Modeling of pore blocking and cake layer formation in membrane filtration for wastewater treatment

被引:103
作者
Broeckmann, A
Busch, J
Wintgens, T
Marquardt, W
机构
[1] Rhein Westfal TH Aachen, Lehrstuhl Prozesstech, D-52056 Aachen, Germany
[2] Rhein Westfal TH Aachen, Inst Verfahrenstech, D-52056 Aachen, Germany
关键词
membrane filtration; modeling; filtration resistances; cake layer formation; adhesion forces; pore blocking;
D O I
10.1016/j.desal.2005.06.018
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Membrane filtration in municipal and industrial wastewater treatment is a technology being, increasingly employed to enhance the quality of purified water, increase the productivity of existing plants, and build smaller, yet more effective purification processes. Barrier to a breakthrough of the technology is the increased operational cost due to fouling and membrane replacement. Simulation studies with rigorous process models are a powerful tool to increase the understanding of the process and its decisive characteristics in order to design optimal processes and efficient operational strategies. In this paper, two enhancements of existing modeling approaches are proposed. One is taking into account the adhesive forces between the particles and the membrane surface, which indeed strongly effect cake layer formation and back flushing efficiency. The other is assessing the decisive influence of particle and membrane pore size distributions on both cake layer formation and pore blocking and their mutual dependencies. Both phenomena are essential characteristics which need to be considered for a reliable prediction of process behavior. The model is successfully tested in simulation studies and compared to experimental data from a pilot wastewater treatment plant with submerged hollow fiber membranes.
引用
收藏
页码:97 / 109
页数:13
相关论文
共 25 条
  • [1] Bard Y., 1974, Nonlinear Parameter Estimation
  • [2] Membrane fouling in membrane bioreactors for wastewater treatment
    Chang, IS
    Le Clech, P
    Jefferson, B
    Judd, S
    [J]. JOURNAL OF ENVIRONMENTAL ENGINEERING, 2002, 128 (11) : 1018 - 1029
  • [3] CZICHOS H, 1996, GRUNDLAGEN INGENIEUR
  • [4] Study of filter cake formation mechanisms during tangential filtration of dust-laden gases at high temperature
    Ferrer, Y
    Templier, JC
    Gonthier, Y
    Bernis, A
    [J]. POWDER TECHNOLOGY, 2000, 113 (1-2) : 197 - 204
  • [5] MODELING THE EFFECTS OF PARTICLE POLYDISPERSITY IN CROSS-FLOW FILTRATION
    FOLEY, G
    MALONE, DM
    MACLOUGHLIN, F
    [J]. JOURNAL OF MEMBRANE SCIENCE, 1995, 99 (01) : 77 - 88
  • [6] Hydrodynamic model for three-phase internal- and external-loop airlift reactors
    Freitas, C
    Fialová, M
    Zahradnik, J
    Teixeira, JA
    [J]. CHEMICAL ENGINEERING SCIENCE, 1999, 54 (21) : 5253 - 5258
  • [7] Modelling of liquid circulation velocity in concentric-tube airlift reactors
    Gavrilescu, M
    Tudose, RZ
    [J]. CHEMICAL ENGINEERING JOURNAL, 1998, 69 (02) : 85 - 91
  • [8] The London - Van Der Waals attraction between spherical particles
    Hamaker, HC
    [J]. PHYSICA, 1937, 4 : 1058 - 1072
  • [9] A simple hydrodynamic model for the liquid circulation velocity in a full-scale two- and three-phase internal airlift reactor operating in the gas recirculation regime
    Heijnen, JJ
    Hols, J
    vanderLans, RGJM
    vanLeeuwen, HLJM
    Mulder, A
    Weltevrede, R
    [J]. CHEMICAL ENGINEERING SCIENCE, 1997, 52 (15) : 2527 - 2540
  • [10] Cross-flow microfiltration of submicron microbial suspension
    Hwang, KJ
    Yu, YH
    Lu, WM
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2001, 194 (02) : 229 - 243