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Selective extraction of In(Ⅲ),Ga(Ⅲ) and Zn(Ⅱ) using a novel extractant with phenylphosphinic acid

Selective extraction of In(Ⅲ),Ga(Ⅲ) and Zn(Ⅱ) using a novel extractant with phenylphosphinic acid

作     者:Yuji Sasaki Naoki Matsuo Tatsuya Oshima Yoshinari Baba 

作者机构:Department of Applied ChemistryFaculty of EngineeringUniversity of Miyazaki 

出 版 物:《Chinese Journal of Chemical Engineering》 (中国化学工程学报(英文版))

年 卷 期:2016年第24卷第2期

页      面:232-236页

核心收录:

学科分类:081704[工学-应用化学] 07[理学] 08[工学] 0817[工学-化学工程与技术] 070302[理学-分析化学] 0703[理学-化学] 

基  金:supported by The Environment Research and Technology Development Fund (3K133005) 

主  题:Liquid-liquid extraction Phosphinic acid Indium(Ⅲ) Gallium(Ⅲ) Zinc(Ⅱ) Mutual separation Extraction equilibrium 

摘      要:A new extractant, [N,N-di(2-ethylhexyl)aminolmethylphenylphosphinic acid (DEAPP), was synthesized to de- velop the mutual separation techniques of In(Ⅲ), Ga(Ⅲ) and Zn(Ⅱ). The extraction selectivity for In(Ⅲ), Ga(Ⅲ) and Zn(Ⅱ) with DEAPP was higher than that of the commercial phosphorus acid extractants such as D2EHPA and PC-88A. The extraction selectivity for metal ions in 1 mob L 1 aqueous ammonium nitrate solution with DEAPP was in the following order: In(Ⅲ) 〉 Ga(Ⅲ) 〉 Zn(Ⅱ). These selective extraction behaviors indicate that the amino moiety of DEAPP plays an important role in the mutual separation of ln(Ⅲ), Ga(Ⅲ) and Zn(ll). The extraction equilibria of In(Ⅲ), Ga(Ⅲ) and Zn(Ⅱ) with DEAPP ( = HR) were expressed by the following reactions: In3+ + 2(HR)2 InR3(HR) + 3H+, Ga3+ + 1.5(HR)2 + N- = GaR2(HR)(NO3) + 2H+, and Zn2+ 4- 2(HR)2 ZnR2 (HR) 2 determined 4- 2H+. The extraction equilibrium constants of In(Ⅲ), Ga(Ⅲ) and Zn(Ⅱ) with DEAPP were to be Kex, M = 1.7 × 104 [*** 1], 4.17 [(***-1)s], and 1.55 × 10 2 [-], respectively.

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