Oxygen permeation study of perovskite hollow fiber membranes

被引:53
作者
Tablet, C
Grubert, G
Wang, HH
Schiestel, T
Schroeder, M
Langanke, B
Caro, J
机构
[1] Univ Hannover, Inst Phys Chem & Electrochem, D-30167 Hannover, Germany
[2] Fraunhofer Inst Interfacial Engn & Biotechnol, IGB, D-70569 Stuttgart, Germany
[3] Rhein Westfal TH Aachen, Inst Phys Chem 1, D-52056 Aachen, Germany
[4] Uhde GMBH, D-44141 Dortmund, Germany
关键词
perovskite; membrane; POM; syngas; oxygen separation; hollow fiber;
D O I
10.1016/j.cattod.2005.03.064
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The first oxygen permeation data of a dense hollow fiber perovskite membrane based on BaCoxFeyZrzO3 (-) (delta) are reported. The hollow fiber was prepared by a phase inversion process. Dense fibers were obtained with the following typical geometries: outer diameter, 800-900 mu m; inner diameter, 500-600 mu m; length, 30 cm. The O-2-permeation through the hollow fiber perovskite membrane was, studied in a high-temperature gas permeation cell under different operation conditions. The increase of the helium gas flow rate reduces the oxygen partial pressure (p(O2)) on the core side and a higher oxygen permeation flux is observed. High oxygen flux of 0.73 m(3) (O-2)/(m(2) (membrane) h) was achieved at 850 degrees C under the operation parameters F-air (shell side) = 150 ml/min and F-He (core side) = 30 ml/min. The oxygen partial pressure dependence of the O-2 permeation flux indicated an interplay of both surface reaction and bulk diffusion as rate limiting steps. During 5 days of permeation a high and stable oxygen flux was observed. X-ray diffraction patterns of fresh and spent membranes after the permeation measurements revealed that no degradation after oxygen permeation appears. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:126 / 130
页数:5
相关论文
共 13 条
  • [1] Dense ceramic membranes for partial oxidation of methane to syngas
    Balachandran, U
    Dusek, JT
    Mieville, RL
    Poeppel, RB
    Kleefisch, MS
    Pei, S
    Kobylinski, TP
    Udovich, CA
    Bose, AC
    [J]. APPLIED CATALYSIS A-GENERAL, 1995, 133 (01) : 19 - 29
  • [2] Oxygen transport through dense La0.6Sr0.4Fe0.8Co0.2O3-δ perovskite-type permeation membranes
    Diethelm, S
    Van herle, J
    [J]. JOURNAL OF THE EUROPEAN CERAMIC SOCIETY, 2004, 24 (06) : 1319 - 1323
  • [3] Investigation on POM reaction in a new perovskite membrane reactor
    Dong, H
    Shao, ZP
    Xiong, GX
    Tong, JH
    Sheng, SS
    Yang, WS
    [J]. CATALYSIS TODAY, 2001, 67 (1-3) : 3 - 13
  • [4] Huang K. Q., 1999, P INT S SOL STAT ION, P95
  • [5] Diffusion and surface exchange coefficients in mixed ionic electronic conducting oxides from the pressure dependence of oxygen permeation
    Kim, S
    Yang, YL
    Jacobson, AJ
    Abeles, B
    [J]. SOLID STATE IONICS, 1998, 106 (3-4) : 189 - 195
  • [6] Investigation of the permeation behavior and stability of a Ba0.5Sr0.5Co0.8Fe0.2O3-δ oxygen membrane
    Shao, ZP
    Yang, WS
    Cong, Y
    Dong, H
    Tong, JH
    Xiong, GX
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2000, 172 (1-2) : 177 - 188
  • [7] Novel and ideal zirconium-based dense membrane reactors for partial oxidation of methane to syngas
    Tong, JH
    Yang, WS
    Cai, R
    Zhu, BC
    Lin, LW
    [J]. CATALYSIS LETTERS, 2002, 78 (1-4) : 129 - 137
  • [8] Catalytic partial oxidation of methane to synthesis gas over Ni-based catalysts - I. Catalyst performance characteristics
    Tsipouriari, VA
    Zhang, Z
    Verykios, XE
    [J]. JOURNAL OF CATALYSIS, 1998, 179 (01) : 283 - 291
  • [9] Wagner C., 1930, Z PHYS CHEM B LPZ, V11, P25
  • [10] Experimental and modeling studies on Ba0.5Sr0.5Co0.8Fe0.2O3-δ (BSCF) tubular membranes for air separation
    Wang, HH
    Wang, R
    Liang, DT
    Yang, WS
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2004, 243 (1-2) : 405 - 415