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Selective extraction of In(Ⅲ),Ga(Ⅲ) and Zn(Ⅱ) using a novel extractant with phenylphosphinic acid 被引量:1
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作者 yuji sasaki Naoki Matsuo +1 位作者 Tatsuya Oshima Yoshinari Baba 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2016年第2期232-236,共5页
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 I... 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 [dm3.mol 1], 4.17 [(dm3.mol-1)s], and 1.55 × 10 2 [-], respectively. 展开更多
关键词 Liquid-liquid extraction Phosphinic acid Indium(Ⅲ) Gallium(Ⅲ) Zinc(Ⅱ) Mutual separation Extraction equilibrium
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