Circulating Fluidised Beds (CFB) are attracting increasing interest for both gas-solid and gas-catalytic reactions, although the operating modes in these two cases are completely different. In modelling CFBs as reactors, the solids residence time is an important parameter. Previous studies mostly as
The solids flow in the CFB-riser quantified by single radioactive particle tracking
β Scribed by Shiva Mahmoudi; Jan Baeyens; Jonathan Seville
- Book ID
- 104089309
- Publisher
- Elsevier Science
- Year
- 2011
- Tongue
- English
- Weight
- 936 KB
- Volume
- 211
- Category
- Article
- ISSN
- 0032-5910
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β¦ Synopsis
Single radioactive particle tracking was used to measure the overall solids residence time (and its distribution) in the riser of a CFB, operating at superficial air velocities (U) of 1 to 9 ms -1 and solids circulation fluxes (G) between 20 to 600 kg m -2 s -1 . The results demonstrate that the particle motion and mixing differ according to the operating mode of the riser, with a fairly constant velocity throughout the riser achieved in the dilute or dense riser flow, but with a significant amount of back-mixing for intermediate values of U and/or G. This back-mixing is due to the coreannulus mode of particle flow. Whereas experimental results and theoretical predictions are in fair agreement for the dilute and dense riser flow, the core-annulus regime needs to account for a U and G dependent slip factor (Ο), in excess of the commonly proposed value Ο = 2, especially at U-U TR b 2 ms -1 . Moreover, the previously published riser operation diagram is confirmed by the experiments, although a further analysis of the core-annulus regime is needed.
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