Optimising dose of antiscalant in membrane filtration systems using a desupersaturation unit

被引:1
|
作者
Bremere, I [1 ]
Kennedy, M [1 ]
Johnson, A [1 ]
Witkamp, GA [1 ]
Schippers, J [1 ]
机构
[1] UNESCO, IHE, NL-2601 DA Delft, Netherlands
来源
MEMBRANES IN DRINKING AND INDUSTRIAL WATER PRODUCTION III | 2003年
关键词
barium sulphate; desupersaturation; organic matter; reverse osmosis; scaling control;
D O I
10.2166/ws.2003.0161
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The strategy behind the desupersaturation unit (DU) is rapid desupersatu ration of the membrane concentrate stream by forced precipitation of sparingly soluble inorganic compounds on seed crystals. The efficiency of deposition will depend on the supersaturation and the condition of seeds, i.e. their reactivity. Poisoning of seeds by adsorption of natural organic matter and/or added commercial antiscalant will hinder the desupersaturation efficiency by blocking centres available for crystallisation. Barium sulphate precipitation in a laboratory scale DU was examined from natural reverse osmosis (RO) concentrates from surface water treatment pilot plant. Tests indicated similar effects on poisoning the barite seed grains by commercial antiscalant and natural organic matter from surface water (the Rhine River) treatment RO pilot plant (80% conversion) while no effect was observed from supersaturated synthetic (no organic matter) concentrate. An attempt was made to relate the effects of organic matter and the RO system conversion (50-85%). The rate of barite seed grain poisoning was attributed to the relative barium supersaturation in the concentrate. The efficiency of natural organic compounds started to decline above the supersaturation ratio of 3.3. Addition of commercial antiscalant enhanced the effect of natural organic matter. If the effects of organic matter in membrane systems are quantified and related to the RO system conversion, a laboratory DU can practically be used to control scaling.
引用
收藏
页码:147 / 153
页数:7
相关论文
共 50 条
  • [1] Controlling scaling in membrane filtration systems using a desupersaturation unit
    Bremere, I
    Kennedy, M
    Michel, P
    van Emmerik, R
    Witkamp, GJ
    Schippers, J
    DESALINATION, 1999, 124 (1-3) : 51 - 62
  • [2] Increasing conversion in membrane filtration systems using a desupersaturation unit to prevent scaling
    Bremere, I
    Kennedy, MD
    Johnson, A
    van Emmerik, R
    Witkamp, GJ
    Schippers, JC
    DESALINATION, 1998, 119 (1-3) : 199 - 204
  • [3] Using antiscalant in membrane fouling (MD)
    Humoud, Madihah
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2017, 254
  • [4] Optimising the flow through a concertinaed filtration membrane
    Pereira, Victoria E.
    Dalwadi, Mohit P.
    Ruiz-Trejo, Enrique
    Griffiths, Ian M.
    JOURNAL OF FLUID MECHANICS, 2021, 913
  • [5] Optimising the flow through a concertinaed filtration membrane
    Pereira, Victoria E.
    Dalwadi, Mohit P.
    Ruiz-Trejo, Enrique
    Griffiths, Ian M.
    Journal of Fluid Mechanics, 2021, 913
  • [6] MEMBRANE FILTRATION SYSTEMS
    ENTIS, P
    FOOD TECHNOLOGY, 1985, 39 (03) : 52 - 52
  • [7] Optimization of membrane filtration systems
    Kalboussi, Nesrine
    Harmand, Jerome
    Ellouze, Fatma
    Ben Amar, Nihel
    2017 INTERNATIONAL CONFERENCE ON CONTROL, AUTOMATION AND DIAGNOSIS (ICCAD), 2017, : 258 - 262
  • [8] MEMBRANE-FILTRATION-UNIT FOR ANALYTICAL PURPOSES
    GEPPERT, G
    THIELEMANN, H
    CHEMISCHE TECHNIK, 1983, 35 (10): : 517 - 519
  • [9] Selecting membrane filtration systems
    Chen, W
    Parma, F
    Patkar, A
    Elkin, A
    Sen, S
    CHEMICAL ENGINEERING PROGRESS, 2004, 100 (12) : 22 - 25
  • [10] Purification of poly(acrylic acid) using a membrane ultra-filtration unit in flow
    Brocken, Laurens
    Price, Paul D.
    Whittaker, Jane
    Baxendale, Ian R.
    REACTION CHEMISTRY & ENGINEERING, 2017, 2 (05): : 656 - 661