Non-Stationary Computer-Aided Simulation of gasoline Fraction Pyrolysis; Petroleum and Coal; Vol. 63, iss. 3

Non-Stationary Computer-Aided Simulation of gasoline Fraction Pyrolysis; Petroleum and Coal; Vol. 63, iss. 3

Bibliographic Details
Parent link:Petroleum and Coal
Vol. 63, iss. 3.— 2021.— [P. 612-620]
Main Author: Bunaev A. A. Ayur Alekseevich
Corporate Author: Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
Other Authors: Dolganov I. M. Igor Mikhailovich, Dolganova I. O. Irena Olegovna
Summary:Title screen
Pyrolysis of hydrocarbons is one of the main processes in petro-chemistry due to the high demand for products derived from light alkenes such as ethene and propene. The process is performed with lackof oxygen and extreme temperatures. Thus, heavier hydrocarbons decay into lighter alkenes. Although, side reactions of these obtained alkenes polymerization with further polycondensation result in coke deposition. Therefore, crossection area of tube decreases as well as residence time. And yield of target products decreases under these conditions, i.e. the process becomes inefficient. The given paper discusses the mechanism of the pyrolysis process, presents the model itself and discusses theinfluence of main technological parameters on the process efficiency.
Language:English
Published: 2021
Subjects:
электронный ресурс
труды учёных ТПУ
pyrolysis
non-stationary simulation
coke deposition
optimum performance
пиролиз
кокс
отложения
производительность
Online Access:https://www.vurup.sk/wp-content/uploads/2021/07/PC-X_Dolganova_34.pdf
Format: Electronic Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=666149

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