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Preferential CO Oxidation over a Copper-Cerium Oxide Catalyst in a Microchannel Reactor Full article

Journal Applied Catalysis A: General
ISSN: 0926-860X , E-ISSN: 1873-3875
Output data Year: 2008, Volume: 350, Number: 1, Pages: 53-62 Pages count : 10 DOI: 10.1016/j.apcata.2008.07.036
Tags CO removal, Copper-ceria oxide catalyst, Hydrogen purification, Microchannel reactor, Preferential CO oxidation, Selective oxidation of carbon monoxide
Authors Snytnikov P.V. 1,2 , Popova M.M. 1,2 , Men Y. 3 , Rebrov E.V. 4 , Kolb G. 3 , Hessel V. 3,4 , Schouten J.C. 4 , Sobyanin V.A. 1,2
Affiliations
1 Boreskov Institute of Catalysis, Pr. Lavrentieva 5, Novosibirsk 630090, Russia
2 Novosibirsk State University, Pirogova Street 2, Novosibirsk 630090, Russia
3 Institut fur Mikrotechnik Mainz GmbH, Carl-Zeiss-Strasse 18-20, 55129 Mainz, Germany
4 Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven, The Netherlands

Funding (1)

1 International Association for the Promotion of Co-operation with Scientists from the New Independent States of the Former Soviet Union YS 06-1000014-5774

Abstract: The activity of a 5-wt% Cu/CeO2x catalyst during preferential CO oxidation in hydrogen-rich gas mixtures was studied in a microchannel reactor. The CO concentration dropped from 1 vol.% to 10 ppm at a selectivity of 60%, at a temperature of 190 8C, and a weight hour space velocity (WHSV) of 55,000 cm3 g1 h1. Both the CO concentration and the temperature increased when the WHSV was increased from 50,000 to 500,000 cm3 g1 h1. An increase of the O2 concentration from a 1.2 to 3 fold excess reduced the CO concentration to 10 ppm in a broad temperature interval of 50 8C at WHSVs up to 275,000 cm3 g1 h1. The preferential CO oxidation could be carried out at higher flow rates and at higher selectivities in the microchannel reactor compared to a fixed-bed flow reactor.
Cite: Snytnikov P.V. , Popova M.M. , Men Y. , Rebrov E.V. , Kolb G. , Hessel V. , Schouten J.C. , Sobyanin V.A.
Preferential CO Oxidation over a Copper-Cerium Oxide Catalyst in a Microchannel Reactor
Applied Catalysis A: General. 2008. V.350. N1. P.53-62. DOI: 10.1016/j.apcata.2008.07.036 WOS Scopus РИНЦ ANCAN OpenAlex
Dates:
Submitted: Jun 23, 2008
Accepted: Jul 29, 2008
Published online: Aug 5, 2008
Published print: Nov 15, 2008
Identifiers:
Web of science: WOS:000260665300008
Scopus: 2-s2.0-52949144198
Elibrary: 13579697
Chemical Abstracts: 2008:1202117
Chemical Abstracts (print): 150:7225
OpenAlex: W2001554734
Citing:
DB Citing
Web of science 64
Scopus 67
Elibrary 67
OpenAlex 73
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