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Leading Edge Materials Announces Positive Preliminary Economic Assessment Results FOR Its Norra Karr REE Project with US$1,026M Pre-Tax NPV (10%) and 30.8% Pre-Tax IRR

Economic Studies

NEWS RELEASE July 22, 2021

LEADING EDGE MATERIALS CORP.

1305 – 1090 West Georgia Street, Vancouver, BC, V6E 3V7

[email protected] | www.leadingedgematerials.com

TSX.V: LEM | Nasdaq First North: LEMSE | OTCQB: LEMIF

TSX.V: LEM | Nasdaq First North: LEMSE | OTCQB: LEMIF

LEADING EDGE MATERIALS ANNOUNCES POSITIVE PRELIMINARY ECONOMIC

ASSESSMENT RESULTS FOR ITS NORRA KARR REE PROJECT WITH US$1,026M

PRE-TAX NPV (10%) AND 30.8% PRE-TAX IRR

Vancouver, July 22, 2021 – Leading Edge Materials Corp. (“Leading Edge Materials” or

the “Company”) (TSXV: LEM) (Nasdaq First North: LEMSE) (OTCQB: LEMIF) is pleased to

announce the results of a Preliminary Economic Assessment study ("PEA" or the “Report”)

for the development of its 100%-owned Norra Karr REE project located in Sweden (“Norra

Karr” or the “Project”). The PEA was prepared by SRK (UK) Ltd. (“SRK”) and all figures in the

PEA are US dollars unless otherwise specified.

As previously announced, the Company commissioned SRK to re-evaluate the Project at

PEA level with the objective to improve resource utilization, project sustainability and

substantially minimize environmental footprint of the Project compared to the design in

the pre-feasibility study which was released in 20151 (the “2015 PFS”) and formed the

basis for the current mining lease permitting process.

Main PEA Highlights (In comparison to the 2015 PFS)

• Significant increase in resource utilization by proposing recovery of nepheline

syenite (NS) industrial mineral, zirconium oxide (Zr) and niobium oxide (Nb)

products in addition to the rare earth oxide (“REO”) products. In the PEA more than

50% of total mined material is planned to be sold as products compared with

previously less than 1% in the 2015 PFS. The PEA also identifies future

opportunities to valorize the residual mined material which could potentially result

in all mineralized material mined to be treated as potential commercial products.

• Introducing a revised Project flowsheet to minimize the environmental footprint at

the Norra Karr site:

o The Norra Karr site will only include mining and comminution methods

consisting of crushing, milling and magnetic separation, eliminating all

chemical processing from Norra Karr and associated waste vs the 2015 PFS

study. In the PEA following physical separation resulting material streams

either are shipped as products or as concentrates for further processing at

other locations and a single waste stream to be stored at the Norra Karr

site.

1 See National Instrument 43-101 report entitled "Amended & Restated Prefeasibility Study - NI-101 - Technical report for

the Norra Karr Rare Earth Element Deposit" prepared for Tasman Metals Ltd. with effective date January 13, 2015 and issue

date July 10, 2015. See Tasman Metals Ltd. SEDAR profile on www.sedar.ca for report and more information.

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o The rare earth, zirconium and niobium bearing concentrate will be

transported to a dedicated off-site location for chemical processing and

further recovery.

• The combination of the above, results in a single waste stream at the Norra Karr

site consisting of the mineral aegirine which can be dry stacked in a lined

impoundment together with waste rock from mining, eliminating the need for a

wet tailings storage facility. This new design substantially reduces land area usage

of the Project by approximately 80% (see Figure 1) and results in no chemical

process tailing dams being required at Norra Karr. These changes considerably

reduce the environment risk profile of the Project at Norra Karr.

• In addition, the removal of chemical processing and wet tailings at Norra Karr

delivers an overall predicted 51% reduction in water requirements over the life of

mine vs the 2015 PFS study. Use of mine dewatering for processing can reduce

additional water requirements by almost 100% and the elimination of discharge

requirements to local water bodies compared with the 2015 PFS design.

• The PEA introduces the design of an off-site chemical recovery plant located close

to reagent supplies within an existing brownfield development area where mixed

REO (MREO), Zr and Nb products are planned to be recovered. Residual process

waste at the off-site facility consists of neutralized leach residue and gypsum

disposed of in geomembrane lined dry stack impoundments. The Report identifies

the future potential to further process the gypsum waste into a gypsum product

for construction material markets.

