Heterogeneous catalysis contributes to producing more than 80 % of all chemical products in the world.Industrial heterogeneous catalysis is a complex process that combines fully three-dimensional mass, momentum, and energy transport on several scales.In the present work, we leverage our previously developed CFD solver for non-isothermal heterogeneously catalyzed reactive flow based on the finite-volume method and extend it with multicomponent Stefan-Maxwell diffusion description to handle high-concetration multicomponent mixtures.The resulting framework is verified and validated on the simple Stefan tube experiment, for which an analytical solution is available.
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Hlavatý et al. (2024) studied this question.
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