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Workflow for computational fluid dynamics modeling of fixed-bed reactors packed with metal foam pellets: Hydrodynamics |
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| Authors: | Ginu R George Marina Bockelmann Leonhard Schmalhorst Didier Beton Alexandra Gerstle Lars Torkuhl Andreas Lindermeir Gregor D Wehinger |
| Affiliation: | 1. Institute of Chemical and Electrochemical Process Engineering, Clausthal University of Technology, Clausthal-Zellerfeld, Germany;2. CUTEC Research Centre, Clausthal University of Technology, Clausthal-Zellerfeld, Germany
Contribution: Data curation, Formal analysis, ?Investigation, Validation, Visualization, Writing - review & editing;3. Alantum Europe GmbH, Munich, Germany Contribution: ?Investigation, Supervision, Writing - review & editing;4. Alantum Europe GmbH, Munich, Germany Contribution: Data curation, Funding acquisition, ?Investigation, Supervision, Writing - review & editing;5. Alantum Europe GmbH, Munich, Germany Contribution: ?Investigation, Resources;6. Alantum Europe GmbH, Munich, Germany Contribution: Funding acquisition, Resources, Supervision;7. CUTEC Research Centre, Clausthal University of Technology, Clausthal-Zellerfeld, Germany Contribution: Data curation, ?Investigation, Resources, Supervision, Validation, Writing - review & editing |
| Abstract: | In recent years, the catalyst pellets made of open-cell metallic foams have been identified as a promising alternative in fixed-bed reactors. A reliable modeling tool is necessary to investigate the suitability of different foam properties and the shapes of foam pellets. In this article, a workflow for a detailed computational fluid dynamics (CFD) model is presented, which aims to study the flow characteristics in the slender packed beds made of metal foam pellets. The CFD model accounts for the actual random packing structure and the fluid flow throughout the interstitial regions is fully resolved, whereas flow through the porous foam pellets is represented by the closure equations for the porous media model. The bed structure is generated using rigid body dynamics (RBD) and the influence of the catalyst loading method is also considered. The mean bed voidage and the pressure drop predicted by the simulations show good agreement with the experimental data. |
| Keywords: | CFD fixed-bed reactor open-cell metal foam pellets pressure drop |