Mathematical Modeling of the Adsorption-Catalytic Process with Internal Heater in a Multisectional Arrangement-Reference-Cited by-同舟云学术

Mathematical Modeling of the Adsorption-Catalytic Process with Internal Heater in a Multisectional Arrangement

Published:2023-11-30 Issue:49 Volume:62 Page:21164-21172
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Zazhigalov Sergey V.¹²,Elyshev Andrey²,Zagoruiko Andrey N.¹²^ORCID

Affiliation:

1. Boreskov Institute of Catalysis, Novosibirsk 630090, Russia

2. The University of Tyumen, Tyumen 625003, Russia

Funder

Ministry of Science and Higher Education of the Russian Federation

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.3c03357

Reference11 articles.

1. Unsteady-state operation of reactors with fixed catalyst beds

2. Robinson, E. Treatment of Gaseous Effluent. UK Patent UK1582441, 1971.

3. Stanley, P.; Ritscher, J. Novel Combustion Process for an Organic Substrate. U.S. Patent US4234549, 1979.

4. Schoubye, P. Method and Apparatus for the Removal of Oxidizable Pollutants from Gases. UK Patent UK2051761, 1979.

5. Orlyk, V.; Tereshenko, A.; Martcenyuk–Kucharuk, M.; Vorobey, A.; Farafonova, I. In Adsorptional-Catalytic Gas Cleaning from Organic Impurities, 1st World Congress on Environmental Catalysis, Pisa, Italy; Societa Chimica Italiana: Roma, 1995; p 671.

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