Optimal Fractionation of Products of Refining Straight-run Gasoline on Zeolite Catalyst with Account of its Deactivation; Procedia Chemistry; Vol. 10 : Chemistry and Chemical Engineering in XXI century

Optimal Fractionation of Products of Refining Straight-run Gasoline on Zeolite Catalyst with Account of its Deactivation

Библиографические подробности
Источник:Procedia Chemistry
Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 332-336]
Корпоративные авторы: 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)
Другие авторы: Samborskaya M. A. Marina Anatolievna, Laktionova E. A., Wolf A. V. Andrey Viktorovich, Mashina V. V., Syskina A. A. Anna Aleksandrovna
Примечания:Title screen
Flowsheet of industrial refining straight-run gasoline on zeolite catalyst includes the necessary stage of fractionation of conversion products to produce commercial gasoline, gas and heavy residue. Changes in qualitative and quantitative compositions of the catalytic conversion products under catalyst deactivation require current parametrical optimization of this stage. Objective functions that take into account catalyst deactivation and the constrains depending on the requirements for product quality and equipment specifications were developed. Optimal conditions were found to differ significantly from those designed for fresh catalyst.
Режим доступа: по договору с организацией-держателем ресурса
Язык:английский
Опубликовано: 2014
Предметы:
электронный ресурс
труды учёных ТПУ
фракционирование
переработка
прямогонные бензины
цеолитовые катализаторы
целевые функции
дезактивация
катализаторы
refining straight-run gasoline
fractionation
current optimization
objective function
catalyst deactivation
Online-ссылка:http://dx.doi.org/10.1016/j.proche.2014.10.056
http://earchive.tpu.ru/handle/11683/35516
Формат: Электронный ресурс Статья
Запись в KOHA:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639518
Описание
Примечания:Title screen
Flowsheet of industrial refining straight-run gasoline on zeolite catalyst includes the necessary stage of fractionation of conversion products to produce commercial gasoline, gas and heavy residue. Changes in qualitative and quantitative compositions of the catalytic conversion products under catalyst deactivation require current parametrical optimization of this stage. Objective functions that take into account catalyst deactivation and the constrains depending on the requirements for product quality and equipment specifications were developed. Optimal conditions were found to differ significantly from those designed for fresh catalyst.
Режим доступа: по договору с организацией-держателем ресурса
DOI:10.1016/j.proche.2014.10.056

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