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Benzene Hydrogenation in the Thiophene Presence over the Sulfide Ni-Mo/γ-Al2O3 Catalyst under Periodic Operation: Kinetics and Process Modelling Научная публикация

Конференция XVII International Conference on Chemical Reactors
15-19 мая 2006 , Athens-Crete
Журнал Chemical Engineering Journal
ISSN: 1385-8947 , E-ISSN: 1873-3212
Вых. Данные Год: 2007, Том: 134, Номер: 1-3, Страницы: 100-105 Страниц : 6 DOI: 10.1016/j.cej.2007.03.048
Ключевые слова Benzene hydrogenation, Periodic operation, Sulfide catalyst, Transient kinetics
Авторы Reshetnikov S.I. 1 , Ivanov E.A. 1 , Startsev A.N. 1
Организации
1 Boreskov Institute of Catalysis, Pr. Lavrentieva, 5, 630090 Novosibirsk, Russia

Реферат: An unsteady-state kinetic model of both benzene hydrogenation (HDA) and thiophene hydrogenolysis (HDS) on the sulfide hydrotreating catalyst Ni-Mo/Al2O3 has been developed. The model adequately describes experimental data obtained at the pressure 2 MPa, temperature 573 K and at various contact times and ratios of benzene/thiophene. The model is based on the assumption that the catalyst surface contains only one type of active sites, i.e., Ni atoms in the sulfide bimetallic species, which are responsible for both hydrogenolysis and hydrogenation reactions. On the base of the kinetic model, a theoretical analysis of the reactor performance under unsteady state conditions was carried out. The unsteady state conditions on the catalyst surface are supposed to be created by forced oscillations of thiophene concentration in the reactor inlet (periodic operation of reactor). The influence of various parameters like cycle split, length of period of forced oscillations in the reactor was investigated with respect to the conversion of the benzene. It is shown that for periodic reactor operation an average conversion was up to several times higher than a steady state value.
Библиографическая ссылка: Reshetnikov S.I. , Ivanov E.A. , Startsev A.N.
Benzene Hydrogenation in the Thiophene Presence over the Sulfide Ni-Mo/γ-Al2O3 Catalyst under Periodic Operation: Kinetics and Process Modelling
Chemical Engineering Journal. 2007. V.134. N1-3. P.100-105. DOI: 10.1016/j.cej.2007.03.048 WOS Scopus РИНЦ CAPlusCA OpenAlex
Даты:
Опубликована online: 28 мар. 2007 г.
Опубликована в печати: 1 нояб. 2007 г.
Идентификаторы БД:
Web of science: WOS:000249877600016
Scopus: 2-s2.0-34548232260
РИНЦ: 13562559
Chemical Abstracts: 2007:987811
Chemical Abstracts (print): 147:504983
OpenAlex: W2017429563
Цитирование в БД:
БД Цитирований
Web of science 14
Scopus 22
РИНЦ 22
OpenAlex 12
Альметрики: