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High-Pressure CO2/CH4 Separation Using SAPO-34 Membranes

Li, Shiguang, Martinek, Janna G., Falconer, John L., Noble, Richard D., Gardner, Tracy Q.·2005·Industrial & Engineering Chemistry Research

Abstract

SAPO-34 membranes on stainless steel, tubular supports separated CO 2 from CH 4 at feed pressures up to 3.1 MPa. The highest CO 2 permeance was 2.4 × 10 -7 mol/(m 2 s Pa) for a 50/50 feed mixture at a pressure drop of 0.14 MPa. For a pressure drop of 3 MPa, the CO 2 /CH 4 separation selectivities at 253 K were 140−150; at lower pressure drops, the highest selectivity was 270. The highest CO 2 flux was 21 kg/(m 2 h) at 295 K and a pressure drop of 3 MPa. Separation selectivity decreased as temperature increased because separation was partly based on competitive adsorption. As transmembrane pressure drop increased, both CO 2 flux and CO 2 permeate concentration increased for a 50/50 mixture. The flux pressure dependence was modeled by Maxwell−Stefan diffusion for mixtures. Methane decreased the CO 2 diffusion rate and, thus, decreased the CO 2 flux. The CH 4 flux was also lower in a mixture because CO 2 inhibits CH 4 adsorption.

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Metadata

Authors
Li, S., Martinek, J. G., Falconer, J. L., Noble, R. D., & Gardner, T. Q.
Venue
Industrial & Engineering Chemistry Research
Published
2005-03-15
Volume
44
Issue
9
Pages
3220-3228
ISSN
  • 0888-5885 (ISSN-L)
  • 1520-5045
OpenAlex
W2004595364
Cited by
184
References
0
FWCI
32.66
Type
journal article
Language
en
Open access
closed

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CoChat. (2026). Citation check: High-Pressure CO2/CH4 Separation Using SAPO-34 Membranes. https://app.cochat.ai/papers/10.1021/ie0490177
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Li, S., Martinek, J. G., Falconer, J. L., Noble, R. D., & Gardner, T. Q. (2005). High-Pressure CO2/CH4 Separation Using SAPO-34 Membranes. Industrial & Engineering Chemistry Research. https://doi.org/10.1021/ie0490177

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