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Abstract
Using DEM simulations, the paper examines the different types of behaviour as the gas velocity is increased to cover the complete range from fixed bed to homogeneous expansion, bubbling, turbulent and fast fluidisation. The paper highlights the transitions between the various regimes. At minimum fluidisation velocity, Umf, the structure of the bed is isostatic. When the gas velocity U is increased the system immediately breaks up into large clusters of contacting particles which gradually disintegrate with further increases in gas velocity until, at minimum bubbling velocity, Umb, the first bubbles start to appear. Conventionally, the regime Umf < U < Umb is referred to as homogeneous expansion. However, it is shown that the expansion is not homogeneous. Above Umb, the amplitude of the pressure drop fluctuations increases to a maximum when U = Uc, which marks the transition from bubbling to turbulent behaviour. The simulations also show that in the turbulent regime the average pressure drop increases with increasing gas velocity. This aspect appears not to have been reported previously in the literature. Finally, when U > Uk, corresponding to “fast fluidisation”, the particle system behaves as a granular gas. A new criterion is suggested to define the transition from turbulent fluidisation to fast fluidisation, defined by Uk.
Original language | English |
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Pages (from-to) | 128-134 |
Journal | Powder Technology |
Volume | 270 |
Early online date | 22 Oct 2014 |
DOIs | |
Publication status | Published - Jan 2015 |
Keywords
- Granular materials
- Fluidisation
- Discrete element method
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Dive into the research topics of 'A DEM investigation of transitional behaviour in gas-fluidised beds'. Together they form a unique fingerprint.Projects
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A numerical and experimental re-examination of fluidised beds of cohesive particles.
Seville, J. (Principal Investigator) & Thornton, C. (Co-Investigator)
Engineering & Physical Science Research Council
1/08/04 → 31/03/08
Project: Research Councils