Development of Complex Mathematical Model of Light Naphtha Isomerization and Rectification Processes; Procedia Chemistry; Vol. 10 : Chemistry and Chemical Engineering in XXI century

Sonraí bibleagrafaíochta
Parent link:Procedia Chemistry
Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 236-243]
Príomhchruthaitheoir: Chuzlov V. A. Vyacheslav Alekseevich
Údar corparáideach: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Rannpháirtithe: Chekantsev N. V. Nikita Vitalievich, Ivanchina E. D. Emilia Dmitrievna
Achoimre:Title screen
The technique of developing a mathematical model of catalytic isomerization of light naphtha is stated Using experimental data from an industrial isomerization unit shows adequacy of the mathematical model to the real process. The paper presents a method for optimizing the operation of the plant together with catalytic isomerization unit and separation columns. Selection of optimal modes of separation columns allows achieving the desired flow separation between units, as well as extension of the life of the catalyst SI-2.
Режим доступа: по договору с организацией-держателем ресурса
Teanga:Béarla
Foilsithe / Cruthaithe: 2014
Ábhair:
Rochtain ar líne:http://dx.doi.org/10.1016/j.proche.2014.10.040
http://earchive.tpu.ru/handle/11683/35501
Formáid: Leictreonach Caibidil leabhair
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639498
Cur síos
Achoimre:Title screen
The technique of developing a mathematical model of catalytic isomerization of light naphtha is stated Using experimental data from an industrial isomerization unit shows adequacy of the mathematical model to the real process. The paper presents a method for optimizing the operation of the plant together with catalytic isomerization unit and separation columns. Selection of optimal modes of separation columns allows achieving the desired flow separation between units, as well as extension of the life of the catalyst SI-2.
Режим доступа: по договору с организацией-держателем ресурса
DOI:10.1016/j.proche.2014.10.040