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SELECTIVE REMOVAL OF TRANSITION METAL IONS IN TRANSPORT THROUGH POLYMER INCLUSION MEMBRANES WITH ORGANOPHOSPHORUS ACIDS

机译:含有机磷酸的聚合物包膜中选择性去除过渡金属离子

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摘要

Separation of transition metal ions from aqueous chloride solutions by transport through polymer inclusion membrane (PIM) process is presented. The competitive transport of equimolar mixtures of Zn(Ⅱ) and Cd(Ⅱ) as well as Zn(Ⅱ), Cu(Ⅱ), Co(Ⅱ), Cd(Ⅱ), and Ni(Ⅱ) was investigated. The selective transport of metal ions from aqueous chloride source phase through PIM-containing cellulose triacetate (support), o-nitrophenyl pentyl ether (plasticizer) and organophosphorus acidic compounds, i.e. di(2-ethylhexyl)phosphoric acid (D2EHPA), di(2,4,4-trimethylpentyl)phosphinic acid (Cyanex 272), di(2,4,4-trimethylpentyl)dithiophosphinic acid (Cyanex 301) and bis(2,4,4-trimethylpentyl)monothiophosphinic acid (Cyanex 302) as ion carriers, is shown. The influence of extractant nature on the selectvity and efficiency of cation transport has been examined. Zn(Ⅱ) can be effectively removed from dilute aqueous chloride solutions containing equilmolar mixture of Zn(Ⅱ) and Cd(Ⅱ) ions in transport through PIMs with di(2,4,4-trimethylpentyl)phosphinic acids, bis(2,4,4-trimethylpentyl)rnonothiophosphinic acid or di(2-ethylhexyl)phosphoric acid as the ionic carriers into 1.0 M HCl as the receiving phase. The per cent removal of Zn(Ⅱ) and Cd(Ⅱ) ions increases with an increase in pH. but more efficient separation of Zn(Ⅱ) than Cd(Ⅱ) ions decreases with pH increase in the source phase. Zn(Ⅱ) can be also effectively removed from dilute aqueous chloride solutions containing equimolar mixture of Zn(Ⅱ), Cd(Il), Cu(Ⅱ), Co(Ⅱ) and Ni(Ⅱ) ions by its transport through PIMs with D2EHPA, Cyanex 272 and Cyanex 302. All ions investigated are effectively removed with di(2,4,4-trimethylpentyl)dithio-phosphinic acids (Cyanex 301) as the ionic carrier into 1.0 M HCl as the receiving phase. The per cent removal of all metal ions investigated increases with an increase in pH of solution in the source phase. The initial transport fluxes of all metal ions through PIM with Cyanex 272 increase with an increase in an initial chloride acid concentration in the receiving phase.
机译:提出了通过转运通过聚合物包含膜(PIM)过程从氯化物水溶液中分离过渡金属离子的方法。研究了Zn(Ⅱ),Cd(Ⅱ),Zn(Ⅱ),Cu(Ⅱ),Co(Ⅱ),Cd(Ⅱ)和Ni(Ⅱ)等摩尔混合物的竞争输运。氯化物源相中的金属离子通过含PIM的三乙酸纤维素(载体),邻硝基苯基戊基醚(增塑剂)和有机磷酸性化合物(即二(2-乙基己基)磷酸(D2EHPA),di(2))的选择性转运,4,4-三甲基戊基)次膦酸(Cyanex 272),二(2,4,4-三甲基戊基)二硫代次膦酸(Cyanex 301)和双(2,4,4-三甲基戊基)单硫代次膦酸(Cyanex 302)显示。已经研究了萃取剂性质对阳离子迁移的选择性和效率的影响。可以通过含二(2,4,4-三甲基戊基)次膦酸双(2,4)的PIM从含Zn(Ⅱ)和Cd(Ⅱ)等摩尔混合物的稀氯化物水溶液中有效去除Zn(Ⅱ)。将作为离子载体的4-4-三甲基戊基)亚氨基硫代次膦酸或二(2-乙基己基)亚磷酸作为1.0 M HCl作为接收相。 Zn(Ⅱ)和Cd(Ⅱ)离子的去除百分率随pH值的增加而增加。但是随着源相中pH值的增加,Zn(Ⅱ)比Cd(Ⅱ)离子更有效的分离降低。还可以通过D2EHPA通过PIM转运从含Zn(Ⅱ),Cd(Il),Cu(Ⅱ),Co(Ⅱ)和Ni(Ⅱ)等摩尔混合物的稀氯化物水溶液中有效去除Zn(Ⅱ)。 ,Cyanex 272和Cyanex302。使用二(2,4,4-三甲基戊基)二硫代次膦酸(Cyanex 301)作为离子载体,有效地将所有研究的离子去除为1.0 M HCl作为接收相。随着源相中溶液pH值的增加,所调查的所有金属离子的去除百分率也随之增加。所有金属离子通过带有Cyanex 272的PIM的初始传输通量随着接收阶段中初始氯酸浓度的增加而增加。

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