Effects of Osmotic Dehydration on the Hot Air Drying of Apricot Halves: Drying Kinetics, Mass Transfer, and Shrinkage

This study aimed to determine the effects of osmotic dehydration on the kinetics of hot air drying of apricot halves under conditions that were similar to the industrial ones. The osmotic process was performed in a sucrose solution at 40 and 60 degrees C and concentrations of 50% and 65%. As expected increased temperatures and concentrations of the solution resulted in increased water loss, solid gain and shrinkage. The kinetics of osmotic dehydration were well described by the Peleg model. The effective diffusivity of water 5.50-7.387 x 10(-9) m(2)/s and solute 8.315 x 10(-10)-1.113 x 10(-9) m(2)/s was calculated for osmotic dehydration. Hot air drying was carried out at 40, 50, and 60 degrees C with air flow velocities of 1.0 m/s and 1.5 m/s. The drying time shortened with higher temperature and air velocity. The calculated effective diffusion of water was from 3.002 x 10(-10) m(2)/s to 1.970 x 10(-9) m(2)/s. The activation energy was sensitive to selected air temperatures, so greater air velocity resulted in greater activation energy: 46.379-51.514 kJ/mol, and with the osmotic pretreatment, it decreased to 35.216-46.469 kJ/mol. Osmotic dehydration reduced the effective diffusivity of water during the hot air drying process. It also resulted in smaller shrinkage of apricot halves in the hot air drying process.