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

Podrobná bibliografie
Parent link:Procedia Chemistry
Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 236-243]
Hlavní autor: Chuzlov V. A. Vyacheslav Alekseevich
Korporativní autor: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Další autoři: Chekantsev N. V. Nikita Vitalievich, Ivanchina E. D. Emilia Dmitrievna
Shrnutí: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
Jazyk:angličtina
Vydáno: 2014
Témata:
On-line přístup:http://dx.doi.org/10.1016/j.proche.2014.10.040
http://earchive.tpu.ru/handle/11683/35501
Médium: Elektronický zdroj Kapitola
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639498