The PEA is preliminary in nature, it includes inferred mineral resources that are

considered too speculative geologically to have the economic considerations applied to

them that would enable them to be categorized as mineral reserves, and there is no

certainty that the PEA will be realized.

Filip Kozlowski, CEO of Leading Edge Materials states “I am very excited to share these

important PEA results, having more than met the strategic goals we set out to achieve. Norra

Karr is a globally recognized significant rare earth project, and the re-evaluated design

strengthens the sustainability, economics and resiliency of the project. By moving chemical

processing off-site, and significantly improving resource utilization we have shown the

opportunity to eliminate the need for a wet tailings storage. Adding further revenue streams

improves the resiliency and cost competitiveness of the project relative to current dominant

supply of rare earths from China. Norra Karr offers a rare opportunity for the European

Commission’s ambitions to develop a sustainable and secure EU based value chain for rare

earths and permanent magnets and we now have a much better path ahead of us.”

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Figure 1 – Graphical illustration of Norra Karr On-site open pit, waste rock facility and physical

beneficiation plant in comparison to 2015 PFS infrastructure and tailings dam (in red)

Project Financial Highlights

• Pre- and post-tax Net Present Value (NPV) of $1,026M and $762M using a 10%

discount rate

• Pre- and Post-tax Internal Rate of Return (IRR) of 30.8% and 26.3%

• Accumulated LoM project revenues of $9,962M

• Average annual EBITDA of $206M

• Initial Capital Expenditures (CAPEX) of $487M

• Pre-tax Payback Period from first production of 5.1 years

• Life of mine average gross basket price per kg of separated mixed REO product at

$53

• Operating cost per kg of separated mixed REO product at $33 including toll

separation charges

• By-product revenue per kg of separated mixed REO product $19

Operational Highlights

• Life of Mine (LOM) is 26 years

• LOM average annual

o Mining rate of 1,150,000 tonnes

o strip ratio of 0.32

o TREO 5,341 tonnes

o Main magnet rare earth oxides (“MagREO”) (Nd, Pr, Dy, Tb) 1,005 tonnes

▪ Dy2O3: 248 tonnes

▪ Tb2O3: 36 tonnes

▪ Nd2O3: 578 tonnes

▪ Pr2O3: 143 tonnes

o Nepheline Syenite co-product 732,885 tonnes

o Zirconium dioxide co-product 10,200 tonnes

o Niobium oxide co-product 525 tonnes

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Location and Infrastructure

On-site – Mining and comminution

The Norra Karr mine site is in the south central of the Kingdom of Sweden approximately

1.5 km from the eastern shore of Lake Vattern with the lake and the deposit separated by

the E4 highway. Advantageously situated close to both Swedish coasts, approximately

240km south-west of Stockholm and 160km east of Gothenburg. The nearest urban

settlement is Granna, 11km south by sealed road.

Regional road access from all major cities and ports to the project site is via the sealed

dual carriageway E4 highway and further local access is by all-weather sealed and

unsealed roads. Access to the national railway is approximately 30km east from the site

with a number of freight terminals in the regional area.

Currently the site is undeveloped within the perimeter and the area still maintains natural

vegetation, forestry plantations, cultivated farmlands and farmhouses. The PEA outlines

the buildings and installations required to support mining, physical comminution, waste

storage, materials handling and product logistics.

Off-site – Chemical leaching and recovery

The ultimate location for the off-site process facility is subject to detailed localization

studies between greenfield and brownfield options. For the purpose of the PEA an

existing brownfield location has been conceptually chosen to demonstrate the new

process flow design of the project. The chosen site is an existing brownfield industrial

area within easy reach of rail and port facilities located in the city of Lulea, Norrbotten

County in the north of Sweden, approximately 1200 km north of the Norra Karr site along

the E4 highway. Lulea has the seventh largest all-year round harbour in Sweden for

shipping goods from several mining districts, major chemical producers and a well-

established steel industry. The PEA outlines the buildings and installations required to

support chemical processing, waste storage, materials handling and product logistics.

Geology and Mineral Resource Estimate

Geologically, Norra Karr is a zoned agpaitic, peralkaline, nepheline syenite complex. The

alkaline intrusive REE-enriched body underwent compressive deformation and folding

during the Sveconorwegian shearing episodes.

