Membrane performance: the key issues for dehydrogenation reactions in a catalytic membrane reactor

被引:76
|
作者
Weyten, H
Luyten, J
Keizer, K
Willems, L
Leysen, R
机构
[1] Vlaamse Instelling Technol Onderzoek, Flemish Inst Technol Res, B-2400 Mol, Belgium
[2] Potchefstroom Univ Christian Higher Educ, Dept Chem, ZA-2520 Potchefstroom, South Africa
关键词
Pd/Ag membrane; membrane reactor; propane dehydrogenation;
D O I
10.1016/S0920-5861(99)00257-6
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
In a high-temperature membrane reactor, one of the reaction products is selectively removed from the reaction mixture, thus preventing the mixture from reaching equilibrium. In a previous study [I], a CVI-silica membrane was used for the direct dehydrogenation of propane in a high-temperature catalytic membrane reactor This H-2 selective membrane had only a moderate permeation (similar to 140 x 10(-9) mol/m(2)Pa s) and a limited H-2/C3H8 permselectivity (alpha(0) approximate to 70-90 at 500 degrees C). These experiments proved that (at 500 degrees C) the propane conversion could be improved from the equilibrium value (similar to 18%) to a value which is about twice as high. The increase was however only significant for relatively small values of the propane feed stream less than or equal to 16.5 mu mol/s. This is because at high propane feed, the hydrogen cannot be removed fast enough through the membrane and conversion is again limited by the thermodynamic equilibrium. In this study, the comparison is made between the performance of the CVI-silica membrane and a Pd/Ag membrane when used as the H-2 selective membrane. The performance of the Pd/Ag membrane is far superior to the performance of the SiO2 membrane. H-2 fluxes of more than 0.1 mol/m(2)s were measured and the H-2/Ar permselectivity exceeds 4500. When it is run under comparable conditions, the performance of the Pd/Ag membrane reactor is much better. The increase in propane conversion persists at values of the propane feed stream that are about six times higher (105 mu mol/s). Since the: H-2 is selectively removed from the reaction mixture, it is not available for any competitive side reactions. The production of methane, which limits the propene selectivity of the reaction in a conventional plug-flow reactor, is much less in a catalytic membrane reactor. This means that the selectivity in the membrane reactor is higher than in the plug-flow reactor when they are fun under similar conditions. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:3 / 11
页数:9
相关论文
共 50 条
  • [1] Performance of catalytic membrane reactor in multiphase reactions
    Vospernik, M
    Pintar, A
    Bercic, G
    Levec, J
    Walmsley, J
    Ræder, H
    Iojoiu, EE
    Miachon, S
    Dalmon, JA
    CHEMICAL ENGINEERING SCIENCE, 2004, 59 (22-23) : 5363 - 5372
  • [2] MODELING OF ETHYLBENZENE DEHYDROGENATION IN A CATALYTIC MEMBRANE REACTOR
    BECKER, YL
    DIXON, AG
    MOSER, WR
    MA, YH
    JOURNAL OF MEMBRANE SCIENCE, 1993, 77 (2-3) : 233 - 244
  • [3] THE STUDY OF ETHANE DEHYDROGENATION IN A CATALYTIC MEMBRANE REACTOR
    CHAMPAGNIE, AM
    TSOTSIS, TT
    MINET, RG
    WAGNER, E
    JOURNAL OF CATALYSIS, 1992, 134 (02) : 713 - 730
  • [4] Application of a carbon membrane reactor for dehydrogenation reactions
    Sznejer, G
    Sheintuch, M
    CHEMICAL ENGINEERING SCIENCE, 2004, 59 (10) : 2013 - 2021
  • [5] EFFECT OF REACTION AND PERMEATION RATES ON THE PERFORMANCE OF A CATALYTIC MEMBRANE REACTOR FOR METHYLCYCLOHEXANE DEHYDROGENATION
    ALI, JK
    RIPPIN, DWT
    SEPARATION SCIENCE AND TECHNOLOGY, 1994, 29 (18) : 2475 - 2492
  • [6] Catalytic oxidative dehydrogenation of isobutane in a Pd membrane reactor
    Raybold, TM
    Huff, MC
    3RD WORLD CONGRESS ON OXIDATION CATALYSIS, 1997, 110 : 501 - 507
  • [7] Simulation of a catalytic membrane reactor for the oxidative dehydrogenation of butane
    Pedernera, M
    Alfonso, MJ
    Menéndez, M
    Santamaría, J
    CHEMICAL ENGINEERING SCIENCE, 2002, 57 (13) : 2531 - 2544
  • [8] Simulation of Catalytic Dehydrogenation of Cyclohexane in Zeolite Membrane Reactor
    Kumar, Shashi
    Gaba, Tanvi
    Kumar, Surendra
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2009, 7
  • [9] CATALYTIC ISOBUTANE DEHYDROGENATION IN A DENSE SILICA MEMBRANE REACTOR
    IOANNIDES, T
    GAVALAS, GR
    JOURNAL OF MEMBRANE SCIENCE, 1993, 77 (2-3) : 207 - 220
  • [10] ANALYSIS OF A MEMBRANE ENCLOSED CATALYTIC REACTOR FOR BUTANE DEHYDROGENATION
    GOKHALE, YV
    NOBLE, RD
    FALCONER, JL
    JOURNAL OF MEMBRANE SCIENCE, 1993, 77 (2-3) : 197 - 206