A Pseudo-Local Approach to Describe Heat Transfer in a Packed Bed Catalytic Reactor with Low Tube to Particle Diameter Ratio: Oxidative Dehydrogenation of Ethane as a Case Study-Reference-Cited by-同舟云学术

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A Pseudo-Local Approach to Describe Heat Transfer in a Packed Bed Catalytic Reactor with Low Tube to Particle Diameter Ratio: Oxidative Dehydrogenation of Ethane as a Case Study

Published:2022 Issue: Volume: Page:
ISSN:1556-5068
Container-title:SSRN Electronic Journal
language:en
Short-container-title:SSRN Journal

Author:

Romero-Limones Alejandro,Poissonnier Jeroen,Thybaut Joris W.,Castillo-Araiza Carlos

Publisher

Elsevier BV

Subject

General Earth and Planetary Sciences,General Environmental Science

Reference111 articles.

1. A study of the influence of the operating parameters on the temperature of the hot spot in a fixed bed reactor;A I Anastasov;Chem. Eng. J,2002

2. Fixed Bed Catalytic Reactor;G F Froment;Ind. Eng. Chem,1967

3. The role of kinetics and heat transfer on the performance of an industrial wall-cooled packed-bed reactor: Oxidative dehydrogenation of ethane;G Che-Galicia;AIChE J,2020

4. A simulation model accounting for structural radial nonuniformities in fixed bed reactors;H Delmas;Chem. Eng. Sci,1988

5. Modeling the partial oxidation of o-xylene in an industrial packed-bed catalytic reactor: The role of hydrodynamics and catalyst activity in the heat transport;C O Castillo-Araiza;Ind. Eng. Chem. Res,2010

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