Continuous ion-exchange membrane electrodialysis of mother liquid discharged from a salt-manufacturing plant and transport of Cl- ions and SO42- ions

被引:0
|
作者
Tanaka, Yoshinobu [1 ]
Uchino, Hazime [2 ]
Murakami, Masayoshi [3 ]
机构
[1] IEM Res, Ushiki, Ibaraki 3001216, Japan
[2] Tokai Univ, Coll Marine Sci & Technol, Shimizu Ku, Shizuoka 4248610, Japan
[3] Japan Fine Salt Co Ltd, Kawasaki Ku, Kawasaki, Kanagawa 2100863, Japan
来源
MEMBRANE AND WATER TREATMENT | 2012年 / 3卷 / 01期
关键词
ion-exchange membrane; electrodialysis; saline water concentration; ion transport; permselectivity; salt production; LIMITING CURRENT-DENSITY; WASTE-WATER; SEPARATION; DIVALENT; MONOVALENT; DIFFUSION; ANIONS;
D O I
暂无
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Mother liquid discharged from a salt-manufacturing plant was electrodialyzed at 25 and 40 degrees C in a continuous process integrated with SO42- ion low-permeable anion-exchange membranes to remove Na2SO4 and recover NaCl in the mother liquid. Performance of electrodialysis was evaluated by measuring ion concentration in a concentrated solution, permselectivity coefficient of SO42- ions against Cl- ions, current efficiency, cell voltage, energy consumption to obtain one ton of NaCl and membrane pair characteristics. The permselectivity coefficient of SO42- ions against Cl- ions was low enough particularly at 40 degrees C and SO42- transport across anion-exchange membranes was prevented successfully. Applying the overall mass transport equation, Cl- ion and SO42- ion transport across anion-exchange membranes is evaluated. SO42- ion transport number is decreased due to the decrease of electro-migration of SO42- ions across the anion-exchange membranes. SO42- ion concentration in desalting cells becomes higher than that in concentration cells and SO42- ion diffusion is accelerated across the anion-exchange membranes from desalting cells toward concentrating cells.
引用
收藏
页码:63 / 76
页数:14
相关论文
共 19 条