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CFD Modeling of Compact Methanol Reformer Научная публикация

Конференция XXI International Conference on Chemical Reactors
22-25 сент. 2014 , Delft
Журнал Chemical Engineering Journal
ISSN: 1385-8947 , E-ISSN: 1873-3212
Вых. Данные Год: 2015, Том: 282, Страницы: 91-100 Страниц : 10 DOI: 10.1016/j.cej.2015.04.006
Ключевые слова CFD simulation, Fuel processor, Hydrogen, Methanol, Methanol steam reformer, Tubular reactor
Авторы Klenov O.P. 1 , Makarshin L.L. 1 , Gribovskiy A.G. 1,2 , Andreev D.V. 1 , Parmon V.N. 1,2
Организации
1 Boreskov Institute of Catalysis, Siberian Branch of the Russian Academy of Sciences, Pr. Akad. Lavrentieva 5, 630090 Novosibirsk, Russia
2 Novosibirsk State University, ul. Pirogova 2, 630090 Novosibirsk, Russia

Реферат: The compact fuel processor that uses methanol as a feedstock for the production of hydrogen and for temperature control was studied by computational fluid dynamics. The processor integrates in a single package the methanol–water evaporator, the gas flow distributors, the steam reformer and the methanol–air catalytic combustor. The reformer and the combustor were formed as tubular reactors that possessed a single metallic body like a monolith with an array of circular cross-section through-holes. Part of holes was filled with reforming catalyst and the other part was filled with a catalyst for the oxidation of methanol. The design provides efficient heat transfer between the reformer and the combustor and efficient temperature control of the reformer. The temperature distribution in the metallic body of the reformer and the combustor is almost uniform. The value of temperature nonuniformity does not exceed the value ΔT = 2.4% in any cross-section of the reaction zone. Maximum overall effectiveness of the fuel processor is achieved at the value of methanol feed equal 17.24 mmol/min (GHSV = 12,424 h−1) and 8.75 mmol/min (GHSV = 16,632 h−1) in the reformer and in the combustor, respectively. Under these conditions the hydrogen performance is equal to 70.0 l/h (48.7 mmol/min) and the temperature is equal to 286.4 °C in the reformer.
Библиографическая ссылка: Klenov O.P. , Makarshin L.L. , Gribovskiy A.G. , Andreev D.V. , Parmon V.N.
CFD Modeling of Compact Methanol Reformer
Chemical Engineering Journal. 2015. V.282. P.91-100. DOI: 10.1016/j.cej.2015.04.006 WOS Scopus РИНЦ OpenAlex CAPlusCA
Даты:
Опубликована online: 11 апр. 2015 г.
Опубликована в печати: 15 дек. 2015 г.
Идентификаторы БД:
≡ Web of science: WOS:000362860100011
≡ Scopus: 2-s2.0-84947862483
≡ РИНЦ: 24973670
≡ OpenAlex: W1972436720
≡ Chemical Abstracts: 2015:662025
≡ Chemical Abstracts (print): 163:413788
Цитирование в БД:
≡ Web of science 27 Сбор данных от 20.02.2026
≡ Scopus 28 Сбор данных от 15.02.2026
≡ РИНЦ 24 Сбор данных от 15.02.2026
≡ OpenAlex 33 Сбор данных от 15.02.2026
Альметрики: