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N1923~P538-煤油溶液萃取Au(Ⅲ)的性能 被引量:1

EXTRACTION EQUILIBRIA OF GOLD(Ⅲ) WITH A MIXTURE OF PRIMARY AMINE N1923 AND MONOALKYLPHOSPHORIC ACID P538 IN KEROSINE
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摘要 本文在298±1K下分别考察了N1923(B)-煤油溶液(Ⅰ)和N1923—P538(H_2A)—煤油溶液(Ⅱ)从1.00mol·L^(-1)(Na,H)Cl水相介质中萃取Au(Ⅲ)的平衡。结果表明,体系(Ⅰ)中萃合物组成为(BH)AuCl_4(BHCl)_3;体系(Ⅱ)中萃合物组成为(BH)AuCl_4(BHCl)_4,H_2A与BHCl形成缔合物(BHCl)_3·(H_2A)_(4·75)。 The equilibrium of The extraction of gold(Ⅲ) (C_(Au)=4.00 10^(-4)mol·dm^(-3))from 1.00 mol·dm^(-3)(Na, H)Cl solution with a mixture of primary amine N1923((?), R′+R=C_(19-23), B)and monoalkylp-hosphoric acid P538(RO—PO(OH)_2,R=C_(12-18),H_2A)in kerosine at 298±1K has been studied.The experimental relults are follows: 1. The determination of an aggregation number of amine salts, BHCl, formed by reaction of N1923(B) dissolved in kerosine with hydrochloric acid from aqueous solution have been performed by two phase emf titration. When the concentration of N1923 in organic phase are in the range of 0.001 mol·dm^(-3), the formation of aggregate as trimer was observed, by assuming the ideal behavior of each species in organic phase. 2. The extraction results of Au(Ⅲ) with N1923 kerosine solution (C_(BHCl(0))~0=0.003-0.019mol·dm^(-3)) show that the extraction machanism is anion exchange reaction described by eq.(1), where a=1.31, LogK_(ex)=4.30. 3. The extraction equilibrium of Au(Ⅲ) with a mixture of P538 (C_(H_2A(0))~0=0-0.05mol·dm^(-3)) and N1923(C_(BHCl(0))~0 0-0.06mol·dm^(-3)) in kerosine can be represented by eq. (2), a′(BHCl)_3(0)+ AuCl_4^-(?)(BH)AuCl_4(3a′-1)(BHCl)_((0))+Cl^- (2) and (BHCl)_(3(0))+(H_2A)_(q(0))(?)(BHCl)_3(H_2A)_(q(0)) (3) C_(BHCl(0))~0=3[(BHCl)_3]_((0))+3[(BHCl)_3·(H_2A)_q]_((0))+3a′[Au]_((0)) (?)3[(BHCl)_3]((0))+3[(BHCl)_3·(H_2A)_q]_((0)) ( 4 ) C_(H_2A(0))~0=q[(H_2A)_q]_((0))+q[(BHCl)_3·(H_2A)_q]_((0)) (5) From eqs. (2)—(5) and [Cl^-]=1.00mol·dm^(-3), the eq. (6) can be obtained. C_(BHCl(0))~0=3(D/K_(ex))^(1/α^′)+3q^(-1)[β^(-1)(D/K′_(ex))^((-1)/α′)+1]^(-1) C_(H_2A(0))~0 (6) The results show that the plots of C_(BHCl(0))~0 VS. C_(H_2A(0)~0 gave a good straight line at constant D (=C_(Au(0))/C_(Au)). The values of intercepts, b=3(D/K′_(ex))^(1/α′), and slopes, S=3q^(-1)[β^(-1)(D/K′_(ex))^((-1)/α′)+1] are changed by varying the values of D. Therefore, the values of a′, K′_(ex) and q can be calculated, thus a′=1.66; LogK′_(ex)=5.14 and q=4.75. From this, it can be seen that the extracted species, (BH)AuCl_4(BHCl)_4, in this system is large than that formed in the system containing N1923 only, and that P538 does not enter into it. The acidity in aqueous phase does not affect the extraction equilibrium of Au(Ⅲ). C_((0))~0 stands for the initial concentration of species in organic phase, [ ]_((0)) and [ ] stand for the equilibrium concentrations of species in the organic phase and in the aqueous phase, respectively.
机构地区 山东大学化学系
出处 《山东大学学报(自然科学版)》 CSCD 1989年第1期71-77,共7页 Journal of Shandong University(Natural Science Edition)
关键词 萃取 N1923 extraction, gold, primary amine N1923
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参考文献5

  • 1盖会法,化学学报,1987年,45卷,383页
  • 2李铃颖,化学学报,1986年,44卷,960页
  • 3蒋启秀,全国第一届溶剂萃取会议论文摘要,1985年
  • 4庄尚瑞,全国第一届溶剂萃取会议论文摘要,1985年
  • 5团体著者,有色金属中元素的分离与测定,1968年

同被引文献4

  • 1王伯勇 张洪林 沈静兰.P538的纯化[J].化学试剂,1987,9(1):60-60.
  • 2孙思修 高自立 沈静兰 张洪林.P538萃取Fe(Ⅲ)的研究[J].应用化学,1987,4(5):78-78.
  • 3孙思修 高自立 盖会法 沈静兰.P538萃取Co(Ⅱ)的平衡研究[J].化学学报,1987,45(8):766-766.
  • 4于秀芳,张洪林.稀释剂对P_(538)萃取Fe(Ⅲ)的影响[J].应用化学,1990,7(2):95-97. 被引量:3

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