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Separation of yttrium from europium using a hollow fiber-supported liquid membrane with 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester as an extractant

机译:使用用2-乙基己基膦酸单-2-乙基己基酯的中空纤维支撑的液膜用中空纤维支撑的液体膜的钇从铕的分离为萃取剂

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摘要

The separation of Y(III) from Eu(III) using a hollow fiber-supported liquid membrane with 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester (EHPNA) as an extractant was studied. The effects of HCl and metal concentrations in the feed solution, the EHPNA concentration in the membrane, and the HCl concentration in the stripping solution on the initial fluxes of the two metals and the separation factor were investigated. The optimum conditions for selective recovery of Y(III) from an equimolar solution of Y(III) and Eu(III) chlorides (0.001molL(-1) each) were as follows: HCl concentration in the feed solution, 0.1molL(-1); EHPNA dimer concentration in the organic phase in the membrane, 0.1molL(-1); and HCl concentration in the stripping solution, 4molL(-1). Under these conditions, complete Y(III) extraction was achieved after 1 ks of operation, and the Y(III) purity in the stripping solution was 84%.
机译:研究了使用中空纤维负载型液体膜与用2-乙基己基膦酸单-2-乙基己基酯(EHPNA)作为萃取剂的y(III)的分离。 研究了HCl和金属浓度在饲料溶液中的影响,膜中的EHPNA浓度,以及在两个金属的初始通量的汽提溶液中的HCl浓度和分离因子的溶液中的HCl浓度。 从Y(III)和EU(III)和EU(III)氯化物的等摩尔溶液(0.001Moll(-1)各自)的最佳条件如下:HCl浓度在进料溶液中,0.1Moll( - 1); EHPNA二聚体浓度在膜中的有机相中,0.1moll(-1); 和剥离溶液中的HCl浓度,4moll(-1)。 在这些条件下,在1千次操作后实现完全Y(III)萃取,汽提溶液中的Y(III)纯度为84%。

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