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

Detalles Bibliográficos
Parent link:	Petroleum and Coal Vol. 58, iss. 7.— 2016.— [P. 721-725]
Autor Corporativo:	Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Otros Autores:	Samborskaya M. A. Marina Anatolievna, Gryaznova I. A. Inga Andreevna, Mashina V. V. Vera Vadimovna, Cherednichenko O. A. Olga Alekseevna
Sumario:	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
Lenguaje:	inglés
Publicado:	2016
Materias:	электронный ресурс труды учёных ТПУ zeolite-catalyst катализаторы кинетическое моделирование реакторы оптимальные режимы
Acceso en línea:	http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_7_2016_samborskaya_503.pdf
Formato:	Electrónico Capítulo de libro
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