Influence of Feedstock Group Composition on the Octane Number and Composition of the Gasoline Fraction of Catalytically Cracked Vacuum Distillate
| Parent link: | Petroleum Chemistry Vol. 58, iss. 3.— 2018.— [P. 225-236] |
|---|---|
| Corporate Author: | |
| Other Authors: | , , , |
| 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
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| 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 |
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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 | |
| 712 | 0 | 2 | |a Национальный исследовательский Томский политехнический университет |b Инженерная школа природных ресурсов |b Отделение химической инженерии |3 (RuTPU)RU\TPU\col\23513 |
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| 856 | 4 | 0 | |u https://doi.org/10.1134/S0965544118030106 |
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