SCALE-UP EFFECT ON HEAT TRANSFER IN FLUIDIZED BEDS NEAR THE ONSET OF TURBULENT FLUIDIZATION

摘要

Heat transfer coefficients were measured in 0.29 m ID and 1.56 m ID fluidization columns with the same heater tube, identical alumina particles and geometrically scaled distributors. The maximum coefficients occurred in the turbulent fluidization flow regime. The Froude number based on superficial velocity and column diameter captures the scale-up effect well, so long as the heater is located in a region of similar flow structure.