Bed-to-wall heat transfer in a pressurized circulating fluidized bed i
s analyzed. The cluster renewal model is modified to account for the e
ffect of pressure on heat transfer. Bed-to-wall heat transfer coeffici
ents at different operating pressures were measured. The effects of sy
stem pressure, bed suspension density, particle size and superficial g
as velocity were investigated in the tests. In addition to the modifie
d model, a semi-empirical equation based on the lest data is proposed
for the prediction of heat transfer coefficients. A comparison with ex
perimental data in the literature, as well as those from the present w
ork, shows a good agreement. Copyright (C) 1996 Elsevier Science Ltd.