Results of detailed experimental measurements of solids mass flux profiles in circulating tfuidized-bed risers of internal diameter 0.152 and 0.305 m are described. The ranges of superficial gas velocity and mean solids mass flux used were 3-5 m s-1 and 2-111 kg m ' s I, respectively, and the solids
Radial profiles of solids loading and flux in a gas–solid circulating fluidized bed
✍ Scribed by P.R. Tortora; S.L. Ceccio; A.G. Mychkovsky; T.J. O'Hern; J.R. Torczynski
- Publisher
- Elsevier Science
- Year
- 2008
- Tongue
- English
- Weight
- 676 KB
- Volume
- 180
- Category
- Article
- ISSN
- 0032-5910
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✦ Synopsis
An electrical-impedance tomography (EIT) system has been developed to non-invasively measure radial voidage profiles in the riser of a pilotscale circulating fluidized bed (CFB), yielding quantitative information that is validated by comparison to a gamma-densitometry tomography (GDT) system. EIT and GDT were applied to the CFB riser (14-cm inner diameter, 5.77-m height) containing fluid catalytic cracking particles in air. For all cases, the average and near-wall voidages from EIT and GDT agreed to within 0.03 and 0.07, respectively. This good agreement suggests that, where feasible, EIT can be used in place of GDT, which is advantageous since EIT systems are often safer, less expensive, and faster than GDT systems. The results also compared well to two correlations for radial voidage profile from the literature. Finally, a procedure for determining radial solids flux profiles from radial voidage profiles using an additional correlation [M.J. Rhodes, X.S. Wang, H. Cheng, T. Hirama, B.M. Gibbs, Similar profiles of solids flux in circulating fluidized-bed risers, Chemical Engineering Science 47 (1992) 1635-1643] was investigated. It was found that the accuracy of this correlation strongly depends on the voidage and/or solids flux measurement at the riser center.
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