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Mathematical Modeling of the Continuous Process for Synthesis of Nanofibrous Carbon in a Moving Catalyst Bed Reactor with Recirculating Gas Flow Full article

Journal Chemical Engineering Journal
ISSN: 1385-8947 , E-ISSN: 1873-3212
Output data Year: 2008, Volume: 137, Number: 3, Pages: 681-685 Pages count : 5 DOI: 10.1016/j.cej.2007.06.036
Tags Filamentous carbon, Gas recirculation, Methane decomposition, Moving catalyst bed, Nanofibrous carbon, Ni-Al2O3 catalyst, Reactor
Authors Zavarukhin Sergei G. 1 , Kuvshinov Gennady G 2
Affiliations
1 Boreskov Institute of Catalysis, Pr. Akad. Lavrentieva, 5, Novosibirsk 630090, Russia
2 Novosibirsk State Technical University, Pr. K. Marx, 20, Novosibirsk 630092, Russia

Funding (1)

1 The Ministry of Education and Science of the Russian Federation 60059

Abstract: A continuous process for synthesis of nanofibrous carbon from methane in a reactor with a moving bed of the Ni–Al2O3 catalyst (90 wt.% Ni) and intensively recirculated gas flow is considered. Dependencies for calculating outlet characteristics of the gas mixture and catalyst are suggested. Comparison of various types of continuous reactors shows that the suggested reactor is preferable.
Cite: Zavarukhin S.G. , Kuvshinov G.G.
Mathematical Modeling of the Continuous Process for Synthesis of Nanofibrous Carbon in a Moving Catalyst Bed Reactor with Recirculating Gas Flow
Chemical Engineering Journal. 2008. V.137. N3. P.681-685. DOI: 10.1016/j.cej.2007.06.036 WOS Scopus РИНЦ ANCAN OpenAlex
Dates:
Submitted: May 5, 2007
Accepted: Jun 29, 2007
Published online: Jul 10, 2007
Published print: Apr 15, 2008
Identifiers:
Web of science: WOS:000254699200026
Scopus: 2-s2.0-40049089805
Elibrary: 13594212
Chemical Abstracts: 2008:275458
Chemical Abstracts (print): 148:429268
OpenAlex: W2074526641
Citing:
DB Citing
Web of science 7
Scopus 7
Elibrary 7
OpenAlex 6
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