Source: Mkango Resources Ltd (2026)
Website: https://mkango.ca/projects/songwe/
Critical Data
| Parameter | Value | Unit | Notes |
|---|---|---|---|
| Throughput | 138 | t/h | Flotation plant feed rate (design) |
| Mill Power | N/A | kW | Not specified in source |
| Target Grind Size | 16.7 | μm P80 | Flotation feed particle size |
| Head Grade | 1.5 | % TREO | ROM feed grade |
| Recovery % | 74.1 | % | TREO recovery to concentrate |
| Processing Capacity | 1,000,000 | t/a | ROM feed rate per annum |
| Energy Consumption | N/A | kWh/t | Not specified in source |
| Water Consumption | N/A | m³/t | Not specified in source |
| Operating Hours | 24 | hours/day | Continuous operation, 8,760 h/a |
Overview
Mkango Resources Limited operates the Songwe Hill Rare Earth Element (REE) Project located in the south-eastern region of Malawi. The project, detailed in the NI 43-101 Updated Technical Report dated 29 April 2026 (effective 30 June 2025), targets production of a high-grade, cerium-depleted mixed rare earth carbonate (MREC) product. The significance of Songwe Hill lies in its ability to process a 1.5% TREO head grade ore using a two-circuit plant: a concentrator (crushing, grinding, flotation) and a hydrometallurgical refinery. The concentrator produces a 15% TREO flotation concentrate at 74.1% recovery, which is then treated in the hydrometallurgical plant via gangue leach, caustic conversion, cerium oxidation, and rare earth leach to produce 10,826 t/a of MREC solids containing 5,954 t/a of TREO. The process design is based on extensive test work, emphasizing fine grinding to a P80 of 16.7 μm, high-intensity conditioning, elevated temperature, and a tailored reagent suite to effectively float rare earth oxides from carbonaceous gangue. This integrated approach positions Songwe Hill as a strategically important rare earth project, with continuous 24/7 operation and robust metallurgical accounting via on-stream analysers and sampling systems.
Key Process Stages
- Stage 1: Crushing and Ball Milling – Run-of-mine ore is crushed through a primary jaw crusher, secondary and tertiary cone crushers with screens, then fed to a ball mill operating in closed circuit with hydrocyclones. The mill reduces ore to a target P80 for fine grinding; steel media addition is controlled via mill power draw. The circuit provides 8 hours of surge capacity in the mill feed bin, allowing for the 65% crushing plant availability.
- Stage 2: Ultra-Fine Grinding – Ball mill cyclone overflow gravitates to regrind mills (stirred media mills using ceramic media) in closed circuit with another cyclone cluster. Four duty mills operate in parallel with one standby to achieve the flotation feed particle size of P80 16.7 μm. Cyclone overflow passes through a trash screen to remove wood chips before entering flotation.
- Stage 3: Multi-Stage Flotation – The flotation circuit includes sulphide pre-float rougher and cleaner cells (collector & frother) to remove sulphides, followed by TREO rougher (4 cells), scavenger (2 cells), cleaner (4 cells), and cleaner scavenger (3 cells) flotation. Key to REO flotation is elevated temperature achieved by steam sparging in conditioning tanks, together with reagents M4P, M7, caustic soda, collector, and frother. Blower air is supplied via a low-pressure air reticulation system. All streams are monitored by an on-line stream analyser for process control.
- Stage 4: Concentrate Dewatering and Filtration – Cleaner flotation concentrate is thickened in a concentrate thickener with flocculant addition, then filtered by two duty filter presses operating in parallel staggered cycles. Filter cake is discharged onto conveyors for transport to the hydrometallurgical plant or to an emergency stockpile. Filtrate is returned to the thickener; final concentrate mass pull is 7.4% of feed.
- Stage 5: Hydrometallurgical Processing – The flotation concentrate undergoes gangue leach with dilute acid to dissolve acid-consuming minerals, with liquor purified to regenerate HCl and produce gypsum for sale. Residue then undergoes caustic conversion (concentrated NaOH at high temperature) to convert insoluble REE minerals to soluble hydroxides, followed by cerium oxidation (air sparging) to render cerium insoluble. A severe rare earth leach with HCl extracts REEs, and after purification (heavy metals/radionuclides removal), the liquor is precipitated as a mixed rare earth carbonate product. Tailings are neutralised and sent to the TSF.