The mineralization is relatively simple with nearly all the REE mineralization is hosted in

the zircono-silicate mineral eudialyte, which in itself is a complex mineral. The eudialyte

has been found to be relatively rich in REE’s, containing a high proportion of heavy rare

earth elements (HREE’s). The mineralized intrusive is an elongated body orientated in an

NNE-SSW direction, shallow dipping angles of 35°- 40° with an approximate strike length

of 1,300 m and 450 m in width. The Norra Karr deposit has the advantage that average

concentrations of uranium and thorium based on 9987 samples, U 11.4 ppm and Th 10.9

ppm, are extremely low compared with other REE deposits.

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Norra Karr was discovered as early as 1906 by SGU (Geological Survey of Sweden),

followed by trench bulk sampling work conducted by Boliden throughout the 1940’s and

1970’s. The first drilling campaigns took place under Tasman Metals between 2009-2012,

completing a total of 119 diamond drillholes for a total length of 20,420 m.

All of the mineral resource estimates are disclosed in accordance with the NI43-101

Standards of Disclosure for Mineral Projects and the classification of levels of confidence

are considered appropriate on the basis of drillhole spacing, sample interval, geological

interpretation, and all currently available assay data. Data obtained from the drilling

undertaken over the exploration permit was verified by WAI for the 2015 PFS and

reviewed by SRK for purpose of the mineral resource estimate in the PEA.

The Mineral Resource classification for the Norra Karr REE deposit is in accordance with

the guidelines of the CIM Definition Standards for Mineral Resources & Mineral Reserves

(CIM, 2014).

For the purpose of reporting the REE grades in the Mineral Resource block model were

converted to rare earth oxides using the conversion factors in Table 1.

Table 1 - Rare Earth (+zirconium and niobium) oxide conversion factors

Element Conversion Oxide Element Conversion Oxide

Ce 1.171 Ce2O3 Nd 1.166 Nd2O3

Dy 1.147 Dy2O3 Pr 1.17 Pr2O3

Er 1.143 Er2O3 Sm 1.159 Sm2O3

Eu 1.157 Eu2O3 Tb 1.151 Tb2O3

Gd 1.152 Gd2O3 Tm 1.142 Tm2O3

Ho 1.145 Ho2O3 Y 1.269 Y2O3

La 1.172 La2O3 Yb 1.138 Yb2O3

Lu 1.137 Lu2O3 Nb 1.431 Nb2O5

Zr 1.35 ZrO2

Table 2 - Norra Karr Mineral Resource Statement (SRK, 2021)*

Mineral Resource

Classification

Tonnes

(Mt)

TREO

(%)

HREO

(%)

ZrO2

(%)

Nb2O5

(%)

Nepheline Syenite

(%)

Inferred 110 0.5 0.27 1.7 0.05 65

*Notes:

1. Effective date 20 July 2021.

2. Qualified Person Mr Martin Pittuck

3. Mineral resources that are not mineral reserves do not have demonstrated economic viability. Mineral Resources are not Mineral

Reserves until they have Indicated or Measured confidence and they have modifying factors applied and they have demonstrated

economic viability based on a Feasibility Study or Prefeasibility Study.

4. The Mineral Resources reported have been constrained using an open pit shell assuming the deposit will be mined using open

pit bulk mining methods, above a cut -off grade of USD150/t ., including a 30% premium on projected commodity prices and

unconstrained by commodity production rates and the 260m highway buffer zone.

5. The Mineral Resources reported represent estimated contained metal in the ground and has not been adjusted for metallurgical

recovery.

6. Total Rare Earth Oxides (TREO) includes: La 2O3, Ce2O3, Pr2O3, Nd 2O3, Sm2O3, Eu 2O3, Gd 2O3, Tb 2O3, Dy 2O3, Ho 2O3, Er 2O3, Tm2O3,

Yb2O3, Lu2O3, Y2O3.

7. Heavy Rare Earth Oxides (HREO) include: Eu2O3, Gd2O3, Tb2O3, Dy2O3, Ho2O3, Er2O3, Tm2O3, Yb2O3, Lu2O3, Y2O3.

8. HREO is 54% of TREO

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The PEA is preliminary in nature, it includes inferred mineral resources that are considered too

speculative geologically to have the economic considerations applied to them that would enable them

to be categorized as mineral reserves, and there is no certainty that the PEA will be realized. The

rationale for re-evaluation of the Project at the PEA level is justified for the following reasons;

Recognition of potentially economic commodities in the mineralization not evaluated in the 2015 PFS,

namely nepheline syenite, niobium and zircon, recognition of the need to reduce the project footprint

and assess alternatives to a large tailing's facility at the mine site, and the need to minimize waste on

the project and have greater utilization of the extracted materials. The Company does not expect the

mineral resource estimates contained in the PEA to be materially affected by metallurgical,

environmental, permitting, legal, taxation, socio-economic, political, and marketing or other relevant

issues.

