Abstract

ABSTRACT The drying characteristics of both blanched and unblanched leek slices were investigated for a temperature range of 60–80C and a constant air velocity of 2.5 m/s. They were investigated as a function of drying parameters, air temperature, slice thickness and pretreatment by hot water at 70C. The temperature of the drying air and slice thickness were observed to be significant factors affecting drying. The experimental data was fitted to four thin‐layer drying models available in the literature. Goodness of fit by these models was based on comparing the coefficient of determination (R2), reduced chi‐square (χ2) and root mean square error (RMSE) between the observed and predicted variable. The Midilli et al. model was the most adequate in describing thin‐layer drying tests. Both drying air temperature and slice thickness had pronounced influences on the values of effective moisture diffusivity (Deff). The values of Deff varied from 2.487 to 5.556 × 10−10 m2/s for blanched samples, and from 1.909 to 4.140 × 10−10 m2/s over the temperature range investigated. The values of activation energy were found to be 35.73, 18.09 and 30.16, 17.54 kJ/mol for blanched and unblanched leek samples with 1‐ and 2‐cm thickness, respectively.PRACTICAL APPLICATIONSThis study determines the blanching and slice thickness on the drying characteristics of leek slices. The parameters, namely drying time and rehydration ratio, are considered for the optimal product. In order to achieve these results, the drying of leek slices could be carried out in a convective dryer. The dried leek slices could be used in preparation of food and meat products.

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