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

Журнал Chemical Engineering Journal
ISSN: 1385-8947 , E-ISSN: 1873-3212
Вых. Данные Год: 2011, Том: 178, Страницы: 276-281 Страниц : 6 DOI: 10.1016/j.cej.2011.10.002
Ключевые слова Catalytic microreactor, Hydrogen production, Methane partial oxidation, Microchannel plate, Syngas
Авторы Makarshin L.L. 1,2 , Andreev D.V. 1 , Gribovskyi A.G. 1,2 , Parmon V.N. 1,2
Организации
1 Boreskov Institute of Catalysis, pr. acad. Lavrentieva 5, Novosibirsk 630090, Russia
2 Novosibirsk State University, ul. Pirogova 2, Novosibirsk 630090, Russia

Информация о финансировании (1)

1 Российский фонд фундаментальных исследований 09-08-01047

Реферат: 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.
Библиографическая ссылка: 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 CAPlusCA OpenAlex
Даты:
Поступила в редакцию: 23 авг. 2010 г.
Принята к публикации: 3 окт. 2011 г.
Опубликована online: 8 окт. 2011 г.
Опубликована в печати: 15 дек. 2011 г.
Идентификаторы БД:
Web of science: WOS:000299025500036
Scopus: 2-s2.0-82755186473
РИНЦ: 18016325
Chemical Abstracts: 2011:1533593
Chemical Abstracts (print): 155:660637
OpenAlex: W2043026492
Цитирование в БД:
БД Цитирований
Web of science 20
Scopus 21
РИНЦ 24
OpenAlex 23
Альметрики: