Particle-based modeling of heterogeneous chemical kinetics including mass transfer

Journal Article (2017)
Author(s)

A. Sengar (Eindhoven University of Technology)

J.R. Kuipers (Eindhoven University of Technology)

Rutger A. Van Santen (Eindhoven University of Technology)

J.T. Padding (TU Delft - Intensified Reaction and Separation Systems)

Research Group
Intensified Reaction and Separation Systems
Copyright
© 2017 A. Sengar, J.R. Kuipers, Rutger A. Van Santen, J.T. Padding
DOI related publication
https://doi.org/10.1103/PhysRevE.96.022115
More Info
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Publication Year
2017
Language
English
Copyright
© 2017 A. Sengar, J.R. Kuipers, Rutger A. Van Santen, J.T. Padding
Research Group
Intensified Reaction and Separation Systems
Issue number
2
Volume number
96
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Abstract

Connecting the macroscopic world of continuous fields to the microscopic world of discrete molecular events is important for understanding several phenomena occurring at physical boundaries of systems. An important example is heterogeneous catalysis, where reactions take place at active surfaces, but the effective reaction rates are determined by transport limitations in the bulk fluid and reaction limitations on the catalyst surface. In this work we study the macro-micro connection in a model heterogeneous catalytic reactor by means of stochastic rotation dynamics. The model is able to resolve the convective and diffusive interplay between participating species, while including adsorption, desorption, and reaction processes on the catalytic surface. Here we apply the simulation methodology to a simple straight microchannel with a catalytic strip. Dimensionless Damkohler numbers are used to comment on the spatial concentration profiles of reactants and products near the catalyst strip and in the bulk. We end the discussion with an outlook on more complicated geometries and increasingly complex reactions.

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