A b s t r a c t. The effect of microwave-convective heating on drying characteristics and colour change of lemon slices was investigated. The drying experiments were carried out at 180, 360, 540 and 720 W and at 22°C, with air velocity of 1 m s -1 . The values of effective moisture diffusivity were found to be in the range between 1.87 10 -8 and 3.95 10 -8 m 2 s -1 , and the activation energy was estimated to be 10.91 W g -1 . The drying data were fitted with six mathematical models available in the literature. The model describing drying kinetics of lemon slices in the best way was found. The colour change of the dried lemon slices was analysed and considered as a quality index affecting the drying quality of the product. The values of lightness/darkness, yellowness/blueness and hue angle increased, while the value of redness/greenness decreased with increasing microwave power.K e y w o r d s: drying kinetics, mathematical modelling, colour, lemon slice
INTRODUCTIONThe fresh weight of lemon fruits contains a high percentage of water (about 87% w.b.). Accordingly, they exhibit relatively high metabolic activity compared with other plantderived foods such as seeds. This metabolic activity continues after harvesting, thus making most fruits highly perishable commodities (Atungulu et al., 2004;Pendre et al., 2012).Drying improves the product shelf life without addition of any chemical preservative and reduces both the size of package and the transport cost (Al-Harahsheh et al., 2009;Figiel, 2010;Singh et al., 2010). Drying also assists in reducing post harvest losses of fruits and vegetables especially, which can be as high as 70% (Tunde-Akintunde and Ogunlakin, 2013).High temperatures or long drying times in conventional air drying may cause serious damage to product flavour, colour and nutrients, reducing bulk density and rehydration capacity of the dried product (Contreras et al., 2008). The desire to avoid these problems to some extent, to prevent significant quality loss, and to achieve fast and effective thermal processing has resulted in the increasing use of microwaves for food drying. However, microwave processing has the disadvantage of non-homogeneous distribution in the microwave cavity, creating problems of non-uniform heating. To overcome some of the limitations of single microwave or hot air driers, one strategy is to combine microwaves with hot air. In the microwave-convective drying method, forced air is supplied to carry away the water vapour driven from the interior of the food to its surface.Colour has to be considered as a special parameter that seems to be one of the first attributes of quality that a consumer perceives, and that may influence the consumer judgment of other attributes such as flavour (Chen et al., 2005).Simulation models may be used to develop new drier systems that result in energy savings and optimum processing conditions (Arumuganathan et al., 2009;Hassan-Beygi et al., 2009). A knowledge of effective moisture diffusivity is necessary for designing and modeling mass-transfer...