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Recovery of indium and gallium from synthetic leach solution of zinc refinery residues using synergistic solvent extraction with LIX 63 and Versatic 10 acid

机译:使用LIX 63和Versatic 10酸协同溶剂萃取从锌提炼厂残余物的合成浸出溶液中回收铟和镓

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摘要

A synergistic solvent extraction (SSX) system consisting LIX 63 and Versatic 10, which are both commercially available, was selected to recover both Ga(III) and In(III) from synthetic sulfate leach solutions of zinc refinery cementation residues in one circuit. With the optimum composition of the SSX system, 86% In(III) and 92% Ga(III) were extracted in a single contact at pH 3.0. The extraction and stripping kinetics of In(III) and Ga(III) were fast at 40 degrees C. In(III) and Ga(III) were stripped readily using solution with low acidity of 0.05 M H2SO4. Based on the McCabe-Thiele diagrams constructed, 4 stages of extraction at an A/O ratio of 1.2 and 3 stages of stripping at an O/A ratio of 5 are required for the extraction and stripping of both In(III) and Ga(III). The synergistic effect on In(III) extraction was significant while that on Ga(III), extraction was insignificant. A conceptual flowsheet is proposed including the SSX system consisting of reagents that are all commercially available and offers the advantages of recovering both In(III) and Ga(III) in one circuit and stripping with low acidity solutions. Crown Copyright (C) 2016 Published by Elsevier B.V. All rights reserved.
机译:选择了由LIX 63和Versatic 10组成的协同溶剂萃取(SSX)系统,它们都可以从市场上买到,以便在一个回路中从锌精炼厂胶结残留物的合成硫酸盐浸出溶液中回收Ga(III)和In(III)。利用SSX系统的最佳组成,可在pH 3.0的单次接触中萃取出86%的In(III)和92%的Ga(III)。 In(III)和Ga(III)的萃取和汽提动力学在40摄氏度时很快。使用低酸度为0.05 M H2SO4的溶液可轻松汽提In(III)和Ga(III)。根据构造的McCabe-Thiele图,In(III)和Ga(两者的提取和汽提需要4个阶段的A / O比为1.2的萃取和3个阶段的O / A比为5的汽提。 III)。 In(III)提取的协同作用显着,而Ga(III)的提取则无明显作用。提出了一种概念上的流程图​​,其中包括由试剂组成的SSX系统,这些试剂都是可商购的,并具有在一条回路中同时回收In(III)和Ga(III)并用低酸度溶液进行汽提的优点。官方版权(C)2016,由Elsevier B.V.保留所有权利。

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