Mathematical modeling of the process catalytic isomerization of light naphtha

Mathematical modeling of the process catalytic isomerization of light naphtha

Bibliographic Details
Parent link:Petroleum and Coal
Vol. 61, iss. 2.— 2019.— [P. 413-417]
Corporate Author: Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
Other Authors: Ivanchina E. D. Emilia Dmitrievna, Chuzlov V. A. Vyacheslav Alekseevich, Ivanchin N. R. Nikita, Borissov A. A. Anatoli Alimpievich, Seytenova G. Zh. Gayni Zhumagalievna, Dyusova (Ilchubaeva) R. Rizagul
Summary:Title screen
The aim of this work is to study the process of catalytic isomerization of light naphtha by the methodof mathematical modelling. The influence of temperature and feedstock flow rate on octane numberand yield of the product (branched alkanes) was studied depending on the feedstock composition. Thetemperature mode of the process was optimized depending on the composition and feedstock flowrate.
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Language:English
Published: 2019
Subjects:
электронный ресурс
труды учёных ТПУ
catalytic isomerization
branched alkanes
octane number
method of mathematical modelling
каталитическая изомеризация
алканы
октановые числа
математическое моделирование
Online Access:https://www.vurup.sk/wp-content/uploads/2019/04/PC-X-2019_Chuzlov_5_rev1.pdf
Format: Electronic Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=661776

Internet

https://www.vurup.sk/wp-content/uploads/2019/04/PC-X-2019_Chuzlov_5_rev1.pdf

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