Performance of tubular SrFe(Al)O3-δ-SrAl2O4 composite membranes in CO2- and CH4-containing atmospheres

被引:21
|
作者
Yaremchenko, A. A. [1 ]
Kharton, V. V. [1 ]
Valente, A. A. [2 ]
Snijkers, F. M. M. [3 ]
Cooymans, J. F. C. [3 ]
Luyten, J. J. [3 ]
Marques, F. M. B. [1 ]
机构
[1] Univ Aveiro, Dept Ceram & Glass Engn, CICECO, P-3810193 Aveiro, Portugal
[2] Univ Aveiro, Dept Chem, CICECO, P-3810193 Aveiro, Portugal
[3] Vlaamse Instelling Technol Onderzoek, Flemish Inst Technol Res, Dept Mat, B-2400 Mol, Belgium
关键词
mixed-conducting membrane; methane activation; synthesis gas; oxygen permeation; composite ceramics; natural gas conversion;
D O I
10.1016/j.memsci.2008.03.028
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The stability and oxygen permeability of dense tubular membranes, made of (SrFeO(3-infinity))(0.7)(SrAl(2)O(4))(0.3) (SFSA) composite by cold isostatic pressing, were assessed under air/CO(2) and air/(CH(4) + CO(2)) gradients at 973-1173K. Mixed-conducting SFSA, comprising SrFe(Al)O(3-delta) perovskite-like and SrAl(2)O(4)-based phases, was selected as a model membrane material for the natural gas conversion reactors due to its attractive oxygen transport, catalytic and thermomechanical properties. As partial dissolution of SrAl(2)O(4) in the perovskite-like component leads to strontium deficiency of the perovskite phase, the composite exhibits an improved stability with respect to interaction with CO(2), although thermogravimetric analysis showed that carbon dioxide adsorption on SFSA is still significant. No degradation was revealed in the course of oxygen permeation tests during 200-300 h with subsequent scanning electron microscopy inspection. However, contrary to that observed for SFSA powders, methane conversion in the tubular SFSA membranes without surface modification results in predominant total combustion caused by the slow kinetics of the reforming reactions. Significantly higher conversion efficiency and synthesis gas yields were achieved passing the pre-reacted gas mixtures into an additional reactor with Pt/LaNiO(3)/Al(2)O(3) catalyst bed at the tubular membrane outlet. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:141 / 148
页数:8
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