Cm. Qi et Ih. Farag, RADIAL PARTICLE-FLUX AND MOMENTUM-TRANSFER IN THE CIRCULATING FLUIDIZED-BED, Chemical engineering communications, 124, 1993, pp. 15-27
The solid particle concentration distribution in the riser of a Circul
ating Fluidized Bed (CFB) is dilute at the center and dense near the w
all because of the axial particle momentum exchange. In our study, the
radial particle concentration distribution was investigated theoretic
ally and experimentally. To assess the radial particle motion, a speci
al flux probe was designed. We found that near the wall, the radial pa
rticle flux was much higher then the net axial particle flux, and that
the measured radial profile of particle flux was similar to that of t
he particle concentration. The resulting radial flux is very valuable
in developing a model of heat transfer between the gas-particle suspen
sions and the wall surface.