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The Research of the Flow Characteristics in Spiral Membrane Separator

Received: 24 January 2019     Accepted: 17 March 2019     Published: 8 April 2019
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Abstract

The spiral membrane separator is a novel module proposed for reducing the concentration polarization and membrane fouling of membrane separation process. This membrane separation process benefits from dean vortices produced by centrifugal instability in enhancing fluid mass transfer. A numerical stimulation of this membrane separation is presented and used to analyze the fluid flow characteristics and thoroughly understand the separation mechanism. The numerical model consists of a spiral flow path with rectangular sector. As the simulation with infiltration, the fluid domain of the ceramic membrane tube was as a porous medium domain. The standard momentum equation, added with the momentum equation source term which composed of the viscosity loss term and the inertia loss term, are figured out through the experimental characterization. In the simulation of spiral membrane separation, the Dean secondary flow structure is identified and found to enhance fluid mass transfer and to increase the permeate flux. The critical unstable state of spiral membrane separation is accordingly De=246 without the flow permeation and De=863 with the permeation, where Dean vortices cause collisions and the mixing of fluid particles. Then in the case of permeation, the fluid in separator at De=1232 is numerically simulated to show that the higher flow velocity and a large fluctuating trend of wall shear stress near the membrane surface (inside), which mainly contributed to alleviate concentration polarization and membrane fouling.

Published in American Journal of Water Science and Engineering (Volume 5, Issue 1)
DOI 10.11648/j.ajwse.20190501.15
Page(s) 29-36
Creative Commons

This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.

Copyright

Copyright © The Author(s), 2019. Published by Science Publishing Group

Keywords

Membrane Separation, Secondary Flow, Numerical Simulation

References
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[4] Wang Xiaolin (2001). Fouling and degradation of membranes and their prevention and control. Industrial Water Treatment 21, 1-5.
[5] Liu Zhongzhou, Zhang Guojun and Ji Shulan (2006). Methods and strategies of study on concentration polarization and membrane fouling. Membrane Science and Technology 26, 1-15.
[6] Jinwei Wang, Farhad Zamani, Andy Cahyadi, Jia Yuan Toh and Jia Wei Chew (2016). Correlating the hydrodynamics of fluidized granular activated carbon (GAC) with membrane-fouling mitigation. Journal of Membrane Science 510, 38-49.
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[8] T. Lohaus, N. Herkenhoff, R. Shankar and M. Wessling (2018). Feed flow patterns of combined Rayleigh-Bénard convection and membrane permeation. Journal of Membrane Science 549, 60-66.
[9] Takaaki Akagi, Takafumi Horie, Hayato Masuda, Keigo Matsuda and Yushi Hirata (2018). Improvement of separation performance by fluid motion in the membrane module with a helical baffle. Separation and Purification Technology 198, 52-59.
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[12] Kaufhold, D.a, Kopf, F.b, Wolff, C.c, Beutel, S.c, Hilterhaus, L.a, Hoffmann, M.b, Scheper, T.c, Schlüter, M.b and Liese, A.a (2012). Generation of Dean vortices and enhancement of oxygen transfer rates in membrane contactors for different hollow fiber geometries. Journal of Membrane Science 423-424, 342-347.
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[14] Ph Moulin, D Veyret and F Charbit (2001). Dean vortices: comparison of numerical simulation of shear stress and improvement of mass transfer in membraneprocesses at low permeation fluxes. Journal of Membrane Science 183, 149-162.
[15] Manno, P., Moulin, P., Rouch, J. C., Clifton, M. and Aptel, P. (1998). Mass transfer improvement in helically wound hollow fiber ultrafiltration modules Yeast suspensions. Separation and Purification Technology 14, 175-182.
[16] Bubolz, M., Wille, M., Langer, G. and Werner, U. (2002). The use of dean vortices for crossflow microfiltration: Basic principles and further investigation. Separation and Purification Technology 26, 81-89.
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[18] Seyed Pouria Motevalian, Ali Borhan, Hongyi Zhou and Andrew Zydney (2016). Twisted hollow fiber membranes for enhanced mass transfer. Journal of Membrane Science 514, 586-594.
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  • APA Style

    Zhou Xiantao, Liu Hui, Wan Xuhui. (2019). The Research of the Flow Characteristics in Spiral Membrane Separator. American Journal of Water Science and Engineering, 5(1), 29-36. https://doi.org/10.11648/j.ajwse.20190501.15

