Expansion of gas fluidized beds

Industrial and Engineering Chemistry Research

Volumn 43, Issue 18, 2004, Pages 5802-5809

  Geldart, Derek ^a,b  

^a UNIVERSITY OF BRADFORD   (United Kingdom)

^b NONE   (United Kingdom)

Author keywords

[No Author keywords available]

Indexed keywords

ALUMINA; FLUIDIZATION; FLUIDIZED BED COMBUSTORS; GASES; HEAT TRANSFER; HYDRODYNAMICS; REFUSE INCINERATORS;

BUBBLE VELOCITY; CRACKING CATALYSTS;

FLUIDIZED BEDS;

ALUMINUM HYDROXIDE;

DESIGN; FLUIDIZED BED; GAS FLOW; VELOCITY;

ARTICLE; CALCULATION; CATALYSIS; CATALYST; DENSITY; FLUIDIZED BED; GAS; GAS FLOW; HEAT TRANSFER; HIGH TEMPERATURE; HYDRODYNAMICS; MATHEMATICAL ANALYSIS; MEASUREMENT; PREDICTION; PRESSURE; TURBULENT FLOW; VELOCITY;

EID: 4344569077     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie040180b     Document Type: Article

References (14)

1. Geldart, D. Predicting the expansion of gas fluidized beds. In Fluidization Technology; Keairns, D. L., Ed.; McGraw-Hill: New York, 1975; Vol. 1, p 237.
2. Baeyens, J.; Geldart, D. Solids Mixing. In Gas Fluidization Technology; Geldart, D., Ed.; John Wiley & Sons: Chichester, U.K., 1986; Chapter 3, p 105.
3. Werther, J. Hydrodynamics and mass transfer between the bubble and emulsion phases in gas fluidized beds of sand and cracking catalyst. In Fluidization IV; Kunii, D., Toei, R., Eds.; Engineering Foundation: New York, 1983; p 93.
4. Darton, R. C.; LaNauze, R. D.; Davidson, J. F.; Harrison, D. Bubble growth due to coalescence in fluidized beds. Trans. Inst. Chem. Eng. (London) 1977, 55, 274.
5. Xavier, A. M.; Lewis, D. A.; Davidson, J. F. The expansion of bubbling fluidized beds. Trans. Inst. Chem. Eng. (London) 1978, 56, 274.
6. Cranfield, R. R.; Geldart, D. Large particle fluidization. Chem. Eng. Sci. 1974, 29, 935.
7. Canada, G. S.; McLaughlin, M. H.; Staub, F. W. Flow regimes and void fraction distribution in gas fluidization of large particles in beds without tube banks. In Fluidization: Application to Coal Conversion Processes; Wen, C. Y., Ed.; AIChE Symposium Series 176; AIChE: New York, 1978; Vol. 74, p 14.
8. Matsen, J. M.; Hovmand, S.; Davidson, J. F. Expansion of Fluidized Beds in Slug Flow. Chem. Eng. Sci. 1969, 24, 1743.
9. Baker, C. G. J.; Geldart, D. An investigation into the slugging characteristics of large particles. Powder Technol. 1978, 19, 177.
10. Abrahamsen, A. R.; Geldart, D. Behaviour of gas fluidized beds of fine powders Part 1 homogeneous expansion. Powder Technol. 1980, 26, 35.
11. King, D. F. Estimation of dense phase voidage in fast and slow fluidized beds of FCC catalyst. In Fluidization VI; Grace, J. R., Shemilt, L. W., Bergougnou, M. A., Eds.; Engineering Foundation: New York, 1989; p 1.
12. Geldart, D. The Behaviour of freely bubbling fluidized beds. PhD. Dissertation, University of Bradford, Bradford, U.K., 1971.
13. Xue, Y. Flow regimes, Bed expansion and entrainment in fluidized beds of fine particles. In Coarse and fine powder fluidization; Electric Power Research Institute Project 8006-16, Final Report TR102428; Geldart, D., Avontuur, P. P. C., Xue, Y., Eds.; University of Bradford: Bradford, U.K., Dec 1993; Section 2.
14. Ellis, N.; Bi, H. T.; Lim, C. J.; Grace, J. R. Hydrodynamics of turbulent fluidized beds of different diameters. Powder Technol. 2004, 141, 124.