(684b) CFD-DEM Simulation of Gas-Solid Fluidized Beds with Detailed Heterogeneous Chemistry
AIChE Annual Meeting
2020
2020 Virtual AIChE Annual Meeting
Catalysis and Reaction Engineering Division
Multi-Scale Modeling
Thursday, November 19, 2020 - 8:15am to 8:30am
For many catalytic processes, gas-solid fluidized beds are preferred over packed bed reactors, mostly because of their excellent heat transfer and mixing characteristics. Two different techniques exist for modeling gas-solid systems. Euler-Euler models treat the gas and particle phase as interpenetrating continua, requiring (empirical) closure models. Euler-Lagrangian models on the other hand, track particles explicitly, resulting in a higher accuracy at the cost of higher computational efforts.
In this work, a reactive compressible four-way coupled CFD-DEM solver was developed with the open-source package CFDEMcoupling, which couples the CFD package OpenFOAM with the DEM solver LIGGGHTS. A heterogeneous catalytic framework was implemented including both surface and gas-phase chemistry, including models for gas-solid mass and heat.
In a first step, hydrodynamic studies were performed to validate the solver under non-reactive conditions, by comparison with experimental PIV data. The reactive framework was then used to simulate reactor geometries for the Oxidative Coupling of Methane (OCM), one of the most promising direct technologies to convert methane into ethylene. For reactive validation, our experimental packed bed set-up was simulated with an in-house microkinetic model, comprising of 39 gas phase and 26 catalytic reactions, between 24 gas phase and 11 surface species. The results of these simulations were compared to both experimental data and pseudo-homogeneous 1D PFR simulations, to which good agreements were found. As a proof-of-concept, the validated reactive CFD-DEM framework was applied to simulate a larger-scale fluidized bed reactor for OCM.