This paper presents an investigation of the solids flux distribution i
n a 0.161 m ID circulating fluidized-bed riser, operating in temperatu
re range 20-550 degrees C. The superficial gas velocity and the impose
d solids flux were varied from 2.5 to 5 m s(-1) and from 2 to 60 kg m(
-1) s(-1), respectively. For the operating conditions examined, the re
duced solids flux, i.e. local solids flux divided by cross-sectional m
ean solids flux, was insensitive to changes in the imposed solids flux
over a wide range at a given superficial gas velocity. As temperature
increased the mean suspension density decreased, whilst the reduced s
olids flux profile became flatter and less parabolic in shape. Local f
luctuations in solids flux were found to increase with increasing temp
erature. Analysis of results suggests that the effect of temperature o
n CFB hydrodynamics (e.g, the mean suspension density and the solids f
lux profiles) is mainly due to the change in viscosity of the fluidizi
ng gas.