Seawater electrodialysis with preferential removal of divalent ions

被引:100
作者
Galama, A. H. [1 ,2 ]
Daubaras, G. [2 ]
Burheim, O. S. [3 ]
Rijnaarts, H. H. M. [1 ]
Post, J. W. [1 ,4 ]
机构
[1] Wageningen Univ, Subdept Environm Technol, NL-6700 EV Wageningen, Netherlands
[2] Welsus, Ctr Excellence Sustainable Water Technol, NL-8900 CC Leeuwarden, Netherlands
[3] HIST Sor Trondelag Univ Coll, Dept Elect & Comp Engn, N-7004 Trondheim, Norway
[4] KWR Watercycle Res Inst, NL-3430 BB Nieuwegein, Netherlands
关键词
Electrodialysis; Seawater; Current density; Divalent ions; Separation; CATION-EXCHANGE MEMBRANES; OF-THE-ART; NANOFILTRATION MEMBRANES; DIFFUSION-COEFFICIENTS; REVERSE-OSMOSIS; CALCIUM-SULFATE; BOUNDARY-LAYER; MONOVALENT; DESALINATION; SEPARATION;
D O I
10.1016/j.memsci.2013.10.050
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work desalination of a ternary salt mixture and at North Sea water is studied with a lab scale electrodialysis stack, which was used in a recycling batch mode. During desalination samples were taken and the ionic composition of the dilute stream was determined. The effect of applied current density (10-300 A/m(2)) On this composition was investigated. A clear effect of applied current density was observed. A lower applied current density leads to a more complete reduction in concentration of divalent ions, in an earlier extent of desalination. This influence of the applied current density could be related to the concentration polarization effects that occur in the diffusional boundary layer and are explained with a model based on the Nernst-Planck flux equation. It was found that the lower initial ion concentration of Ca2+, Mg2+ but also of K+ and SO42- compared to respectively Na+ and Cl-, leads to stronger depletion of these ions in the transport layer adjacent the membrane. These boundary layer effects are more pronounced at higher applied current densities, resulting in reduced transport of ions with a low initial concentration. High monovalent over divalent ion ratios can be found at low applied current. (C) 2013 Elsevier By. All rights reserved.
引用
收藏
页码:219 / 228
页数:10
相关论文
共 58 条
  • [1] Multi-effect distillation plants: state of the art
    Al-Shammiri, M
    Safar, M
    [J]. DESALINATION, 1999, 126 (1-3) : 45 - 59
  • [2] CONVENTIONAL PRETREATMENT OF SURFACE SEAWATER FOR REVERSE-OSMOSIS APPLICATION, STATE OF THE ART
    ALBORNO, AY
    ABDELJAWAD, M
    [J]. DESALINATION, 1989, 74 (1-3) : 3 - 36
  • [3] Alternative design to dual stage NF seawater desalination using high rejection brackish water membranes
    AlTaee, Ali
    Sharif, Adel O.
    [J]. DESALINATION, 2011, 273 (2-3) : 391 - 397
  • [4] A modified anion-exchange membrane applied to purification of effluent containing different anions. Pre-treatment before desalination
    Amara, Mourad
    Kerdjoudj, Hacene
    [J]. DESALINATION, 2007, 206 (1-3) : 205 - 209
  • [5] Current-Induced Membrane Discharge
    Andersen, M. B.
    van Soestbergen, M.
    Mani, A.
    Bruus, H.
    Biesheuvel, P. M.
    Bazant, M. Z.
    [J]. PHYSICAL REVIEW LETTERS, 2012, 109 (10)
  • [6] [Anonymous], 2004, ION EXCHANGE MEMBRAN
  • [7] Two-fluid model for the simultaneous flow of colloids and fluids in porous media
    Biesheuvel, P. M.
    [J]. JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2011, 355 (02) : 389 - 395
  • [8] TRANSPORT COMPETITION BETWEEN MONOVALENT AND DIVALENT-CATIONS THROUGH CATION-EXCHANGE MEMBRANES - EXCHANGE ISOTHERMS AND KINETIC CONCEPTS
    CHAPOTOT, A
    POURCELLY, G
    GAVACH, C
    [J]. JOURNAL OF MEMBRANE SCIENCE, 1994, 96 (03) : 167 - 181
  • [9] Crespo J.G., 1993, Membrane Processes in Separation Purification
  • [10] On the resistances of membrane, diffusion boundary layer and double layer in ion exchange membrane transport
    Dlugolecki, Piotr
    Ogonowski, Piotr
    Metz, Sybrand J.
    Saakes, Michel
    Nijmeijer, Kitty
    Wessling, Matthias
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2010, 349 (1-2) : 369 - 379