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This thesis examines the hydrodynamics of a three-phase fluidized bed using low density wood particles. Experiments were conducted to determine the bed pressure drop, minimum fluidization velocity, and bed expansion ratio for various particle sizes, static bed heights, liquid velocities, and gas velocities. Models were developed using factorial design analysis to correlate the bed expansion ratio with the operating parameters. The results show that bed pressure drop and minimum fluidization velocity decreas

Author

caterineflorez

Language

EN