Heat transfer from an immersed vertical tube to a gas fluidized bed

Fluidization and heat transfer experiments have been conducted in gas fluidized beds of two different sizes, viz., 305 × 305 mm² and 305 × 152.5 mm² and with particles of silica sands ($\text{d}\text{?}{}_{\mathrm{p}}\text{= 167, 488, 504, and 745 μ}\text{m}$), glass beads (d_p = 427 μm) and millet seeds (d_p = 2064 μm) with immersed smooth vertical heated tubes of diameter 12.7, 28.6, and 50.8 mm. Important conclusions are drawn concerning the dependence of heat transfer coefficient on fluidization velocity, bed particle diameter, tube diameter and nature of bed fluidization. The heat transfer data are employed to assess the available literature correlations for heat transfer coefficient and for its maximum value.