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Recovery of metals from chloride leach solutions of anode slimes by solvent extraction. Part I: Recovery of gold with Cyanex 272

机译:通过溶剂萃取从阳极沉体溶液溶液中回收金属。 第一部分:使用Cyanex 272回收黄金

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A separation process was developed to recover Au(III) from the chloride leach solution of anode slime using selective extraction and stripping step. The anode slime contained Ag, Au, Cu, Ni, Sn and Zn. The extraction with Cyanex 272 in kerosene was conducted by varying the HCl concentration of the solution from 0.5 to 9 M. Most of Au(III) and Sn(II) were extracted into Cyanex 272/kerosene phase together with a small amount of Cu(II) and Zn (II). The Au(III) in the loaded Cyanex 272 was selectively stripped over Sn(II) by (NH4)(2)S2O3. The McCabe-Thiele diagrams for the extraction and stripping were constructed. Extra pure Au(III) solution was recovered from the leach liquor by batch simulation experiments of two stage countercurrent extraction with Cyanex 272 and by one stage stripping with (NH4)(2)S2O3. The developed process can be applied to recover gold from a hydrochloric acid solution containing Ag(I), Cu(II), Sn(II) and Zn(II).
机译:开发了分离过程以使用选择性提取和汽提步骤从阳极粘液的氯浸出溶液中回收Au(III)。 阳极粘液含有Ag,Au,Cu,Ni,Sn和Zn。 通过改变溶液的HCl浓度从0.5至9米的HCl浓度改变溶液的HCl浓度,大部分Au(III)和Sn(II)与少量Cu( ii)和Zn(ii)。 通过(NH 4)(2)S2O3,选择性地剥离装载的氰基272中的Au(III)。 构建了提取和汽提的McCabe-Thiele图。 通过用Cyanex 272的两级逆流萃取的批量模拟实验从浸出液中回收额外的纯AU(III)溶液,并用(NH4)(2)S2O3的一个阶段剥离。 可以应用开发的方法来从含有Ag(I),Cu(II),Sn(II)和Zn(II)的盐酸溶液中恢复金。

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