A Comparative Study of the Performance of Symmetric and Asymmetric Mixed-conducting Membranes

被引:21
作者
Chang Xianfeng [1 ]
Zhang Chun [1 ]
He Yanjun [1 ]
Dong Xueliang [1 ]
Jin Wanqin [1 ]
Xu Nanping [1 ]
机构
[1] Nanjing Univ Technol, State Key Lab Mat Oriented Chem Engn, Coll Chem & Chem Engn, Nanjing 210009, Peoples R China
基金
中国国家自然科学基金; 国家高技术研究发展计划(863计划);
关键词
comparison; mixed-conducting oxide; symmetric membrane; asymmetric membrane; oxygen permeability; chemical stability; DENSE CERAMIC MEMBRANES; PEROVSKITE-TYPE MEMBRANE; PARTIAL OXIDATION; OXYGEN PERMEATION; SYNTHESIS GAS; METHANE; REACTORS; SYNGAS; SEPARATION; PERMEABILITY;
D O I
10.1016/S1004-9541(08)60245-1
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
According to the configuration, mixed-conducting membranes are classified as symmetric membranes and asymmetric membranes consisting of a thin dense layer and a porous support. In this study, these two kinds of SrCo0.4Fe0.5Zr0.1O3-delta oxide-based membranes were systematically compared in terms of oxygen permeability and chemical stability, and their differences were elucidated by means of the theoretical calculation. For the oxygen permeability, the asymmetric membrane was greater than the symmetric membrane due to the significant decrease of bulk diffusion resistance in the thin dense layer of the asymmetric membrane. In regard to the chemical stability, the increase of oxygen partial pressure on the asymmetric membrane surface at CH4 side produced the stable time of over 1032 h in partial oxidation of methane at 1123 K, while the symmetric membrane was only of 528 h. This study demonstrated that the asymmetric membrane was a promising geometrical configuration for the practical application.
引用
收藏
页码:562 / 570
页数:9
相关论文
共 26 条
[1]   Dense ceramic membranes for partial oxidation of methane to syngas [J].
Balachandran, U ;
Dusek, JT ;
Mieville, RL ;
Poeppel, RB ;
Kleefisch, MS ;
Pei, S ;
Kobylinski, TP ;
Udovich, CA ;
Bose, AC .
APPLIED CATALYSIS A-GENERAL, 1995, 133 (01) :19-29
[2]   Mixed-conducting dense ceramic membranes for air separation and natural gas conversion [J].
Balachandran, U. ;
Ma, Beihai .
JOURNAL OF SOLID STATE ELECTROCHEMISTRY, 2006, 10 (08) :617-624
[3]  
Bouwmeester H.J., 1996, FUNDAMENTALS INORGAN
[4]   Dense ceramic membranes for methane conversion [J].
Bouwmeester, HJM .
CATALYSIS TODAY, 2003, 82 (1-4) :141-150
[5]   Preparation and properties of thin La1-xSrxCo1-yFeyO3-δ perovskitic membranes supported on tailored ceramic substrates [J].
Buechler, O. ;
Serra, J. M. ;
Meulenberg, W. A. ;
Sebold, D. ;
Buchkremer, H. P. .
SOLID STATE IONICS, 2007, 178 (1-2) :91-99
[6]   Contribution of the surface reactions to the overall oxygen permeation of the mixed conducting membranes [J].
Chang, XF ;
Zhang, C ;
Wu, ZT ;
Jin, WQ ;
Xu, NP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (08) :2824-2829
[7]   Match of thermal performances between the membrane and the support for supported dense mixed-conducting membranes [J].
Chang, Xianfeng ;
Zhang, Chun ;
Jin, Wanqin ;
Xu, Nanping .
JOURNAL OF MEMBRANE SCIENCE, 2006, 285 (1-2) :232-238
[8]   Prospects and problems of dense oxygen permeable membranes [J].
Hendriksen, PV ;
Larsen, PH ;
Mogensen, M ;
Poulsen, FW ;
Wiik, K .
CATALYSIS TODAY, 2000, 56 (1-3) :283-295
[9]   Solid state synthesis of SrFeCo0.5Ox asymmetric membranes for oxygen separation [J].
Ikeguchi, M ;
Uchida, Y ;
Sekine, Y ;
Kikuchi, E ;
Matsukata, M .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2005, 38 (07) :502-508
[10]   Experimental and simulation study on a catalyst packed tubular dense membrane reactor for partial oxidation of methane to syngas [J].
Jin, W ;
Gu, X ;
Li, S ;
Huang, P ;
Xu, N ;
Shi, J .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (14) :2617-2625