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| Title: | Prediction of the Fluctuation Ratio for Gas Solid Fluidization of Regular Particles in a Conical Vessel |
| Authors: | Biswal, K C
Sahu, S
Roy, G K |
| Issue Date: | 1982 |
| Citation: | The Chemical Engineering Journal, 23 (1982) 97 -100 |
| Abstract: | Fluidization as an established fluid-solid
contacting technique has found extensive
applications in carbonization, gasification,
combustion and many other process industries in the last four decades. In spite of the many advantages claimed for the fluidization
phenomenon, the efficiency and quality
of large-scale and deep gas-solid continuous
fluidized beds are seriously affected by
bubbling and slugging behaviour, when gas
velocities are higher than the minimum
fluidization velocity. |
| URI: | http://hdl.handle.net/2080/946 |
| Appears in Collections: | Journal Articles
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| gkroy41.pdf | | 76Kb | Adobe PDF | View/Open |
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