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

Chi tiết về thư mục
Parent link:Procedia Chemistry
Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 332-336]
Nhiều tác giả của công ty: 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)
Tác giả khác: Samborskaya M. A. Marina Anatolievna, Laktionova E. A., Wolf A. V. Andrey Viktorovich, Mashina V. V., Syskina A. A. Anna Aleksandrovna
Tóm tắt: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
Được phát hành: 2014
Những chủ đề:
Truy cập trực tuyến:http://dx.doi.org/10.1016/j.proche.2014.10.056
http://earchive.tpu.ru/handle/11683/35516
Định dạng: Điện tử Chương của sách
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639518
Miêu tả
Tóm tắt: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