammonium Chloride

CSS

closed-side setting

NI

43-101 Canadian National Instrument 43-101

CSV

comma separated values

NN

Nearest Neighbor

CTBD

Cooling Tower Blow Down

NORM

naturally occurring radioactive material

CTW

calculated true width

NPDES

national pollutant discharge elimination system

dia.

diameter

NPV

Net Present Value

DNR

Department of Natural Resources

NRCS

Natural Resources Conservation Service

DOL

Department of Labor

NSR

Net Smelter Return

EBITDA

Earning Before Interest, Taxes, Depreciation and Amortization

OCC

Operations Control Center

EIS

Environmental Impact Statement

OK

Ordinary Kriging

EMP

Environmental Management Plan

OP

open pit

EPA

U.S. Environmental Protection Agency

OPEX

operating expense

FeNb

ferroniobium

pCi/g

picocuries per gram

FGD

flue gas desulfurization

PCN

Process Control Network

FPA

Furnace Feed Preparation Area

PDP

power distribution panels

ft

foot (feet)

PDS

paste distribution system

ft2

square foot (feet)

PENN

Pennsylvanian-aged mudstone and limestone (Pennsylvanian strata)

ft3

cubic foot (feet)

PLC

programmable logic controller

g

gram

PLS

pregnant leach solution

G&A

General and Administrative

PMF

probable maximum flood

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Abbreviation

Unit or Term

Abbreviation

Unit or Term

g/cm3

grams per cubic centimeter

ppm

parts per million

g/L

gram per liter

PSD

prevention of significant deterioration

g/t

grams per tonne

QA/QC

quality assurance/quality control

Ga

giga-annum (1 billion years)

RC

rotary circulation drilling

gal

gallon

REE/REEs

Rare Earth Element(s)

GHG

greenhouse gases

RIO

Remote I/O

g-mol

gram-mole

RO

reverse osmosis

gpd

gallons per day

ROM

run of mine

gpm

gallons per minute

RPD

relative percentage difference

ha

hectare (10,000 square meters)

RQD

rock quality description

HAP

hazardous air pollutant

SEC

U.S. Securities & Exchange Commission

HCl

hydrochloric acid

sec

second

HDPE

height density polyethylene

SEG

samarium (Sm), eropium (Eu) and gadolinium (Gd)

HG

high grade

SG

specific gravity

High-Ti

high titanium basalt

SOFC

solid oxide fuel cells

HMI

Human Machine Interface

SPCC

spill prevention, control, and countermeasure

hp

horsepower

SPLP

synthetic precipitation leach procedure

HPGR

High Pressure Grinding Rolls

SPT

standard penetration testing

HQ

standard diamond drill core size; 2.5in diameter

SRCE

Standardized Reclamation Cost Estimator

HREO

Heavy Rare Earth Oxide (Samarium through Lutetium incl. Yttrium)

SSF

surge storage facility

HsSO4

sulfuric acid

t

tonne (metric ton) (2,204.6 pounds)

HTW

horizontal true width

t/d

tonnes per day

ICP

induced couple plasma

t/h

tonnes per hour

ID2

Inverse-Distance Squared

t/m3

tonnes per cubic meter

IFC

International Finance Corporation

t/y

tonnes per year

ILS

intermediate leach solution

TCLP

toxicity characteristic leaching procedure

IRR

internal rate of return

TiCl4

titanium tetrachloride

kA

kiloamperes

TiO2

Titanium Dioxide

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Abbreviation

Unit or Term

Abbreviation

Unit or Term

kg

kilogram

ton

short ton (2,000 pounds)

kg/m2

Kilogram per cubic meter

TREO

Total Rare Earth Oxide

kg/m3

Kilogram per square meter

TSF

tailings storage facility

km

kilometer

TSP

total suspended particulates

km2

square kilometer

UCC

Underground Control Center

koz

thousand troy ounce

UCS

uniaxial compressive strength

kt

thousand tonnes

UDS

underground distribution systems

kt/d

thousand tonnes per day

UG

underground

kt/y

thousand tonnes per year

UIC

underground injection control

kV

kilovolt

USACE

U.S. Army Corps of Engineers

kW

kilowatt

USD

US Dollars

kWh

kilowatt-hour

USGS

United States Geological Survey

kWh/t

kilowatt-hour per metric tonne

UTM

Universal Transverse Mercator

L

liter

V

volts

L/s

liters per second

VFD

variable frequency drive

L/s/m

liters per second per meter

VOD

ventilation on demand

lb

pound

W

watt

LG

low grade

XRD

x-ray diffraction

LHD

long-haul dump truck

XRF

x-ray fluorescence

LLDDP

linear low-density polyethylene plastic

y

year

 

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

25 Reliance on Information Provided By the Registrant

In preparing this Technical Report Summary, Qualified Persons have relied upon certain information provided by NioCorp and its professional advisors in areas outside the Qualified Persons' respective fields of expertise. Such reliance is limited to matters permitted under Regulation S-K 1300 and includes, as applicable, information concerning mineral title and tenure, surface rights, legal agreements, royalties and encumbrances, permitting, environmental obligations, taxation, governmental matters, stakeholder agreements, and commercial arrangements.

