This technical report describes the mineral processing and metallurgical testing approaches for the Lalor mine and associated Snow Lake satellite deposits, with ore processed at the Stall and New Britannia concentrators.
Report context
This Form 43-101F1 Technical Report, dated 2021, covers the Lalor Mine and nearby Snow Lake satellite deposits in Manitoba, Canada. The report presents a mine plan that contemplates 5,300 tonnes per day of base metal, gold and copper-gold ore feed to the Stall and New Britannia concentrators, with the New Britannia mill under refurbishment and planned start-up in spring 2021.
Processing route
Existing processing infrastructure
Hudbay operates two ore concentrators: the Stall mill located approximately 16 km from Lalor and the Flin Flon mill located in Flin Flon. The Stall mill is currently operating seven days per week, producing at or above 3,800 tpd. The Stall mill has two circuits with design capacities of 900 tpd and 2,180 tpd.
Both concentrators have two flotation circuits producing a zinc concentrate and a copper concentrate. The zinc concentrate produced at Stall is hauled by truck to Hudbay metallurgical facilities in Flin Flon. The copper concentrates are sold to market. The tailings from the Stall mill are deposited in the Anderson Tailings Impoundment Area or used at the paste plant.
During the 2021-2022 period, although 100% of Lalor's production will be processed at the Stall or New Britannia mills, any additional production could be trucked to the Flin Flon mill until this facility shuts down at the same time as the zinc plant closes.
New Britannia mill
The New Britannia mill is located approximately 16 km north of the Lalor mine and was under construction (refurbishment) with a planned start-up of operations in the spring of 2021. Historical production at the New Britannia mill saw throughput rates of up to 2,000 tpd based on the availability of ore from the underground operation. The mill infrastructure consists mainly of three buildings and houses the crusher and mill/gold circuits. There are two existing crusher buildings: primary and secondary. The primary building houses the jaw crusher, and the secondary building houses the cone crusher and screen deck, each building with associated conveyors. The existing mill building contains the grinding and gold circuits, elution, EW and refining. The outside equipment includes thickener and leach tanks.
Proposed processing configuration
Once the New Britannia mill becomes fully operational in the second half of 2021, the mine plan will target a production of 1,500 tonnes per day of gold ore, supplemented by 3,800 tonnes per day of base metal ore. The total production rate of Lalor is maintained at 5,300 t/d from the second half of 2022 until 2026.
The strategy for the 2021 mine plan at Lalor is to mine base metals of higher grade zinc while at the same time advancing the development required to start mining the gold and copper gold zones.
Stall mill configuration
The Stall mill processes base metal ore from Lalor. A traditional sequential Cu-Pb-Zn flotation circuit is used at Stall. Several metallurgical projects are being advanced to match the configuration of the mill to the requirement of the ore, including addressing the increasing Pb:Cu ratio, increasing gold recovery at Stall, and improving flotation recoveries through reduction of the feed size.
Paste plant
The Lalor paste plant was commissioned in the third quarter of 2018, is located northeast of the existing head frame complex, and is capable of delivering 165 tph solids (tails) or 93 m³/hr of paste. The paste plant is capable of varying the binder content in the paste to provide flexibility in the strength gained from the paste where higher and early strength may be required depending on mining method.
Tails are currently pumped from the Stall concentrator to the Anderson TIA and diverted, as needed, to the Anderson booster station. Two pipelines are installed between the Anderson booster pump station and the paste plant located at Lalor mine site, which are situated approximately 13 km apart.
Proposed upgrades
With the increase in the mineral reserves of the Lalor gold zones alongside additional satellite deposits, an opportunity exists to increase the throughput rate in the future. The study to date has identified that the tailings pipeline, pre-leach thickener and various minor pumping systems would require upgrade to accommodate the increased tonnage rate. In addition to the processing equipment upgrades, the study includes the upgrade of the pipeline corridor road to accommodate ore haulage from Stall to New Britannia to remove traffic from the public access road.
Metallurgical testwork
Several metallurgical projects are being advanced, including: confirming the amenability of the 1901 gold lenses to processing at the New Britannia mill, increasing gold recovery at Stall, and improving flotation recoveries through reduction of the feed size.
For the WIM deposit, seven metallurgical holes were completed for a total of 2,533 metres in 2019. Mineralization from these holes was sent off for metallurgical testwork. Results have confirmed that the mineralization at Wim could attain processing recoveries in copper, silver and gold similar to the ones estimated for the Lalor copper-gold zones.
For the 1901 deposit, in 2020 Hudbay completed a pre-feasibility study on the engineering and mineral processing of the 1901 measured and indicated mineral resources.
Processing satellite deposits
The 1901 deposit would be accessed by lateral development from the ramp and would use the existing surface infrastructures. The Pen II deposit, WIM deposit, and Watts deposit are within trucking distance to either Stall or New Britannia mill. The Watts deposit located within 200 km of the Snow Lake processing facilities offers additional opportunities to maximise the use of the Stall and New Britannia mills and/or extend their operating life.
Future operations timeline
While the Stall mill closes in 2031 based on mineral reserve estimates only, the New Britannia mill remains in operation for an additional six years until 2038 supported by the WIM and 3 zone mining production.
Key reported parameters
| Parameter | Value | Basis |
|---|---|---|
| Stall mill design capacity (circuit 1) | 900 tpd | Design |
| Stall mill design capacity (circuit 2) | 2,180 tpd | Design |
| Stall mill current throughput | 3,800 tpd | Actual operating data |
| New Britannia mill historical throughput | up to 2,000 tpd | Historical operating data |
| New Britannia mill planned gold ore throughput | 1,500 tpd | Proposed design |
| Base metal ore throughput supplement | 3,800 tpd | Proposed design |
| Total Lalor production rate (H2 2022-2026) | 5,300 t/d | Proposed design |
| Paste plant solids capacity | 165 tph | Design |
| Paste plant volumetric capacity | 93 m³/hr | Design |
| Zinc plant capacity (Flin Flon) | 115,000 tpa refined zinc | Design |
| WIM deposit metallurgical testwork | 7 holes, 2,533 m | Testwork |
| 1901 deposit metallurgical study | Pre-feasibility study | Testwork |
Technical qualifications
The author considers that the mineral resources and reserves as classified and reported comply with all disclosure in accordance with requirements and CIM Definitions. The author is not aware of any mining, metallurgical, infrastructure, permitting or other relevant factors that could materially affect the mineral reserve estimate.
Standard professional procedures were followed when preparing the contents of this Technical Report. Data used in this Technical Report has been verified where possible and the QP has no reason to believe that the data was not collected in a professional manner and no information has been withheld that would affect the conclusions made herein.
The information, conclusions, opinions, and estimates contained herein are based on: information available to Hudbay at the time of preparation of this Technical Report, and assumptions, conditions, and qualifications as set forth in this Technical Report.
All the relevant capital and operating expenditures required to execute the life of mine plan of the Snow Lake operations have been accounted for in the demonstration of economic viability of the mineral reserve estimates including growth and sustaining capital costs and operating costs for the mining, milling and refining activities as well as the attributable general and administrative costs.
Source: Lalor and Snow Lake Operations, Manitoba, Canada, Form 43-101F1 Technical Report, Section 17 – Recovery Methods, and relevant processing sections.
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.
Lalor Deposit — 2012 Pre-Feasibility Study Technical Report
This review of the 2012 Pre-Feasibility Study technical report summarizes the planned design of the Lalor concentrator, a new facility at the Snow Lake, Manitoba site, focusing on the conventional crushing, grinding, and flotation process.
The 2012 Pre-Feasibility Study for the Lalor Deposit details the design of a new concentrator complex to be located at the existing project site in Snow Lake, Manitoba. The facility is designed for a nominal throughput of 4,500 tonnes per day, operating 24 hours a day, 365 days a year, with scheduled downtime for maintenance. The processing plant is intended to produce a bulk copper-lead concentrate with gold and silver credits and a zinc concentrate, both for shipment by truck to Flin Flon.
Ore processing will use conventional crushing, grinding, and flotation methods. Coarse ore, as large as 610 mm in one dimension, will be withdrawn from the head frame ore bin and fed to a jaw crusher. The crushed discharge at minus 150 mm will be conveyed to an enclosed stockpile with a maximum capacity of 10,000 tonnes and a live capacity of approximately 2,000 tonnes. From the stockpile, ore is fed to a Semi Autogenous Grinding (SAG) mill operating in a closed circuit with a vibrating screen. The SAG mill discharge undersize is processed through primary cyclones, with the overflow, at a target P80 of 80 microns, flowing to the flotation circuit. Cyclone underflow is directed to a ball mill also operating in closed circuit with the cyclones.
