A. Svensson et al., FLUIDIZATION REGIMES IN NON-SLUGGING FLUIDIZED-BEDS - THE INFLUENCE OF PRESSURE-DROP ACROSS THE AIR DISTRIBUTOR, Powder technology, 86(3), 1996, pp. 299-312
The purpose of the present work is to study the influence of the press
ure drop across the air distributor on the bubbling conditions of the
bottom bed of circulating fluidized beds (CFB). The bottom bed is the
dense bubbling zone just above the distributor. The experimental work
was carried out in a 12 MW(th) CFB boiler and in a cold CFB. Three dif
ferent distributions of the bubble flow in time and space, termed flui
dization regimes, were identified in the cold CFB: the multiple bubble
regime with many small bubbles evenly distributed in the bed; the sin
gle bubble regime, characterized by the presence of only one bubble at
a time in the bed; and the exploding bubble regime with large, single
, irregular voids stretching from the air distributor to the bed surfa
ce. These bubbling conditions were observed during variations in the g
as velocity and the distributor pressure drop. A comparison with the 2
m(2) cross-section CFB boiler showed that the boiler always operates
in the single or in the exploding bubble regime, which indicates a bub
ble flow that is not continuous and not well distributed over the cros
s-section of the bed. The conditions in the boiler are influenced by t
he relatively large area of gas passage and the low pressure drop of t
he boiler air distributor.