Modeling of Reactor of Straight–run Gasoline Fractions Refining on Zeolite Catalysts

Modeling of Reactor of Straight–run Gasoline Fractions Refining on Zeolite Catalysts

Bibliographic Details
Parent link:	Procedia Chemistry Vol. 15 : Chemistry and Chemical Engineering in XXI century (CCE 2015).— 2015.— [P. 237-244]
Corporate Authors:	Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ), Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра иностранных языков (ИЯПР)
Other Authors:	Samborskaya M. A. Marina Anatolievna, Mashina V. V., Cherednichenko O. A., Makarovskikh A. V. Aleksandra Viktorovna
Summary:	Title screen Zeolites are widely used as catalysts and catalyst supports for fuel and lubricants production processes with enhanced performance properties. Design of industrial reactor requires the construction of a mathematical model and selection of optimal operating conditions for reducing the number of scaling stages. The authors have proposed a scheme of hydrocarbons conversion on zeolite catalysts, thermodynamics of reactions has been considered and the inverse kinetic problem has been solved. The model of reactor of straight–run gasoline fractions refining in software HYSYS Aspen Plus™ process simulator has been developed and its adequacy to experimental data has been shown. Режим доступа: по договору с организацией-держателем ресурса
Language:	English
Published:	2015
Subjects:	электронный ресурс труды учёных ТПУ цеоформинг реакторы кинетика прямогонные бензины фракции переработка нефти цеолитные катализаторы
Online Access:	http://dx.doi.org/10.1016/j.proche.2015.10.038 http://earchive.tpu.ru/handle/11683/15059
Format:	Electronic Book Chapter
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=645364

Internet

http://dx.doi.org/10.1016/j.proche.2015.10.038
http://earchive.tpu.ru/handle/11683/15059