In this study, the drying of thin layers of the 'Violet de Galmi' onion (a variety mainly grown in West Africa) is presented in this article, along with the Reaction Engineering Approach (REA) modeling for a comprehensive understanding of the drying kinetics.The experiments were conducted on a lab-scale dryer to form thin layer of cylindrical onion slice. By performing this experiment, the standard activation energy is evaluated and modeled. The model is validated by simulating the drying rates under various drying conditions. The comparison of simulation and experimental data is found to be satisfactory. This approach allows the determination of the internal characteristics of the onion for the further studies such as design of solar dryer for onion. Downloaded by [University of Birmingham] at 00:09 24 June 2016 2 NOMENCLATURE A Surface of the product (m 2 ) a w Activity of water Bi Biot number C ps Specific heat of dry mass (J kg -1 K -1 ) C pw Specific heat of water (J kg -1 K -1 ) D AB Water air diffusivity (m 2 s -1 ) H Heat transfer coefficient (W m -2 K -1 ) h m Mass transfer coefficient (m s -1 ) L p Diameter (m) m s Dry mass (kg) P sat Saturation pressure (Pa) R Universal gas constant = 8314.46 J mol -1 K -1 R 2 Coefficient of determination RH b Relative humidity RMSE Root-Mean-Square error T s Temperature at surface (K) T p Temperature of product (K or °C) T b Bulk air temperature (°C) Sh Sherwood number SSE Sum of squared error X Water content (kg water /kg dry mass ) X eq Equilibrium water content (kg water /kg dry mass ) Downloaded by [University of Birmingham] at 00:09 24 June 2016 3 ΔE v Activation energy (J kmol -1 ) ΔE v,b Equilibrium activation energy (J kmol -1 ) ΔH v Latent heat of vaporization (J kg -1 ) ρ v,b Vapor density in bulk air (kg m -3 ) ρ v,s Vapor density at surface (kg m -3 ) ρ v,sat Vapor density at saturation (kg m -3 ) μ air Dynamic viscosity of air(kg m -1 s -1 ) Ψ Fractional coefficient of vapor pressure
INTRODUCTIONDrying is a final key process during the manufacturing of products in the food industry, such as fabrication of milk powder, production of drying of cereals and preservation of fruits [1] . Principally, drying removes most of the water content of the product to less than 5%. In addition, it is also an energy-intensive process that commonly requires hot air to allow the product to dry by combining simultaneous transfer of heat and mass between the drying air and the product. Indeed, the drying of food products is a traditional way of preservation of these products. However, as food products are one of the most complex materials in their natural form, then the fundamental understanding of the drying of these food products has not been fully comprehended [2,3] . Many studies have been published on the modeling of drying, but the extent of the differences between formulations of different models is quite significant. Each model of the drying of food products is reasonably effective to correlate experimental data obtained, but limited only to the similar type of food p...