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    ACS Style

    Zhou Xiantao; Liu Hui; Wan Xuhui. The Research of the Flow Characteristics in Spiral Membrane Separator. Am. J. Water Sci. Eng. 2019, 5(1), 29-36. doi: 10.11648/j.ajwse.20190501.15

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    AMA Style

    Zhou Xiantao, Liu Hui, Wan Xuhui. The Research of the Flow Characteristics in Spiral Membrane Separator. Am J Water Sci Eng. 2019;5(1):29-36. doi: 10.11648/j.ajwse.20190501.15

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  • @article{10.11648/j.ajwse.20190501.15,
      author = {Zhou Xiantao and Liu Hui and Wan Xuhui},
      title = {The Research of the Flow Characteristics in Spiral Membrane Separator},
      journal = {American Journal of Water Science and Engineering},
      volume = {5},
      number = {1},
      pages = {29-36},
      doi = {10.11648/j.ajwse.20190501.15},
      url = {https://doi.org/10.11648/j.ajwse.20190501.15},
      eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajwse.20190501.15},
      abstract = {The spiral membrane separator is a novel module proposed for reducing the concentration polarization and membrane fouling of membrane separation process. This membrane separation process benefits from dean vortices produced by centrifugal instability in enhancing fluid mass transfer. A numerical stimulation of this membrane separation is presented and used to analyze the fluid flow characteristics and thoroughly understand the separation mechanism. The numerical model consists of a spiral flow path with rectangular sector. As the simulation with infiltration, the fluid domain of the ceramic membrane tube was as a porous medium domain. The standard momentum equation, added with the momentum equation source term which composed of the viscosity loss term and the inertia loss term, are figured out through the experimental characterization. In the simulation of spiral membrane separation, the Dean secondary flow structure is identified and found to enhance fluid mass transfer and to increase the permeate flux. The critical unstable state of spiral membrane separation is accordingly De=246 without the flow permeation and De=863 with the permeation, where Dean vortices cause collisions and the mixing of fluid particles. Then in the case of permeation, the fluid in separator at De=1232 is numerically simulated to show that the higher flow velocity and a large fluctuating trend of wall shear stress near the membrane surface (inside), which mainly contributed to alleviate concentration polarization and membrane fouling.},
     year = {2019}
    }
    

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  • TY  - JOUR
    T1  - The Research of the Flow Characteristics in Spiral Membrane Separator
    AU  - Zhou Xiantao
    AU  - Liu Hui
    AU  - Wan Xuhui
    Y1  - 2019/04/08
    PY  - 2019
    N1  - https://doi.org/10.11648/j.ajwse.20190501.15
    DO  - 10.11648/j.ajwse.20190501.15
    T2  - American Journal of Water Science and Engineering
    JF  - American Journal of Water Science and Engineering
    JO  - American Journal of Water Science and Engineering
    SP  - 29
    EP  - 36
    PB  - Science Publishing Group
    SN  - 2575-1875
    UR  - https://doi.org/10.11648/j.ajwse.20190501.15
    AB  - The spiral membrane separator is a novel module proposed for reducing the concentration polarization and membrane fouling of membrane separation process. This membrane separation process benefits from dean vortices produced by centrifugal instability in enhancing fluid mass transfer. A numerical stimulation of this membrane separation is presented and used to analyze the fluid flow characteristics and thoroughly understand the separation mechanism. The numerical model consists of a spiral flow path with rectangular sector. As the simulation with infiltration, the fluid domain of the ceramic membrane tube was as a porous medium domain. The standard momentum equation, added with the momentum equation source term which composed of the viscosity loss term and the inertia loss term, are figured out through the experimental characterization. In the simulation of spiral membrane separation, the Dean secondary flow structure is identified and found to enhance fluid mass transfer and to increase the permeate flux. The critical unstable state of spiral membrane separation is accordingly De=246 without the flow permeation and De=863 with the permeation, where Dean vortices cause collisions and the mixing of fluid particles. Then in the case of permeation, the fluid in separator at De=1232 is numerically simulated to show that the higher flow velocity and a large fluctuating trend of wall shear stress near the membrane surface (inside), which mainly contributed to alleviate concentration polarization and membrane fouling.
    VL  - 5
    IS  - 1
    ER  - 

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Author Information
  • Institute of Chemical Machinery, East China University of Science and Technology, Shanghai, China

  • Institute of Chemical Machinery, East China University of Science and Technology, Shanghai, China

  • Institute of Chemical Machinery, East China University of Science and Technology, Shanghai, China

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