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THE SELECTIVE EXTRACTION OF MOLYBDENUM FROM A URANIUM STREAM IN A SULPHATE MEDIUM

机译:硫酸盐介质中铀溪流中钼的选择性提取

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Molybdenum can be found in significant amounts in certain uranium ores, such as the Karoo Sands in South Africa. During sulphuric acid leaching, molybdenum is leached together with uranium. If untreated the molybdenum is co-extracted during the uranium recovery process, using either anion exchange resins or amine-type solvent extractants. The molybdenum could poison these extractants and also cause contamination of the uranium yellow cake product. A further problem is possible crud formation due to limited solubility in the organic phase of certain molybdenum complexes. Carbon columns could be used for molybdenum adsorption; however carbon columns are preferred for molybdenum removal from pregnant strip solutions as opposed to pregnant leach liquors to reduce the carbon inventories that are required. Another drawback of carbon columns is the slow molybdenum adsorption rate.This paper focuses on a solvent extraction process for the selective extraction of molybdenum in the presence of uranium in sulphuric acid leach liquors. The efficiency of the molybdenum removal from the uranium leach stream was evaluated using 2-hydroxy-5-nonylacetophenone oxime. Metal-distribution equilibria, extraction equilibrium isotherm and batch counter-current tests were done for molybdenum extraction using 15 (v/v) % 2-hydroxy-5-nonylacetophenone oxime with the addition of 7.5 (v/v) % Isodecanol in Shellsol D70 using uranium pregnant leach liquor. It was found that, at a pH value of 1.5, selective extraction of molybdenum was possible. Batch counter-current extraction tests produced a loaded organic phase which contained 1.26 g/L molybdenum at steady state leaving 4 mg/L molybdenum in the raffinate, which related to >96% extraction. Degradation tests were carried out using 15 (v/v) % 2-hydroxy-5-nonylacetophenone oxime, and 7.5 (v/v) % Isodecanol in Shellsol D70, simulating extraction conditions, at 20°C and 40°C over a period of 91 days. Results obtained indicated that there were negligible variations in molybdenum maximum loadings over the 91 day period. The process described will result in a higher purity uranium yellow cake product and a saleable molybdenum product. This will increase the revenue potential of a deposit which contains both uranium and molybdenum in significant quantities.
机译:钼可以在某些铀矿石中以显着的量存在,例如南非的karoo砂。在硫酸浸出过程中,钼与铀浸出。如果未经处理过的钼在铀回收过程中,使用阴离子交换树脂或胺型溶剂萃取剂在铀回收过程中是共萃取的。钼可以毒害这些萃取剂,并引起铀黄色蛋糕产品的污染。由于某些钼配合物的有机相中的有限溶解度,可能是可能的伯爵形成的进一步问题。碳柱可用于钼吸附;然而,碳柱优选用于从怀孕条状溶液中除去糖酵果,而不是怀孕的浸渍液,以减少所需的碳库存。碳柱的另一个缺点是慢性钼吸附速率。本文侧重于在硫酸浸渍液中铀存在下选择性提取钼的溶剂提取方法。使用2-羟基-5-壬酮肟评价从铀浸料流中除去钼​​的效率。使用15(V / V)%2-羟基-5-壬基酮酮肟来进行金属分布平衡,提取平衡等温线和批次逆流试验,并在Shellsol D70中加入7.5(v / v)%异癸醇使用铀孕浸渍液。发现,在pH值为1.5时,可以选择性提取钼。批量逆流提取试验产生了载有1.26g / L钼的负载有机相,稳定状态下留在萃余液中4mg / L钼,其提取> 96%的提取。使用15(v / v)%2-羟基-5-壬基酮肟肟和7.5(v / v)%异黄糖,在Shellsol D70中,在20℃和40℃下模拟萃取条件,在一段时间内91天。获得的结果表明,在91天期间,钼最大载荷的变化可以忽略不计。所描述的方法将导致更高纯度的铀黄饼产品和可销售的钼产品。这将提高沉积物的收入潜力,其含有铀和钼的大量。

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