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The 12th International Conference on Fluidization - New Horizons in Fluidization Engineering
May 13-17, 2007 - Vancouver, Canada
| Editors: |
Franco Berruti, The University of Western Ontario, London, Canada
Xiaotao (Tony) Bi, The University of British Columbia, Vancouver, Canada
Todd Pugsley, University of Saskatchewan, Saskatoon, Saskatchewan, Canada |
The articles for these proceedings are peer-reviewed.
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Bubble Distribution in Cylindrical Fluidized Beds: The Effects of Bed Depth and Gas Speed
Anthony Croxford, University of Bristol
Mark A. Gilbertson, University of Bristol
ABSTRACT:
The dynamic behaviour of a bubbling fluidised bed markedly changes when the bed is run close to Umf or when it is shallow. It is shown that these changes can be explained using the kinematic models of Clift and Grace (1,2) and Davidson (3) (the model implementation is described in detail by Croxford (11)). The use of this model and tomographic measurements allows the conclusions to be made for three-dimensional fluidised beds, which can be difficult to observe directly.
Anthony Croxford and Mark A. Gilbertson, "Bubble Distribution in Cylindrical Fluidized Beds: The Effects of Bed Depth and Gas Speed" in "The 12th International Conference on Fluidization - New Horizons in Fluidization Engineering", Franco Berruti, The University of Western Ontario, London, Canada
Xiaotao (Tony) Bi, The University of British Columbia, Vancouver, Canada
Todd Pugsley, University of Saskatchewan, Saskatoon, Saskatchewan, Canada Eds, ECI
Symposium Series, Volume RP4 (2007). http://services.bepress.com/eci/fluidization_xii/25
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