Simulation of multistage electrodialysis

被引：6

作者：

Cruz, GPT

Nii, S

Kawaizumi, F

Takahashi, K ^{[1
]}

机构：

[1] Nagoya Univ, Dept Chem Engn, Nagoya, Aichi 4648603, Japan

[2] De La Salle Univ, Dept Chem Engn, Manila, Philippines

来源：

JOURNAL OF CHEMICAL ENGINEERING OF JAPAN | 1999年 / 32卷 / 01期

关键词：

electrodialysis; multistage operation; ion exchange membrane; permselectivity; separation factor;

D O I：

10.1252/jcej.32.142

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

A simulation for multistage electrodialysis for separation of metal ions is developed, The experimental results for the separation of potassium and sodium ions by a 4-stage electrodialyzer are compared, and can be satisfactorily reproduced by the present simulation method. It is observed that the separation factor increases largely with increasing stage number and flow rate of reflux, The increase in the stage number is effective to achieve a large separation factor and a large recovery fraction of potassium.

引用

页码：142 / 145

页数：4