Study of the influence of catalyst activity on the reaction rateduring hydrotreating of diesel fractions using mathematical modeling; Journal of Economics and Social Sciences; № 14

Dettagli Bibliografici
Parent link:Journal of Economics and Social Sciences: electronic scientific journal.— , 2012-.— 2312-2978
№ 14.— 2019.— [3 p.]
Autore principale: Kotkova E. Elena
Ente Autore: Engineering school of natural resources, Tomsk Polytechnic University
Riassunto:Title screen
The previously developed mathematical model takes into account the activity of the catalyst. The influence of the activityof the catalyst on the rate of the reactions occurring during hydrotreating, the resulting rate constants of the deactivation.The adequacy of calculations of the improved model is checked. It was found that the reduction of catalyst activity byonly 30% significantly affects the reaction rate constants, the reactions are slowed down by 18 times. The quality of theproduct is reduced when the catalyst is deactivated. To compensate for the loss of catalyst activity, it is necessary to varythe technological parameters, in particular, to increase the temperature in the reactor.
Lingua:inglese
Pubblicazione: 2019
Serie:Социологические науки
Soggetti:
Accesso online:http://earchive.tpu.ru/handle/11683/55737
Natura: Elettronico Capitolo di libro
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=584047
Descrizione
Descrizione fisica:1 файл (324 Кб)
Riassunto:Title screen
The previously developed mathematical model takes into account the activity of the catalyst. The influence of the activityof the catalyst on the rate of the reactions occurring during hydrotreating, the resulting rate constants of the deactivation.The adequacy of calculations of the improved model is checked. It was found that the reduction of catalyst activity byonly 30% significantly affects the reaction rate constants, the reactions are slowed down by 18 times. The quality of theproduct is reduced when the catalyst is deactivated. To compensate for the loss of catalyst activity, it is necessary to varythe technological parameters, in particular, to increase the temperature in the reactor.