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Modeling the Synthesis of Nitrous Oxide in a Microchannel Reactor: Effect of Parameters on Temperature Regimes and Capacity Full article

Journal Catalysis in Industry
ISSN: 2070-0504 , E-ISSN: 2070-0555
Output data Year: 2021, Volume: 13, Number: 3, Pages: 269–279 Pages count : 11 DOI: 10.1134/S2070050421030065
Tags mathematical modeling, ammonia oxidation, nitrous oxide, microchannel reactor
Authors Ignatov A.S. 1,2 , Vernikovskaya N.V. 1,2 , Chumachenko V.A. 1 , Noskov A.S. 1,2
Affiliations
1 Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, Novosibirsk, 630090 Russia
2 Novosibirsk State Technical University, Novosibirsk, 630073 Russia

Funding (1)

1 Ministry of Science and Higher Education of the Russian Federation 0239-2021-0014

Abstract: A study on the synthesis of nitrous oxide via the selective oxidation of ammonia in a microreactor in the form of a metallic disk with cylindrical channels filled with a manganese–bismuth oxide catalyst has been. A 3D mathematical model is presented for this microreactor that considers the transfer of mass and axial and radial heat, the catalytic reactions, the change they produce in the volume of the reaction mixture, the transfer of heat between the disk and the channels, and the heat conductivity of the disk. Parameters are determined that ensure the maximum nitrous oxide production with allowance for the limitations of temperature in the microreactor channels. The highest efficiency of nitrous oxide production is attained at an outer reactor edge temperature of 370°C and an inlet ammonia concentration of 20 vol %. The production capacity per unit catalyst volume in the microreactor is nearly 1.5 times higher than in a tubular reactor, and the maximum temperature corresponds to the level that provides the best process selectivity toward nitrous oxide.
Cite: Ignatov A.S. , Vernikovskaya N.V. , Chumachenko V.A. , Noskov A.S.
Modeling the Synthesis of Nitrous Oxide in a Microchannel Reactor: Effect of Parameters on Temperature Regimes and Capacity
Catalysis in Industry. 2021. V.13. N3. P.269–279. DOI: 10.1134/S2070050421030065 WOS Scopus РИНЦ OpenAlex
Original: Игнатов А.С. , Верниковская Н.В. , Чумаченко В.А. , Носков А.С.
Моделирование процесса получения закиси азота в микроканальном реакторе: влияние параметров на температурные режимы и производительность
Катализ в промышленности. 2021. Т.21. №1-2. С.74-85. DOI: 10.18412/1816-0387-2021-1-2-74-85 РИНЦ AN OpenAlex
Dates:
Submitted: Jan 29, 2021
Accepted: Feb 24, 2021
Published print: Jul 1, 2021
Published online: Sep 29, 2021
Identifiers:
Web of science: WOS:000701694500009
Scopus: 2-s2.0-85116010808
Elibrary: 47064471
OpenAlex: W3203983538
Citing:
DB Citing
Scopus 1
Elibrary 1
Web of science 1
OpenAlex 1
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