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

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

Opis bibliograficzny
Parent link:	Procedia Chemistry Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 236-243]
1. autor:	Chuzlov V. A. Vyacheslav Alekseevich
Korporacja:	Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Kolejni autorzy:	Chekantsev N. V. Nikita Vitalievich, Ivanchina E. D. Emilia Dmitrievna
Streszczenie:	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
Język:	angielski
Wydane:	2014
Hasła przedmiotowe:	электронный ресурс труды учёных ТПУ математические модели изомеризация моделирование реакторы колонки катализаторы rectification isomerization simulation reactor column
Dostęp online:	http://dx.doi.org/10.1016/j.proche.2014.10.040 http://earchive.tpu.ru/handle/11683/35501
Format:	Elektroniczne Rozdział
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639498

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