Ion Exchange Equilibrium Prediction for the System Cu2+-Zn2+-Na+

被引:14
作者
Borba, C. E. [1 ]
Silva, E. A. [2 ]
Spohr, S. [2 ]
Santos, G. H. F. [2 ]
Guirardello, R. [1 ]
机构
[1] Univ Estadual Campinas, UNICAMP, Sch Chem Engn, BR-13083970 Campinas, SP, Brazil
[2] Univ Estadual Oeste Parana, UNIOESTE, Sch Chem Engn, BR-85903000 Toledo, PR, Brazil
关键词
AQUEOUS-SOLUTIONS; AMBERLITE IR-120; CA2+ IONS; CLINOPTILOLITE; ELECTROLYTES; TERNARY; RESINS; NA+; H+; REMOVAL;
D O I
10.1021/je900649e
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this work, ion exchange experimental data were obtained in batch operation for the binary systems Cu2+-Na+, Zn2+-Na+, and Zn2+-Cu2+ and for the ternary system Cu2+-Zn2+-Na+. The ionic exchanger employed was the cationic resin Amberlite IR 120. The experimental data for the binary systems and the ternary system were obtained at total concentrations of (1, 3, and 5) mEq.L-1. The total exchange capacity of the Amberlite IR 120 resin was obtained by the column technique. All experiments were carried Out at 25 degrees C. To model the ion exchange equilibrium, the Mass Action Law Was used. The model considered both ideal and nonideal behavior to represent the experimental data. The nonideality in the Solution phase and in the resin phase was described by Bromley's model and by Wilson's model. Wilson's model interaction parameters and the thermodynamic equilibrium constants were obtained from the experimental data for each binary system, from which ternary system ion exchange equilibrium was predicted. Oil the basis of the results obtained to represent the ion exchange equilibrium for the binary systems, a prediction was made using only the nonideal Mass Action Law. Good agreement was obtained between the calculated and Measured values of the resin phase composition.
引用
收藏
页码:1333 / 1341
页数:9
相关论文
共 29 条
[11]   Multicomponent equilibria on ion-exchange resins [J].
Melis, S ;
Markos, J ;
Cao, G ;
Morbidelli, M .
FLUID PHASE EQUILIBRIA, 1996, 117 (1-2) :281-288
[12]   Equilibrium studies of phenylalanine and tyrosine on ion-exchange resins [J].
Moreira, MJA ;
Ferreira, LMGA .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (18) :5022-5034
[13]   A SIMPLEX-METHOD FOR FUNCTION MINIMIZATION [J].
NELDER, JA ;
MEAD, R .
COMPUTER JOURNAL, 1965, 7 (04) :308-313
[14]   Experimental and modeling study of ion exchange between aqueous solutions and the zeolite mineral clinoptilolite [J].
Pabalan, RT ;
Bertetti, EP .
JOURNAL OF SOLUTION CHEMISTRY, 1999, 28 (04) :367-393
[15]   Heavy metal removal by clinoptilolite. An equilibrium study in multi-component systems [J].
Petrus, R ;
Warchol, JK .
WATER RESEARCH, 2005, 39 (05) :819-830
[16]   Ion exchange equilibria between clinoptilolite and aqueous solutions of Na+/Cu2+, Na+/Cd2+ and Na+/Pb2+ [J].
Petrus, R ;
Warchol, J .
MICROPOROUS AND MESOPOROUS MATERIALS, 2003, 61 (1-3) :137-146
[17]   THERMODYNAMICS OF ELECTROLYTES .1. THEORETICAL BASIS AND GENERAL EQUATIONS [J].
PITZER, KS .
JOURNAL OF PHYSICAL CHEMISTRY, 1973, 77 (02) :268-277
[18]  
Puigdomenech I., 2004, HYDRA: Hydrochemical equilibrium-constant database
[19]   Combination of the steric mass action and non-ideal surface solution models for overload protein ion-exchange chromatography [J].
Raje, P ;
Pinto, NG .
JOURNAL OF CHROMATOGRAPHY A, 1997, 760 (01) :89-103
[20]   AN IMPROVED MODEL FOR THE PREDICTION OF MULTICOMPONENT ION-EXCHANGE EQUILIBRIA [J].
SHALLCROSS, DC ;
HERRMANN, CC ;
MCCOY, BJ .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (02) :279-288