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PTFE多孔膜气体渗透数学模型和膜孔结构的影响

张秀莉a; 张卫东a; 郝新敏b; 张慧峰a; 张泽廷a; 张建春b   

  1. a College of Chemical Engineering, Beijing University of Chemical Technology, Beijing
    100029, China
    b Textile Institute, Donghua University, Shanghai 200051, China
  • 收稿日期:1900-01-01 修回日期:1900-01-01 出版日期:2003-08-28 发布日期:2003-08-28
  • 通讯作者: 张秀莉

Mathematical Model of Gas Permeation Through PTFE Porous Membrane and the Effect of
Membrane Pore Structure

ZHANG Xiulia; ZHANG Weidonga; HAO Xinminb; ZHANG Huifenga; ZHANG Zetinga; ZHANG Jianchunb   

  1. a College of Chemical Engineering, Beijing University of Chemical Technology, Beijing
    100029, China
    b Textile Institute, Donghua University, Shanghai 200051, China
  • Received:1900-01-01 Revised:1900-01-01 Online:2003-08-28 Published:2003-08-28
  • Contact: ZHANG Xiuli

摘要: Membrane-based separation processes are new technology combined membrane separation with
conven-tional separation. Hydrophobic porous membranes are often used in these processes.
The structure of hydrophobicporous membrane has significant effect on mass transfer
process. The permeabilities of five kinds of gas, He, N2,O2, CO2 and water vapor, across
six polytetrafiuoroethylene(PTFE) flat membranes were tested experimentally.Results
indicated that the greater the membrane mean pore size and the wider the pore size
distribution are, thehigher the gas permeability. A gas permeation model, including the
effects of membrane structure parameter and gasproperties, was established. A comprehensive
characteristic parameter (including porosity, thickness and tortuosity)was found more
effective to express the influence of membrane structure in gas permeation process. The
predictedpermeation coefficients were in good agreement with experimental data.

关键词: porous membrane;gas permeability;mathematical model

Abstract: Membrane-based separation processes are new technology combined membrane separation with
conven-tional separation. Hydrophobic porous membranes are often used in these processes.
The structure of hydrophobicporous membrane has significant effect on mass transfer
process. The permeabilities of five kinds of gas, He, N2,O2, CO2 and water vapor, across
six polytetrafiuoroethylene(PTFE) flat membranes were tested experimentally.Results
indicated that the greater the membrane mean pore size and the wider the pore size
distribution are, thehigher the gas permeability. A gas permeation model, including the
effects of membrane structure parameter and gasproperties, was established. A comprehensive
characteristic parameter (including porosity, thickness and tortuosity)was found more
effective to express the influence of membrane structure in gas permeation process. The
predictedpermeation coefficients were in good agreement with experimental data.

Key words: porous membrane, gas permeability, mathematical model