(671g) Modeling of Catalytic Fixed-Bed Reactors: Comparison of 1D/2D Porous Media and 3D Particle-Resolved Simulations
AIChE Annual Meeting
2024
2024 AIChE Annual Meeting
Catalysis and Reaction Engineering Division
Modeling and Analysis of Chemical Reactors II: New Developments
Thursday, October 31, 2024 - 2:18pm to 2:36pm
Several validation tests were performed comparing 1D vs. 3D PRCFD. Catalytic Partial Oxidation (CPOX) and Dry Reforming of Methane (DRM) at three different tube to particle ratios N of 1.1, 2, and 7, and three different particle Reynolds numbers (Rep = 29, 145, 290 and 1450) have been investigated. Results were generally good, demonstrating that for these reactions and conditions a 1D model can achieve the same results as PRCFD in a fraction of the time (seconds vs. hours).
DUO can also simulate porous media [2] using different energy model assumptions: i.e., separate (aka heterogeneous or non-equilibrium) or combined (aka homogeneous or equilibrium) energy equations for the fluid and solid phases. Under tested conditions, PBR-1D, DUO-2D (both heterogenous and homogeneous energy models), and DUO-3D (PRCFD, Fig. 1) produced similar results for CPOX and DRM cases.
[1] DETCHEM v3.0 2024. omegadot software & consulting, GmbH. www.omegadot.software .
[2] OpenFOAM v11, The Open Source CFD Toolbox, www.openfoam.org .
[3] E. Daymo, M. Hettel, O. Deutschmann, G. Wehinger. Chem. Eng. Sci. 250 (2022) 117408.
[4] E.A. Daymo, A.L. Tonkovich, M Hettel, A. Shirsath, 1D and 2D porous media fixed bed reactor simulations with DUO. Meccanica (2024). https://doi.org/10.1007/s11012-024-01764-8