An investigation of the hydrodynamic similarity of single-spout fluidized beds using CFD-DEM simulations

- Glicksman's law was applied in the CFD-DEM simulation of a spout fluidized bed.
- A good agreement was observed between the base and scaled case simulation results.
- In some cases, applying the scaling law lead to a shorter computational time.
- Glicksman's scaling laws can be considered as a way of scaling spout fluidized beds.

The applicability of the hydrodynamic similarity criteria (scaling law) introduced by Glicksman (1988) was investigated using fully coupled Computational Fluid Dynamics and Discrete Element Method (CFD-DEM) simulations for single-spout fluidized beds. Four test cases were performed to investigate the scaling law in a pseudo-2D spouted-fluidized bed. In addition, the applicability of Glicksman's scaling law for simulating 3D fluidized beds was studied. In all simulations, characteristic dimensionless groups, i.e. the Reynolds number (Re), Froude number (Fr), particle-to-fluid density, bed initial height to particle diameter and bed width to particle diameter were kept constant for the both base and scaled cases. Comparing the time averaged particle velocities, gas velocities and volume fractions between the base and scaled cases indicated a very good overall hydrodynamic similarity for all test cases. A minor discrepancy observed between the simulation results of the base and scaled cases was explained by a force analysis.An advantage of the scaling approach, i.e., reducing computational time, was also presented in the last four test cases, including a large-scale simulation, showing that this approach can be considered as a promising way to simulate large-scale spouted-fluidized beds.

Instantaneous particle positions and time-averaged particle volume fraction contours.89