Process intensification in precipitation of uranium from post alkali leach liquor using re-dissolution of sodium diuranate slurry: A short review of laboratory and pilot scale test results
IF 4.8 2区 材料科学Q1 METALLURGY & METALLURGICAL ENGINEERING
Vipin Kumar Sharma , P. Sriharsha , L.K. Rao , Suman Sarkar , M.S. Rao
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Abstract
The Uranium Corporation of India Limited (UCIL) Tummalapalle facility processes a low-grade uranium ore (0.042 % U3O8), necessitating the enhancement of low uranium concentration (0.74 g/L U3O8) in the clarified leach liquor as a critical goal for process optimization in the precipitation stage. Enhanced concentration of U3O8 in the process liquor is pivotal for maximizing the recovery of the final uranium product. Various filtration technologies were evaluated at laboratory and pilot scales to recover ultra-fine sodium diuranate (SDU) particles to improve recovery. These technologies included candle filters, ceramic filters, cartridge filters, and ultrafiltration. However, none of these methods proved viable for a sustained operation under plant conditions. Additional techniques such as ion exchange, centrifugation, and nanofiltration were also assessed but failed due to inherent technical constraints. Experimental results from laboratory and pilot scale tests indicated that precipitation at approximately 2.5 g/L U3O8 in the leach liquor yielded a product with optimal settling characteristics and minimized uranium losses, both in unprecipitated and precipitated forms. In order to achieve this target and enhance precipitation efficiency, a bleed stream of the sodium diuranate slurry from the precipitation circuit was combined with clarified low grade leach liquor to redissolve SDU and heated to approximately 75–80 °C to prepare a concentrated solution of 2.5 g/L. This approach significantly improved the precipitation efficiency of the process liquor in the low-grade ore processing unit.
期刊介绍:
Hydrometallurgy aims to compile studies on novel processes, process design, chemistry, modelling, control, economics and interfaces between unit operations, and to provide a forum for discussions on case histories and operational difficulties.
Topics covered include: leaching of metal values by chemical reagents or bacterial action at ambient or elevated pressures and temperatures; separation of solids from leach liquors; removal of impurities and recovery of metal values by precipitation, ion exchange, solvent extraction, gaseous reduction, cementation, electro-winning and electro-refining; pre-treatment of ores by roasting or chemical treatments such as halogenation or reduction; recycling of reagents and treatment of effluents.