Mathematical Modeling of the Linear Alkylbenzene Sulfonation Process in A Multitube Film Reactor

Bibliographic Details
Parent link:Petroleum and Coal
Vol. 63, iss. 1.— 2021.— [P. 245-251]
Corporate Author: Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
Other Authors: Ivanchina E. D. Emilia Dmitrievna, Ivashkina E. N. Elena Nikolaevna, Dolganova I. O. Irena Olegovna, Dolganov I. M. Igor Mikhailovich, Solopova A. A. Anastasia Alexandrovna
Summary:Title screen
In this paper, we analyze the influence of the content of aromatic hydrocarbon in the raw material flow on the concentration of the alkylbenzenesulfonic acid in the product mixture, the optimal sulfur consumption for combustion to obtain sulfonating gas, and the duration of the reactor operating period. It is shown that an increase in content in the raw material flow of aromatic hydrocarbon leads to a decrease of the alkylbenzenesulfonic acid in the product mixture, an increase the sulfur consumption, and a decrease in the duration of the reactor operating period.
Language:English
Published: 2021
Subjects:
Online Access:https://www.vurup.sk/wp-content/uploads/2021/02/PC-X_Dolganova_254.pdf
Format: Electronic Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=665347

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200 1 |a Mathematical Modeling of the Linear Alkylbenzene Sulfonation Process in A Multitube Film Reactor  |f E. D. Ivanchina, E. N. Ivashkina, I. O. Dolganova [et al.] 
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330 |a In this paper, we analyze the influence of the content of aromatic hydrocarbon in the raw material flow on the concentration of the alkylbenzenesulfonic acid in the product mixture, the optimal sulfur consumption for combustion to obtain sulfonating gas, and the duration of the reactor operating period. It is shown that an increase in content in the raw material flow of aromatic hydrocarbon leads to a decrease of the alkylbenzenesulfonic acid in the product mixture, an increase the sulfur consumption, and a decrease in the duration of the reactor operating period. 
461 |t Petroleum and Coal 
463 |t Vol. 63, iss. 1  |v [P. 245-251]  |d 2021 
610 1 |a электронный ресурс 
610 1 |a труды учёных ТПУ 
610 1 |a sulfonation 
610 1 |a linear alkylbenzene 
610 1 |a alkylbenzenesulfonic acid 
610 1 |a multi-tube film reactor 
610 1 |a tetralines 
610 1 |a mathematical modeling 
610 1 |a сульфирование 
610 1 |a линейный алкилбензол 
610 1 |a пленочные реакторы 
610 1 |a сульфоны 
610 1 |a математическое моделирование 
610 1 |a линейные процессы 
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 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 Dolganova  |b I. O.  |c chemist  |c Associate Scientist of Tomsk Polytechnic University, postgraduate student, candidate of technical Sciences  |f 1988-  |g Irena Olegovna  |3 (RuTPU)RU\TPU\pers\31271  |9 15449 
701 1 |a Dolganov  |b I. M.  |c Chemical Engineer  |c Associate Professor of Tomsk Polytechnic University, Candidate of Technical Sciences  |f 1987-  |g Igor Mikhailovich  |3 (RuTPU)RU\TPU\pers\32216  |9 16216 
701 1 |a Solopova  |b A. A.  |c Chemical engineer  |c Engineer of Tomsk Polytechnic University, Candidate of technical sciences  |f 1994-  |g Anastasia Alexandrovna  |3 (RuTPU)RU\TPU\pers\46604  |9 22262 
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801 2 |a RU  |b 63413507  |c 20210915  |g RCR 
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