The Qualified Persons have reviewed the information provided to the extent considered appropriate for the purposes of this Technical Report Summary. The categories of information relied upon, the portions of the Technical Report Summary affected by such reliance, the extent of reliance, and the basis upon which the Qualified Persons consider such reliance reasonable are summarized in Table 25-1.

Table 25‑1: Information supplied by Registrant

Category

Information / Source

TRS Section

Extent of Reliance

Basis for Reasonable Reliance

Mineral Tenure

Title information supplied by Registrant/legal counsel

Section 3

Used to describe ownership, mineral rights and tenure

Legal matters are outside the QP's expertise and information was prepared/reviewed by qualified legal counsel

Permitting

Permit register supplied by Registrant/environmental consultant

Section 17

Used to describe current permit status

Information maintained by project personnel responsible for permitting

Environmental

Environmental studies and liabilities supplied by Registrant

Section 17

Used in assessment of environmental obligations and closure requirements

Prepared by appropriately qualified environmental specialists

Taxation

Tax assumptions supplied by Registrant/tax advisors

Section 19

Incorporated into economic analysis

Tax matters are outside QP expertise, and assumptions were supplied by qualified advisors

Offtake / Contracts

Commercial terms supplied by Registrant

Sections 16/19

Used in revenue and economic assumptions

Commercial agreements maintained by Registrant

 

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

26 Signature Page

This TRS entitled “SK-1300 Technical Report Summary – Elk Creek Project, Nebraska”, with an effective date of June 30, 2026, was prepared and signed by:

 

Dahrouge Geological Consulting USA Ltd.

Signed and dated at Centennial, CO

Date: September 23, 2026

/s/ Trevor Mills

 

on behalf of Dahrouge Geological Consulting USA Ltd.

SMH Process Innovation

Signed and dated at West Jordan, UT

Date: September 23, 2026

/s/ Eric Larochelle

 

on behalf of SMH Process Innovation

Dumas Contracting USA Inc.

Signed and dated at Timmins, ON, Canada

Date: September 23, 2026

/s/ Tony Linton

 

on behalf of Dumas Contracting USA Inc.

Amplify Mine Planning LLC

Signed and dated at Denver, CO

Date: September 23, 2026

/s/ Scott Britton

 

on behalf of Amplify Mine Planning LLC

BBA Consultants International LP

Signed and dated at Ridgway, CO

Date: September 23, 2026

/s/ Troy Meyer

 

on behalf of BBA Consultants International LP

Adrian Brown Consultants Inc.

Signed and dated at Granby, CO

Date: September 23, 2026

/s/ Adrian Brown

 

on behalf of Adrian Brown Consultants Inc.

Olsson

Signed and dated at Omaha, NE

Date: September 23, 2026

/s/ Brian Osborn

 

on behalf of Olsson

Andrieux & Associates Geomechanics Consulting, L.P.

Signed and dated at Nain, NL, Canada

Date: September 23, 2026

/s/ Patrick Andrieux

 

on behalf of Andrieux & Associates Geomechanics Consulting, L.P.

Tetra Tech

Signed and dated at Salt Lake City, UT

Date: September 23, 2026

/s/ David Winters

 

on behalf of Tetra Tech.

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SK-1300 Technical Report Summary – Elk Creek Project, Nebraska

NioCorp Developments Ltd.

Metallurgy Concept Solutions

Signed and dated at Montreal, QC

Date: September 23, 2026

/s/ Sylvain Harton

 

on behalf of Metallurgy Concept Solutions

Magemi Mining Inc.

Signed and dated at Toronto, ON

Date: September 23, 2026

/s/ Georgi Doundarov

 

on behalf of Magemi Mining Inc.

T Engineering

Signed and dated at Montreal, QC

Date: September 23, 2026

/s/ Bernie Ting

 

on behalf of T Engineering

Scott Honan, M.Sc., SME-RM, NioCorp

Signed and dated at Centennial, CO

Date: September 23, 2026

/s/ Scott Honan

 

 

 

 

 

496 | Page