Mathematical Modeling of Toluene Oxidation with a Periodic Reactor Operation Full article
| Journal |
Reaction Kinetics and Catalysis Letters
ISSN: 0133-1736 , E-ISSN: 1588-2837 |
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| Output data | Year: 2010, Volume: 99, Number: 1, Pages: 23-28 Pages count : 6 DOI: 10.1007/s11144-009-0097-y | ||
| Tags | Mathematic modeling, Nonsteady-state kinetic model, Toluene partial oxidation, Vanadia/titania catalyst | ||
| Authors |
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| Affiliations |
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Funding (1)
| 1 | Russian Foundation for Basic Research | 09-03-90406 |
Abstract:
Mathematical modeling of toluene oxidation under unsteady state catalyst created by forced oscillations of concentration of toluene in the reactor inlet was carried out. It is shown that, under periodic reactor operation, the benzaldehyde yield was up to several times higher than the steady state value. This was explained by the participation of different oxygen species in the partial and total oxidation on the catalyst surface.
Cite:
Reshetnikov S.I.
Mathematical Modeling of Toluene Oxidation with a Periodic Reactor Operation
Reaction Kinetics and Catalysis Letters. 2010. V.99. N1. P.23-28. DOI: 10.1007/s11144-009-0097-y WOS Scopus РИНЦ ANCAN OpenAlex
Mathematical Modeling of Toluene Oxidation with a Periodic Reactor Operation
Reaction Kinetics and Catalysis Letters. 2010. V.99. N1. P.23-28. DOI: 10.1007/s11144-009-0097-y WOS Scopus РИНЦ ANCAN OpenAlex
Dates:
| Submitted: | Apr 29, 2009 |
| Accepted: | May 23, 2009 |
| Published online: | Dec 22, 2009 |
| Published print: | Feb 1, 2010 |
Identifiers:
| Web of science: | WOS:000277581400004 |
| Scopus: | 2-s2.0-77955020759 |
| Elibrary: | 18348602 |
| Chemical Abstracts: | 2010:323422 |
| Chemical Abstracts (print): | 152:405185 |
| OpenAlex: | W1979367475 |