Mathematical Modeling Sulfuric Acid Catalyzed Alkylation of Isobutane with Olefins; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)

Mathematical Modeling Sulfuric Acid Catalyzed Alkylation of Isobutane with Olefins; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)

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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]
Korporativní autor: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Další autoři: 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
Shrnutí: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.
Jazyk:angličtina
Vydáno: 2016
Témata:
электронный ресурс
труды учёных ТПУ
mathematical modeling
alkylate
optimization
octane number
sulfuric acid alkylation
математическое моделирование
оптимизация
октановые числа
сернокислотное алкилирование
алкилаты
On-line přístup:http://dx.doi.org/10.1016/j.proeng.2016.07.632
Médium: Elektronický zdroj Kapitola
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=651757

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