Coke formation reduction in the cataltic reforming reactors at the optimal catalyst activity / E. S. Chernyakova [et al.]

Уровень набора: Petroleum and CoalАльтернативный автор-лицо: Chernyakova, E. S., chemist, Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences, 1984-, Ekaterina Sergeevna;Ivanchina, E. D., chemist, Professor of Tomsk Polytechnic University, Doctor of technical sciences, 1951-, Emilia Dmitrievna;Yakupova, I. V., Inna Vagizovna;Vinidiktova, M. V., Margarita Vladimirovna;Seytenova, G. Zh.Коллективный автор (вторичный): Национальный исследовательский Томский политехнический университет (ТПУ), Институт природных ресурсов (ИПР), Кафедра химической технологии топлива и химической кибернетики (ХТТ)Язык: английский.Страна: .Резюме или реферат: Analysis of the catalyst operation effectiveness of the reforming process was conducted with mathematical modelling method using. The proposed method allows estimating the process unsteadiness bytaking adverse reactions and the formation of reversible and graphite coke into account. The main characteristics of two reforming catalysts were calculated and compared. The criterion of effectiveness determining the coke accumulation and selectivity for the given technological conditions was used as the comparative characteristic. It was found that the coke accumulations at the current and optimal activity operation are different, vary from 2.65 % mass. for Catalyst 2 to 3.40 % mass. for Catalyst 1 and depends on the raw material volume..Примечания о наличии в документе библиографии/указателя: [References: p. 751-752 (16 tit.)].Тематика: электронный ресурс | труды учёных ТПУ | каталитический риформинг | коксообразование | математическое моделирование | катализаторы Ресурсы он-лайн:Щелкните здесь для доступа в онлайн
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[References: p. 751-752 (16 tit.)]

Analysis of the catalyst operation effectiveness of the reforming process was conducted with mathematical modelling method using. The proposed method allows estimating the process unsteadiness bytaking adverse reactions and the formation of reversible and graphite coke into account. The main characteristics of two reforming catalysts were calculated and compared. The criterion of effectiveness determining the coke accumulation and selectivity for the given technological conditions was used as the comparative characteristic. It was found that the coke accumulations at the current and optimal activity operation are different, vary from 2.65 % mass. for Catalyst 2 to 3.40 % mass. for Catalyst 1 and depends on the raw material volume.

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