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

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

Xehetasun bibliografikoak
Parent link:	Petroleum Chemistry Vol. 58, iss. 3.— 2018.— [P. 225-236]
Erakunde egilea:	Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
Beste egile batzuk:	Ivanchina E. D. Emilia Dmitrievna, Ivashkina E. N. Elena Nikolaevna, Nazarova G. Yu. Galina Yurievna, Seytenova G. Zh. Gayni Zhumagalievna
Gaia:	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
Argitaratua:	2018
Gaiak:	электронный ресурс труды учёных ТПУ catalytic cracking deep oil processing coke light fractions resource-saving efficiency gasoline diesel fuel olefins глубокая переработка нефти каталитический крекинг кокс легкие фракции ресурсосберегающие технологии бензины дизельные топлива олефины
Sarrera elektronikoa:	https://doi.org/10.1134/S0965544118030106
Formatua:	Baliabide elektronikoa Liburu kapitulua
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=667019

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