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机构地区:[1]中国科学院长春应用化学研究所稀土化学与物理开放实验室,长春130022
出 处:《分析化学》2001年第10期1163-1166,共4页Chinese Journal of Analytical Chemistry
基 金:国家重点基础研究发展规划(G1998061301);国家自然科学基金(No.29771028;29801004)资助课题
摘 要:利用中空纤维膜器,采用逆流循环萃取法,用二(2,4,4-三甲基戊基)硫代膦酸(Cyanex302)从硫酸溶液中萃取分离锌和铕。探讨了膜萃取的反应机制,考察了料液酸度、萃取剂浓度等因素对传质系数的影响,提出利用动力学竞争可以实现锌、铕混合组分的分离。研究了不同酸度、不同配比以及膜器串联的不同级数等条件对锌、铕混合物分离的影响。采用单级萃取时,只有锌被萃取,而铕不被萃取,且锌的萃取不完全;当采用膜器二级串联,经过 100min后锌的萃取率达到 94.92%,而铕的萃取率仅为8.59%;当采用膜器三级串联时,经过 40min后,锌的萃取率达到 99.9%以上,而铕的萃取率仅为6.53%。Extraction and separation of Eu3+ and Zn2+ in sulfuric acid solution was investigated by hollow fiber membrane with cyanex 302 (bis (2,4, 4-trimethylpentyl) monothiophosphinic acid) in counter-currently circulating operation. Reaction mechanism of membrane extraction and effect of extractant concentration and H concentration in aqueous phase on the mass transfer coefficient were discussed. It can be concluded that Zn2+ can be extracted completely fmm Eu3+ sulfate solution according to the kinetics competing difference. In one extractor pmcess, extraction percentage of Zn2 + was not completely and Eu3+ was not extracted. Extraction percentage of Zn2+ reached 94.92%, but Eu3+ only reached 8.59% after 100 minutes extraction in two series connectors and that of Zn2+ and Eu3++ reached 99.9% and 6.53% respectively after 40 minutes extraction in three series connectors.
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