Drying kinetics of the product are the most important data required for the
design and simulation of air dryers. This essential information can be obt
ained through simple lab-scale experiments. Nevertheless, due to the uncert
ainty of the process, specially when dealing with biological materials, all
the necessary data at different operating conditions are not usually avail
able. Olt the other hand, drying kinetic models are either too simple to ex
pect reasonably good predictions, or too complicated to be applied easily.
The key assumptions of a previously developed lumped-parameter model for ai
r drying kinetics were revised to examine their application to biological m
aterials. A short cut method has been developed to simulate kinetic curves
from a minimum number of experimental data. A simple parameter study was ca
rried our to detect the most important variables that affect the mass trans
fer Blot number in order to predict kinetics data safely. Experimental (hot
air) drying curves for bananas, grapes and mushrooms were obtained in a la
b scale dryer, at different air temperatures (50 to 70C) and air velocities
(1 to 3 m/s). A comparison between experimental and predicted data was don
e for different operating conditions.