Estimation of the Moisture Diffusivity and Activation Energy in Thin Layer Drying of Ginger Slices
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Estimation of the Moisture Diffusivity and Activation Energy in Thin Layer Drying of Ginger Slices

Authors: Ebru Kavak Akpinar, Seda Toraman

Abstract:

In the present work, the effective moisture diffusivity and activation energy were calculated using an infinite series solution of Fick-s diffusion equation. The results showed that increasing drying temperature accelerated the drying process. All drying experiments had only falling rate period. The average effective moisture diffusivity values varied from 2.807x10-10 to 6.977x10-10m2 s_1 over the temperature and velocity range. The temperature dependence of the effective moisture diffusivity for the thin layer drying of the ginger slices was satisfactorily described by an Arrhenius-type relationship with activation energy values of 19.313- 22.722 kJ.mol-1 within 40–70 °C and 0.8-3 ms-1 temperature range.

Keywords: Ginger, Drying, Activation energy, Moisture diffusivity.

Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1075372

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References:


[1] L. Hassini, S. Azzouz, A. Belghith, "Estimation of the moisture diffusion coefficient of potato during hot-air drying", Drying 2004 - Proceedings of the 14th International Drying Symposium (IDS 2004), São Paulo, Brazil, 22-25 August 2004, vol. B, pp. 1488-1495.
[2] I. Doymaz, M. Pala, "The effects of dipping pretreatment on air-drying rates of seedless grapes", Journal of Food Engineering, vol. 52, 2002, pp. 413-427.
[3] E. Akpinar, A. Midilli, Y. Bicer, "Single layer drying behavior of potato slices in a convective cyclone and mathematical modeling", Energy Conversion and Management, 2003, vol. 44, pp. 1689-1705.
[4] E. Mirzaee1, S. Rafiee, A. Keyhani, Z. Emam-Djomeh, "Determining of moisture diffusivity and activation energy in drying of apricots", Res. Agr. Eng., 2009, vol. 55, no. 3, pp. 114-120.
[5] H. Pahlavanzadeh, A. Basiri, M. Zarrabi, "Determination of parameters and pretreatment solution for grape drying", Drying Technology, 2001, vol. 19, pp. 217-226.
[6] P. Singhanat, S. Saentaweesuk, "Effect of two stage, tray and heat pump assisted-dehumidified drying on drying characteristics and qualities of dried ginger", Food and Bioproducts Processing, 2011, vol. 89, pp. 429-437.
[7] ID. Thorat, D. Mohapatra, RF. Sutar, SS. Kapdi, DD. Jagtap, "Mathematical modeling and experimental study on thin-layer vacuum drying of ginger (Zingiber Officinale R.) slices", Food Bioprocess Technol, DOI 10.1007/s11947-010-0429-y, 2010.
[8] J. Crank, The Mathematics of Diffusion, Clarendon press, Oxford,1975.
[9] EK. Akpinar, "The development of a cyclone type dryer for agricultural products", PhD Thesis, Firat University, Elazig, Turkey, 2002.
[10] I. Doymaz, "Evaluation of some thin-layer drying models of persimmon slices (Diospyros kaki L.)", Energy Conversion and Management, 2012, vol. 56, pp. 199-205,.
[11] I. Doymaz, O. Ismail, "Drying characteristics of sweet cherry", Food and Bioproducts Processing, 2011, vol. 89, pp. 31-38.
[12] S. Simal, A. Femenia, J.A. Carcel, and C. Rossello, "Mathematical modeling of the drying curves of kiwi fruits: influence of the ripening stage", Journal of the Science of Food and Agriculture, 2005, vol. 85, pp. 425-432.