from EV Nickel Inc. (isin : CA26928V1058)
EV Nickel Reports CarLang A PEA: Robust Economics for Large Scale Nickel Project
Pre-Tax NPV(8%) of $1.91 Billion
Post-Tax NPV(8%) of $1.48 Billion
Net C1 Cash Costs of US$4.36/lb Ni and Net AISC of US$4.87/lb Ni after by-product credits
Producing 1.6B lbs of payable Ni over 20 year mine life
Annual EBITDA of C$681 Million and Annual Free Cash of C$313 Million
(All amounts in Canadian Dollars unless otherwise indicated)
TORONTO, ON / ACCESS Newswire / May 5, 2025 / EV NICKEL INC. (TSX-V:EVNI) ("EVNi" or the "Company is pleased to report the results of a Preliminary Economic Assessment ("PEA") on its 100% owned CarLang A Nickel Project (the "Project"), located approximately 30 kilometres southeast of Timmins, Ontario. The PEA was prepared by SRK Consulting (Canada) Inc. ("SRK") and Caracle Creek International Consulting Inc. ("CCIC"). The updated PEA used a pit constrained Measured resource of 1,007 million tonnes ("Mt") grading 0.24% Ni, consisting of Indicated resource of 510 Mt grading 0.25% Ni and an Inferred mineral resource of 497 Mt grading 0.23% Niand was initially modeled with a 20-year mine life and 120,000 tonnes mined per day.
"This PEA Study demonstrates the excellent potential of the large scale CarLang A Nickel Project as a near surface, moderate capex production asset," said John Paterson, Interim President and CEO of EV Nickel. "The shallow overburden cover and low strip ratio significantly reduces the overall Capex of the CarLang A project and allows for a rapid ramp-up of production to meet the 120,000 tonnes per day mill design. We are excited by these results and continue to move forward, advancing the permitting and optimizing the mine design and processing facilities. EV Nickel continues to execute our Strategic Plan, de-risking the large scale CarLang A Nickel Project while continuing to explore for additional high-quality, large-scale nickel deposits along the CarLang Trend and throughout the Shaw Dome Project area."
"The CarLang A Nickel Deposit demonstrates the potential of the CarLang Trend to host large-scale zones of mineralization suitable for advancement towards a production decision with significant expansion potential," said Paul Davis, Vice President Exploration of EV Nickel. "When combined with our successful, ongoing exploration program, including the Gemini North Sulphide Nickel Zone, the CarLang Trend has the potential to expand into a significant area of multiple large-scale zones of nickel mineralization with similar, or better, nickel grades and recovery characteristics as the CarLang A Deposit. If the Company continues to be successful in defining additional zones of nickel mineralization within the CarLang Trend, then work can begin to determine the best sequencing of the area and realize the benefits of multiple zones allowing for the optimization project development and the tailings storage schedules, to extract the best zones early on, to maximize the potential project economics in the area, while limiting the overall environmental impacts. The CarLang Trend potentially represents an area that could host large-scale nickel zones that would continue for multiple decades within a contiguous, well-defined area that could feed a single processing facility, just south of Timmins, Ontario."
A Technical Report in support of the PEA will be filed on SEDAR (www.sedar.com) within 45 days of the date of this news release. The PEA is effective as of March 24, 2025.
CarLang A 2025 PEA Summary
Strong Economics (based on long term price and exchange rate assumptions)
$1.91 Billion Pre-Tax NPV(8%), 15% IRR
$1.48 Billion After-Tax NPV(8%), 14% IRR
Large Scale, Low Cost Project
Average annual production of 83 million pounds of nickel, 615 million tonnes of iron and 36.7 million pounds of chrome and 31 thousand pounds of cobalt
By-product credits associated with iron, chrome and cobalt
Life of Mine C1 Cash Costs of US$4.36/lb Ni; Net AISC Costs of US$4.87/lb nickel net of by-product credits (based on long term price and exchange rate assumptions)
20 year mine life totalling 753,000 tonnes of nickel
Low strip ratio of 0.38 reflective of thin overburden cover averaging 3 metres over the proposed open pit
Robust Project Economics
$681 Million of annual EBITDA
$360 Million of annual Free Cash Flow over the 20 years of production
A PEA is preliminary in nature and includes inferred mineral resources that are considered too geologically speculative to have economic considerations applied that would allow them to be categorized as mineral reserves whereby there is no certainty that the results of the PEA will be realized.
The key project metrics are summarized in Table 1 and Table 2.
