Monitoring of the commercial operation of reforming catalysts using a computer simulation system; Catalysis in Industry; Vol. 1, iss. 2

Podrobná bibliografie
Parent link:Catalysis in Industry: Scientific Journal
Vol. 1, iss. 2.— 2009.— [P. 128-133]
Další autoři: Sharova E. S. Ekaterina Sergeevna, Poluboyartsev D. S., Chekantsev N. V. Nikita Vitalievich, Kravtsov А. V. Anatoly Vasilyevich, Ivanchina E. D. Emilia Dmitrievna
Shrnutí:Title screen
A methodology of constructing nonstationary kinetic models of multicomponent catalytic processes of hydrocarbon conversion on platinum-containing catalysts was developed. Their kinetic and technological parameters in industrial catalytic reforming were estimated. The simulation system in gasoline production allows for the testing and choosing of an optimum catalyst depending on the composition of the processed hydrocarbon raw materials. The developed testing technique is based on the processing of the results of the commercial operation of platinum-containing reforming catalysts using the computer simulation system. It allows the estimation of kinetic parameters, the prediction of selectivity, and raw cycle duration after catalyst regeneration under conditions of commercial operation, taking into account the reactivity of hydrocarbons.
Режим доступа: по договору с организацией-держателем ресурса
Jazyk:angličtina
Vydáno: 2009
Témata:
On-line přístup:http://dx.doi.org/10.1134/S2070050409020068
Médium: xMaterials Elektronický zdroj Kapitola
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639835

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200 1 |a Monitoring of the commercial operation of reforming catalysts using a computer simulation system  |f E. S. Sharova [et al.] 
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320 |a [References: p. 133 (7 tit.)] 
330 |a A methodology of constructing nonstationary kinetic models of multicomponent catalytic processes of hydrocarbon conversion on platinum-containing catalysts was developed. Their kinetic and technological parameters in industrial catalytic reforming were estimated. The simulation system in gasoline production allows for the testing and choosing of an optimum catalyst depending on the composition of the processed hydrocarbon raw materials. The developed testing technique is based on the processing of the results of the commercial operation of platinum-containing reforming catalysts using the computer simulation system. It allows the estimation of kinetic parameters, the prediction of selectivity, and raw cycle duration after catalyst regeneration under conditions of commercial operation, taking into account the reactivity of hydrocarbons. 
333 |a Режим доступа: по договору с организацией-держателем ресурса 
461 |t Catalysis in Industry  |o Scientific Journal 
463 |t Vol. 1, iss. 2  |v [P. 128-133]  |d 2009 
610 1 |a электронный ресурс 
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701 1 |a Sharova  |b E. S.  |c chemist  |c Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences  |f 1984-  |g Ekaterina Sergeevna  |3 (RuTPU)RU\TPU\pers\34056  |9 17620 
701 1 |a Poluboyartsev  |b D. S. 
701 1 |a Chekantsev  |b N. V.  |c chemical-technologist  |c Associate Professor of Tomsk Polytechnic University, Junior research, Candidate of technical sciences  |f 1985-  |g Nikita Vitalievich  |3 (RuTPU)RU\TPU\pers\33870 
701 1 |a Kravtsov  |b А. V.  |c Russian chemical engineer  |c Consulting Professor, Doctor of Technical Sciences (DSc)  |f 1938-2012  |g Anatoly Vasilyevich  |3 (RuTPU)RU\TPU\pers\29428 
701 1 |a Ivanchina  |b E. D.  |c chemist  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1951-  |g Emilia Dmitrievna  |3 (RuTPU)RU\TPU\pers\31274 
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