Petrol production resource-efficiency increase with the help of mathematical modeling method; IFOST 2012; Vol. 1

Detalles Bibliográficos
Parent link:IFOST 2012: The 7th International Forum on Strategic Techology, September 17-21, 2012, Tomsk/ National Research Tomsk Polytechnic University (TPU).— , 2012
Vol. 1.— 2012.— P. 111-114
Autor principal: Gyngazova M. S. Mariya Sergeevna
Otros Autores: Ivanchina E. D. Emilia Dmitrievna, Korolenko M. V. Mikhail Vladimirovich
Sumario:Catalytic reforming is one of the most important processes for high octane gasoline manufacture and aromatic hydrocarbons production. There are several ways of this process modernization. It is effective to use mathematical modeling method to examine all possible variants because it requires low time and financial investments. In this work we analyzed the set of possible reactions, proposed kinetic model for catalytic reforming process, calculated thermodynamic and kinetic parameters, investigated catalyst layer hydrodynamics. A mathematical model for a moving-bed catalytic reforming reactor taking into account activity and circulating factor of the catalyst was presented. The model allows analyzing various variants of process modernization and can help to find optimal operation regimes.
Lenguaje:inglés
Publicado: 2012
Colección:Section 1. Chemical engineering and "Green technology"
Materias:
Formato: Capítulo de libro
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=259897

MARC

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200 1 |a Petrol production resource-efficiency increase with the help of mathematical modeling method  |f M. S. Gyngazova, E. D. Ivanchina, M. V. Korolenko 
225 1 |a Section 1. Chemical engineering and "Green technology" 
320 |a References: p. 114 (11 tit.) 
330 |a Catalytic reforming is one of the most important processes for high octane gasoline manufacture and aromatic hydrocarbons production. There are several ways of this process modernization. It is effective to use mathematical modeling method to examine all possible variants because it requires low time and financial investments. In this work we analyzed the set of possible reactions, proposed kinetic model for catalytic reforming process, calculated thermodynamic and kinetic parameters, investigated catalyst layer hydrodynamics. A mathematical model for a moving-bed catalytic reforming reactor taking into account activity and circulating factor of the catalyst was presented. The model allows analyzing various variants of process modernization and can help to find optimal operation regimes. 
461 1 |0 (RuTPU)RU\TPU\book\270770  |t IFOST 2012  |o The 7th International Forum on Strategic Techology, September 17-21, 2012, Tomsk  |f National Research Tomsk Polytechnic University (TPU)  |d 2012 
463 1 |0 (RuTPU)RU\TPU\book\269458  |t Vol. 1  |v P. 111-114  |d 2012  |p 809 p. 
610 1 |a лигроины 
610 1 |a каталитический риформинг 
610 1 |a математическое моделирование 
610 1 |a процессы 
610 1 |a оптимизация 
610 1 |a труды учёных ТПУ 
700 1 |a Gyngazova  |b M. S.  |c Chemical-technologist  |c Engineer of Tomsk Polytechnic University, Candidate of technical sciences  |f 1985-  |g Mariya Sergeevna  |2 stltpush  |3 (RuTPU)RU\TPU\pers\31995 
701 1 |a Ivanchina  |b E. D.  |c chemist  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1951-  |g Emilia Dmitrievna  |2 stltpush  |3 (RuTPU)RU\TPU\pers\31274 
701 1 |a Korolenko  |b M. V.  |c chemist  |c Postgraduate of Tomsk Polytechnic University  |f 1986-  |g Mikhail Vladimirovich  |2 stltpush  |3 (RuTPU)RU\TPU\pers\32186 
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