A new modeling approach for the prediction of yeast drying rates in fluidized beds

The mass exchange between solid particles and air during the drying of yeast in a fluidized bed is first modeled following a standard approach, using an isotherm equation and assuming that the resistance to mass transfer is localized at the external surface of the particles. The agreement between ex...

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Veröffentlicht in:Journal of food engineering 2008, Vol.84 (2), p.335-347
Hauptverfasser: Debaste, F., Halloin, V., Bossart, L., Haut, B.
Format: Artikel
Sprache:eng
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