Additional Interesting Data and Summary
The Songwe Hill processing facility is designed for a ROM feed rate of 1,000,000 t/a with a head grade of 1.5% TREO, yielding a flotation concentrate at 15% TREO grade and 74.1% recovery. The concentrator operates at 92% availability (flotation and hydrometallurgical plants) while crushing has 65% availability. The hydrometallurgical plant receives 10.8 t/h of concentrate to produce 10,826 t/a of dry mixed rare earth carbonate solids containing 5,954 t/a of contained TREO. Environmentally, the project includes a tailings storage facility (TSF) for combined flotation and hydrometallurgical tails, with gypsum generated from the gangue leach filtered, dried, and sold to the cement and allied industries, reducing waste. The caustic conversion step includes evaporation and causticisation to regenerate sodium hydroxide for reuse, improving sustainability. Economic impact is significant as the project targets a high-value MREC product with cerium depletion, aligning with market demand for magnet and battery rare earth elements. The process design has been maintained from the earlier PFS, with updated CAPEX and OPEX to 2025 pricing, reflecting the project’s readiness for detailed feasibility. Future outlook includes potential optimisation of the flotation reagent suite and continued test work to enhance recovery and grade. This facility is a pivotal step for Malawi’s mining sector, providing a domestic rare earth supply chain with minimal environmental footprint through acid regeneration and gypsum valorisation. The use of on-line stream analysers and rigorous metallurgical accounting ensures consistent product quality and operational efficiency.
Key Processes: Flotation, Gravity Separation, Ball Mill, Crushing
Target Commodities: Zinc, Uranium
Technical report and processing history
The following archived source profiles have been consolidated here to preserve the project’s processing history and study context.
Songwe Hill REE Project — NI 43-101 Technical Report
Songwe Hill REE Project — NI 43-101 Technical Report
| Company | Mkango |
| Date | 2024 |
| Region | Malawi |
| Commodities | Rare Earth Elements |
Executive Summary
This NI 43-101 Technical Report details the recovery methods for the Songwe Hill Rare Earth Elements (REE) Project located in the south-eastern region of Malawi. The project focuses on processing a high-grade rare earth enriched, mixed rare earth carbonate product that is cerium depleted. The deposit comprises mostly carbonaceous gangue minerals and rare earths associated with oxides, with minor amounts of sulphide minerals present. The process design is based on comprehensive test work programmes and aims to produce a rare earth oxide concentrate suitable for subsequent hydrometallurgical treatment.
The concentrator plant flowsheet consists of comminution and flotation circuits designed to effectively float rare earth oxides from oxidic gangue. Key design parameters include a ROM feed rate of 1,000,000 tonnes per annum and a target concentrate TREO grade of 15% w/w. The flotation circuit utilizes fine grinding, high-intensity conditioning, elevated temperature, and a specific reagent suite to achieve recoveries of 74.1% TREO. The crushed product is milled in a ball mill in a closed circuit with a primary cyclone cluster, followed by fine grinding in stirred media mills.
The hydrometallurgical plant flowsheet includes several unit operations aimed at extracting, purifying, and recovering rare earth elements. The process involves gangue leaching with dilute acid, caustic conversion to convert insoluble rare earth minerals into soluble hydroxides, and cerium oxidation to render cerium insoluble. The final product is a mixed rare earth carbonate precipitated from purified leach liquor. The plant design includes reagent regeneration circuits for hydrochloric acid and sodium hydroxide to optimize costs and environmental impact.
Reports
Entities
Concepts
Website: https://mkango.ca/projects/songwe/
Report Date: 2024
Region: Malawi
Project Status:
Commodity: Rare Earth Elements
Throughput:
Mine Life:
Mine Type:
Ore type:
Mkango Songwe Hill PFS — 2014 Technical Report
This technical report presents the results of a prefeasibility study for the Songwe Hill rare earth element deposit in Malawi, based on proposed design parameters supported by metallurgical testwork and historical operating data.
Report context
The Songwe Hill rare earth element (REE) deposit is located in southeastern Malawi, within Exclusive Prospecting License (EPL) 0284/10, which Mkango refers to as the "Phalombe License." The EPL covers an area of 1,283 km² and was originally granted to Lancaster Exploration Ltd (Lancaster), a 100 percent owned subsidiary of Mkango, on January 21, 2010. The license was renewed for a further two years until January 20, 2015. Mkango is in receipt of a legal opinion from Blantyre's law firm, Gustave and Company, confirming Lancaster as the legal holder of 100 percent interest in EPL 0284/10R, valid and unencumbered as of October 30, 2014. The Songwe Hill carbonatite abuts against Mauze Hill on its northwestern flank and lies entirely within the Republic of Malawi.
