Kinetics of solvent extraction of copper(II) by bis-(2,4,4-trimethylpentyl)phosphonic acid using the single drop technique

被引:23
作者
Biswas, Ranjit K. [1 ]
Ali, Muhammad R. [1 ]
Karmakar, Aneek K. [1 ]
Kamruzzaman, Muhammad [1 ]
机构
[1] Rajshahi Univ, Dept Appl Chem & Chem Technol, Rajshahi 6205, Bangladesh
关键词
kinetics; single drop technique;
D O I
10.1002/ceat.200600284
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The kinetics of the forward and backward extractions of copper(II) by the bis(2,4,4-Trimethylpentyl)phosphonic acid process have been investigated using the single drop technique and flux (F)-method of data treatment. The (F)-equation for the forward extraction of Cu(II) from the sufate-acetato medium bybis-(2,4,4-trimethylpentyl)phosphinic acid can be represented by: F-f (kmol m(-2) s(-1)) = 10(-8.64) [Cu2+]((ini)) [H+]((int))(-1) [H(2)A(2)]((o))(0.5) [HSO4-](1). Analysis of this equation gives, F-f (kmol m(-2) s(-1)) = 10(-4.88) [CuHSO4+ and A(-) to the aqueous film of the interface (and not the chemical reaction between these two species to form CuHSO4.A) are rate controlling. The (F)-equation for the backward extraction of Cu(II) from the [CuHSO(4)A.HA] complex in the organic phase by an aqueous sulfate-acetato solution can be expressed as: F-b (kmol m(-2) s(-1)) = 10(-5.68) [CuHSO(4)A.HA]((0)) (1 + 10(-3,67) [H+](-1))(-1) [H(2)A(2)]((o))(-0.5) [SO42-](-1) . Analysis of this equation results in two equations, F-b (kmol m(-2) s(-1)) = 10(-9.797) [CuHSO(4)A.HA]((0)) [A(-)](-1) [HSO4-](-1) and F-b (kmol m(-2 S-)1) = 10(-8.127) [CuHSO(4)A.HA]((o)) [A(-)](-1) [SO42-](-1) at higher and lower aqueous acidities, respectively. Low activation energies (< 20 kJ mol(-1)) indicate that the stripping processes are diffusion controlling at both regions of H+ concentration. The value of K-ex ((rate)) (k(f)/k(b) = 10(-2.967)) matches well with the K-ex ((eq)) (10(-3.19)) value within the experimental limitations.
引用
收藏
页码:774 / 781
页数:8
相关论文
共 36 条
[21]   DISSOCIATION-CONSTANTS OF ORGANOPHOSPHINIC ACID COMPOUNDS [J].
MARTINEZ, M ;
MIRALLES, N ;
SASTRE, A ;
BOSCH, E .
TALANTA, 1993, 40 (09) :1339-1343
[22]   Kinetics of iron(III) extraction with primary amine and TBP using a modified rotating diffusion cell [J].
Meng, MX ;
Yu, SQ ;
Chen, JY .
HYDROMETALLURGY, 1996, 41 (01) :55-70
[23]  
NITHSCH W, 1979, BER BUNSEN PHYS CHEM, V83, P1105
[24]   KINETICS AND MECHANISM OF EXTRACTION OF ZINC AND NICKEL WITH SUBSTITUTED DIPHENYLTHIOCARBAZONES [J].
OH, JS ;
FREISER, H .
ANALYTICAL CHEMISTRY, 1967, 39 (03) :295-&
[25]   THE EFFECT OF TRIOCTYLPHOSPHINE OXIDE ON PHASE AND EXTRACTION EQUILIBRIA IN SYSTEMS CONTAINING BIS(2,4,4-TRIMETHYLPENTYL)PHOSPHINIC ACID [J].
PAATERO, E ;
LANTTO, T ;
ERNOLA, P .
SOLVENT EXTRACTION AND ION EXCHANGE, 1990, 8 (03) :371-388
[26]   Kinetics of lanthanum(III) extraction from nitrate-acetato medium by Cyanex 272 in toluene using the single drop technique [J].
Saleh, MI ;
Bari, MF ;
Jab, MS ;
Saad, B .
HYDROMETALLURGY, 2002, 67 (1-3) :45-52
[27]   EXTRACTION OF DIVALENT METALS WITH BIS (2,4,4-TRIMETHYLPENTYL) PHOSPHINIC ACID [J].
SASTRE, AM ;
MIRALLES, N ;
FIGUEROLA, E .
SOLVENT EXTRACTION AND ION EXCHANGE, 1990, 8 (4-5) :597-614
[28]  
SMITH RM, 1981, SERIES CRITICAL STAB, V4
[29]  
SOLDENHOFF K, 1998, P 1998 EPD C
[30]   SOLVENT-EXTRACTION CHARACTERISTICS OF THIOSUBSTITUTED ORGANOPHOSPHINIC ACID EXTRACTANTS [J].
SOLE, KC ;
HISKEY, JB .
HYDROMETALLURGY, 1992, 30 (1-3) :345-365