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Catalytic Partial Oxidation of Methane in Microchannel Reactors with Co-Current and Countercurrent Reagent Flows: An Experimental Comparison Full article

Journal Chemical Engineering Journal
ISSN: 1385-8947 , E-ISSN: 1873-3212
Output data Year: 2011, Volume: 178, Pages: 276-281 Pages count : 6 DOI: 10.1016/j.cej.2011.10.002
Tags Catalytic microreactor, Hydrogen production, Methane partial oxidation, Microchannel plate, Syngas
Authors Makarshin L.L. 1,2 , Andreev D.V. 1 , Gribovskyi A.G. 1,2 , Parmon V.N. 1,2
Affiliations
1 Boreskov Institute of Catalysis, pr. acad. Lavrentieva 5, Novosibirsk 630090, Russia
2 Novosibirsk State University, ul. Pirogova 2, Novosibirsk 630090, Russia

Funding (1)

1 Russian Foundation for Basic Research 09-08-01047

Abstract: Microchannel catalytic reactors have repeatedly proved their high efficiency in the process of partial oxidation of methane (POM) as compared to traditional fixed-bed catalytic reactors. However, a serious problem of the microchannel reactor operation at this process appears to be high thermal power evolved on the narrow front edge of the microchannel (MC) plates. As a result, the front edge of the plates may undergo thermal corrosion and destruction during the POM process. The way out is to develop microchannel plates, which design would provide a countercurrent reagent flow inside the reactors. A comparison of the operation of microchannel reactors using co-current and countercurrent reagent flows shows substantial advantages of the latter. At high and prolong heating load, a microchannel reactor with the countercurrent reagent flow (MCR-Z) outperforms a reactor with the co-current reagent flow (MCR-P) both in the methane conversion and carbon monoxide selectivity. This is associated with the lower temperature of the front edge of the microchannel plate as well as the lower inner temperature gradient in the MCR-Z in comparison to the MCR-P. Thus, the countercurrent flow scheme allows solving some serious problems of corrosion and destruction of the microchannel plate front edge at high heat loads during the POM process.
Cite: Makarshin L.L. , Andreev D.V. , Gribovskyi A.G. , Parmon V.N.
Catalytic Partial Oxidation of Methane in Microchannel Reactors with Co-Current and Countercurrent Reagent Flows: An Experimental Comparison
Chemical Engineering Journal. 2011. V.178. P.276-281. DOI: 10.1016/j.cej.2011.10.002 WOS Scopus РИНЦ OpenAlex ANCAN
Dates:
Submitted: Aug 23, 2010
Accepted: Oct 3, 2011
Published online: Oct 8, 2011
Published print: Dec 15, 2011
Identifiers:
≡ Web of science: WOS:000299025500036
≡ Scopus: 2-s2.0-82755186473
≡ Elibrary: 18016325
≡ OpenAlex: W2043026492
≡ Chemical Abstracts: 2011:1533593
≡ Chemical Abstracts (print): 155:660637
Citing:
≡ Web of science 21 Сбор данных от 20.02.2026
≡ Scopus 22 Сбор данных от 15.02.2026
≡ Elibrary 24 Сбор данных от 15.02.2026
≡ OpenAlex 24 Сбор данных от 15.02.2026
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