F. Sharifian - Department of Mechanical engineering of biosystems, Faculty of Agriculture, Urmia University, Urmia, Iran.
A. Mohammad Nikbakht - Department of Mechanical engineering of biosystems, Faculty of Agriculture, Urmia University, Urmia, Iran.
A. Arefi - Department of Mechanical engineering of biosystems, Faculty of Agriculture, Urmia University, Urmia, Iran.
A. Modarres Motlagh - Department of Mechanical engineering of biosystems, Faculty of Agriculture, Urmia University, Urmia, Iran.

Energy and mass transfer investigations in thermal processing of fruits serve as a breakthrough in the design and scale up of drying systems. Diffusivity characteristics and specific energy consumption for drying of fig fruit in a laboratory scale microwave dryer were assessed. Several intervals for microwave power intensity including ۰.۵, ۱, ۱.۵, ۲, and ۲.۵ W g-۱, and ۶ levels of power on-off stated as pulsing ratios of ۱.۵, ۲, ۲.۵, ۳, ۳.۵, and ۴ were employed. The results showed that the drying rate decreased with the pulsing ratio and increased with microwave power intensity. Effective moisture diffusivity as an indicator of mass transfer was obtained to be higher at elevated microwave power intensities. Also, increased pulsing ratios had a reducing effect on moisture diffusivity. Using ۲nd law of Fick, moisture diffusivity was calculated to be varying from ۵.۹۳E-۱۰ to ۱.۴۲E-۰۸ m۲ s-۱ depending on the experimental conditions. Furthermore, the activation energy of fig fruit was obtained to be in the range of ۶۰.۰۹۴ to ۹۲.۱۸۹ kJ mol-۱. Specific energy consumption variations showed a positive correlation with pulsing ratio and drying time. However, due to the dependence of energy consumption on MW power intensity, a multiple regression analysis with R۲ of ۰.۹۶۸ was developed.

Activation Energy, Diffusivity, Pulsed drying, Specific energy consumption