A fixed or moving boundary problem was considered for the drying of gr
een peas. The first model was solved by separation of variables, assum
ing that sample size and geometry remain constant during the process.
For the second model, a finite difference method was used. Using exper
imental data from experiments carried out at different air-drying temp
eratures (40, 60 and 80 degrees C), two different expressions, of Arrh
enius type, for the effective diffusivity dependence on the air temper
ature were obtained. Throughout these expressions, it was possible to
simulate the drying kinetics of green peas at temperatures (50, 70 and
90 degrees C) different from those used to obtain the models. The sec
ond model was found to be more precise (percentage of explained varian
ce >99.8%) than the first one (>98.4%).