Heat transfer to a liquid fluidized bed

Abstract

Abstract An experimental study of the rate of heat transfer from the retaining wall to a fluidized bed of solids was carried out for liquid water and glass spheres. The independent variables included mass velocity, particle size, bulk temperature, and wall temperature. Significant increases in heat transfer were observed, owing to the presence of the suspended solids, even to the extent of tripling the coefficient. For each of several particle sizes, the coefficient passed through a maximum corresponding to a particular mass velocity. The behavior of the bed at velocities below and above those for maximum coefficient was studied and categorized. Tentative correlations for both regions are offered.