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GAS-SOLID FLOW BEHAVIOR IN A PRESSURIZED HIGH-FLUX CIRCULATING FLUIDIZED BED RISER

✍ Scribed by Yin, Shangyi; Jin, Baosheng; Zhong, Wenqi; Lu, Yong; Shao, Yingjuan; Liu, Hao


Book ID
126840853
Publisher
Taylor and Francis Group
Year
2013
Tongue
English
Weight
828 KB
Volume
201
Category
Article
ISSN
0098-6445

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πŸ“œ SIMILAR VOLUMES


Gas-solids flow in the riser of a circul
✍ Yinghe He; Victor Rudolph πŸ“‚ Article πŸ“… 1995 πŸ› Elsevier Science 🌐 English βš– 773 KB

Abstraet--A new approach to the modelling of gross gas-solids flow through the riser in a circulating fluidized-bed system is proposed in this paper. This approach differs from the previous ones, which are found to be theoretically incorrect based on a fundamental analysis of the riser process hydro

Modelling and simulation of a gas–solids
✍ J.C.S.C. Bastos; L.M. Rosa; M. Mori; F. Marini; W.P. Martignoni πŸ“‚ Article πŸ“… 2008 πŸ› Elsevier Science 🌐 English βš– 399 KB

Radial solids velocity profiles were computed on seven axial levels in the riser of a high-flux circulating fluidized bed (HFCFB) using a twophase 3-D computational fluid dynamics model. The computed solids velocities were compared with experimental data on a riser with an internal diameter of 76 mm

Similar profiles of solid flux in circul
✍ M.J. Rhodes; X.S. Wang; H. Cheng; T. Hirama; B.M. Gibbs πŸ“‚ Article πŸ“… 1992 πŸ› Elsevier Science 🌐 English βš– 773 KB

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