Mass Transport in Multilayer Porous Metallic Membranes - Diagnosis, Identification and Validation

被引:2
作者
Edreva, Velislava [1 ]
Zhang, Fan [2 ]
Mangold, Michael [2 ]
Tsotsas, Evangelos [1 ]
机构
[1] Univ Magdeburg, D-39106 Magdeburg, Germany
[2] Max Planck Inst Dynam Complex Tech Syst Magdeburg, Magdeburg, Germany
关键词
Composite; Mass transport; Membrane reactor; Metallic membrane; Parameter identification; INORGANIC MEMBRANES; CERAMIC MEMBRANES; REACTOR; DEHYDROGENATION; SIMULATION; DIFFUSION; PERFORMANCE; PERMEATION;
D O I
10.1002/ceat.200800448
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
For a reliable description of mass transfer in membrane reactors the multilayer structure of the membrane is essential. This paper discusses methods which are sufficient to distinguish between homogeneous and composite membranes, and some others which are not. Different mass transport experiments (single gas permeation, isobaric diffusion, transient diffusion) with a porous metallic membrane consisting of two layers and the dusty gas model were used for this purpose. Simultaneous identification of mass transport parameters of both layers was achieved by modern optimization techniques on single gas permeation data. These parameters were validated by isobaric or transient diffusion measurements.
引用
收藏
页码:632 / 640
页数:9
相关论文
共 31 条
  • [1] Ethylene epoxidation in a catalytic packed-bed membrane reactor: experiments and model
    Al-Juaied, MA
    Lafarga, D
    Varma, A
    [J]. CHEMICAL ENGINEERING SCIENCE, 2001, 56 (02) : 395 - 402
  • [2] The influence of the porous support layer of composite membranes on the separation of binary gas mixtures
    Beuscher, U
    Gooding, CH
    [J]. JOURNAL OF MEMBRANE SCIENCE, 1999, 152 (01) : 99 - 116
  • [3] Biesheuvel PM, 1999, J MEMBRANE SCI, V156, P141
  • [4] A LIMITED MEMORY ALGORITHM FOR BOUND CONSTRAINED OPTIMIZATION
    BYRD, RH
    LU, PH
    NOCEDAL, J
    ZHU, CY
    [J]. SIAM JOURNAL ON SCIENTIFIC COMPUTING, 1995, 16 (05) : 1190 - 1208
  • [5] Multicomponent mass transport in porous solids and estimation of transport parameters
    Capek, P
    Seidel-Morgenstern, A
    [J]. APPLIED CATALYSIS A-GENERAL, 2001, 211 (02) : 227 - 237
  • [6] Catalytic membrane reactors for partial oxidation using perovskite hollow fiber membranes and for partial hydrogenation using a catalytic membrane contactor
    Caro, Jurgen
    Caspary, Karl J.
    Hamel, Christof
    Hoting, Born
    Koelsch, Peter
    Langanke, Bernd
    Nassauer, Konrad
    Schiestel, Thomas
    Schmidt, Andrea
    Schomaecker, Reinhard
    Seidel-Morgenstern, Andreas
    Tsotsas, Evangelos
    Voigt, Ingolf
    Wang, Haihui
    Warsitz, Rafael
    Werth, Steffen
    Wolf, Aurel
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (08) : 2286 - 2294
  • [7] Dixon AG, 2003, INT J CHEM REACT ENG, V1
  • [8] GASEOUS DIFFUSION IN POROUS MEDIA .2. EFFECT OF PRESSURE GRADIENTS
    EVANS, RB
    WATSON, GM
    MASON, EA
    [J]. JOURNAL OF CHEMICAL PHYSICS, 1962, 36 (07) : 1894 - &
  • [9] Two-dimensional simulation of a membrane reactor for dehydrogenation of ethylbenzene, considering heat and mass transfer
    Fukuhara, C
    Igarashi, A
    [J]. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2003, 36 (05) : 530 - 539
  • [10] Hsieh H. P., 1996, INORGANIC MEMBRANE S