“…The bed parameters, mentioned above, strongly influence single-phase and multiphase flow aspects, degree of pressure loss along the height of the bed, axial and radial dispersion qualities in common with interparticle and interparticle heat, and mass transfer properties. ,− For example, the pressure drop of a fluid passing through the packing is highly dependent on the size of the interparticle voids . Therefore, different researchers have studied the hydrodynamics, packing structure, and the filling of this type of the reactor modeling fixed-beds using Computational Fluid Dynamics (CFD) simulations based on the discrete element method (DEM) and Finite–Discrete Element Method (FDEM), ,− with subsequent flow, heat, and/or mass transfer simulation by known tools such as COMSOL Multiphysics, Ansys Fluent, STAR-CCM+,CFD-ACE+, or OpenFOAM, the latter being open source, allowing users the freedom to modify and extend its functionality. , If the reader wishes to dive deeper in this interesting topic, we recommend reading the interesting review by Hettel et al who discuss CFD analysis of catalytic reactors. In addition, the analysis made from such calculations that can be coupled to the multiscale modeling of the catalytic reactor .…”