Mathematical model for the process of benzene alkylation by higher olefins

Dades bibliogràfiques
Parent link:Catalysis in Industry: Scientific Journal
Vol. 2, iss. 1.— 2010.— [P. 55-61]
Altres autors: Fetisova V. A., Ivashkina E. N. Elena Nikolaevna, Ivanchina E. D. Emilia Dmitrievna, Kravtsov A. V. Anatoly Vasilyevich
Sumari:Title screen
In this work, we considered the results on the modeling of the industrial catalytic alkylation process, one of the terminal stages in the production of linear alkyl benzene sulfonates (LAS) used as the basis for the synthesis of synthetic detergents. Taking into account the experimental data obtained under regular operational conditions of alkylation unit at the Linear Alkyl Benzene and Linear Alkyl Benzene Sulfonates (LAB-LAS) Plant of OOO Kirishinefteorgsintez (OOO KINEF), we developed a scheme of chemical reactions for the purpose of creating the kinetic model for the alkylation process. The kinetic parameters of this model were identified by solving the inverse kinetic problem under the lack of necessary experimental data, so we had to reduce the number of estimated kinetic parameters with the use of thermodynamic data. The software model of this process permitted us to calculate quite precisely the material and heat balances of the reactor and also to study the influence of changes in different technological parameters on the effectiveness of the process.
Режим доступа: по договору с организацией-держателем ресурса
Idioma:anglès
Publicat: 2010
Matèries:
Accés en línia:http://dx.doi.org/10.1134/S2070050410010095
Format: Electrònic Capítol de llibre
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=655716

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200 1 |a Mathematical model for the process of benzene alkylation by higher olefins  |f V. A. Fetisova [et al.] 
203 |a Text  |c electronic 
300 |a Title screen 
320 |a [Ref.: p. 61 (15 tit.)] 
330 |a In this work, we considered the results on the modeling of the industrial catalytic alkylation process, one of the terminal stages in the production of linear alkyl benzene sulfonates (LAS) used as the basis for the synthesis of synthetic detergents. Taking into account the experimental data obtained under regular operational conditions of alkylation unit at the Linear Alkyl Benzene and Linear Alkyl Benzene Sulfonates (LAB-LAS) Plant of OOO Kirishinefteorgsintez (OOO KINEF), we developed a scheme of chemical reactions for the purpose of creating the kinetic model for the alkylation process. The kinetic parameters of this model were identified by solving the inverse kinetic problem under the lack of necessary experimental data, so we had to reduce the number of estimated kinetic parameters with the use of thermodynamic data. The software model of this process permitted us to calculate quite precisely the material and heat balances of the reactor and also to study the influence of changes in different technological parameters on the effectiveness of the process. 
333 |a Режим доступа: по договору с организацией-держателем ресурса 
461 |t Catalysis in Industry  |o Scientific Journal 
463 |t Vol. 2, iss. 1  |v [P. 55-61]  |d 2010 
610 1 |a электронный ресурс 
610 1 |a труды учёных ТПУ 
701 1 |a Fetisova  |b V. A. 
701 1 |a Ivashkina  |b E. N.  |c Chemical Engineer  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1983-  |g Elena Nikolaevna  |3 (RuTPU)RU\TPU\pers\31275  |9 15453 
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 
701 1 |a Kravtsov  |b A. V.  |c Chemical Engineer  |c Consulting Professor, Doctor of Technical Sciences (DSc)  |f 1938-2012  |g Anatoly Vasilyevich  |3 (RuTPU)RU\TPU\pers\29428 
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