Influence of Feedstock Group Composition on the Octane Number and Composition of the Gasoline Fraction of Catalytically Cracked Vacuum Distillate

Bibliographic Details
Parent link:Petroleum Chemistry
Vol. 58, iss. 3.— 2018.— [P. 225-236]
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, Nazarova G. Yu. Galina Yurievna, Seytenova G. Zh. Gayni Zhumagalievna
Summary:Title screen
Thermodynamic parameters for the reactions of vacuum distillate catalytic cracking in a riser reactor have been calculated using the density functional theory. The list of the reactions has been compiled on the basis of laboratory studies on determining the group and structural-group composition of the vacuum distillate and the results of thermodynamic analysis. A kinetic model of the catalytic cracking process has been developed on the basis of a formalized scheme of the hydrocarbon conversion mechanism. By using the kinetic model derived, the effect of the group composition of four vacuum distillate samples on the octane number and the composition of the gasoline fraction of the catalytic cracking process has been assessed.
Режим доступа: по договору с организацией-держателем ресурса
Language:English
Published: 2018
Subjects:
Online Access:https://doi.org/10.1134/S0965544118030106
Format: Electronic Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=667019

MARC

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200 1 |a Influence of Feedstock Group Composition on the Octane Number and Composition of the Gasoline Fraction of Catalytically Cracked Vacuum Distillate  |f E. D. Ivanchina, E. N. Ivashkina, G. Yu. Nazarova, G. Zh. Seytenova 
203 |a Text  |c electronic 
300 |a Title screen 
320 |a [References: 47 tit.] 
330 |a Thermodynamic parameters for the reactions of vacuum distillate catalytic cracking in a riser reactor have been calculated using the density functional theory. The list of the reactions has been compiled on the basis of laboratory studies on determining the group and structural-group composition of the vacuum distillate and the results of thermodynamic analysis. A kinetic model of the catalytic cracking process has been developed on the basis of a formalized scheme of the hydrocarbon conversion mechanism. By using the kinetic model derived, the effect of the group composition of four vacuum distillate samples on the octane number and the composition of the gasoline fraction of the catalytic cracking process has been assessed. 
333 |a Режим доступа: по договору с организацией-держателем ресурса 
461 |t Petroleum Chemistry 
463 |t Vol. 58, iss. 3  |v [P. 225-236]  |d 2018 
610 1 |a электронный ресурс 
610 1 |a труды учёных ТПУ 
610 1 |a catalytic cracking 
610 1 |a deep oil processing 
610 1 |a coke 
610 1 |a light fractions 
610 1 |a resource-saving efficiency 
610 1 |a gasoline 
610 1 |a diesel fuel 
610 1 |a olefins 
610 1 |a глубокая переработка 
610 1 |a нефти 
610 1 |a каталитический крекинг 
610 1 |a кокс 
610 1 |a легкие фракции 
610 1 |a ресурсосберегающие технологии 
610 1 |a бензины 
610 1 |a дизельные топлива 
610 1 |a олефины 
701 1 |a Ivanchina  |b E. D.  |c chemist  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1951-2022  |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 Nazarova  |b G. Yu.  |c chemist  |c assistant of Tomsk Polytechnic University  |f 1990-  |g Galina Yurievna  |3 (RuTPU)RU\TPU\pers\35588  |9 18757 
701 1 |a Seytenova  |b G. Zh.  |g Gayni Zhumagalievna 
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