Author:
Hernandez-Aguirre Alberto,Hernandez-Martinez Eliseo,López-Isunza Felipe,Castillo Carlos O.
Funder
Consejo Nacional de Ciencia y Tecnología
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,Environmental Chemistry,General Chemistry
Reference109 articles.
1. H. Lopez-Isunza, Steady state and dynamic behaviour of an industrial scale fixed bed catalytic reactor, Ph.D. thesis, University of London (1983).
2. F. Lopez-Isunza, L.S. Kershenbaum, The role of reversible changes in catalyst activity in the observed multiple steady stated during partial oxidation dynamics, Chemical Engineering Science 47 (9) (1992) 2817–2822, twelfth International Symposium on Chemical Reaction Engineering Today. doi: 10.1016/0009-2509(92)87135-D.
3. 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;Castillo-Araiza;Ind. Eng. Chem. Res.,2010
4. C. Castillo-Araiza, F. López-Isunza, The role of catalyst activity on the steady state and transient behavior of an industrial-scale fixed bed catalytic reactor for the partial oxidation of o-xylene on V2O5/TiO2 catalysts, Chemical Engineering Journal 176–177 (2011) 26–32, XIX 4 International Conference on Chemical Reactors (CHEMREACTOR-19). doi: 10.1016/j.cej.2011.06.051.
5. Decoding complexity during the modeling of the microscopic energetic path in a wall-cooled packed-bed reactor;Castillo-Araiza;Energy: Sci. Techno. Manage.,2021
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