An Improved Model Describing Mass Transfer In Three-Phase Fluidized Beds

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An Improved Model Describing Mass Transfer In Three-Phase Fluidized Beds

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dc.contributor.author Asfour, Abdel Fattah A. en_US
dc.date.accessioned 2009-11-25T13:03:12Z
dc.date.available 2009-11-25T13:03:12Z
dc.date.issued 1990 en_US
dc.identifier.citation Engineering Journal of Qatar University, 1990, Vol. 3, Pages 213-233. en_US
dc.identifier.uri http://hdl.handle.net/10576/7824
dc.description.abstract A model for describing mass transfer in three-phase fluidized beds has been developed and tested using experimental data. The presence of two distinguishable mass transfer zones in three-phase fluidized beds led to the idea of interfacing a plug flow model (PFM) with an axial dispersion model (ADM) at the separation boundary between these zones to yield the proposed model. The model reported here has been valildated at a wide range of operating conditions and proved to perform better than other existing models. en_US
dc.language.iso en en_US
dc.publisher Qatar University en_US
dc.subject Engineering: Chemical Engineering en_US
dc.title An Improved Model Describing Mass Transfer In Three-Phase Fluidized Beds en_US
dc.type Article en_US
dc.identifier.pagination 213-233 en_US
dc.identifier.volume 3 en_US

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