Numerical investigation of the particle circulation characteristics in a tapered fluidized bed

Purpose The objective of this study is to investigate several issues related to particle circulation within the TFB, including exploring an appropriate method to quantify particle circulation time, the effects of different operational parameters on particle circulation time, and the relationship between particle mixing and particle circulation. Design/methodology/approach The computational fluid dynamics coupled with the discrete element method (CFD-DEM) is applied to investigate the particle circulation characteristics of a tapered fluidized bed (TFB). An approach for defining particle circulation, which accounts for the horizontal motion of each particle, is proposed to estimate particle circulation time. Findings It is found that the overall particle circulation in a TFB could be accelerated by increasing air velocity and wall inclination angle, while an increase in particle size and an increase in inter-particle cohesive forces decelerate particle circulation; the increase in the open area ratio of the central region of the air distributor would decelerate the particle circulation. Moreover, the particle circulation time and mixing rate are independent variables that describe the flow dynamics of particles from different perspectives. Practical implications A large part of fluidized beds in industrial applications can be classified as TFB. This study presents a numerical method to obtain detailed knowledge about particle circulation in a TFB, which is essential for the design, optimization, and control of related processes. Originality/value The particle circulation in a TFB is important but rarely investigated, and it is hard to be quantified using existing experimental approaches. The proposed numerical workflow reveals the characteristics of particle circulation from a particle-scale perspective.

Automated summary

The objective of this study is to investigate the particle circulation characteristics in a tapered fluidized bed (TFB). The study explores an appropriate method to quantify particle circulation time, the effects of operational parameters on particle circulation time, and the relationship between particle mixing and particle circulation. The findings suggest that air velocity, wall inclination angle, particle size, inter-particle cohesive forces, and the open area ratio of the central region of the air distributor all have significant effects on particle circulation. The study provides valuable insights for the design, optimization, and control of processes involving TFBs.