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

Bibliografische gegevens
Parent link:	Petroleum and Coal Vol. 58, iss. 7.— 2016.— [P. 721-725]
Coauteur:	Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Andere auteurs:	Samborskaya M. A. Marina Anatolievna, Gryaznova I. A. Inga Andreevna, Mashina V. V. Vera Vadimovna, Cherednichenko O. A. Olga Alekseevna
Samenvatting:	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
Taal:	Engels
Gepubliceerd in:	2016
Onderwerpen:	электронный ресурс труды учёных ТПУ zeolite-catalyst катализаторы кинетическое моделирование реакторы оптимальные режимы
Online toegang:	http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_7_2016_samborskaya_503.pdf
Formaat:	Elektronisch Hoofdstuk
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=654352

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