Simulation of Ethanol to Ethylene Dehydration on Alumina Catalyst in Multitubular Reactor Conference Abstracts
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Catalyst Design: 4th International School-Conference on Catalysis for Young Scientists 05-06 Sep 2015 , Казань |
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Source | CATALYST DESIGN. From Molecular to Industrial level / 4th International School-Conference on Catalysis for Young Scientists (ISCC-2015) (September 5-6, 2015 Kazan, Russia) Compilation, BIC. Novosibirsk.2015. 218 c. ISBN 9785906376114. РИНЦ |
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Output data | Year: 2015, Pages: 162-163 Pages count : 2 | ||
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Abstract:
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.
Cite:
Banzaraktsaeva S.P.
, Ovchinnikova E.V.
, Vernikovskaya N.V.
, Chumachenko V.A.
Simulation of Ethanol to Ethylene Dehydration on Alumina Catalyst in Multitubular Reactor
In compilation 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
In compilation 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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