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Zinc and copper separation through an emulsion liquid membrane containing di-(2-ethylhexyl) phosphoric acid as a carrier

机译:通过以二(2-乙基己基)磷酸为载体的乳状液膜分离锌和铜

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摘要

The separation of zinc and copper ions from sulfuric acid solutions by an emulsion liquid membrane (ELM), using di-(2-ethylhexyl) phosphoric acid (D2EHPA) as a carrier, has been investigated. The batch extraction of zinc and copper was carried out while varying a selection of experimental conditions, i.e., stirring speed, treatment ratio, concentrations of metal ions in the feed phase, carrier and Span 80 concentration in the membrane, and internal phase concentration. The results obtained demonstrate the effectiveness of D2EHPA as a carrier for the separation of zinc and copper from sulfuric acid media using an ELM. An increase of the D2EHPA concentration beyond 2 vol.-% does not result in the improved extraction of zinc because the viscosities of the membrane and emulsion have a trend to increase for higher carrier concentrations. It was found that the extraction rate of copper was affected by the carrier concentration in the liquid membrane and by the pH and metal content in the external phase. A 3 vol.-% concentration of surfactant in the organic phase was required to stabilize the emulsion. The number of stages required for the extraction of zinc and copper by an ELM was determined from McCabe-Thiele plots.
机译:研究了使用二(2-乙基己基)磷酸(D2EHPA)作为载体的乳化液膜(ELM)从硫酸溶液中分离锌和铜离子的方法。在改变实验条件的选择下进行锌和铜的批量萃取,所述条件是搅拌速度,处理比,进料相中金属离子的浓度,膜中的载体和Span 80的浓度以及内相浓度。获得的结果证明了D2EHPA作为使用ELM从硫酸介质中分离锌和铜的载体的有效性。 D2EHPA浓度增加到2%(体积)以上不会改善锌的提取率,因为膜和乳液的粘度对于较高的载剂浓度具有增加的趋势。发现铜的提取速率受液膜中载流子浓度以及外相中的pH和金属含量的影响。需要使有机相中表面活性剂的浓度为3体积%以稳定乳液。由ELCA提取锌和铜所需的阶段数由McCabe-Thiele图确定。

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