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Combined Steam and Carbon Dioxide Reforming of Methane over Porous Nickel Based Catalysts Научная публикация

Журнал Catalysis Science and Technology
ISSN: 2044-4753 , E-ISSN: 2044-4761
Вых. Данные Год: 2015, Номер: 5, Страницы: 2761-2768 Страниц : 8 DOI: 10.1039/c4cy01614a
Ключевые слова Carbon; Carbon dioxide; Carbonization; Catalysts; Crystallites; Data handling; Magnesia; Methane; Nickel; Nickel deposits; Reforming reactions; Steam reforming; Synthesis (chemical); Synthesis gas; Synthesis gas manufacture
Авторы Danilova M.M. 1 , Fedorova Z.A. 1 , Kuzmin V.A. 1 , Zaikovskii V.I. 1 , Porsin A.V. 1 , Krieger T.A. 1,2
Организации
1 Boreskov Institute of Catalysis SB RAS, Russian Federation
2 Novosibirsk State University, Russian Federation

Информация о финансировании (1)

1 Российский фонд фундаментальных исследований 15-03-04001

Реферат: The phase composition and texture of nickel catalysts supported on a porous nickel ribbon with a MgO underlayer were studied. In the supported reduced catalysts (900 °C, H2), nickel crystallites were epitaxially bound to MgO. The reaction of combined steam and carbon dioxide reforming of methane to synthesis gas (750 °C, CH4/CO2/H2O/N2 = 35/23/39/3, GHSV = 62.5 L g−1 h−1) was performed in a flow reactor in the presence of the developed catalysts. The catalysts with the MgO underlayer completely covering the nickel ribbon showed stable activity throughout the test period (18 h); after the reaction, no carbon deposits were found in them. The resistance of these catalysts to carbonization was attributed to both the formation of nickel crystallites epitaxially bound to MgO and the formation of the MgO underlayer that covers the nickel ribbon and prevents its contact with the reaction medium. Based on the supported nickel catalysts, a monolithic catalyst was prepared and tested in the developed flow reactor. According to the test data, methane conversion over the monolithic catalyst at a contact time of 0.29 s was not lower than 94% and the synthesis gas yield was 90%; at this contact time, experimental values were close to the calculated equilibrium values.
Библиографическая ссылка: Danilova M.M. , Fedorova Z.A. , Kuzmin V.A. , Zaikovskii V.I. , Porsin A.V. , Krieger T.A.
Combined Steam and Carbon Dioxide Reforming of Methane over Porous Nickel Based Catalysts
Catalysis Science and Technology. 2015. N5. P.2761-2768. DOI: 10.1039/c4cy01614a WOS Scopus РИНЦ CAPlusCA OpenAlex
Даты:
Поступила в редакцию: 5 дек. 2014 г.
Принята к публикации: 24 февр. 2015 г.
Опубликована online: 25 февр. 2015 г.
Опубликована в печати: 1 мая 2015 г.
Идентификаторы БД:
Web of science: WOS:000353641800023
Scopus: 2-s2.0-84929429025
РИНЦ: 24033014
Chemical Abstracts: 2015:331428
Chemical Abstracts (print): 162:529518
OpenAlex: W1967954812
Цитирование в БД:
БД Цитирований
Web of science 29
Scopus 32
РИНЦ 27
OpenAlex 32
Альметрики: