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Artemis Gold Inc
Symbol	ARTG
Shares Issued	198,714,588
Close 2024-02-21	C$ 7.04
Market Cap	C$ 1,398,950,700
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Artemis pegs Blackwater expansion NPV at $3.25-billion

2024-02-21 18:27 ET - News Release

Mr. Steven Dean reports

ARTEMIS GOLD ANNOUNCES RESULTS OF EXPANSION STUDY FOR BLACKWATER MINE

Artemis Gold Inc. has released the results of an expansion study for the Blackwater mine in Central British Columbia. Blackwater is a world-class, large-scale, advanced development project in a Tier 1 mining jurisdiction.

The construction of the Phase 1 processing plant of 6 million tonnes per annum ("Mtpa") is well advanced, and the expansion study considers that Phase 1 has been completed. The purpose of the expansion study is to optimize the timing of mine expansion through the advancing of Phase 2 to year 3 of operations at an increased production capacity of 15 Mtpa, and Phase 3 to year 7 of operations at an increased production capacity of 25 Mtpa. The expansions are expected to be funded from operating cash flows based on the input assumptions of the expansion study.

The expansion study is based on Blackwater's existing Proven and Probable Mineral Reserves and no changes were made to the Mineral Reserve and Mineral Resource estimates. The relevant capital and operating estimates have been updated to reflect 2024 cost estimates. The Company's Board of Directors is yet to commit to the acceleration of the Phase 2 expansion. A decision is expected to be considered in H2 2024.

Phase 1 Investments

In Q2 2023, Artemis Gold announced additional investments of approximately C$50 million in the Phase 1 scope of work to facilitate the potential fast-tracking of Phase 2. These additional investments were included in the Phase 1 guided initial capital cost of C$730-C$750 million and included additional structural steel and increased conveyor belt widths in the crushing circuits, as well as the introduction of variable-speed drives to the ball mill. Selected electrical components were also upgraded to facilitate the Phase 2 requirements and to include optionality in relation to the use of redundancy backup power sources. Other Phase 1 optimizations included upsizing of the oxygen plant coupled with down-shaft-sparging of oxygen to the pre-leach and carbon-in-leach ("CIL") trains, along with the optimization of the CIL layout to facilitate non-intrusive expansion to Phase 2, as well as full conversion of the detoxification process to remove the need for tanker-supplied liquid sulphur dioxide. At the end of December 2023, C$389 million of the guided initial capital had been spent, and C$615 million, or 84% of the lower end of the guided capital range, was fully contractually committed.

For the expansion study, the Phase 1 guided initial capital costs are considered to have been spent and are not included in the reported net present value. The net present value is reported net of the scheduled repayment of the PLF associated with Phase 1 of C$385 million and all gold and silver stream participations.

Infrastructure

On completion of Phase 1, the majority of infrastructure requirements for the Phase 2 expansion will already be in place, including the primary crushing circuit, water storage and distribution, hydro-electric power, maintenance workshops, laboratory, site administration buildings, warehouse and workforce facilities. Additional infrastructure required for Phase 2 includes a secondary crushing circuit, crushed ore stockpile, a second ball mill, a semi-autogenous ("SAG") grinding mill, the associated expansion of the mill, gold recovery and reagent buildings, additional leach and CIL tanks, expansion of the elution circuit, as well as the associated expansion of mobile maintenance infrastructure to support additional mining equipment.

Mining

The expansion study mine plan considers conventional open pit mining methods (drill-blast-load-haul) in all phases. Open pit mining operations are anticipated to run for 15 years, excluding pre-production mining. Following mining operations, stockpiled low-grade material is expected to be processed for an additional two years, resulting in a total mine life of 17 years. The open pit would be developed with a series of pushbacks. The initial stages would expose near-surface, high-grade, lower-strip-ratio ore providing mill feed over the early years of the project. The remaining stages expand the pit to the north and south, targeting progressively deeper ore.

Owner-managed mining and fleet maintenance operations are planned for 365 days/year, with two 12-hour shifts planned per day. Contractor drill and blast services are planned for the first three years of operations, with drill operations converting to an owner-operated function thereafter, and contractor blasting services continuing throughout the remaining life of operations. Mining will be undertaken using 600-tonne class hydraulic shovels, 400-tonne class hydraulic excavators, and 240-tonne payload class haul trucks. The initial drill and loading fleets are planned to be diesel-drive, with the expansion fleet for drill and loading being electric-drive. The haul fleet is currently assumed to be diesel-drive for the entire life of mine ("LOM"). The initial mine equipment fleet is paid back through a lease arrangement with the supplier the expansion fleet being funded from operating cash flows.

Details of mining volumes and material movements contemplated in the expansion study are included in Appendix A to this news release.

Metallurgy and Processing

Phase 1

The processing plant for Phase 1 comprises the following:

Three-stage crushing, consisting of a primary gyratory crusher, a secondary cone crusher and two tertiary cone crushers, each of which will be housed in stand-alone structures, with conveyors transporting material between each stage;
Crushed product will be stored in a crushed ore stockpile and conveyed to a dual-drive variable-speed ball mill for grinding, with the circuit being closed by cyclones. Gravity concentration will be incorporated into the grinding circuit using two centrifugal concentrators. An intensive cyanide leach unit will be used for recovering gold from the gravity concentrate;
The leach and adsorption circuits will consist of one pre-oxidation tank, two leach tanks and six CIL tanks fitted with mechanical agitators, with cyanide being added to the leach tanks and CIL tanks. The leach and adsorption circuit residence time will be 24 hours, with gravity flow between the pre-oxidation and leach tanks and interstage screens moving leached slurry between the tank units. The carbon will advance counter current to the main slurry flow during periodic transfers of slurry;
The loaded carbon will be treated in an AARL elution and electrowinning circuit consisting of an acid wash column and an elution column operating at 120degreeC. An electric heating system will provide the necessary temperature, and two additional heat exchangers will control the temperature around the circuit. An electric-powered rotary kiln operating at approximately 750degreeC will be used to reactivate carbon. Electrowinning will be carried out to recover gold and silver from the elution solution and the resulting metallic values will be dried and smelted into dore bars;
Cyanide destruction will be carried out in the final tailings slurry, using oxygen and the sulfur dioxide produced by the combustion of sulfur prill.

Phase 2 Expansion

The expansion study assumes the Phase 2 expansion to 15 Mtpa would be implemented with some modifications and upgrades to the Phase 1 process, including splitting the ore crushed in the primary crusher into two streams. One stream would be fed through the existing Phase 1 crushing and grinding circuits. Another stream would be processed with another secondary stage of crushing, stockpiling, followed by SAG and ball mill grinding. The rest of the plant circuits, including gravity concentration, leaching, adsorption, elution and cyanide destruction, as well as the process and reagent buildings would be expanded. Minor upgrades would be carried out on some infrastructure to accommodate the increased throughput. The capital cost estimate to complete the Phase 2 expansion is C$592 million.

Phase 3 Expansion

The Phase 3 expansion to 25 Mtpa would require a new process line comprised of two-stage crushing, stockpiling, SAG and ball mill grinding and other plant circuits similar to the processing methods of Phases 1 and 2. The capital cost estimate to complete the Phase 3 expansion is C$852 million.

Production Profile and Costs

The average annual production per the expansion study is 469,000 AuEq oz at an average AISC of US$781 per gold oz, with average gold equivalent production of greater than 500,000 oz per annum throughout Phases 2 and 3. AuEq oz are determined using a gold:silver ratio of 78:1 (or US$1,800 to US$23).

Operating Costs

Phase 1 operating costs are estimated at C$28.67/t milled, with economies of scale driving down the processing and G&A costs to achieve an average estimated operating cost of C$20.03/t milled over the LOM.

Selling Costs

The expansion study assumes payable factors on gold and silver of 99.9% and 95%, respectively. Refining, treatment, transport, and insurance charges have been included at C$3/oz, applied to gold equivalent ounces.

Hedging and Commodity Price Assumptions

The expansion study reflects the impact of the Company's hedge program in place as of the date of the study. This includes forward gold sales contracts to deliver a total of 190,000 ounces of gold bullion between March 2025 and December 2027 at a weighted average price of C$2,851/ounce, as well as zero cost collars for 30,000 oz gold with settlement dates from December 2024 to February 2025. The collars have a weighted average put price of C$2,600/oz and a weighted average call price of C$3,353/oz.

The commodity price assumptions for unhedged production and exchange rate assumptions in the expansion study were derived from market consensus forecasts and are as follows:

Taxes

The expansion study includes estimates for the following taxes:

British Columbia mining tax: 2% provincial minimum tax payable on net current proceeds which is creditable against the 13% effective mining tax rate which is calculated based on operating profit less applicable capital cost deductions. The mining tax is deductible in computing provincial and federal income tax;
British Columbia provincial income tax: 12.0%, payable after applicable deductions are made; Canadian federal income tax: 15.0%, payable after applicable deductions are made.

Economic Outputs

The expansion study returns a base case after-tax NPV5% of C$3.25 billion and takes into account the repayment of the PLF of $385 million, as well as the effect of the gold stream and silver stream arrangements.

Artemis Gold Chairman and CEO Steven Dean commented: "The expansion study underlines that Blackwater is a true tier one asset, with gold equivalent production in excess of 500,000 ounces per year once Phase 2 is implemented, with lowest-decile operating costs, in a safe, stable and mining-friendly jurisdiction, as well as industry-leading ESG."

The Study

The expansion study is led by Lycopodium Minerals Canada Ltd.("Lycopodium") together with Knight Piesold Ltd. ("KP"), Moose Mountain Technical Services ("MMTS"), ERM Consultants Ltd. ("ERM"), Lorax Environmental Services Ltd. ("Lorax") and JAT MetConsult Ltd. ("JAT MetConsult"), all of which are independent of the Company.

An updated Technical Report will be filed on SEDAR+ within 45 days of this news release.

Data Verification

Data verification programs have included a review of QA/QC data, re-sampling and sample analysis programs, and database verification. Validation checks were performed on data, and comprise checks on surveys, collar coordinates and assay data.

In the opinion of MMTS, sufficient verification checks were undertaken on the database to provide confidence that the database is virtually error-free and appropriate to support Mineral Resource and Reserve estimation.

Additional Opportunities

The expansion study does not reflect the following additional opportunities which the Company continues to evaluate:

Increased mine life - the current reserve estimate is based on a US$1,400/oz gold price. By applying a higher gold price for pit design and cut-off grade, some of Blackwater's estimated resources could be converted into reserves and extend the mine life. The next steps would include re-running a pit optimization incorporating updated gold pricing and mine economics to assess the potential for increased reserves and mine life.
Exploration of open resource extensions - past exploration data suggests Blackwater has additional exploration potential and that the resource is open to the North, Northwest and at depth. The Blackwater land package also remains largely under-explored. The next step will be to design an exploration program to test these extensions and the regional potential.
Evaluation of alternative methods for transportation of waste material - the ex-pit haul route for waste material is expected to be relatively fixed for the LOM, opening up the possibility to perform hauling of waste material using alternative methods which may have the potential to significantly reduce operating costs and lower Blackwater's greenhouse gas ("GHG") emissions. The next steps will include further engineering and analysis, including engaging with the vendors of these systems.
Electrification of the hauling fleet - the deployment of battery electric vehicles has the potential to significantly reduce operating costs and reduce Blackwater's GHG emissions. The Company is currently working with Caterpillar Technology to assess the economic potential for incorporation of battery electric vehicles into the mine fleet.
Automation of hauling operations - the potential to automate hauling operations presents an opportunity to optimize production efficiencies and reduce operating costs. The Company is currently undertaking the implementation of a fleet management system that would allow for potential automation of hauling operations in the future.
Process engineering initiatives - as Blackwater starts producing more fresh rock ore at depth in the pit, the Company may evaluate alternative processing methodologies which may result in lower capital and operating costs for Phase 3. The next steps would include an assessment of alternatives, preliminary flowsheet design, and identification of any additional metallurgical test work required to support further engineering.

Conference Call and Webinar

Live

Artemis Gold will host a conference call and webinar on Thursday, February 22, 2024 at 9am PT (12pm ET). Participants may dial in using the numbers below (no access code is needed).

Toll-free (Canada and US): 1 844 763 8274
International: +1 647 484 8814

The webinar may be accessed here.