Mathematical Modeling Sulfuric Acid Catalyzed Alkylation of Isobutane with Olefins

Mathematical Modeling Sulfuric Acid Catalyzed Alkylation of Isobutane with Olefins

Bibliographic Details
Parent link:	Procedia Engineering Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft).— 2016.— [P. 81-86]
Corporate Author:	Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Other Authors:	Ivashkina E. N. Elena Nikolaevna, Ivanchina E. D. Emilia Dmitrievna, Nurmakanova A. E. Asem Eslyambekovna, Boychenko S. S. Stanislav Sergeevich, Ushakov A. S. Anton Sergeevich, Dolganova I. O. Irena Olegovna
Summary:	Title screen The article provides the results of applied mathematical model of sulfuric acid catalyzed alkylation of isobutane with olefins. It was shown that increasing the content of propylene in the feedstock to 2 % leads to decrease in octane number of alkylate to 0.5-1.0 points. Alkylates produced from feedstock with less isobutane mass fraction have a smaller value of octane number. Using mathematic model it was determined that the main parameter influencing the acid activity in the alkylation process is the fresh acid concentration.
Published:	2016
Subjects:	электронный ресурс труды учёных ТПУ mathematical modeling alkylate optimization octane number sulfuric acid alkylation математическое моделирование оптимизация октановые числа сернокислотное алкилирование алкилаты
Online Access:	http://dx.doi.org/10.1016/j.proeng.2016.07.632
Format:	Electronic Book Chapter
KOHA link:	https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=651757

Internet

http://dx.doi.org/10.1016/j.proeng.2016.07.632