1987
DOI: 10.1002/aic.690331113
|View full text |Cite
|
Sign up to set email alerts
|

A generalized bubble diameter correlation for gas‐solid fluidized beds

Abstract: A new bubble diameter correlation is derived to predict bubbling characteristics of fluidized beds of varieties of powders. The present model is founded on the postulate that the steady bubble size, which is often called the maximum stable diameter, observed in a bed of Geldart group A powder is formed as a result of an equilibrium of successive coalescence and splitting. For the cases of group B powders the present correlation automatically converges to the conventional correlation of Mori and Wen (1975), who… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

10
70
2

Year Published

2006
2006
2020
2020

Publication Types

Select...
5
3

Relationship

0
8

Authors

Journals

citations
Cited by 169 publications
(83 citation statements)
references
References 23 publications
10
70
2
Order By: Relevance
“…7 Thus, even though the Harrison et al criterion can be useful for an estimation of the fluidization homogeneity, the collective interaction between bubbles through splitting-coalescence mechanism can ultimately lead to equilibrium bubble sizes larger than Harrison's maximum stable size as seen in experiments. 12 Note, however, that the Harrison criterion conforms to the Wilhelm & Kwauk empirical criterion (Eq. 1) if the Froude number is defined based on the terminal settling velocity of an individual particle (Fr 0 5 v 2 p0 /(gd p )).…”
Section: Introductionmentioning
confidence: 78%
“…7 Thus, even though the Harrison et al criterion can be useful for an estimation of the fluidization homogeneity, the collective interaction between bubbles through splitting-coalescence mechanism can ultimately lead to equilibrium bubble sizes larger than Harrison's maximum stable size as seen in experiments. 12 Note, however, that the Harrison criterion conforms to the Wilhelm & Kwauk empirical criterion (Eq. 1) if the Froude number is defined based on the terminal settling velocity of an individual particle (Fr 0 5 v 2 p0 /(gd p )).…”
Section: Introductionmentioning
confidence: 78%
“…For group A particles, where both bubble coalescence and splitting are important, Horio and Nonaka's correlation 26 is more appropriate and is thus chosen in the present work for the estimation of bubble size.…”
Section: Fluid-dynamic Modelmentioning
confidence: 99%
“…According to Horio and Nonaka, 26 the initial bubble diameter for a porous plate must be calculated by using the equation given in Table 1, but results obtained by this equation for the experimental conditions used in this work forecast an initial bubble diameter that is too small (Ͻ0.05 mm). Since the initial bubble diameter must be at least as large as the particle diameter (0.2 mm), the initial bubble diameter was varied between 0.2 and 2 mm, the best results being obtained for a value of 0.5 mm.…”
Section: Fluid-dynamic Modelmentioning
confidence: 99%
“…These low voidages support to rise the bubbles faster than the inlet superficial velocity. Increase or decrease of bubble diameter depends on the balance of coalescence and splitting frequencies (Horio M & Nonaka A, 1987). Group-B particle showed higher mixing than Group-A particles due to the more bubbles in the bed.…”
Section: Pressure Gradientmentioning
confidence: 99%