Kinetic Study of Hydrogen Production by the High Temperature Water Gas Shift Reaction of Reformate Gas in Conventional and Membrane Packed Bed Reactors over Ca-Promoted CeO2–ZrO2 Supported Ni

Kinetic Study of Hydrogen Production by the High Temperature Water Gas Shift Reaction of Reformate Gas in Conventional and Membrane Packed Bed Reactors over Ca-Promoted CeO2–ZrO2 Supported Ni–Cu Catalyst

Published:2015-01-12 Issue:2 Volume:54 Page:612-622
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Oluku Ishioma Judith¹,Ibrahim Hussameldin¹,Idem Raphael¹

Affiliation:

1. Clean Energy Technologies Institute (CETI), Process Systems Engineering, Faculty of Engineering and Applied Science, University of Regina, Regina, Saskatchewan S4S 0A2, Canada

Funder

Natural Sciences and Engineering Research Council of Canada

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/ie502082q

Reference37 articles.

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4. Evaluating the performance of non-precious metal based catalysts for sulfur-tolerance during the dry reforming of biogas

5. An innovative configuration of a Pd-based membrane reactor for the production of pure hydrogen

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