Separations
Influence of the preparation methods on the microstructure and oxygen permeability of a CO2-stable dual phase membrane
Article first published online: 17 DEC 2010
DOI: 10.1002/aic.12488
Copyright © 2010 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
Luo, H., Jiang, H., Efimov, K., Caro, J. and Wang, H. (2011), Influence of the preparation methods on the microstructure and oxygen permeability of a CO2-stable dual phase membrane. AIChE J., 57: 2738–2745. doi: 10.1002/aic.12488
Publication History
- Issue published online: 9 SEP 2011
- Article first published online: 17 DEC 2010
- Accepted manuscript online: 4 NOV 2010 08:48AM EST
- Manuscript Revised: 16 SEP 2010
- Manuscript Received: 26 JUL 2010
Funded by
- China Scholarship Council (CSC)
- State of Lower Saxony. Grant Number: 21-71023-25-7/09
- National Natural Science Foundation of China. Grant Numbers: 20706020, U0834004
- National Basic Research Program of China. Grant Number: 2009CB623406
- International Joint Project of Guangdong Province Science and Technology. Grant Number: 2009B050700017
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Keywords:
- homogeneity;
- dual phase membrane;
- oxygen separation;
- CO2-stable
Abstract
A CO2-stable dual phase membrane of the composition 40 wt % NiFe2O4-60 wt % Ce0.9Gd0.1O2-δ (40NFO-60CGO) was synthesized in three different ways: mixing of the starting powders (1) in a mortar and (2) in a ball-mill as well as by (3) direct in situ one-pot sol–gel powder synthesis. Backscattered scanning electron microscopy revealed that the direct one-pot synthesis of 40NFO-60CGO gives the smallest grains in a homogeneous distribution, compared with powder homogenization in the mortar or the ball-mill. The smaller is the grains, the higher is the oxygen permeability. The permeation of the membrane can be improved by coating a porous La0.6Sr0.4CoO3-δ (LSC) layer on the surface of the air side. The dual phase membrane of 40NFO-60CGO prepared by in situ synthesis shows a steady oxygen flux of 0.30 ml/(min cm2) over more than 100 h when pure CO2 was used as sweep gas, which indicated that the dual phases membrane is CO2-resistant at least over this 5 days testing period. © 2010 American Institute of Chemical Engineers AIChE J, 2011

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