Mathematical modeling of the process catalytic isomerization of light naphtha

Mathematical modeling of the process catalytic isomerization of light naphtha

Detalles Bibliográficos
Parent link:	Petroleum and Coal Vol. 61, iss. 2.— 2019.— [P. 413-417]
Autor Corporativo:	Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
Outros autores:	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. Свободный доступ из сети Интернет
Idioma:	inglés
Publicado:	2019
Subjects:	электронный ресурс труды учёных ТПУ catalytic isomerization branched alkanes octane number method of mathematical modelling каталитическая изомеризация алканы октановые числа математическое моделирование
Acceso en liña:	https://www.vurup.sk/wp-content/uploads/2019/04/PC-X-2019_Chuzlov_5_rev1.pdf
Formato:	Electrónico Capítulo de libro
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=661776

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