Extraction of cobalt(II) and nickel(II) by a solvent impregnated resin containing bis(2,4,4-trimethylpentyl)monothiophosphinic acid

被引:13
作者
Mu, F. T. [1 ]
Jia, Q. [1 ]
Tian, Y. M. [1 ]
Shang, Q. K. [2 ]
机构
[1] Jilin Univ Nanling Campus, Coll Chem, Changchun 130022, Peoples R China
[2] NE Normal Univ, Coll Chem, Changchun 130024, Peoples R China
来源
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY | 2008年 / 14卷 / 01期
关键词
extraction; cobalt; nickel; solvent impregnated resin; bis(2,4,4-trimethylpentyl)monothiophosphinic acid;
D O I
10.1007/s10450-007-9043-3
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In the present work, studies have been conducted on the equilibrium distribution of cobalt (II) and nickel (II) between aqueous hydrochloric solution and macromolecular resin impregnated with bis(2,4,4-trimethylpentyl)monothiophosphinic acid (Cyanex302, HL). Effects of extraction time, pH values, metal ion concentration, and temperature were investigated. Analysis of the results shows that the extraction of the two metal ions can be explained assuming the formation of metal complexes in the resin phase with a general composition ML (2). An extraction reaction is proposed and the equilibrium constants of the complexes were determined. The Freundlich isotherm and thermodynamic quantities, i.e., Delta G, Delta H and Delta S were also obtained. Both of the extraction reactions of cobalt (II) and nickel (II) are endothermic ones. The efficiency of the resin in the separation of cobalt (II) and nickel (II) is provided according to the separation factors. Under the experimental conditions employed, pH(50) values for cobalt (II) and nickel (II) are 3.76, 5.01, respectively. The logarithmic value of separation factor was calculated as 2.50.
引用
收藏
页码:31 / 36
页数:6
相关论文
共 30 条
[1]   SORPTION AND SEPARATION OF DIVALENT METALS BY A MACROMOLECULAR RESIN CONTAINING ORGANOPHOSPHORUS ACIDS [J].
AKITA, S ;
TAKEUCHI, H .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1992, 37 (03) :303-306
[2]  
Castillo E, 1999, SOLVENT EXTR ION EXC, V17, P1571
[3]   Distribution studies of Zn(II), Cu(II) and Cd(II) with Levextrel resins containing di(2,4,4-trimethylpentyl)phosphinic acid (Lewatit TP807'84) [J].
Cortina, JL ;
Miralles, N ;
Aguilar, M ;
Sastre, AM .
HYDROMETALLURGY, 1996, 40 (1-2) :195-206
[4]  
CORTINA JL, 1997, ION EX SOLV, V13, P195
[5]   SELECTIVITY-STRUCTURE TRENDS IN THE EXTRACTION OF CO(II) AND NI(II) BY DIALKYL PHOSPHORIC, ALKYL ALKYLPHOSPHONIC, AND DIALKYLPHOSPHINIC ACIDS [J].
DANESI, PR ;
REICHLEYYINGER, L ;
MASON, G ;
KAPLAN, L ;
HORWITZ, EP ;
DIAMOND, H .
SOLVENT EXTRACTION AND ION EXCHANGE, 1985, 3 (04) :435-452
[6]   THE SOLVENT-EXTRACTION SEPARATION OF COBALT AND NICKEL USING 2-ETHYLHEXYLPHOSPHONIC ACID MONO-2-ETHYLHEXYL ESTER [J].
DREISINGER, DB ;
COOPER, WC .
HYDROMETALLURGY, 1984, 12 (01) :1-20
[7]  
ENSOR DD, 2002, 223 ACS NAT M IEC 06
[8]  
FEATHER AM, 1996, VALUE ADDING SOLVENT, P511
[9]   EQUILIBRIUM AND MASS-TRANSFER FOR THE EXTRACTION OF COBALT AND NICKEL FROM SULFATE-SOLUTIONS INTO BIS (2,4,4-TRIMETHYLPENTYL) PHOSPHINIC ACID - CYANEX-272 [J].
FU, X ;
GOLDING, JA .
SOLVENT EXTRACTION AND ION EXCHANGE, 1988, 6 (05) :889-917
[10]   Selective separation of Fe(III), Cd(II), and Ni(II) from dilute solutions using solvent-impregnated resins [J].
Gonzalez, MP ;
Saucedo, I ;
Navarro, R ;
Avila, M ;
Guibal, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (25) :6004-6013