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首页> 外文期刊>Hydrometallurgy >Direct solvent extraction of indium from a zinc residue reductive leach solution by D2EHPA
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Direct solvent extraction of indium from a zinc residue reductive leach solution by D2EHPA

机译:D2EHPA从锌残留还原浸出液中直接溶剂萃取铟

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摘要

A direct solvent-extraction process was developed to selectively recover indium from solutions generated by reductive leaching of zinc residues. This approach avoids the traditional steps of intermediate precipitation, solid-liquid separation, and re-leaching. Copper in the leach solution is easily removed by cementation with iron powder and the remaining Fe(III) is reduced to the ferrous state, which avoids the possibility of its co-extraction with indium. Indium is effectively extracted from the zinc sulfate solution by 20% (v/v) di(2-ethylhexyl)phosphoric acid (D2EHPA) dissolved in kerosene at an initial pH of 0.5 and aqueous-to-organic phase ratio (A:O) of 6:1 using three countercurrent stages. Indium extraction is 96.1%, zinc and iron are barely extracted, and the separation factors of indium with respect to zinc and iron are 3640 and 4809, respectively. The complete stripping of indium from the loaded organic phase is achieved using 4 mol/L HCl at an A:O of 1:6.A scheme for direct solvent extraction of indium in zinc hydrometallurgical processing is suggested, by which indium can be concentrated into a small volume of strip solution containing 11 g/L of indium, which is 85 times its concentration in the feed solution. (C) 2015 Elsevier B.V. All rights reserved.
机译:开发了一种直接溶剂萃取工艺,以从还原性浸出锌残留物所产生的溶液中选择性地回收铟。该方法避免了中间沉淀,固液分离和再浸出的传统步骤。浸出溶液中的铜很容易通过与铁粉的固结去除,剩余的Fe(III)还原为亚铁态,从而避免了与铟共萃取的可能性。在初始pH值为0.5且水与有机相比为(A:O)的情况下,通过溶于煤油中的20%(v / v)二(2-乙基己基)磷酸(D2EHPA)从硫酸锌溶液中有效提取铟。使用三个逆流阶段实现6:1的比例。铟的提取率为96.1%,几乎未提取锌和铁,铟相对于锌和铁的分离系数分别为3640和4809。使用4 mol / L HCl以1:6的A:O完全去除负载的有机相中的铟。提出了一种在锌湿法冶金工艺中直接溶剂萃取铟的方案,通过该方案可以将铟浓缩为含有11 g / L铟的少量汽提溶液,是进料溶液中铟浓度的85倍。 (C)2015 Elsevier B.V.保留所有权利。

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