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Combined Steam and Carbon Dioxide Reforming of Methane over Porous Nickel Based Catalysts Full article

Journal Catalysis Science and Technology
ISSN: 2044-4753 , E-ISSN: 2044-4761
Output data Year: 2015, Number: 5, Pages: 2761-2768 Pages count : 8 DOI: 10.1039/c4cy01614a
Tags Carbon; Carbon dioxide; Carbonization; Catalysts; Crystallites; Data handling; Magnesia; Methane; Nickel; Nickel deposits; Reforming reactions; Steam reforming; Synthesis (chemical); Synthesis gas; Synthesis gas manufacture
Authors 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
Affiliations
1 Boreskov Institute of Catalysis SB RAS, Russian Federation
2 Novosibirsk State University, Russian Federation

Funding (1)

1 Russian Foundation for Basic Research 15-03-04001

Abstract: 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.
Cite: 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 ANCAN OpenAlex
Dates:
Submitted: Dec 5, 2014
Accepted: Feb 24, 2015
Published online: Feb 25, 2015
Published print: May 1, 2015
Identifiers:
Web of science: WOS:000353641800023
Scopus: 2-s2.0-84929429025
Elibrary: 24033014
Chemical Abstracts: 2015:331428
Chemical Abstracts (print): 162:529518
OpenAlex: W1967954812
Citing:
DB Citing
Web of science 29
Scopus 32
Elibrary 27
OpenAlex 32
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