Table 1: Life of Mine Physicals
Item | Units | Value |
Physicals (Mill Feed) | ||
Mill Feed | Mt | 840 |
Ni Feed Grade | % | 0.23 |
Co Feed Grade | % | 0.01 |
Cr Feed Grade | % | 0.23 |
Fe Feed Grade | % | 5.33 |
S Feed Grade | % | 0.06 |
MgO Feed Grade | % | 37.0 |
S/Ni Feed Ratio | 0.25 | |
Ni Concentrate | ||
Ni Recovery | % | 14.6 |
Co Recovery | % | 2.2 |
Ni Concentrate Grade | % | 25.0 |
Co Concentrate Grade | % | 0.17 |
Ni Concentrate | Mt | 1,147 |
FeCr Concentrate | ||
Fe Recovery | % | 55.0 |
Cr Recovery | % | 26.3 |
Ni Recovery | % | 26.2 |
Fe Concentrate Grade | % | 48.0 |
Cr Concentrate Grade | % | 1.0 |
Ni Concentrate Grade | % | 1.0 |
FeCr Concentrate | Mt | 51,287 |
Salable Metal Total Recovery | ||
Ni Recovery | % | 40.8 |
Co Recovery | % | 2.2 |
Cr Recovery | % | 26.3 |
Fe Recovery | % | 55.0 |
Source: SRK 2025
Table 2: Economic Analysis Summary
Item | Units | Value (C$) | Value (US$) |
Payable Ni | Mlbs | 1,603 | 1,603 |
Net Smelter Return | $/t-milled | 27.93 | 19.55 |
Site Operating Costs | $/t-milled | 11.69 | 8.19 |
Net C1 Costs | $/lb Ni-Eq | 6.22 | 4.36 |
EBITDA | $/t-milled | 16.24 | 11.37 |
Total Capital | $M | 4,805 | 3,363 |
Initial Capital | $M | 3,317 | 2,322 |
Sustaining Capital | $M | 1,487 | 1,041 |
Net AISC | $/lb Ni-Eq | 6.96 | 4.87 |
Pre-Tax NPV0% | $M | 8,830 | 6,181 |
Pre-Tax NPV8% | $M | 1,917 | 1,342 |
Post-Tax IRR | % | 15 | 15 |
Post-Tax NPV0% | $M | 7,201 | 5,041 |
Post-Tax NPV8% | $M | 1,480 | 1,036 |
Post-Tax IRR | % | 14 | 14 |
Payback (from Project Start) | Yrs | 9 | 9 |
Payback (from Production) | Yrs | 6 | 6 |
Source: SRK 2025
The key assumptions used in the economic analysis are shown in Error! Reference source not found. 3.
Table 3: Economic Analysis Assumptions
Assumption | Units | Value |
Ni Price | US$/t | 20,000 |
Co Price | US$/t | 40,000 |
Fe Price | US$/dmt | 162 |
Cr Price | US$/lb | 1.75 |
Exchange Rate | US$:C$ | 0.70 |
Fuel Price | C$/L | 1.20 |
Electricity Cost | C$/kWh | 0.75 |
Royalty | % | - |
Source: SRK 2025
Project Opportunities
Significant potential related to a number of opportunities associated with the CarLang A Project for additional value have been identified including:
Additional near surface exploration potential along the 10 kilometres of strike length associated with the CarLang Trend.
Potential for higher grade nickel and sulphur zones within the CarLang Trend that could represents areas with significantly improved recovery characteristics including the recently identified Gemini North Zone located approximately 2.5 kilometres to the north of the CarLang A Deposit along the CarLang Trend.
Optimized processing of nickel concentrates to recover platinum group metals.
Capital cost reductions associated with mine scheduling and Tailings storage options.
Inclusion of Carbon Credits into the economic model related to the Carbon Capture Storage potential of the mine tailings and Carbon Footprint reductions with the incorporation of low-carbon, electric mining equipment.
Application of the Company's bioleaching process to the nickel concentrates with the potential to reduce smelting and refining costs and produce products directly for the electric battery market producers.
Project Overview
The CarLang A Project is designed as a conventional open pit mine/mill operation utilizing traditional mining and milling equipment. The project will develop two products including a high-grade nickel concentrate estimated at 25% nickel and a magnetite concentrate estimated at 48% iron and 1% chromium. Both of the products are assumed to be sold based on the nickel, iron, chromite and cobalt content of the concentrates.
The process plant will utilize a conventional milling operation consisting of crushing, grinding, desliming and flotation operations similar to other ultramafic hosted nickel operations. The processing plant will be constructed at a full capacity of 120,000 tonnes per day from the initiation of production.
Location and Infrastructure
The CarLang Nickel Property, within National Topographic System ("NTS") 1:50 000 map sheets 042A/06 (Timmins) and 042A/07 (Watabeag River), is situated in portions of Carman, Langmuir, and Shaw townships, Porcupine Mining Division, northeastern Ontario, Canada. The centre of the Property is approximately 30 km southeast of the City of Timmins.
The Property is accessed by motor vehicle via Tisdale Street (Forks River Road), which originates in South Porcupine (Timmins), travelling for about 15 km southward, after 15 km taking the left logging road diversion (Langmuir Road). Rail access is located nearby.
Regional 3-phase power lines extend south of Timmins following Forks River Road and supplying power to the Redstone Mill Facility and previously to the Carshaw Mill Site, 5 km west and 4 km northwest of the CarLang A Zone, respectively. A 500 kV transmission line runs along the western boundary of the Property to Timmins, about 18 km west of the CarLang A Zone Deposit. The project envisions that a 230 kV powerline will be constructed from Hydro One Porcupine Substation to the site, then step down the voltage as required to feed the various electricity consumers.
The other infrastructure to be developed for the project includes on site haul and service roads, water and power supply, mine waste rock and tailings storage facilities (TSF), processing facilities and site buildings.
Mining Method
The CarLang A deposit is expected to be mined using conventional open pit mining methods using trucks and shovels. The life of mine (LOM) is 20 years at a mill feed rate of 43.3 million tonnes per annum (Mtpa) and a maximum total material movement of 72 Mtpa. The mine schedule includes one year of pre-production to generate waste fill for the tailings management facility. The primary equipment will be 34 m3 shovels and 229 t haul trucks.
The resource model was regularized to 20x20x15 m, which resulted in 1.7% dilution and 0.1% loss. No additional factors were applied to the tonnes and grades. A revenue factor of 67% was selected from the pit optimization results as the basis of the pit design, which resulted in 840 Mt of plant feed at an average grade of 0.23% Ni with a strip ratio of 0.38.
Mineral Processing and Metallurgical Testing
Corem metallurgical laboratory was contracted to perform sample characterization and bench-scale laboratory testwork on A zone material, with the objective of producing saleable nickel sulphide and magnetite (or ferrochrome) concentrates. The lab flowsheet and conditions closely followed the results reported in the Canada Nickel Company Crawford technical reports.
A total of 20 intervals were selected for metallurgical testing from 2022 drilling performed by EVNi. Of the 20 samples, 11 were included in the 2024 testwork program and four were sent for quantitative mineralogical analysis. From the analysis of these samples, CarLang A zone mineralogy is highly variable in both nickel deportment as well as non-sulphide gangue that is independent of the consistent assays shown for Ni, Fe, S and MgO. While this also reported for the Crawford project, the quality of both nickel sulphide and magnetite concentrates may be at the lower end of the range expected from the Crawford process flowsheet. Continued metallurgical testing on A zone samples will better quantify this.
Limited optimization work was done but based on the testwork completed by Corem on 11 samples from the CarLang A zone, recoveries to a nickel sulphide concentrate and magnetite concentrate were estimated. These estimates are preliminary but are suitable for the mine plan completed by SRK. Considering the highly variable nature of the A zone test samples, further metallurgical testwork is recommended.
Recovery Methods
The CarLang A mineralization will be processed through a single, on-site plant with a design capacity of 120,000 tonnes per day, producing saleable nickel sulphide and magnetite concentrates.
The plant flowsheet includes crushing, grinding, sulphide flotation and magnetic separation to generate the two concentrates. Nickel sulphide recovery is done in stages with both coarse and fine flotation following grinding and deslime removal. Both concentrates are thickened and filtered prior to storage before transport off-site. The plant is based on average head grades of 0.23% Ni and 5.3% Fe.
Preliminary recoveries have been estimated at 5% to 20% Ni to the sulphide concentrate and 55% Fe and 20% Ni to the magnetite concentrate. The sulphide concentrate is assumed to be 25% Ni and 0.17% Co as payables with 25% MgO and 27% SiO2 as potential penalty elements. The magnetite concentrate is assumed to be 48% Fe and 1% Cr as payables with 15% MgO, 12% SiO2 and 0.04% S as potential penalty elements.
Capital and Operating Cost Estimate
The capital and operating costs have been estimated based on benchmarks of similar projects and on first principles where possible. Costs have been estimated to a scoping level of accuracy with capital costs summarized in Table 4 and operating costs in Table 5.
Table 4: Capital Cost Estimate Summary
Item | Unit | Initial Capital | Sustaining Capital | Total Capital | ||
Mining1 | M$ | 56 | 207 | 263 | ||
Mill2 | M$ | 2,263 | - | 2,263 | ||
On-Site Infrastructure | M$ | 166 | 16 | 182 | ||
Tailings & Water Management | M$ | 228 | 1,100 | 1,329 | ||
Closure Costs | M$ | 11 | 164 | 175 | ||
Construction Indirects & Owner Costs | M$ | 425 | - | 425 | ||
Total Project Capital | M$ | 3,150 | 1,487 | 4,637 | ||
Source: SRK 2025 |
Table 5: Operating Cost Estimate Summary
Item | LOM Total (M$) | Unit Cost ($/t-milled) | Unit Cost ($/t-mined) | |
Mining1 | 3,231 | 3.85 | 2.85 | |
Processing2 | 5,726 | 6.82 | 6.82 | |
General & Administrative | 671 | 0.80 | 0.80 | |
Tailings Management | 208 | 0.23 | 0.23 | |
Total Site Operating Cost | 9,818 | 11.69 | 10.69 | |
1 Mine operating costs exclude capitalized pre-production operating costs. 2 Processing operating costs include mill sustaining costs. |
Sensitivities
The key project economic indicators (NPV and IRR) are the most sensitive to exchange rate and metal prices, then capital expenditure, and the least sensitive to operating expenditure, see Figure 1 and Figure 2. The trends of the project sensitivity are generally in line with a typical greenfield mining project.