Complex modeling system for optimization of compounding process in gasoline pool to produce high-octane finished gasoline fuel; Chemical Engineering Journal; Vol. 277

Dettagli Bibliografici
Parent link:Chemical Engineering Journal
Vol. 277.— 2015.— [12 р.]
Ente Autore: Национальный исследовательский Томский политехнический университет
Altri autori: Ivanchina E. D. Emilia Dmitrievna, Kirgina M. V. Mariya Vladimirovna, Chekantsev N. V. Nikita Vitalievich, Sakhnevich B.V., Sviridova E. V. Elizaveta Vitaljevna, Romanovskiy R. V. Rostislav Vladimirovich
Riassunto:Title screen
The process of gasoline compounding is a difficult multistage industrial technology. Octane number is a numerical equivalent of gasoline detonation resistance, the main operational characteristic of trade gasoline. Prediction of octane numbers of individual hydrocarbons was performed with calculations of dissociation energy of their molecules. In this paper, a new approach is proposed for optimization and prediction of the unit operation modes for processing of multicomponent hydrocarbon mixtures, based on a complex mathematical model that considers reactivities of hydrocarbons of wide gasoline fraction in the reforming, isomerization, and compounding processes. The accuracy of calculations is confirmed with huge massive of experimental data obtained from catalytic reforming, catalytic cracking (FCC), isomerization and alkylation units.
Режим доступа: по договору с организацией-держателем ресурса
Lingua:inglese
Pubblicazione: 2015
Soggetti:
Accesso online:http://dx.doi.org/10.1016/j.cej.2015.03.014
Natura: Elettronico Capitolo di libro
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=643002
Descrizione
Riassunto:Title screen
The process of gasoline compounding is a difficult multistage industrial technology. Octane number is a numerical equivalent of gasoline detonation resistance, the main operational characteristic of trade gasoline. Prediction of octane numbers of individual hydrocarbons was performed with calculations of dissociation energy of their molecules. In this paper, a new approach is proposed for optimization and prediction of the unit operation modes for processing of multicomponent hydrocarbon mixtures, based on a complex mathematical model that considers reactivities of hydrocarbons of wide gasoline fraction in the reforming, isomerization, and compounding processes. The accuracy of calculations is confirmed with huge massive of experimental data obtained from catalytic reforming, catalytic cracking (FCC), isomerization and alkylation units.
Режим доступа: по договору с организацией-держателем ресурса
DOI:10.1016/j.cej.2015.03.014