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High CO2-resistance Ag modified La0.8Ca0.2Fe0.94O3-δ hollow fiber membrane with a three-layer sandwich structure for oxygen separation.

Authors :
Zhou, Zhengwei
Zhang, Shude
Meng, Xiuxia
Song, Jian
Yang, Naitao
Li, Claudia
Kawi, Sibudjing
Liu, Shaomin
Source :
Separation & Purification Technology. Jul2023, Vol. 317, pN.PAG-N.PAG. 1p.
Publication Year :
2023

Abstract

[Display omitted] • A three-layer sandwich hollow fiber was prepared using one-step sintering. • Excellent membrane can hold up to 240-h testing under pure CO 2 sweep gas. • The maximum oxygen flux of 2.15 mL min−1 cm−2 obviously surpasses the traditional membrane. Cobalt-free mixed ionic and electronic conducting (MIEC) oxygen permeation membrane is a kind of promising materials for advanced air separation technology. However, its low oxygen permeability limits its practical application. In this work, we successfully prepared a type of La 0.8 Ca 0.2 Fe 0.94 O 3-δ -0.05Ag (LCF-Ag) hollow fiber membrane with "three-layer sandwich" structure by using a combined one-step sintering and phase conversion technology. Under the same experimental conditions, the oxygen permeation flux of the membrane structure was 1.79 times that of the traditional membrane structure, and the maximum oxygen flux was achieved at 2.15 mL min−1 cm−2. The model fitting proved that the membrane with new structure can effectively reduce the resistance of bulk diffusion. The stability test of oxygen permeation flux was carried out alternately in pure He and CO 2 atmosphere. The membrane displays high stability during the long-term operation of 240 h. Despite the oxygen flux had decreased slightly when CO 2 was used as sweep gas due to chemical adsorption of CO 2 to occupy the active sites on the membrane surface. The oxygen flux could be fully recovered once sweep gas switching to He, which indicates that the perovskite structure was not been damaged due to its good chemical stability. These results prove the feasibility of the new membrane structure for oxygen separation with CO 2 resistance, which may expand their applications to membrane reactors where the presence of CO 2 is not avoidable. [ABSTRACT FROM AUTHOR]

Details

Language :
English
ISSN :
13835866
Volume :
317
Database :
Academic Search Index
Journal :
Separation & Purification Technology
Publication Type :
Academic Journal
Accession number :
163513038
Full Text :
https://doi.org/10.1016/j.seppur.2023.123879