Modelling the transport of Cl- ions through the anion-exchange membrane NEOSEPTA-AFN -: Systems HCl/membrane/H2O and HCl-FeCl3/membrane/H2O

被引:37
|
作者
Palaty, Z [1 ]
Zaková, A [1 ]
Dolecek, P [1 ]
机构
[1] Univ Pardubice, Dept Chem Engn, Pardubice 53210, Czech Republic
关键词
diffusion dialysis; anion-exchange membrane; HCl-FeCl3; solutions; solution/membrane equilibrium;
D O I
10.1016/S0376-7388(99)00239-2
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The paper deals with the diffusion dialysis of hydrochloric acid in a mixed batch cell with an anion-exchange membrane NEOSEPTA-AFN. The systems HCl/membrane/H2O and HCl-FeCl3/membrane/H2O were investigated. The overall dialysis coefficient and the membrane mass transfer coefficient were used for a quantitative evaluation of the mass transfer rate of Cl- ions in the membrane. Both these quantities were calculated by numerical integration of differential equations, which describe the unsteady state transport of Cl- ions, with subsequent optimization procedure. The model suggested presumes the zero flux of Fe3+ ions, existing equilibria and mass transfer resistances on both sides of the membrane. It was found that, in the range of HCl concentration from 0.27 to 3.48 kmol m(-3), and of Fe3+ ions from 0.17 to 1.66 kmol m(-3), the rate of transport of Cl- ions decreases with increasing concentration of Fe3+ ions in the solution dialyzed. (C)2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:237 / 249
页数:13
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