05 and 0.10 g 100 g−1) which were used in the formulations of coatings for minimally processed strawberries. Good integrity of cassava

edible coatings on the strawberry surface was observed for 2 and 3 g 100 g−1 starch concentrations, and the use of coatings at these concentrations reduced the strawberry respiration rate, representing a possibility for extending the shelf life of fruits. Vicentini, de Castro, and Cereda (1999) used cassava starch Panobinostat concentration films on green pepper fruits and observed that the film at the concentration of 3 g 100 g−1 led to reduction in weight loss of 1.03 g 100 g−1, maintained the texture of the fruits and did not alter the chemical properties of the product. Most of these studies showed interest in the mechanical properties of the dried product. It is very clear that a successful

gel-based sponge should exhibit appropriate mechanical strength along with appropriate chemical compatibility, sorption capacity, and biodegradability for its intended use (Jaya & Durance, 2007). Structure and surface properties of an edible protein film combined with canola oil, dried at 80 °C for 30 min, explained the adsorption of water as a function of moisture content and, consequently, TGF-beta inhibitor the permeable behavior of water vapor (Kokoszka, Debeaufort, Lenart, & Voilley, 2010). This confirms the importance of determining the drying curves for filmogenic solutions. Parameters involved in drying of filmogenic solutions should be considered in the preparation of biodegradable films. In general, variations in moisture contribute to the variation in thickness of the films and also influence mechanical properties due to the plasticizer effect of water (Torres, 1994). In the development and improvement of drying equipment, the acquisition of simulations and theoretical information on the behavior of each product is essential for reducing processing tuclazepam costs (Corrêa, Resende, Martinazzo, Goneli, & Botelhos, 2007). Drying curves of the dispersed polymer have been studied, and upon observing two distinct drying periods, two equations for mathematical modeling were developed: the first to demonstrate moisture varying in a linear manner until reaching

critical moisture, and the second for the drying rate, which decreases exponentially (Stupa, Platonov, & Milkhailov, 2003). However, information on the kinetics of drying biodegradable films, which is fundamental for the optimization of this operation, is not encountered in the literature. This information would result in decreased costs and preparation of final products of better quality. The objective of this study was thus to obtain drying curves for filmogenic solutions, and to adjust mathematical models to both constant and falling rate periods. Furthermore, the influence of yam starch and glycerol levels was analyzed, as well as the temperature effect, to verify which conditions would lead to lowest production cost. Starch was extracted from yams (Dioscorea spp.