Simulation of Ethanol to Ethylene Dehydration on Alumina Catalyst in Multitubular Reactor Тезисы доклада
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Catalyst Design: 4th International School-Conference on Catalysis for Young Scientists 05-06 сент. 2015 , Казань |
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| Сборник | CATALYST DESIGN. From Molecular to Industrial level / 4th International School-Conference on Catalysis for Young Scientists (ISCC-2015) (September 5-6, 2015 Kazan, Russia) Сборник, BIC. Novosibirsk.2015. 218 c. ISBN 9785906376114. РИНЦ |
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| Вых. Данные | Год: 2015, Страницы: 162-163 Страниц : 2 | ||
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Реферат:
In the present paper, kinetic model was used for theoretical study of the ethanol dehydration process on alumina catalyst under wider variation of catalysts activity and process parameters.
The effect of catalyst activity and selectivity on the process productivity and parametric sensitivity was analyzed; optimized operating conditions that favor the high yield of ethylene in multi-tubular reactor were determined.
Библиографическая ссылка:
Banzaraktsaeva S.P.
, Ovchinnikova E.V.
, Vernikovskaya N.V.
, Chumachenko V.A.
Simulation of Ethanol to Ethylene Dehydration on Alumina Catalyst in Multitubular Reactor
В сборнике CATALYST DESIGN. From Molecular to Industrial level / 4th International School-Conference on Catalysis for Young Scientists (ISCC-2015) (September 5-6, 2015 Kazan, Russia). – BIC., 2015. – C.162-163. – ISBN 9785906376114.
Simulation of Ethanol to Ethylene Dehydration on Alumina Catalyst in Multitubular Reactor
В сборнике CATALYST DESIGN. From Molecular to Industrial level / 4th International School-Conference on Catalysis for Young Scientists (ISCC-2015) (September 5-6, 2015 Kazan, Russia). – BIC., 2015. – C.162-163. – ISBN 9785906376114.
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