This work aims to test the application of computational fluid dynamics (CFD) modeling to fixed
bed equipment design. Studies of CFD with a fixed bed design commonly use a regular packing
approach to define bed geometry. However, assuming nonregular packing is a more realistic
way to simulate the behavior of a fixed bed and therefore to estimate important design
parameters. As a fluid flow simulation tool, CFD allows us to obtain a more accurate view of
the fluid flow and heat transfer mechanisms present in fixed bed equipment. Forty-four spheres
stacked in a nonregular maximum-space-occupying arrangement in a cylindrical container were
used as the geometrical model. Estimates of the pressure drop along the bed, and wall heat
transfer parameters were chosen as validation parameters. ΔP, Nu
w, and k
r/k
f are given for
different values of Re (transition and turbulent flow), and they are compared to commonly used
correlations. Air was chosen as the flowing fluid. Cases of laminar and turbulent flows are
presented, and their results are compared. To account for the fluid flow and thermally fluctuating
components in the turbulent cases, one- and two-equation turbulence models were used for
simulation.