Concentration and purification of chromate from electroplating wastewater by two-stage electrodialysis processes

被引:70
作者
Chen, Shiao-Shing [2 ]
Li, Chi-Wang [1 ]
Hsu, Hong-Der [2 ]
Lee, Po-Ching [1 ]
Chang, Yu-Min [2 ]
Yang, Chia-Hao [2 ]
机构
[1] Tamkang Univ, Dept Water Resources & Environm Engn, Tamsui 251, Taipei County, Taiwan
[2] Natl Taipei Univ Technol, Inst Environm Engn & Management, Taipei 106, Taiwan
关键词
Chromate; Concentration; Purification; Two-stage electrodialysis; Electroplating wastewater; TRIVALENT CHROMIUM; ACID RECOVERY; EXCHANGE; SEPARATION; CR(VI); IONS;
D O I
10.1016/j.jhazmat.2008.04.106
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A designed two-stage electrodialysis system is proposed to concentrate and purify chromate from a low pH electroplating wastewater using monovalent selective electrodialysis membranes. With low pH of the raw water (pH 2.2) in the first stage. chromate was presented as HCrO4- and monovalent ions (HCrO4-, NH2SO3-, Na+ and Cl-) were able to pass through the membrane thus chromate was concentrated up to 191%. Higher current density, flowrate and more membrane area all increased the chromium recovery. When pH was adjusted to 8.5 before entering the second stage, the chromate species was presented as divalent CrO42- and retained in the concentrated stream, and the rest monovalent ions (NH2SO3-, Na+ and Cl-) were separated by passing through the membrane. For example, 45% of the chlorides were separated in this study. The separation efficiencies in the second stage were also increased when the current density, flowrate and membrane area were increased. Electron Spectroscopy for Chemical Analysis was used to examine the surface chromate species for stage 1, and anion exchange membrane showed more chromate fouling comparing to cation exchange membrane due to more adsorption and concentration polarization effects for the anion exchange membrane. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:1075 / 1080
页数:6
相关论文
共 21 条
  • [1] [Anonymous], 1998, Standard Methods for the Examination of Water and Wastewater
  • [2] Electrochemical treatment of cigarette industry wastewater: feasibility study
    Bejankiwar, RS
    [J]. WATER RESEARCH, 2002, 36 (17) : 4386 - 4390
  • [3] Cr(VI) transport through ceramic ion-exchange membranes for treatment of industrial wastewaters
    Dzyazko, Yu. S.
    Mahmoud, A.
    Lapicque, F.
    Belyakov, V. N.
    [J]. JOURNAL OF APPLIED ELECTROCHEMISTRY, 2007, 37 (02) : 209 - 217
  • [4] Electrosorption of chromium ions on carbon aerogel electrodes as a means of remediating ground water
    Farmer, JC
    Bahowick, SM
    Harrar, JE
    Fix, DV
    Martinelli, RE
    Vu, AK
    Carroll, KL
    [J]. ENERGY & FUELS, 1997, 11 (02) : 337 - 347
  • [5] Chromic acid recovery by electro-electrodialysis II. Pilot scale process, development, and optimization
    Frenzel, I
    Holdik, H
    Stamatialis, DF
    Pourcelly, G
    Wessling, A
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2005, 47 (1-2) : 27 - 35
  • [6] Chromic acid recovery by electro-electrodialysis - I. Evaluation of anion-exchange membrane
    Frenzel, I
    Holdik, H
    Stamatialis, DF
    Pourcelly, G
    Wessling, A
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2005, 261 (1-2) : 49 - 57
  • [7] Treatment of complexed copper(II) solutions with electrochemical membrane processes
    Juang, RS
    Lin, LC
    [J]. WATER RESEARCH, 2000, 34 (01) : 43 - 50
  • [8] Electrochemical membrane reactor: In situ separation and recovery of chromic acid and metal ions
    Khan, Jeeshan
    Tripathi, Bijay P.
    Saxena, Arunima
    Shahi, Vinod K.
    [J]. ELECTROCHIMICA ACTA, 2007, 52 (24) : 6719 - 6727
  • [9] Separation of sodium ions from trivalent chromium by electrodialysis using monovalent cation selective membranes
    Lambert, J.
    Avila-Rodriguez, M.
    Durand, G.
    Rakib, M.
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2006, 280 (1-2) : 219 - 225
  • [10] Cadmium electroplating wastewater treatment using a laboratory-scale electrodialysis system
    Marder, L
    Bernardes, AM
    Ferreira, JZ
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2004, 37 (03) : 247 - 255