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 |
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Format: | Artikel |
Sprache: | eng |
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