Development of a Mathematical Model of the Vacuum Oil Distillates Hydrocracking Process Taking into Account Catalyst Deactivation by Coke / N. S. Belinskaya, D. A. Afanasjeva, V. V. Bykova, M. S. Kosten

Уровень набора: Petroleum and CoalАльтернативный автор-лицо: Belinskaya, N. S., chemist, Associate Professor of Tomsk Polytechnic University, Candidate of Sciences, 1989-, Natalia Sergeevna;Afanasjeva, D. A., Darjya Aleksandrovna;Bykova, V. V., Violetta Vitaljevna;Kosten, M. S., Mikhail SergeevichКоллективный автор (вторичный): Национальный исследовательский Томский политехнический университет, Инженерная школа природных ресурсов, Отделение химической инженерииЯзык: английский.Страна: .Резюме или реферат: A mathematical model of the vacuum oil distillates hydrocracking process, which takes into account catalyst deactivation by coke, was developed. The mathematical model was implemented in the form of a computer modelling system. Using the developed computer modelling system, predictive calculations of the decrease in the catalyst activity during the working cycle were carried out for various compositions of the feedstock. The influence of the ratio Hydrogen-containing gas / Feedstock on the rate of catalyst deactivation during the working cycle was shown..Примечания о наличии в документе библиографии/указателя: [References: 20 tit.].Тематика: электронный ресурс | труды учёных ТПУ | vacuum distillate | hydrocracking | mathematical model | дистилляты | гидрокрекинг | математическая модель Ресурсы он-лайн:Щелкните здесь для доступа в онлайн
Тэги из этой библиотеки: Нет тэгов из этой библиотеки для этого заглавия. Авторизуйтесь, чтобы добавить теги.
Оценка
    Средний рейтинг: 0.0 (0 голосов)
Нет реальных экземпляров для этой записи

Title screen

[References: 20 tit.]

A mathematical model of the vacuum oil distillates hydrocracking process, which takes into account catalyst deactivation by coke, was developed. The mathematical model was implemented in the form of a computer modelling system. Using the developed computer modelling system, predictive calculations of the decrease in the catalyst activity during the working cycle were carried out for various compositions of the feedstock. The influence of the ratio Hydrogen-containing gas / Feedstock on the rate of catalyst deactivation during the working cycle was shown.

Для данного заглавия нет комментариев.

оставить комментарий.