The effect of ring baffles on the hydrodynamics of a gas-solid bubbling fluidized bed using computational fluid dynamics

An Eulerian-Eulerian two-fluid model (TFM) integrating the kinetic theory for emulsion phase was used to simulate gas-solid fluidized beds. Validation of the model was investigated based on hydrodynamic parameters such as bed expansion ratio, H/H-0, gas volume fraction profile, bubble behaviour, and motion of the particles. A good agreement was found between numerical results and experimental values. The model was used to study a bubbling fluidized bed (BFB) including the ring baffles. Predicted results show that the ring baffles have an important role in the flow pattern of the bed. Baffles increase the bed expansion height and particle velocities at axial locations on the top of the highest baffle as well as uniform distribution of gas volume fraction between the baffles area. In spite of increasing the dead zones in the bed, ring baffles cause the improvement of mixing and heat transfer in the bed. The present study provides a useful basis for further works on the effect of baffles in BFBs.