Droplet evaporation in fluidized beds is of great interest in applications like fluidized catalytic cracking units. Although a significant number of analyses are available for modelling of droplet vaporization in a fluidized bed, very little work has been performed experimentally to measure the vapour concentration followed by numerical validation. In the present work, acetone droplet evaporation in a bubbling fluidized bed is studied experimentally as well as numerically. A liquid jet of acetone is injected into a hot bubbling fluidized bed kept well above saturation temperature of acetone. Non-intrusive Schlieren imaging, based on the difference in refractive index, is used to trace the acetone vapour concentration profile. The bubbling fluidized bed is modelled in an Eulerian framework using a simplistic porous media approach while the droplets are modelled in a Lagrangian framework. Intense interactions are observed between the evaporating droplets and hot particles during contact with re-suspension of particles. Experimental measurement and CFD results and measured vapour concentration are compared and found to be in qualitative agreement.
History
Source title
Proceedings of the Ninth International Conference on CFD in the Minerals and Process Industries
Name of conference
9th International Conference on Computational Fluid Dynamics in the Minerals and Process Industries (CFD2012)