با همکاری انجمن علوم و صنایع غذایی ایران

نوع مقاله : مقاله پژوهشی لاتین

نویسندگان

فردوسی مشهد

چکیده

In this study, mathematical modeling of hot air-drying of thin-layer papaya (Carica papaya L.) slices with 5±1 mm thickness pretreated in osmotic solution (50% sucrose) was investigated. Thin-layer drying was conducted under three different drying temperatures of 40, 50 and 60 °C at a constant air velocity of 0.9±0.1 m/s and absolute humidity of 0.6 ± 0.02 g of water/kg of dry air. It was found that the drying process occurred in falling rate period over the drying time. The osmosis dehydration characteristics obtained by solid gain (SG), water loss (WL) and weight reduction (WR) parameters that increased with increasing immersion time. The effective diffusivity for papaya slices was within the range of 2.13×10-9 to 4.84×10-9 m2/s over the temperature range. The activation energy was 38.63 kJ/mol indicated the effect of temperature on the diffusivity. Based on the statistical analysis using coefficient of determination (R²) and root mean square error (RMSE), it was concluded that the best model in terms of fitting performance for hot air-drying of papaya pretreated in osmosis solution in all temperature range was Midilli et al. model.

عنوان مقاله [English]

The Kinetics of Forced Convective Air-drying of Papaya (Carica papaya L.) Slices Pretreated in Osmotic Solution

نویسندگان [English]

  • Alireza Yousefi
  • Shahla Khodabakhsh Aghdam
  • Mahdi Pourafhar Chenar
  • Mehrdad Niakosari

چکیده [English]

In this study, mathematical modeling of hot air-drying of thin-layer papaya (Carica papaya L.) slices with 5±1 mm thickness pretreated in osmotic solution (50% sucrose) was investigated. Thin-layer drying was conducted under three different drying temperatures of 40, 50 and 60 °C at a constant air velocity of 0.9±0.1 m/s and absolute humidity of 0.6 ± 0.02 g of water/kg of dry air. It was found that the drying process occurred in falling rate period over the drying time. The osmosis dehydration characteristics obtained by solid gain (SG), water loss (WL) and weight reduction (WR) parameters that increased with increasing immersion time. The effective diffusivity for papaya slices was within the range of 2.13×10-9 to 4.84×10-9 m2/s over the temperature range. The activation energy was 38.63 kJ/mol indicated the effect of temperature on the diffusivity. Based on the statistical analysis using coefficient of determination (R²) and root mean square error (RMSE), it was concluded that the best model in terms of fitting performance for hot air-drying of papaya pretreated in osmosis solution in all temperature range was Midilli et al. model.

