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

מידע ביבליוגרפי
Parent link:Procedia Chemistry
Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 236-243]
מחבר ראשי: Chuzlov V. A. Vyacheslav Alekseevich
מחבר תאגידי: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
מחברים אחרים: Chekantsev N. V. Nikita Vitalievich, Ivanchina E. D. Emilia Dmitrievna
סיכום: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
שפה:אנגלית
יצא לאור: 2014
נושאים:
גישה מקוונת:http://dx.doi.org/10.1016/j.proche.2014.10.040
http://earchive.tpu.ru/handle/11683/35501
פורמט: אלקטרוני Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639498