Optimal design of straight- run gasoline conversion on zeolite catalyst; Petroleum and Coal; Vol. 58, iss. 7

Optimal design of straight- run gasoline conversion on zeolite catalyst; Petroleum and Coal; Vol. 58, iss. 7

Podrobná bibliografie
Parent link:	Petroleum and Coal Vol. 58, iss. 7.— 2016.— [P. 721-725]
Korporativní autor:	Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Další autoři:	Samborskaya M. A. Marina Anatolievna, Gryaznova I. A. Inga Andreevna, Mashina V. V. Vera Vadimovna, Cherednichenko O. A. Olga Alekseevna
Shrnutí:	Title screen The HYSYS Aspen Plus software is used to develop a model of the reactor unit including a plug flow reactor and distillation sequence for conversion of gasoline fractions. The constructive and process variables of the key equipment were optimized stepwise with the model. The developed objective dimensionless function allows choosing optimal conditions for work in the mode of maximum yield or in the mode of maximum octane number of the product. The reactor was designed and optimal modes were found for both the reactor and fractionation unit. Свободный доступ из сети Интернет
Jazyk:	angličtina
Vydáno:	2016
Témata:	электронный ресурс труды учёных ТПУ zeolite-catalyst катализаторы кинетическое моделирование реакторы оптимальные режимы
On-line přístup:	http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_7_2016_samborskaya_503.pdf
Médium:	Elektronický zdroj Kapitola
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=654352

Internet

http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_7_2016_samborskaya_503.pdf