A new computational single-droplet drying model is presented. The model considers heat and mass transfer simultaneously together with the receding evaporation front approach. A spherical droplet under constant drying conditions is considered. Computations are performed to predict the drying of colloidal silica-water suspension and skimmed milk. It is shown that the results agree well with those of experimental observations available in the literature.
INTRODUCTIONSpray drying has found applications in many fields such as chemical, agricultural, food, polymer, pharmaceutical, ceramics, and mineral processing industries due to its flexibility in meeting product requirements as well as its high energy efficiency compared to other drying methods. In a typical spray-drying operation, atomization of the feed into small droplets generates large surface area for both heat and mass transfer.Experiments [1][2][3] on drying of droplets containing suspended or dissolved solids have provided qualitative description of drying of droplets. Drying first occurs at a constant rate, followed by a falling rate similar to what is usually observed in other drying operations. In the constant rate period, after an initial adjustment, droplet temperature reaches air wet-bulb temperature. In the falling rate period, however, an additional resistance to both heat and mass transfer arises due to formation of a porous solid layer. Temperature gradients within the droplet become higher compared to constant rate period since surface temperature of the droplet continuously increases from wetbulb temperature to dry-bulb temperature of air as drying proceeds. Obtaining important drying quantities such as drying rate, temperature, and moisture distributions is