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 solids fraction profiles in inlet region of high density circulating fluidized bed
โ Scribed by Guoqiang Yang; Fei Wei; Yong Jin; Zhiqing Yu
- Publisher
- John Wiley and Sons
- Year
- 1997
- Tongue
- English
- Weight
- 369 KB
- Volume
- 20
- Category
- Article
- ISSN
- 0930-7516
No coin nor oath required. For personal study only.
๐ SIMILAR VOLUMES
Electrical conductivity probes were used to measure the radial distributions of solids holdup and liquid velocity in a liquid-solid circulating fluidized bed. These distributions are found to be non-uniform, unlike those in a non-circulating bed. The effects of superficial liquid velocity and partic
## Abstract The gas/solid flow characteristics in a circulating fluidized bed with two different inlet configurations were investigated by numerical simulation based on an Eulerian approach. In order to describe the interaction between the gas phase and the solid phase and the influence of the soli