FLUIDIZATION REGIMES IN NON-SLUGGING FLUIDIZED-BEDS - THE INFLUENCE OF PRESSURE-DROP ACROSS THE AIR DISTRIBUTOR

Citation
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
Citations number
16
Categorie Soggetti
Engineering, Chemical
Journal title
ISSN journal
00325910
Volume
86
Issue
3
Year of publication
1996
Pages
299 - 312
Database
ISI
SICI code
0032-5910(1996)86:3<299:FRINF->2.0.ZU;2-4
Abstract
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.