Development of Complex Mathematical Model of Light Naphtha Isomerization and Rectification Processes

Development of Complex Mathematical Model of Light Naphtha Isomerization and Rectification Processes

Bibliographic Details
Parent link:Procedia Chemistry
Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 236-243]
Main Author: Chuzlov V. A. Vyacheslav Alekseevich
Corporate Author: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Other Authors: Chekantsev N. V. Nikita Vitalievich, Ivanchina E. D. Emilia Dmitrievna
Summary: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
Published: 2014
Subjects:
электронный ресурс
труды учёных ТПУ
математические модели
изомеризация
моделирование
реакторы
колонки
катализаторы
rectification
isomerization
simulation
reactor
column
Online Access:http://dx.doi.org/10.1016/j.proche.2014.10.040
http://earchive.tpu.ru/handle/11683/35501
Format: Electronic Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639498

Internet

http://dx.doi.org/10.1016/j.proche.2014.10.040
http://earchive.tpu.ru/handle/11683/35501

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