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Modeling of Membrane Reactor for Steam Methane Reforming: From Granular to Structured Catalysts Full article

Journal Theoretical Foundations of Chemical Engineering
ISSN: 0040-5795 , E-ISSN: 1608-3431
Output data Year: 2012, Volume: 46, Number: 2, Pages: 97-107 Pages count : 11 DOI: 10.1134/S004057951202011X
Tags Steam; Methane Conversion; Membrane Reactor; Reformer; Membrane Module
Authors Shigarov A.B. 1 , Kirillov V.A. 1
Affiliations
1 Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, pr. Akademika Lavrent’eva 5, Novosibirsk, 630090 Russia

Funding (1)

1 The Ministry of Education and Science of the Russian Federation 16.516.11.6060

Abstract: Different types and operating modes of a tubular membrane reactor for steam methane reforming with a production rate of 0.6 m3/h are compared using the results of mathematical modeling. It is shown that, for a cylindrical membrane, the use of a catalytic bed based on waved bands of porous nickel instead of a granular bed of a commercial catalyst (NIAP-18) can theoretically increase the yield of hydrogen by 15–18%.
Cite: Shigarov A.B. , Kirillov V.A.
Modeling of Membrane Reactor for Steam Methane Reforming: From Granular to Structured Catalysts
Theoretical Foundations of Chemical Engineering. 2012. V.46. N2. P.97-107. DOI: 10.1134/S004057951202011X WOS Scopus РИНЦ ANCAN OpenAlex
Original: Шигаров А.Б. , Кириллов В.А.
Моделирование мембранного реактора парового риформинга метана: от зернистого к структурированному катализатору
Теоретические основы химической технологии. 2012. Т.46. №2. С.131-142. РИНЦ
Dates:
Submitted: Jul 11, 2011
Published print: Apr 1, 2012
Published online: Apr 17, 2012
Identifiers:
Web of science: WOS:000302903800001
Scopus: 2-s2.0-84862107138
Elibrary: 17990461
Chemical Abstracts: 2012:557594
Chemical Abstracts (print): 156:480522
OpenAlex: W2042745347
Citing:
DB Citing
Web of science 16
Scopus 19
Elibrary 23
OpenAlex 26
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