A portion of the cyclone underflow is diverted to a flash flotation cell to recover liberated gold and copper, with the concentrate sent to a regrind circuit. The flotation feed is conditioned with reagents before entering a bulk copper-lead rougher/scavenger flotation circuit comprised of six tank cells in series. The rougher concentrate, along with the flash flotation concentrate, is reground to a target P80 of 30 microns. The reground bulk concentrate is cleaned in a closed three-stage tank cell flotation circuit. Tailings from the flotation circuit will be used to produce cemented paste backfill for the underground mine, with excess pumped to the existing Anderson Tailings Impoundment Area.
Critical Data
| Parameter | Value | Unit | Notes |
|---|---|---|---|
| Nominal throughput | 4,500 | tpd | Not stated |
| Coarse ore maximum size | 610 | mm | In one dimension |
| Crusher discharge top size | 150 | mm | Minus 150 mm |
| Stockpile maximum capacity | 10,000 | tonnes | Enclosed to minimize dust |
| Stockpile live capacity | 2,000 | tonnes | Approximately |
| Primary cyclone overflow target P80 | 80 | microns | Flotation feed |
| Regrind mill target P80 | 30 | microns | For bulk concentrate |
| Estimated water consumption | 2,768,000 | m³/yr | Total for the concentrator |
| Estimated fresh water consumption | 344,000 | m³/yr | 12.4% of total |
| Estimated reclaim water consumption | 2,424,000 | m³/yr | 87.6% of total from thickener overflows, TIA, and mine water |
| Estimated water consumption total | 1.69 | m³/tonne | Based on nominal throughput |
| Fresh water pipeline length | 13.3 | km | 150mm insulated polyethylene |
| Reclaim water pipeline length | 16.2 | km | 200mm insulated polyethylene |
| Fresh water pumps max flow | 91 | m³/h | Existing pumps to be replaced with larger units |
| Reclaim water pumps max flow | 233 | m³/h | Existing pumps to be replaced with larger units |
| Filter feed tank storage | 6 | hours | For paste backfill feed |
| Process water tank sources | Not stated | Not stated | Mine water first, then reclaim water |
Project website: https://gov.mb.ca/iem/geo/gis/activity/hudbay_minerals_inclalor_lake_deposit.html
Overview
The planned Lalor concentrator is designed as a conventional flotation plant with a nominal capacity of 4,500 tonnes per day. The process flowsheet incorporates a jaw crusher, a SAG mill, a ball mill, and a regrind mill for size reduction. Flotation is conducted in tank cells for bulk copper-lead and zinc recovery. The process water system is designed for high recirculation, sourcing from mine water and reclaim systems to minimize fresh water consumption.
Key Process Stages
Run-of-mine ore from the head frame bin is crushed in a jaw crusher before being conveyed to a crushed ore stockpile. Grinding is achieved in a SAG mill and ball mill circuit. A flash flotation cell is included to recover fine liberated gold and copper from the ball mill cyclone underflow. Flotation feed is conditioned with reagents and processed in a bulk copper-lead rougher/scavenger circuit followed by a three-stage cleaning circuit. Regrinding of the rougher concentrate to a P80 of 30 microns occurs before cleaning. The final concentrate is dewatered, and tailings are thickened for use as paste backfill or for deposition in the Anderson Tailings Impoundment Area.
Additional Interesting Data and Summary
The technical report states that flash flotation was not tested in the laboratory but was included in the flowsheet based on successful experience in the Flin Flon Concentrator for recovering fine gold. A significant portion of the water used in the process, approximately 87.6 percent, comes from reclaimed or mine sources. The paste backfill system includes a filter feed tank with six hours of storage capacity. The tailings pumping system will have a leak detection system installed along its full length. A small amount of fresh water will be required for applications where process water is not acceptable.
Key Processes
- Crushing
- Semi Autogenous Grinding (SAG) and ball milling
- Flash flotation for gold and copper recovery
- Bulk copper-lead and zinc flotation
- Regrinding
- Dewatering and paste backfill production
Source: Lalor Deposit , 2012 Pre-Feasibility Study Technical Report, 2012.
Project website: Lalor Deposit, 2012 Pre-Feasibility Study Technical Report


