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Performance Enhancement by Unsteady-State Reactor Operation: Theoretical Analysis for Two-Sites Kinetic Model Научная публикация

Журнал Chemical Engineering and Technology
ISSN: 0930-7516 , E-ISSN: 1521-4125
Вых. Данные Год: 2003, Том: 26, Номер: 7, Страницы: 751-758 Страниц : 8 DOI: 10.1002/ceat.200301640
Ключевые слова Catalysts; Chemical reactors; Oscillations; Reactor operation
Авторы Reshetnikov S.I. 1 , Ivanov E.A. 1 , Kiwi-Minsker L. 2 , Renken A. 2
Организации
1 Boreskov Institute of Catalysis SB RAS, Pr. Akad. Lavrentieva 5, Novosibirsk 630090, Russia
2 Laboratory of Chemical Reaction Engineering, Swiss Federal Institute of Technology (EPFL), Lausanne CH-1015, Switzerland

Информация о финансировании (3)

1 Российский фонд фундаментальных исследований 01-03-32790
2 European Commission INCO-COPERNICUS IC15-CT97-0709
3 Swiss National Science Foundation

Реферат: Theoretical analysis of the reactor performance under unsteady-state conditions was carried out. The reactions are described by two kinetic models, which involve the participation in catalytic reaction of two types of active sites. The kinetic model I assumes the blocking of one of the active sites by a reactant, and the kinetic model II suggests a transformation of active sites of one type into another under the influence of the reaction temperature. The unsteady-state conditions on the catalyst surface are supposed to be created (i) by forced oscillations of temperature and concentration in the reactor inlet (periodic operation of reactor) and (ii) by catalyst circulation between two reactors in a dual-reactor system (spatial regulation). The influence of various parameters like concentration of reactant, cycle split, length of period of forced oscillations, temperatures and the ratio of catalyst volumes in the dual-reactor was investigated with respect to the yield of the desired product. It is shown that for both cases of unsteady-state conditions (periodic reactor operation as well as in a dual-reactor system), a mean reaction rate predicted by the kinetic model I was up to two times higher than the steady-state value. The kinetic model II shows a 20 % increase of the selectivity towards the desired product.
Библиографическая ссылка: Reshetnikov S.I. , Ivanov E.A. , Kiwi-Minsker L. , Renken A.
Performance Enhancement by Unsteady-State Reactor Operation: Theoretical Analysis for Two-Sites Kinetic Model
Chemical Engineering and Technology. 2003. V.26. N7. P.751-758. DOI: 10.1002/ceat.200301640 WOS Scopus РИНЦ CAPlusCA OpenAlex
Файлы: Полный текст от издателя
Даты:
Поступила в редакцию: 26 июн. 2002 г.
Опубликована online: 7 июл. 2003 г.
Опубликована в печати: 9 июл. 2003 г.
Идентификаторы БД:
Web of science: WOS:000184242900006
Scopus: 2-s2.0-0042322843
РИНЦ: 13421161
Chemical Abstracts: 2003:587983
Chemical Abstracts (print): 139:135436
OpenAlex: W1982302289
Цитирование в БД:
БД Цитирований
Web of science 5
Scopus 7
РИНЦ 8
OpenAlex 8
Альметрики: