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Fluidization of Ultrafine Particles in a Bubbling Fluidized Bed with Sound Assistance

โœ Scribed by Q. Guo; M. Wang; Y. Li; C. Yang


Publisher
John Wiley and Sons
Year
2005
Tongue
English
Weight
234 KB
Volume
28
Category
Article
ISSN
0930-7516

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โœฆ Synopsis


However, the bubbling up vapor flows just through the downcomer bottom-orifices. The vapor occupies the part the of orifice area, so the orifice area for liquid descending is reduced and the downcomer liquid height increases which causes a premature downcomer flood as well. Moreover, the orifice area for liquid descending will be reduced further because bridging occurs, accompanied by vapor bubbling, with the area ratio of bridging being 0.4ยฑ1.8 of the area ratio of vapor bubbling. Therefore, the bubbling vapor rate and also the ratio of bridging are restricted for the sealed hangingdowncomer.

5 Conclusions

There are three states of (liquid descending, bridging, and vapor bubbling) at hanging downcomer bottom-orifices. Momentary variations in P i cause the occurrence of the three states. The three states are affected by superficial F-factor and liquid rate. The time and area ratios of bridging and vapor bubbling increase with increasing F-factor, and decrease with increasing liquid rate. Bridging really exists and is not negligible. The ratio of bridging is 0.4ยฑ1.8 of the ratio of vapor bubbling. Moreover, due to bridging, the bubbling vapor rate and also the ratio of bridging is restricted for the sealed hanging-downcomer.


๐Ÿ“œ SIMILAR VOLUMES


Estimation of bed expansions in a freely
โœ A. Hepbasli ๐Ÿ“‚ Article ๐Ÿ“… 1998 ๐Ÿ› John Wiley and Sons ๐ŸŒ English โš– 178 KB ๐Ÿ‘ 2 views

Knowledge of bed expansions is important in the design and operation of gas-solid fluidized beds. This paper presents a study on the estimation of expanded bed height in a large three-dimensional gas-fluidized bed with a square section of 0)61;0)61 m. All experiments were performed at the freely bub