PERMEATION AND SEPARATION OF LIGHT-HYDROCARBONS THROUGH A SILICALITE-1 MEMBRANE - APPLICATION OF THE GENERALIZED MAXWELL-STEFAN EQUATIONS

被引:112
|
作者
KAPTEIJN, F
BAKKER, WJW
ZHENG, GH
POPPE, J
MOULIJN, JA
机构
[1] Department of Chemical Engineering, Delft University of Technology, 2628BL Delft
关键词
MICROPOROUS MEMBRANE; ZEOLITE; DIFFUSION; SEPARATION; HYDROCARBON;
D O I
10.1016/0923-0467(94)02941-5
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Single-component permeation data are given for methane, ethane, propane, ethene and propene through a silicalite-1 membrane of approximately 40 mu m thickness at 293 K as a function of their partial pressure. The permeation fluxes generally decrease with increasing molecular size, while the alkenes permeate more rapidly than their corresponding alkanes at identical conditions. In 1:1 mixtures of ethane-ethene and propane-propene (1 bar total pressure) the alkanes permeate faster, yielding selectivity factors of 1.9 and 1.3 respectively. The generalized Maxwell-Stefan (GMS) equations, adapted for surface diffusion, could describe the permeation data well. The unary systems yielded diffusivity data that were fairly constant or varied at most by a factor of 2-3. These diffusivities compare well with literature values obtained with other (transient) techniques that yield transport diffusivities. The binary system permeation data could be quantitatively described by the GMS equations without exchange contributions (''single-file'' diffusion) and need only the diffusivity values of the unary permeation experiments.
引用
收藏
页码:145 / 153
页数:9
相关论文
共 30 条
  • [1] Permeation and separation of light hydrocarbons through a silicalite-1 membrane application of the generalized Maxwell-Stefan equations
    Kapteijn, Freek
    Bakker, Wridzer J.W.
    Zheng, Guhong
    Poppe, Jeroen
    Moulijn, Jacob A.
    Chemical Engineering Journal and Biochemical Engineering Journal, 1995, 57 (02): : 145 - 153
  • [2] Maxwell-Stefan Equations Applied to the Modeling of Multi-Component Permeation through a Silicalite-1 Membrane
    Xu, Chunhui
    Chen, Yunchao
    Peng, Anna
    Wang, Ningwei
    Shang, Hao
    Zhong, Yijun
    Zhu, Weidong
    ADVANCES IN CHEMICAL ENGINEERING, PTS 1-3, 2012, 396-398 : 674 - 679
  • [3] PERMEATION AND SEPARATION BEHAVIOR OF A SILICALITE-1 MEMBRANE
    KAPTEIJN, F
    BAKKER, WJW
    VANDEGRAAF, J
    ZHENG, G
    POPPE, J
    MOULIJN, JA
    CATALYSIS TODAY, 1995, 25 (3-4) : 213 - 218
  • [4] Binary permeation through a silicalite-1 membrane
    van den Broeke, LJP
    Bakker, WJW
    Kapteijn, F
    Moulijn, JA
    AICHE JOURNAL, 1999, 45 (05) : 976 - 985
  • [6] Analytic solution of the Maxwell-Stefan equations for multicomponent permeation across a zeolite membrane
    Krishna, R
    Baur, R
    CHEMICAL ENGINEERING JOURNAL, 2004, 97 (01) : 37 - 45
  • [7] Natural gas purification with a DDR zeolite membrane; permeation modelling with maxwell-stefan equations
    van den Bergh, Johan
    Zhu, Weidong
    Groen, Johan C.
    Kapteijn, Freek
    Moulijn, Jacob A.
    Yajima, Kenji
    Nakayama, Kunio
    Tomita, Toshihiro
    Yoshida, Shuichi
    FROM ZEOLITES TO POROUS MOF MATERIALS: THE 40TH ANNIVERSARY OF INTERNATIONAL ZEOLITE CONFERENCE, PROCEEDINGS OF THE 15TH INTERNATIONAL ZEOLITE CONFERENCE, 2007, 170 : 1021 - 1027
  • [8] Helium permeation through a silicalite-1 tubular membrane
    Hernandez, M. G.
    Salinas-Rodriguez, E.
    Gomez, S. A.
    Roa-Neri, J. A. E.
    Alfaro, S.
    Valdes-Parada, F. J.
    HEAT AND MASS TRANSFER, 2015, 51 (06) : 847 - 857
  • [9] Helium permeation through a silicalite-1 tubular membrane
    M. G. Hernández
    E. Salinas-Rodríguez
    S. A. Gómez
    J. A. E. Roa-Neri
    S. Alfaro
    F. J. Valdés-Parada
    Heat and Mass Transfer, 2015, 51 : 847 - 857
  • [10] Modeling transient permeation of polar organic mixtures through a MFI zeolite membrane using the Maxwell-Stefan equations
    Yu, Mao
    Falconer, John L.
    Noble, Richard D.
    Krishna, R.
    JOURNAL OF MEMBRANE SCIENCE, 2007, 293 (1-2) : 167 - 173