Akgun, N., & Doymaz, I., 2005, Modeling of olive cake thin-layer drying process. Journal of food Engineering, 68, 455-461.
Antonio, G. C., Azoubel, P. M., Alves, D. G., El-Aouar, A. A., & Murr, F. E. X., 2004, Osmotic dehydration of papaya (carica papaya L.): influence of process variables. Proceedings of the 14th International Drying Symposium, Sao Paulo, Brazil, vol. C, pp. 1998-2004.
Barnabas, M., Siores, E., & Lamb, A., 2010, Non-thermal microwave reduction of pathogenic cellular population. International Journal of Food Engineering, 6, 1-18.
Crank, J., 1975, The mathematics of diffusion (2nd ed.). Oxford, UK: Clarendon Press.
Demirats, C., Ayhan, T., & Kaygusuz, K., 1998, Drying behavior of hazelnuts. Journal of the Science of Food and Agriculture, 76, 559-564.
Doymaz, I., 2004, Pretreatment effect on sun drying of mulberry fruits (Morus alba L.). Journal of Food Engineering, 65, 205–209.
Doymaz, I., 2007, The kinetics of forced convective air-drying of pumpkin slices. Journal of Food Engineering, 79, 243–248.
Drouzas, A. E., Tsami, E., & Saravacos, G. D., 1999, Microwave/vacuum drying of model fruit gels. Journal of Food Engineering, 39, 117-122.
Fernandes, F., Oliveira, F., & Rodrigues, S., 2008, Use of ultrasound for dehydration of papayas. Food Bioprocess Technology, 1, 339–345.
Funebo, T., & Ohlsson, T., 1998, Microwave-assisted air dehydration of apple and mushroom. Journal of Food Engineering, 38, 353-367.
Guarte, R., 1996, Modeling the drying behavior of copra and development of a natural convection dryer for production of high quality copra in the Philippines. Ph.D. dissertation, 287. Hohenheim University, Stuttgart, Germany.
Haghi, A. K., & Amanifard, N., 2008, Analysis of heat and mass transfer during microwave drying of food products. Brazilian Journal of Chemical Engineering, 25, 491-501.
Heng, W., Guilbert, S., & Cuq, J. L., 1990, Osmotic dehydration of papaya: influence of process variables on the quality. Sciences des Aliments, 10, 831-848.
Kaleemullah, S., & Kailappan, R., 2005, Drying kinetics of red chillies in rotary dryer. Biosystems Engineering, 92, 15–23.
Kaymak-Ertekin, F., & Sultanoglu, M., 2000, Modelling of mass transfer during osmotic dehydration of apples. Journal of Food Engineering, 46, 243–250.
Kaymak-Ertekin, F., 2002, Drying and rehydrating kinetics of green and red peppers. Journal of Food Science, 67, 168–175.
Kingsly, A. R. P., & Singh, D. B., 2007, Drying kinetics of pomegranate arils. Journal of Food Engineering, 79,741–744.
Lazarides, H. N., Katsanidis, E., & Nickolaidis, A., 1995, Mass transfer kinetics during osmotic preconcentration aiming at minimal solid uptake. Journal of Food Engineering, 25, 151-166.
Levic, L. J., Koprivica, G., Misljenovic, N., Filipcev, B., Simurina, O., & Kuljanin, T., 2008, Effect of starch as an edible coating material on the process of osmotic dehydration of carrot in saccharose solution and sugar beet molasses. Acta Periodica Technologica, 39, 29-36.
Lozano, J. E., Rotstein, E., & Urbicain, M. J., 1980, Total porosity and open-pore porosity in the drying of fruits. Journal of Food Science, 45, 1403-1407.
Madamba, P. S., Driscoll, R. H., & Buckle, K. A., 1996, The thin-layer drying characteristics of garlic slices. Journal of Food Engineering, 29, 75–97.
Mauro, M. A., & Menegalli, F. C., 2003, Evaluation of water and sucrose diffusion coefficients in potato tissue during osmotic concentration. Journal of Food Engineering, 57, 367-374.
Midilli, A., Kucuk, H., & Yapar, Z. A., 2002, New model for single-layer drying. Drying Technology, 20, 1503-1513.
Momenzadeh, L., Zomorodian, A., & Mowla, D., 2011, Experimental and theoretical investigation of shelled corn drying in a microwave-assisted fluidized bed dryer using Artificial Neural Network. Food and Bioproducts Processing, 89, 15-21.
Morton, J., 1987, Papaya. In: Morton J.F., Editor. Fruits of Warm Climates. (1st ed.) Miami: Florida Flair Books. p. 336–346.
Mujica-Paz, H., Valdez-Fragoso, A., Lopez-Malo, A., Palou, E., & Welti-Chanes, J., 2003, Impregnation and osmotic dehydration of some fruits: effect of the vacuum pressure and syrup concentration. Journal of Food Technology, 57, 305-314.
Ozdemir, M., & Devres, Y., 1999, The thin layer drying characteristics of hazelnuts during roasting. Journal of Food Engineering, 42, 225-233.
Park, K. J., Vohnikova, Z., & Brod, F. P. R., 2002, Evaluation of drying parameters and desorption isotherms of garden mint leaves (Mentha crispa L.). Journal of Food Engineering, 51, 193–199.
Petchi, M., & Manivasagan, R., 2009, Optimization of osmotic dehydration of radish in salt solution using response surface methodology, International Journal of Food Engineering, 5, 1-11.
Prothon, F., & Ahrne, L. M., 2004, Application of the Guggenheim, Anderson and De Boer model to correlate water activity and moisture content during osmotic dehydration of apples. Journal of Food Engineering, 61, 467-470.
Rahman, M., 1998, Desorption isotherm and heat pump drying kinetics of peas. Food International Research, 30, 485-491.
Sacilik, K., Keskin, R., & Elicin, A., 2006, Mathematical modeling of solar tunnel drying of thin layer organic tomato. Journal of Food Engineering, 73, 231-238.
Sharma, G. P., Prasad, S., & Datta, A. K., 2003, Drying kinetics of garlic cloves under convective drying conditions. Journal of Food Science and Technology, 40, 45–51.
Simal, S., Mulet, A., Tarrazo, J., & Rosello, C., 1996, Drying models for green peas. Food Chemistry, 55, 121–128.
Sogi, D. S., Shivhare, U. S., Garg, S. K., & Bawa, A. S., 2003, Water sorption isotherms and drying characteristics of tomato seeds. Biosystems Engineering, 84, 297–301.
Vergara, F., Amezaga, E., Barcenas, M. E., & Welti, J., 1997, Analysis of the drying processes of osmotically dehydrated apple using the characteristic curve model. Drying Technology, 15, 949–963.
Westerman, P., & White, W., 1973, Relative humidity effect on the high temperature drying of shelled corn. Transaction of American Society of Agricultural Engineering, 16, 1136-1139.
Yagcioglu, A., Degirmencioglu, A., & Cagatay, F., 1999, Drying characteristics of laurel leaves underdifferent drying conditions. In proceedings of the 7th international congress on agricultural mechanization and energy. (pp. 565-569), 26-27 May, Adana, Turkey.
Yaldiz, O., Ertekin, C., & Uzun, H. I., 2001, Mathematical modeling of thin layer solar drying of Sultana grapes. Energy, 42, 167-171.
Yousefi, A. R., Asadi, V., Nassiri, S. M., Niakousari, M., & Khodabakhsh Aghdam, Sh., 2012, Comparison of mathematical and neural network models in the estimation of papaya fruit moisture content. Philippine Journal of Agricultural Scientist, 95, 192-198.
Zomorodian, A., & Moradi, M., 2010, Mathematical modeling of forced convection thin layer solar drying for Cuminum cyminum. Journal of Agriculture Science and Technology, 12, 401-408.
CAPTCHA Image