Rook I Project — 2021 Technical Report

This feasibility study presents a proposed uranium processing plant design for the Arrow deposit at the Rook I Project in Saskatchewan.

Report context

This NI 43-101 Technical Report on the Arrow Deposit, Rook I Project in Saskatchewan presents the results of a feasibility study completed in February 2021. The report documents proposed process plant design, mine infrastructure, capital and operating cost estimates, and economic analysis for the project. The study was prepared by Stantec Consulting Ltd., Wood Canada Ltd., RPA (now part of SLR Consulting Ltd.), and Golder Associates. The effective date of the Mineral Resource estimate is February 2021. The project is located in northern Saskatchewan and is based on the Arrow uranium deposit.

Processing route

Ore sorting and grinding

The process plant design is based on metallurgical testing and on unit processes successfully used in uranium process plants across the world, including plants in northern Saskatchewan. The proposed plant will include ore sorting and grinding as initial steps. Plant throughput is designed at 1,300 t/d with design production of 30 million pounds U₃O₈ per annum. A 3-month ramp-up period is expected to reach design throughput.

Leaching and liquid-solid separation

Following grinding, the process includes leaching, then liquid-solid separation via counter current decantation and clarification.

Solvent extraction and precipitation

The process continues with solvent extraction (SX), followed by gypsum precipitation and washing, then yellowcake (YC) precipitation and washing, and finally YC drying, calcining and packaging.

Tailings preparation and effluent treatment

The design of tailings preparation has been improved to facilitate a more reliable tailings deposition strategy through the paste plant. The process plant includes tailings preparation and paste tailings plant, and effluent treatment.

Water supply and reagent requirements

Water from the settling pond and fresh water from Patterson Lake will be fed to the process plant. The amount of water recycled from the settling pond has been further optimized to reduce fresh water requirements by using settling pond water for counter current decantation (CCD) wash water and using belt filter filtrate for paste process water.

Major reagents required will include sulphur, sulphuric acid, unslaked lime, hydrogen peroxide, flocculant, kerosene, tertiary amine, isodecanol, sodium carbonate, magnesia, barium chloride and ferric sulphate.

Power requirements

The process plant will require approximately 7.4 megawatts (MW) of power to operate at full capacity. The paste plant will require approximately 0.9 MW of power.

Ore and special waste stockpiles

There will be an ore stockpile consisting of four piles of differing grades, each approximately 6,500 m³. It is estimated that about 1% of waste rock brought to surface will be mineralized but below economic grade, and this material is stored in a special waste rock stockpile area with an anticipated volume of 60,000 m³. The special waste will be processed during normal operations to ensure the mill head grade remains below the 5% U₃O₈ design limit, with remaining special waste processed at end of mine life. Both ore and special waste stockpiles will be dual lined with high-density polyethylene (HDPE) and designed as self-contained facilities capable of holding a full probable maximum precipitation (PMP) 24-hour event.

Process plant optimizations proposed

The report recommends further studies including: loaded strip acid recovery, gypsum belt filter optimization, YC particle size enhancement, YC belt filter optimization, clarifier optimization, paste plant optimization, geo-metallurgical characterization, and mine water pre-treatment technology. The total estimated cost for this program is $1.0–1.5 million.

Key reported parameters

Parameter Units Value Basis
Plant throughput t/d 1,300 Proposed design
Design production Mlb U₃O₈/a 30 Proposed design
Process plant power requirement MW 7.4 Proposed design
Paste plant power requirement MW 0.9 Proposed design
Mill head grade design limit % U₃O₈ 5 Design parameter
LNG power plant requirement MW 26.5 Proposed design
Nominal power demand MW 24.1 Design basis
Ore stockpile pile volume 6,500 each (four piles) Proposed design
Special waste stockpile volume 60,000 Proposed design
Total waste rock LOM Mm³ 5.9 Estimate
PAG waste rock Mm³ 4.6 (78%) Estimate
NPAG waste rock Mm³ 1.3 Estimate
Ramp-up period months 3 Expected
Capital estimate classification , AACE Class 3 Estimate
Capital estimate accuracy , ±15% Intended
Pre-tax NPV at 8% $ million 5,577 Economic analysis
Pre-tax IRR % 64.9 Economic analysis
Pre-tax payback period years 0.8 Economic analysis
Post-tax NPV at 8% $ million 3,465 Economic analysis
Post-tax IRR % 52.4 Economic analysis
Post-tax payback period years 0.9 Economic analysis
Uranium price assumption US$/lb U₃O₈ 50 Financial analysis
Exchange rate assumption C$:US$ 0.75 Financial analysis
Discount rate base case % 8 Economic analysis

Technical qualifications

Development and licensing approvals are not currently in place, and statutory permits, including environmental permits, are required to be granted prior to mine commencement. The environmental assessment (EA) process for the Rook I Project is in progress as of the effective date of this report, and no recommendations from the EA or licensing processes for future monitoring and/or management of environmental and social aspects have been determined. Contracts have currently not been entered into for the project. The capital cost estimate meets the classification standard for a Class 3 estimate with intended accuracy of ±15%, reported in Q4 2020 Canadian dollars. The report notes that if additional mining, technical, and engineering studies are conducted, these may alter the project assumptions and may result in changes to calendar timelines and information contained in the report.

*Source: Arrow Deposit, Rook I Project, Saskatchewan, NI 43-101 Technical Report on Feasibility Study, February 2021, Sections 1.0 (Summary) and 2.0 (Introduction).*

Mineral processing basics

Scroll to Top