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Particle-fluid heat transfer and dispersion in fluidised beds

✍ Scribed by D.J. Gunn; P.V. Narayanan


Publisher
Elsevier Science
Year
1981
Tongue
English
Weight
724 KB
Volume
36
Category
Article
ISSN
0009-2509

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✦ Synopsis


The dynamic response of a gas fluidised bed has been measured for a range of particle sizes of lead glass ballotini and a range of particle Reynolds numbers. A dispersion model has been formulated that includes the effects of gas and particle mixing,fluid-to-particle heat transfer and intraparticle thermalconductivity,and the dynamic thermal response in theory has been found by solving the partial differential equations in the Laplace transform domain. The coefficient of thermal dispersion, the particle-to-fluid heat transfer coefficient and the intraparticle thermal conductivity have been found for the experimental response by non-linear regression. The coefficient of axial dispersion wasfoundtobelargeand theparticle tofluidheattransfercoefficientsagreedwithanestablished correlationforfixedand fluidisedbeds.Theintraparticlethermalconductivityagreed withliteraturevaluesforleadglass,theestimatesshowedno trend with flowrate, and the standard deviation of the estimate was three times smaller than the deviation found from similar experiments in fixed beds.


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