before the production of high value-added products [5]. Also, the by-products do not only cause disposal costs, but also are a major environmental problem. Drying has always been of great importance to the preservation of agricultural products and their by-products.Drying is the most widely used commercial process to preserve foods because, compared to other long-term preservation methods, it is less costly and easier to operate. The main purpose of drying products is to allow longer periods of storage, minimize packaging requirements, and reduce shipping weights [6]. There are many drying methods, of which sun drying is the most traditional and economical one. However, sun drying has some significant disadvantages, such as the fact that it is time-consuming, weatherdependent, results in nutrient loss, is labor-intensive, and may result in possible environmental contamination [7]. In order to improve the quality of products, the sun drying technique should be replaced with industrial drying methods such as hot air drying [8,9].The most relevant aspects of drying technology are the mathematical modeling of the process and the experimental setup. The modeling is basically based on the design of a set of equations to describe the system as accurately as possible. Drying characteristics of the particular products being dried and mathematical models are needed in the design, construction and operation of drying systems [10]. Many mathematical models have proposed to describe the drying process, of them, thin-layer drying models have been widely in use. These models can be categorized as theoretical, semi-theoretical, and empirical [11]. Several mathematical modelling and experimental studies have been revealed concerning the drying characteristics of fruit and vegetable pomaces, such as grape pomace [12], tomato pomace [10,13], carrot pomace [14], and olive pomace [15,16]. So far, there a little information available about Abstract Drying of apple pomace representing byproducts from apple juice processing was studied. The results obtained show that moisture content of the pomace decreases with time and temperature. The Midilli et al. model was selected as the best mathematical model for describing the drying kinetics of the apple pomace. The effective moisture diffusivity varied from 1.73 × 10 −10 to 4.40 × 10 −10 m 2 /s and the activation energy was calculated to be 29.65 kJ/mol.