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Study of dynamic multi-dimensional temperature and concentration distributions in liquid-sprayed fluidized beds
Publikationstyp
Journal Article
Date Issued
2003-12
Sprache
English
Journal
Volume
58
Issue
23-24
Start Page
5135
End Page
5160
Citation
Chemical Engineering Science 58 (23-24): 5135-5160 (2003-12)
Publisher DOI
Scopus ID
A physically based model was developed for heat and mass transfer processes in liquid-sprayed fluidized beds. Such fluidized beds are used for granulation, coating and agglomeration. The complex correlations of a number of microprocesses, spraying, wetting, drop deposition, heat transfer, drying and mass transfer were studied, and transient three-dimensional distributions of air humidity, air temperature, particle wetting efficiency, liquid film temperature, particle temperature, local liquid loading and local evaporation rate were calculated. For the evaluation of the model, the stationary spatial air temperature distributions were measured at a fluidized bed pilot plant of the institute. The fluidized bed of monodisperse wood- or glass beads was sprayed with clear water. Conclusions are drawn on the relevance of particle dispersion, spraying and drying to simulating temperature and concentrations distributions.
Subjects
Drying
Dynamic simulation
Evaporation
Fluidization
Fluidized bed
Heat transfer
Mass transfer