Mining

The mine planning work for the PEA was carried out using a mining model, which was

generated from the mineral resource model. An optimal pit shell was chosen based on

the highest average discounted cashflow assuming a production rate of 1.15 Mtpa of

plant feed and a discount rate of 10%. The generated extraction schedule and pit design

also sought to maximize the potential for waste backfill quantities which results in a four

staged approach which provides a 25 year LOM, a total of 29.3 Mt of run-of-mine (ROM)

and a total of 9.4 Mt of waste for an average strip ratio of 0.32. The staged approach

commences with the planned 1.15mtpa crusher feed target, which is expected to be met

starting in Year 1 due to the limited waste stripping requirements. The mine schedule

sequence starts in Stage 1, with Stage 2 commencing in Year 2. Stage 3 begins in Year 3,

while Stage 4 is delayed until Year 16 to maximize backfill options. The total production

averages 1,625 ktpa from Year 3 to 9, after which the total material movement decreases

as the strip ratio in Stage 3 decreases. Waste stripping requirements increase starting in

Year 16 as Stage 4 begins, averaging 1.8 Mtpa until Year 20. The delay of Stage 4 allows

for 1.9 Mt or 21% of total waste to be backfilled in the pit void.

Figure 2 – Open pit and waste rock facility through the different stages

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Mining equipment includes two 5.5 m3 excavators with up to six 46.8 t payload haul trucks

and in addition a stockpile loader and two 110 mm drills. Although there was no readily

available electric mining equipment to consider for the purpose of the PEA this option

was noted as a future opportunity to further increase the sustainability merits of the

Project.

The waste rock storage plan is designed to minimise the waste footprint by pit backfill in

the northern part of the pit once that area has been mined as well as an external waste

dump. The external waste dump design has a capacity of 8.8M loose cubic meters. The

backfill waste dump design has a capacity of 1.35 m loose cubic meters. It is also expected

that some of the waste mined in the earlier years of the operation will be used for

construction purposes as required.

Processing Overview

In the 2015 PFS, chemical processing for leaching and recovery of REO was envisioned to

occur on site. This required a large tailings storage facility and comprehensive water

treatment to ensure environmental protection. Even with this, considerable risk was

perceived to the processing operation and waste storage in local proximity to a number

of designated natural protection areas.

In order to reduce any risk of potentially hazardous substances away from the

environmentally sensitive areas the PEA re-evaluation proposes to move the chemical

processing to a more suitable off-site location. The on-site mine site will only include

physical comminution and magnetic separation, eliminating chemically leached waste

streams and the need for toxic reagents at site.

The PEA demonstrates the potential to produce a eudialyte concentrate at site through

crushing, milling and a two-stage magnetic separation. This concentrate is shipped to an

off-site chemical processing facility elsewhere in Sweden, close to a well-established

chemical industry allowing reagents to be readily supplied, reducing the carbon footprint

of the reagents and any transport risks and costs associated. Availability of cost

competitive and low carbon footprint hydropower electricity in the region for the off-site

facility offers a reduction in operating costs and climate impact for the energy intensive

process. The proposed conceptual flowsheet is provided in Figure 3.

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Figure 3 – On-site and Off-site high-level flow sheets as used in the PEA

For the PEA, SRK has relied on past testwork, both prior and subsequent to the 2015 PFS

and industry accepted practices as a basis for the redesigned flowsheet. The process

design criteria in Table 3 and Table 4 formed the operational basis for the process

flowsheet design.

Table 3 - Process design criteria

Description Magnitude Unit

On site process plant throughput 1150 000 t/a

ROM TREO grade 0.56 %

ROM Zr grade 1.86 %

ROM Nb grade 0.06 %

Contained TREO 6,946 t/a

Contained Zr 21,394 t/a

Contained Nb 657 t/a

Process plant operation 24/7/365 -

Crushing mechanical availability 80 %

Griding and beneficiation availability 91 %

Hydrometallurgy plant availability 91 %

On-site

Off-site