Plateau Energy Metals Inc. (“Plateau” or the “Company”) (TSX-V: PLU | OTCQB: PLUUF) is pleased to announce it has completed a preliminary test work program (“Program”) for the recovery of potential by-products such as sulfate of potash (“SOP”), caesium and rubidium from its Falchani Lithium Project in Peru. This Program was conducted by ANSTO Minerals, based in Sydney, Australia.
The Program focused on recovery and precipitation of SOP and caesium concentrate from a pregnant leach solution (“PLS”) created from the Falchani Project Preliminary Economic Assessment (“PEA”) flowsheet.
Highlights of the Program:
“These preliminary results are encouraging and support potential by-products that our Falchani project could supply in addition to lithium carbonate,” stated Dr. Laurence Stefan, President & COO. “By simply controlling pH with lime re-agent addition combined with solution cooling, ANSTO has demonstrated the precipitation of a critical caesium-rubidium sulfate chemical from leach solutions at temperatures above 25°C and of a potential SOP at lower temperatures. The SOP could be used as a strategic fertilizer for Peru and possibly in the rest of South America.”
Program Details
This Program was an extension of ANSTO’s previous test work to support the Falchani Project National Instrument 43-101 PEA technical report titled “Falchani Lithium Project NI 43-101 Technical Report – Preliminary Economic Assessment” prepared by DRA Pacific, effective February 4, 2020 (filed on SEDAR March 20, 2020), in which a mixed alkali metal alum is crystallized from the PLS prior to purification (refer to flowsheet linked above). This mixed alkali metal alum is where >99% of Cs and Rb report to in the process, which forms a potential feed for further processing to realize the value of the contained caesium.
Three different processing options were examined in the Program, including:
The results of the Program have demonstrated excellent rejection of aluminum, iron, and other trace elements, and substantial recoveries of the alkali metals (potassium, rubidium and caesium) using either an initial treatment of calcination at between 700 to 800oC in the Calcination Option, or dissolution of alum followed by neutralization using lime in the Neutralization Option.
The test work also demonstrated selective crystallization of >99% of the Cs and Rb, in both the Neutralization Option and Calcination Option from actual PLS by cooling to between 20 to 30°C (see Figure 1). At this point the Rb and Cs content is reduced to below detection limits (1 mg/L). A proportion of potassium also crystalizes in this step.
At temperatures below 20°C a portion of the K available in solution precipitated out while lithium and other metals, remained in the sulfate solution. This resulted in an unoptimized first pass recovery of approximately 18% of the K in solution and ANSTO believes future test work may further improve the yield. As described in the PEA flowsheet, the lithium-rich solution continues with an additional three-stage conventional impurity removal prior to the next steps utilized to precipitate a low impurity, battery quality lithium carbonate.
These two options for processing of alum are used on an industrial scale today and with the success of this Program, future test work will follow well established process designs.
While sulfate crystallization was not examined in this Program in the first two options, the pronounced differences in the solubility of SOP versus caesium and rubidium sulfates is expected to allow the ready crystallization of a SOP product in accordance with conventional approaches employed for alum processing.
The third processing option of Pre-Concentration was examined to determine if the caesium grade of the mixed alkali metal alum could be improved prior to further processing using the first two options. This approach simply represents an optimization of the alum crystallization step already considered for the PEA flowsheet. Alum crystallization is adopted by the lithium industry to control the build-up of alkali metals such as potassium, caesium and rubidium in sulfate-based processing liquors. At this stage, further work is required to demonstrate the viability of this processing route.
Figure 1: Precipitation versus Temperature (staged cooling of PLS)
Figure 1 is available at https://www.globenewswire.com/NewsRoom/AttachmentNg/43d68ea1-8c1a-4ad4-b98f-94299137507c
Table 1: Extraction and Precipitation in Current Program
Precipitation % | |||
Element | Extraction in Leach % |
At 25°C | At 5°C |
K | 43 | 61 | 87 |
Rb | 67 | 100 | 100 |
Cs | 84 | 100 | 100 |
Future Test Work
These preliminary test work results support the need for future test work including:
Qualified Person
Doug Collier (FAusIMM) of ANSTO Minerals, an Independent Qualified Person as defined by National Instrument 43-101 Standards of Disclosure for Mineral Projects, has reviewed and approved the scientific and technical information contained in this news release.
About ANSTO Minerals
ANSTO (Australian Nuclear Science and Technology Organisation) Minerals is an international mining consultancy group located in Sydney, Australia, with an experienced team of 60+ engineers, metallurgists, chemists, and scientists who have been providing consulting services and process development services to the mining and minerals processing industries for well over 35 years. ANSTO Minerals has world-leading expertise in uranium ore processing, rare earth processing, zirconium/niobium/hafnium processing, base metals processing, lithium processing, and radioactivity control and management.
About Plateau Energy Metals
Plateau Energy Metals Inc., a Canadian exploration and development company, is enabling the new energy paradigm through exploring and developing its Falchani lithium project and Macusani uranium project in southeastern Peru, both of which are situated near significant infrastructure.
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IR@PlateauEnergyMetals.com | Website: www.PlateauEnergyMetals.com |