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This document summarizes a model of a porous reactor for studying heterogeneous catalysis. The model couples fluid flow and transport equations to simulate the flow fields, pressure, and concentration distributions within the reactor. Species A and B enter the reactor and react within the porous catalyst bed to produce species C according to a mass action law irreversible reaction. The results show the velocity and pressure drop mainly within the porous bed, and the consumption and reaction distribution of
- Author
- Tomás Barrientos Bruna
- Language
- EN