Application of the mass action law to describe ion exchange equilibrium in a fixed-bed column

被引:31
作者
Borba, C. E. [1 ]
Silva, E. A. [1 ]
Spohr, S. [1 ]
Santos, G. H. F. [1 ]
Guirardello, R. [2 ]
机构
[1] Univ Estadual Oeste Parana, UNIOESTE, Sch Chem Engn, BR-85903000 Toledo, PR, Brazil
[2] Univ Estadual Campinas, UNICAMP, Sch Chem Engn, BR-13083872 Campinas, SP, Brazil
关键词
Fixed bed; Ion exchange; Mass action law; AQUEOUS-SOLUTIONS; AMBERLITE IR-120; PACKED-BEDS; RESIN; PREDICTION; REMOVAL; ADSORPTION; SYSTEMS; ZN(II); DIFFUSION;
D O I
10.1016/j.cej.2011.06.002
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Ion exchange experiments were carried out in a fixed-bed column employing the binary systems Cu2+-Na+ and Zn2+-Na+. Amberlite IR 120 was used as the ion exchange resin. The ion exchange dynamics within the column was described by a model considering the external mass transfer and the diffusion within the particle. A linear driving force model was used to represent the mass transfer within the resin particles. The model considered the thermodynamic equilibrium on the liquid-solid interface, which was described by the Langmuir isotherm and by the mass action law. The results indicate that both models represent well the ion exchange dynamics in all cases. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:312 / 320
页数:9
相关论文
共 37 条
[1]   Chromium(III) recovery from waste acid solution by ion exchange processing using Amberlite IR-120 resin: batch and continuous ion exchange modelling [J].
Alguacil, FJ ;
Alonso, M ;
Lozano, LJ .
CHEMOSPHERE, 2004, 57 (08) :789-793
[2]  
[Anonymous], CRC HDB CHEM PHYS
[3]   Removal of Cr(III) in the fixed bed column and batch reactors using as adsorbent zeolite NaX [J].
Barrosa, MASD ;
Silva, EA ;
Arroyo, PA ;
Tavares, CRG ;
Schneider, RM ;
Suszek, M ;
Sousa-Aguiar, EF .
CHEMICAL ENGINEERING SCIENCE, 2004, 59 (24) :5959-5966
[4]   Ion Exchange Equilibrium Prediction for the System Cu2+-Zn2+-Na+ [J].
Borba, C. E. ;
Silva, E. A. ;
Spohr, S. ;
Santos, G. H. F. ;
Guirardello, R. .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2010, 55 (03) :1333-1341
[5]   THERMODYNAMIC PROPERTIES OF STRONG ELECTROLYTES IN AQUEOUS-SOLUTIONS [J].
BROMLEY, LA .
AICHE JOURNAL, 1973, 19 (02) :313-320
[6]   Generalized linear driving force approximation for adsorption of multicomponent mixtures [J].
Cruz, P ;
Magalhaes, FD ;
Mendes, A .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (11) :3519-3531
[7]   CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES [J].
DANCKWERTS, PV .
CHEMICAL ENGINEERING SCIENCE, 1953, 2 (01) :1-13
[8]   Adsorption of Cu(II), Zn(II), Ni(II), Pb(II), and Cd(II) from aqueous solution on amberlite IR-120 synthetic resin [J].
Demirbas, A ;
Pehlivan, E ;
Gode, F ;
Altun, T ;
Arslan, G .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2005, 282 (01) :20-25
[9]   MULTICOMPONENT ION EXCHANGE COLUMN CALCULATIONS [J].
DRANOFF, JS ;
LAPIDUS, L .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1958, 50 (11) :1648-1653
[10]   Effects of mass action equilibria oil fixed-bed multicomponent ion-exchange dynamics [J].
Ernest, MV ;
Whitley, RD ;
Ma, ZD ;
Wang, NHL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (01) :212-226