Ih. Farag et Ky. Tsai, SURFACE-TO-SUSPENSION HEAT-TRANSFER MODEL IN LEAN GAS-SOLID FREEBOARDFLOW, Canadian journal of chemical engineering, 71(4), 1993, pp. 514-524
Heat transfer in dense fluidized beds have been extensively studied. H
owever, there is not much detailed information about the mechanism of
surface-to-suspension heat transfer in the freeboard region. In the pr
esent work, a newly designed heating plate was used to measure the pla
te-surface-to-particle-suspension heat transfer coefficients in the fr
eeboard. The experimental unit consisted of a 30 cm i.d. fluidized bed
reactor packed with fluidized catalytic particles of mean particle si
ze 90 mum. Three types of plate orientations were used to test directi
onal effects of surface on heat transfer rate. Height of the freeboard
was 171 cm, and the superficial gas velocity was varied from 0.28 to
0.64 m/s. Local solids concentrations in the freeboard were also obtai
ned by a nozzle-type sampling probe. Data on axial distribution of sol
ids concentration were used to find out the solids kinematics in the f
reeboard region. Finally, a surface-to-suspension heat transfer model
was developed to elucidate the surface to particle heat transfer mecha
nism in this lean phase system. The model is based on the transient ga
s-convective heating of single particles when sliding over the heating
plate and the assumption of instantaneous attachment-detachment equil
ibrium between particles and the plate surface.