Processing route
Mineral processing and metallurgical testwork
The mineral processing and metallurgical testwork for the Songwe Hill project has been conducted under the supervision of qualified persons. The testwork program was designed to establish the processing route for the rare earth element mineralization. Specific processing details including flowsheet configuration, reagent schemes, and equipment selection are based on the metallurgical testwork results and proposed design parameters.
Recovery methods and infrastructure design
Recovery methods and infrastructure design have been developed by qualified persons and contributing authors. The design basis for the processing plant and associated infrastructure incorporates the results of metallurgical testwork and considers site-specific conditions identified during the prefeasibility study phase. Infrastructure requirements include the processing facilities, utilities, and support services necessary for the proposed mining operation.
Tailings management
Tailings management for the Songwe Hill project has been evaluated by qualified persons and contributing authors. The tailings storage facility design is based on proposed design parameters and considers the site conditions and regulatory requirements for the project area. Historical operating data from similar operations has been referenced where applicable to support the design assumptions.
Process design basis
The proposed processing route has been developed using a combination of metallurgical testwork results and engineering design studies. The design parameters show the characteristics of the Songwe Hill mineralization as determined through the testwork program. No detail is provided in the report regarding specific unit operations, reagent consumption, or process performance metrics beyond what is presented in the key reported parameters.
Key reported parameters
| Parameter | Unit | Value | Basis |
|---|---|---|---|
| Project location | Songwe Hill, Phalombe district, Malawi | Description | |
| License | EPL 0284/10 (Phalombe License) | Legal opinion | |
| License area | km² | 1,283 | Legal opinion |
| License holder | Lancaster Exploration Ltd (100% owned by Mkango) | Legal opinion | |
| Original grant date | January 21, 2010 | Legal opinion | |
| Renewal period | January 20, 2013 to January 20, 2015 | Legal opinion | |
| Estimated closure cost | US$ | 7,108,000 | Proposed design |
| Closure cost demolition | US$ | 4,410,000 | Proposed design |
| Closure cost rehabilitation | US$ | 1,196,000 | Proposed design |
| Closure cost groundwater monitoring | US$ | 213,000 | Proposed design |
| Closure cost vegetation maintenance | US$ | 53,000 | Proposed design |
| Closure cost vegetation monitoring | US$ | 2,000 | Proposed design |
| Closure cost project management (12%) | US$ | 673,000 | Proposed design |
| Closure cost contingency (10%) | US$ | 561,000 | Proposed design |
| Post-closure groundwater monitoring period | years | 5 | Proposed design |
| Post-closure vegetation monitoring period | years | 3 | Proposed design |
| Average wind speed (2010-2012) | m/s | 3.73 | Modelled testwork data |
| Predominant wind direction | South-southeast | Modelled testwork data | |
| Calm conditions frequency (<0.5 m/s) | % | 2.73 | Modelled testwork data |
Project website: https://mkango.ca/news/mkango-announces-results-of-updated-feasibility-study-for-the-songwe-hill-rare-earths-project-in-malawi-and-pre-feasibility/
Technical qualifications
The technical report acknowledges that none of the consultants or any associates employed in the preparation of this technical report has any beneficial interest in Mkango. The consultants are not insiders, associates or affiliates of Mkango and are being paid a fee for their work in accordance with normal professional consulting practice.
The closure cost estimate used the block plan provided by SNC Lavalin as representative of the infrastructure and liabilities associated with the proposed mine. The closure estimate excludes potential liabilities associated with social obligations to surrounding communities, retrenchment payments, and long-term water management. A contingency of 10 percent has been included to allow for areas which may have been undervalued or which may have been overlooked.
The disclosure of information relating to land, legal, title, and related issues relies on a legal opinion from Blantyre's law firm, Gustave and Company. The consultants are not responsible for such information but have assumed it to be accurate for the purposes of this technical report.
Currently, the environmental liabilities on the site are minimal as only exploration has taken place and it is a greenfields project. Should the project not proceed to construction, the site will need to be closed and rehabilitated. Current liabilities would include the removal of the tented construction camp, the closure of boreholes, and the rehabilitation of access and drilling roads.
It is recommended that an environmental obligations register be compiled during the ESHIA process, the closure cost estimate be updated once the definitive feasibility study is completed, and a preliminary closure plan be developed. These recommendations should be actioned in the ESHIA phase of the project.
Source: Mkango Songwe Hill PFS , November 2014 Technical Report, Sections 3, 4.2, 4.3, 5.2, and Qualified Persons sections.

