The effect of pressure in membrane reactors: Trade-off in permeability and equilibrium conversion in the catalytic reforming of CH4 with CO2 at high pressure

D. Lee; P. Hacarlioglu; S. T. Oyama

doi:10.1023/b:toca.0000024927.26174.9b

The effect of pressure in membrane reactors: Trade-off in permeability and equilibrium conversion in the catalytic reforming of CH₄ with CO₂ at high pressure

D. Lee, P. Hacarlioglu, S. T. Oyama

Department of Chemical Engineering

Virginia Polytechnic Institute and State University

Research output: Contribution to journal › Article › peer-review

53 Scopus citations

Original language	English
Pages (from-to)	45-57
Number of pages	13
Journal	Topics in Catalysis
Volume	29
Issue number	1-2
DOIs	https://doi.org/10.1023/b:toca.0000024927.26174.9b
State	Published - May 2004

Keywords

Dry-reforming of CH
Hydrogen separation
Membrane reactor
Silica membrane

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10.1023/b:toca.0000024927.26174.9b

Cite this

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KW - Hydrogen separation

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KW - Silica membrane

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The effect of pressure in membrane reactors: Trade-off in permeability and equilibrium conversion in the catalytic reforming of CH4 with CO2 at high pressure

Keywords

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The effect of pressure in membrane reactors: Trade-off in permeability and equilibrium conversion in the catalytic reforming of CH₄ with CO₂ at high pressure