The purpose of present work was to study the drying kinetics of whole acorn and its kernel at different drying air temperatures and their effective moisture diffusivity. The results indicated that the drying time of whole acorn was 442, 206 and 188 min at the air temperature of 65, 75 and 85ºC, respectively. At the same temperatures, the drying time of kernel was 131, 56 and 76min. The results showed that the effect of drying air temperature increasing on the drying time reduction could not be significant on acorn drying at all conditions. The effective moisture diffusivity of whole acorn and kernel increased with increasing air temperature from 65 to 75ºC. However more air temperature increasing, led to decreasing this property of acorn kernel. The critical temperature of acorn drying was about 75°C in which acorn kernel had the highest effective moisture diffusivity., {"references":["S. Seiiedlou, H.R. Ghasemzadeh, N. Hamdami, F. Talati and M. \nMoghaddam, \"Convective drying of apple: Mathematical modeling and \ndetermination of some quality parameters,\" Int. J. Agri. Bio., vol. 12, pp. \n171-178, 2010.","N. Hamdami, J-Y. Monteau, and A. Le Bail, \"Moisture diffusivity and \nwater activity of part-baked bread at above sub-freezing temperatures,\" \nInt. J. Food Eng., vol. 14, pp 259-28, 2006.","I. Doymaz, \"Drying behavior of green beans,\" J. Food Eng., vol. 69, pp. \n161-165, 2005.","M. Aghabashlu, M.H. Kiyanmehr, H. Sammi-akh ijahani, \"Influence of \ndrying condition on the effective moisture diffusivity, energy of \nactivation and energy consumption during the thin layer drying of \nberberis fruit (Berberidaceae) ,\" Energy Conversion and Management, \nvol. 32, pp. 157-165, 2008.","D-W. Sun, Thermal food processing: New technologies and quality \nissues. Taylor and Francis, 2006.","AOAC, 1990. Official Method of Analysis, Association of Official \nAnalytical Chemists (No.934.06). Washington, DC, 1990.","A. Chakraverty and S.R. Poul, Post harvest technology: cereals, pulses \nand vegetables. Science Publishers, Inc. India. Pp. 183-188, 2001.","T. Koyuncu, U. Serdar and I. Tosun, \"Drying characteristics and energy \nrequirement for dehydration of chestnuts (Castanea sativa Mill.),\" J. \nFood Eng., vol. 62, pp. 165-168, 2004.","R.P.F. Guine and M.C. Fernandes, \"Analysis of the drying kinetics of \nchestnuts,\" J. Food Eng., vol. 76, pp. 460-467, 2006. \n[10] H. Tugrul, \"Simple modeling of infrared drying of fresh apple slices,\" J. \nFood Eng., vol. 71, pp. 311-323, 2005. \n[11] K. Sacilik and A.K. Elicin, \"The thin layer drying characteristics of \norganic apple slices,\" J. Food Eng., vol. 73, pp. 281-289, 2006. \n[12] K.O. Falade and O.J. Solademi, \"Modelling of air drying of fresh and \nblanched sweet potato slices,\" Int. J. Food Sci. Tech., vol. 45, pp. 278–\n288, 2010. \n[13] I.T. Togrul, \"Modelling of heat and moisture transport during drying \nblack grapes,\" Int. J. Food Sci. Tech., vol. 45, pp.1146–1152, 2010. \n[14] A. Kaleta and K. Gornicki, \"Evaluation of drying models of apple (var. \nMcIntosh) dried in a convective dryer,\" Int. J. Food Sci. Tech., vol. 45, \npp.891–898, 2010. \n[15] J.S. Babalis and G.V. Belessiotis, \"Influence of drying condition on the \ndrying constants and moisture diffusivity during the thin layer drying of \nfigs,\" J. Food Eng., vol. 65, pp. 449-458, 2004. \n[16] A. Biju Cletus and J.K. Carson, \"Drying curves and apparent diffusivity \nof New Zealand chestnut varity'1015',\" J. Food Eng., vol. 85, pp. 381-\n386, 2008. \n[17] M. Rasouli, S. Seiiedlou, H.R. Ghasemzadeh and H. Nalbandi, \n\"Influence of drying conditions on the effective moisture diffusivity and energy of activation during the hot air drying of garlic,\" Aus. J. Agri. \nEng., vol. 2(4), pp. 96-101, 2011. \n[18] T.Y. Tunde-Akintunde and G.O. Ogunlakin, \"Influence of drying \nconditions on the effective moisture diffusivity and energy requirements \nduring the drying of pretreated and untreated pumpkin,\" Energy Conv. \nManag., vol. 52(2), pp. 1107-1113, 2011."]}