Chromic acid recovery by electro-electrodialysis II. Pilot scale process, development, and optimization

被引:23
作者
Frenzel, I
Holdik, H
Stamatialis, DF
Pourcelly, G
Wessling, A
机构
[1] Univ Twente, Fac Sci & Technol, Membrane Technol Grp, NL-7500 AE Enschede, Netherlands
[2] FuMA Tech GmbH, D-66386 St Ingbert, Germany
[3] Univ Montpellier 2, IEM, CNRS,UMR 5635,ENSCM,UM2, Inst Europeen Membranes, F-34095 Montpellier, France
关键词
electro-electrodialysis; chromic acid recovery; anion exchange membrane; industrial implementation;
D O I
10.1016/j.seppur.2005.06.002
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Electro-electrodialysis is a promising technology for chromic acid recovery and static rinse water purification. It combines the recovery of the plating chemicals from rinse water, the elimination of metallic impurities from the process and rinse water treatment in one step. Previous industrial use was restricted due to non-resistant anion-exchange membranes and process ineffectiveness. In this work, a stable and economical process is developed and high-quality chromic acid is recovered using a new oxidative stable anion exchange membrane (AEM Fumasep(R) FAP, FuMA-Tech GmbH). The membrane stability and performance is evaluated by a long-term experiment for 400 h. Recovery rates were determined for batch and continuous operation and at different operation temperatures. The highest chromic acid production was reached by batch processing at 40 degrees C. Both measures increase significantly the chromate transfer and result in lower equipment size and operational costs. (C) 2005 Published by Elsevier B.V.
引用
收藏
页码:27 / 35
页数:9
相关论文
共 15 条
[1]   Loss of permselectivity of anion exchange membranes in contact with zinc chloride complexes [J].
Aouad, F ;
Lindheimer, A ;
Chaouki, M ;
Gavach, C .
DESALINATION, 1999, 121 (01) :13-22
[2]  
AUDINOS R, 1992, SEPARATION PURIFICAT, P229
[3]  
BERGMANN H, 1997, GALVANOTECHNIK, V88, P775
[4]  
BLATT W, 1996, METALLOBERFLACHE, V50, P694
[5]  
FRENZEL I, IN PRESS J MEMBR SCI
[6]  
HARTINGER L, 1991, HDB ABWASSER REYCLIN
[7]  
Mandich NV, 1997, PLAT SURF FINISH, V84, P108
[8]  
MUHLE A, 2002, METALLOBERFLACHE, V56, P12
[9]  
POURCELLY G, 2003, P WORKSH ENV CLEAN T
[10]  
Sarmaitis R, 1996, PLAT SURF FINISH, V83, P53