Dimethyl ether reforming in a mesoporous γ-alumina membrane reactor combined with a water gas shift reaction

Sang Jun Park; Dong Wook Lee; Chang Yeol Yu; Kwan Young Lee; Kew Ho Lee

doi:10.1021/ie070910q

Dimethyl ether reforming in a mesoporous γ-alumina membrane reactor combined with a water gas shift reaction

Sang Jun Park, Dong Wook Lee, Chang Yeol Yu, Kwan Young Lee, Kew Ho Lee

Department of Chemical and Biological Engineering

Research output: Contribution to journal › Article

17 Citations (Scopus)

Abstract

Dimethyl ether (DME) steam reforming was performed in a γ-alumina/silica/stainless steel composite membrane reactor combined with a water gas shift (WGS) reaction to achieve three important aims simultaneously, such as DME conversion improvement, high hydrogen recovery, and CO elimination. The Knudsen membrane with high permeability was used to increase conversion improvement and hydrogen recovery. In one process of the DME steam reforming membrane reactor combined with the WGS reaction, the DME conversion was improved up to 35% in comparison with a conventional reactor, and hydrogen recovery was about 20%. The CO was not detected in the permeate side of the membrane reactor. The high CO removal efficiency was obtained from the WGS reaction with the Pt/TiO₂ catalyst in the permeate side of the membrane reactor.

Original language	English
Pages (from-to)	1416-1420
Number of pages	5
Journal	Industrial and Engineering Chemistry Research
Volume	47
Issue number	5
DOIs	https://doi.org/10.1021/ie070910q
Publication status	Published - 2008 Mar 5

ASJC Scopus subject areas

Chemistry(all)
Chemical Engineering(all)
Industrial and Manufacturing Engineering

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Park, S. J., Lee, D. W., Yu, C. Y., Lee, K. Y., & Lee, K. H. (2008). Dimethyl ether reforming in a mesoporous γ-alumina membrane reactor combined with a water gas shift reaction. Industrial and Engineering Chemistry Research, 47(5), 1416-1420. https://doi.org/10.1021/ie070910q

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abstract = "Dimethyl ether (DME) steam reforming was performed in a γ-alumina/silica/stainless steel composite membrane reactor combined with a water gas shift (WGS) reaction to achieve three important aims simultaneously, such as DME conversion improvement, high hydrogen recovery, and CO elimination. The Knudsen membrane with high permeability was used to increase conversion improvement and hydrogen recovery. In one process of the DME steam reforming membrane reactor combined with the WGS reaction, the DME conversion was improved up to 35% in comparison with a conventional reactor, and hydrogen recovery was about 20%. The CO was not detected in the permeate side of the membrane reactor. The high CO removal efficiency was obtained from the WGS reaction with the Pt/TiO2 catalyst in the permeate side of the membrane reactor.",

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