A simple approach to describe hydrodynamics and its effect on heat and mass transport in an industrial wall-cooled fixed bed catalytic reactor: ODH of ethane on a MoVNbTeO formulation

Author:

Aparicio-Mauricio Gustavo,Ruiz Richard S.,López-Isunza Felipe,Castillo-Araiza Carlos O.

Publisher

Elsevier BV

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,Environmental Chemistry,General Chemistry

Reference75 articles.

1. Transport effects in packed-bed oxidation reactors;Rosendall;Comput. Chem. Eng.,1995

2. Modeling of oxidative dehydrogenation of ethane to ethylene on a MoVTeNbO/TiO2 catalyst in an industrial-scale packed bed catalytic reactor;Che-Galicia;Chem. Eng. J.,2015

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

4. Simulation models accounting for radial voidage profiles in fixed-bed reactors;Papageorgiou;Chem. Eng. Sci.,1995

5. Modeling of heat and mass transport in wall-cooled tubular reactors;Koning;Chem. Sustainable Dev.,2003

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