Source: Lomiko Metals Inc (2026)
Website: https://lomiko.com/projects/la-loutre/
Critical Data
| Parameter | Value | Unit | Notes |
|---|---|---|---|
| Throughput | 4,750 | tpd | Nominal ore processing rate; 1,733,750 tpy |
| Mill Power | 12.5 | MW | Total installed power for major equipment |
| Target Grind Size | 3,000 | μm | SAG mill discharge screen undersize (3 mm bottom deck aperture) |
| Head Grade | 4.79 | % | Feed grade of graphitic carbon (Cg) |
| Recovery % | 93.0 | % | Overall graphite recovery to concentrate |
| Processing Capacity | 1,733,750 | tpy | Total ore processed per year |
| Energy Consumption | N/A | kWh/t | Not explicitly provided in the report; total installed power 12.5 MW |
| Water Consumption | 0.108 | m³/t | Make-up water: 514 m³/d for 4,750 tpd feed |
| Operating Hours | 24 | hours/day | Design basis; concentrator effective utilization 92% |
Overview
Lomiko Metals Inc. operates the La Loutre Graphite Project, a pre-feasibility stage development in Quebec, Canada. The mineral processing plant is designed to treat 1.7 million tonnes per year of ore using a conventional flotation-based recovery method that maximizes graphite flake size and concentrate purity. The flowsheet integrates crushing, semi-autogenous grinding (SAG), flash flotation, multi-stage cleaner flotation, and polishing steps to achieve a blended graphite concentrate grade of 97.0% graphitic carbon (Cg) with an overall recovery of 93%. The plant will produce three size fractions — coarse (+80 mesh), intermediate (-80+200 mesh), and fine (-200 mesh) — totaling 79,601 dry tonnes per year. Designed to operate 24 hours per day, the concentrator achieves 92% effective utilization, while the crushing circuit runs at 66.7% utilization. The recovery process was developed from extensive metallurgical test programs and is tailored to minimize flake degradation. Key reagents include diesel as a collector and methyl isobutyl carbinol (MIBC) as a frother. Tailings are thickened, filtered, and dry-stacked to reduce environmental impact, with a desulphurization circuit planned to produce non-acid generating tailings. The project benefits from Canadian government support, with NRCan contributing $4.9 million (75% of project cost) for graphite anode piloting, expected to finalize in early 2027.
Key Process Stages
- Stage 1: Crushing and Stockpiling – Run-of-mine ore passes a static grizzly and vibrating grizzly screen (90 mm spacing). Oversize material is crushed by a 1,300 mm × 1,000 mm jaw crusher to a P80 of 105 mm. Tramp steel is removed via a self-cleaning permanent magnet before the ore is conveyed to a covered dome stockpile. Two apron feeders reclaim crushed material for the grinding circuit.
- Stage 2: Grinding and Classification – The SAG mill (7.3 m Ø × 3.1 m EGL, 2,600 kW) operates in closed circuit with a double-deck vibrating screen (8 mm top deck, 3 mm bottom deck). Screen undersize feeds the rougher flotation cell, while oversize is recirculated to the SAG mill. A hydrocyclone cluster further classifies material, with underflow returning to the SAG mill for additional grinding.
- Stage 3: Rougher and Scavenger Flotation – Flash flotation in a single 85 m³ cell recovers coarse graphite flakes before overgrinding. Rougher concentrate is sent to polishing. Rougher tails are classified, with cyclone overflow feeding a scavenger bank of four 20 m³ conventional flotation cells. Combined rougher and scavenger concentrate reaches ~25.7% Cg. Scavenger tails report to the tailings thickener.
- Stage 4: Polishing and Multi-Stage Cleaner Flotation – The combined concentrate passes through two polishing mills (6.1 m Ø and 4.3 m Ø, using ceramic media) to liberate gangue without reducing flake size. Four cleaner flotation stages (5 m³ cells) operate in series, with tailings recycled to the previous stage. Fourth cleaner concentrate achieves ~93.0% Cg and is screened at 80 mesh (177 µm) into coarse and fine streams, each undergoing dedicated stirred media milling and additional cleaner flotation stages (coarse: two stages; fine: three stages) to reach final concentrate grades of 96.6% Cg and 97.2% Cg, respectively.
- Stage 5: Concentrate Dewatering, Drying, and Packaging – The combined coarse and fine concentrates are filtered in a vertical plate pressure filter, producing a cake at 15% moisture. An indirect rotary natural gas dryer reduces moisture to 0.3%. Dried concentrate is pneumatically conveyed to a sifting system that yields three size fractions. Each fraction is stored in dedicated bins and packaged into 1.0 t bags, which are palletized and stretch-wrapped for shipment.
Additional Interesting Data and Summary
The La Loutre Graphite Project’s processing plant is designed with robust equipment to deliver high-grade graphite concentrate. The major mechanical equipment includes a single SAG mill (2,600 kW), two polishing mills (1,200 kW and 630 kW), multiple flotation cells totalling over 500 m³ of installed capacity, and two stirred media mills (90 kW each) for coarse and fine streams. The total installed power is 12.5 MW. Reagent consumption is low: less than 1 t/d each for diesel (collector) and MIBC (frother). Flocculant is used for tailings thickening. Water management emphasizes recycling, with make-up water of 514 m³/d sourced from pit dewatering and polishing ponds, and only 45 m³/d of additional process water make-up. The tailings dewatering circuit includes a 21 m diameter high-capacity thickener and a vertical plate filter press, producing a filter cake at 12% moisture for dry stacking. This reduces the environmental footprint and supports the project’s sustainability goals. The concentrator mass balance shows 4,750 dry t/d solids entering, with 318 t/d of final concentrate and 4,432 t/d of dry-stacked tailings. The concentrate is divided into three fractions: 24.0% coarse (+80 mesh), 45.1% intermediate (-80+200 mesh), and 30.8% fine (-200 mesh), enabling flexible market supply for lithium-ion battery anodes and other industrial applications. The project has strong economic significance, producing 79,601 tpy of 97.0% Cg concentrate at 93% recovery from a 4.79% feed grade. Environmental considerations include a low-sulfur tailings product through desulphurization, and the use of dry stack tailings storage eliminates the need for conventional tailings ponds. The future outlook is positive: with NRCan funding of $4.9 million, graphite anode piloting is ongoing and expected to finalize in early 2027, further validating the product for battery markets. This pre-feasibility study, based on metallurgical test work and flowsheet development, positions La Loutre as a significant potential supplier of high-purity, large-flake graphite concentrate for the growing electric vehicle and energy storage sectors.
Key Processes: Flotation, Gravity Separation, SAG Mill, Crushing
Target Commodities: N/A
Consolidated report summaries
The following former standalone pages about this operation were consolidated here on October 25, 2026. They are retained for source traceability; dates and figures reflect each report’s own effective date and may be superseded by the current information above.
La Loutre Graphite Project — 2021 Technical Report
This 2021 technical report and preliminary economic assessment presents a conceptual graphite processing route for the La Loutre project, based on historical testwork and proposed flowsheet design.
Report context
The La Loutre Graphite Project 2021 Technical Report, dated September 10, 2021, constitutes a National Instrument 43-101 technical report and preliminary economic assessment. The effective date of the mineral resource estimate presented in this report is May 14, 2021. The report includes sections on geology and mineralization, exploration and drilling, metallurgical testwork, mineral resource estimates, mine plan, recovery methods, infrastructure, and capital and operating cost estimates.
Processing route
Metallurgical Testwork Background
Metallurgical testwork was conducted on composites from the La Loutre property. Table 13-1 details the metallurgical composites used, while Table 13-2 reports carbon speciation and total sulphur analysis, Table 13-3 presents whole rock analysis, and Table 13-4 provides ICP-scan results, all with values expressed in percent or grams per tonne as applicable. Size fraction analysis of combined concentrate from the Lac Loutre (sic) composite is presented in Table 1-1, showing the distribution of graphite concentrate across particle size fractions.
Proposed Processing Design
The report describes proposed recovery methods under Section 25.9, within the overall framework of a preliminary economic assessment. The processing route is conceptual in nature at this stage, based on the metallurgical characterization work completed. No specific flowsheet details are provided in the available report sections; the processing approach is derived from the mineralogical and metallurgical data collected during testwork programs.
Historical Processing Context
Historical operating data from previous work on the property is referenced through the metallurgical testwork results. Table 1-1, titled "Size Fraction Analysis of Combined Concentrate of LCT," provides analytical results that show testwork completed during the characterization of graphite mineralization from the La Loutre deposit.
Key reported parameters
| Parameter | Value | Units | Basis |
|---|---|---|---|
| Mineral resource estimate effective date | May 14, 2021 | , | Resource estimate |
| Size fraction analysis of combined concentrate | Refer to Table 1-1 | % retained | Testwork (historical) |
| Carbon speciation and total sulphur | Refer to Table 13-2 | % | Testwork |
| Whole rock analysis | Refer to Table 13-3 | % | Testwork |
| ICP-scan analysis | Refer to Table 13-4 | g/t | Testwork |
| Metallurgical composites | Refer to Table 13-1 | , | Testwork |
| Capital cost estimate | Table 1-4 summary | Canadian dollars | Proposed design (PEA level) |
| Operating cost estimate | Table 1-5 summary | Canadian dollars per tonne | Proposed design (PEA level) |
| Project life-of-mine cash flow assumptions | Table 1-6 summary | Various | Proposed design (PEA level) |
Project website: https://lomiko.com/fr/projets/projet-la-loutre/
Technical qualifications
This report is a preliminary economic assessment based on conceptual processing design and historical testwork data. The mineral resource estimate is not a mineral reserve and does not have demonstrated economic viability. The recovery methods described are proposed designs that have not been confirmed through detailed engineering. All cost estimates in Tables 1-4, 1-5, and 1-6 are at a preliminary level and subject to change. The processing route relies on metallurgical testwork that may require additional confirmation through further testing. The report identifies specific risks under Section 25.15.1 and opportunities under Section 25.15.2 that should be considered in evaluating the project. Recommendations for additional metallurgical testwork are provided in Section 26.4.
Source: La Loutre Graphite Project , N.I. 43-101 Technical Report and Preliminary Economic Assessment, September 10, 2021, Sections 25.9–25.15, Tables 1-1 through 1-6, and Tables 13-1 through 13-4.

