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Separation of CO2/N2 mixtures using MFI‐type zeolite membranes

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Bernal, M. P., Coronas, J., Menéndez, M., Santamaría, J.·2004·AIChE Journal

Abstract

MFI‐type zeolite (ZSM5) membranes were prepared on alumina and stainless steel tubular supports and tested for the separation of CO 2/N 2 mixtures. The effect of several operating variables (temperature, feed and permeate pressures, feed composition, use of sweep gas, presence of water in the feed, membrane module configuration) was investigated. The separation between CO 2 and N 2 takes place because of the preferential adsorption of CO 2, which hinders the permeation of N 2 through the zeolite pore network. The best results in this work were obtained with a Na‐ZSM5 membrane, and using a large pressure gradient. In this case, a permeation flux as large as 9.2 kg/(m 2 · h) [permeance of 2.6 × 10−6 mol/(m 2 · s · Pa)] with a CO 2/N 2 separation factor of 13.7 was obtained. © 2004 American Institute of Chemical Engineers AIChE J, 50: 127–135, 2004

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Metadata

Authors
Bernal, M. P., Coronas, J., Menéndez, M., & Santamaría, J.
Venue
AIChE Journal
Publisher
Wiley
Published
2004-01
Volume
50
Issue
1
Pages
127-135
ISSN
  • 0001-1541 (ISSN-L)
  • 1547-5905
OpenAlex
W1996413005
Cited by
175
References
0
FWCI
15.15
Type
journal article
Language
en
Open access
bronze

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CoChat. (2026). Citation check: Separation of CO2/N2 mixtures using MFI‐type zeolite membranes. https://app.cochat.ai/papers/10.1002/aic.10012
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Bernal, M. P., Coronas, J., Menéndez, M., & Santamaría, J. (2004). Separation of CO2/N2 mixtures using MFI‐type zeolite membranes. AIChE Journal. https://doi.org/10.1002/aic.10012

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