DOI QR코드

DOI QR Code

Determination of Hot Air Drying Characteristics of Squash (Cucurbita spp.) Slices

  • Hong, Soon-jung (Smart Farm Education Team, Rural Human Resource Development Center) ;
  • Lee, Dong Young (Department of Biosystems Machinery Engineering, College of Agricultural and Life Science, Chungnam National University) ;
  • Park, Jeong Gil (Department of Biosystems Machinery Engineering, College of Agricultural and Life Science, Chungnam National University) ;
  • Mo, Changyeun (National Institute of Agricultural Sciences, Rural Development Administration) ;
  • Lee, Seung Hyun (Department of Biosystems Machinery Engineering, College of Agricultural and Life Science, Chungnam National University)
  • 투고 : 2017.10.30
  • 심사 : 2017.11.15
  • 발행 : 2017.12.01

초록

Purpose: This study was conducted to investigate the hot air drying characteristics of squash slices depending on the drying conditions (input air velocity, input air temperature, and sample thickness). Methods: The developed drying system was equipped with a controllable air blower and electric finned heater, drying chamber, and ventilation fan. Squash (summer squash called Korean zucchini) samples were cut into slices of two different thicknesses (5 and 10 mm). These were then dried at two different input air temperatures (60 and $70^{\circ}C$) and air velocities (5 and 7 m/s). Six well-known drying models were tested to describe the experimental drying data. A non-linear regression analysis was applied to determine model constants and statistical indices such as the coefficient of determination ($R^2$), reduced chi-square (${\chi}^2$), and root mean square error (RMSE). In addition, the effective moisture diffusivity ($D_{eff}$) was estimated based on the curve of ln(MR) versus drying time. Results: The results clearly showed that drying time decreased with an increase in input air temperature. Slice thickness also affected the drying time. Air velocity had a greater influence on drying time at $70^{\circ}C$ than at $60^{\circ}C$ for both thicknesses. All drying models accurately described the drying curve of squash slices regardless of slice thickness and drying conditions; the Modified Henderson and Pabis model had the best performance with the highest R2 and the lowest RMSE values. The effective moisture diffusivity ($D_{eff}$) changes, obtained from Fick's diffusion method, were between $1.67{\times}10^{-10}$ and $7.01{\times}10^{-10}m^2/s$. The moisture diffusivity was increased with an increase in input air temperature, velocity, and thickness. Conclusions: The drying time of squash slices varied depending on input temperature, velocity, and thickness of slices. The further study is necessary to figure out optimal drying condition for squash slices with retaining its original quality.

키워드

참고문헌

  1. Afzal, T. M., T. Abe and Y. Hikida. 1999. Energy and quality aspects during combined FIR-convection drying of barley. Journal of food engineering 42(4):177-182. https://doi.org/10.1016/S0260-8774(99)00117-X
  2. Andres, A., C. Bilbao and P. Fito. 2004. Drying kinetics of apple cylinders under combined hot air-microwave dehydration. Journal of Food Engineering 63(1):71-78. https://doi.org/10.1016/S0260-8774(03)00284-X
  3. Akgun, N. A. and I. Doymaz. 2005. Modelling of olive cake thin-layer drying process. Journal of food Engineering 68(4):455-461. https://doi.org/10.1016/j.jfoodeng.2004.06.023
  4. AOAC. 1990. Official Method of Analysis. Association of Official Analytical Chemists (No. 934. 06), Arlington, VA.
  5. Chayjan, R. A., K. Salari, Q. Abedi and A. A., Sabziparvar. 2013. Modeling moisture diffusivity, activation energy and specific energy consumption of squash seeds in a semi fluidized and fluidized bed drying. Journal of food science and technology 50(4):667-677. https://doi.org/10.1007/s13197-011-0399-8
  6. Doymaz, I. 2007. The kinetics of forced convective air-drying of pumpkin slices. Journal of food engineering 79(1):243-248. https://doi.org/10.1016/j.jfoodeng.2006.01.049
  7. Doymaz, I. and I. Osman. 2011. Drying characteristics of sweet cherry. Food and Bioproducts Processing 89(1):31-38. https://doi.org/10.1016/j.fbp.2010.03.006
  8. Henderson, S. M. and S. Pabis. 1961. Grain drying theory. II. Temperature effects on drying coefficients. Journal of Agricultural Engineering Research 6:169-174.
  9. Karathanos, V. T. 1999. Determination of water content of dried fruits by drying kinetics. Journal of Food Engineering 39:337-344. https://doi.org/10.1016/S0260-8774(98)00132-0
  10. Kaya, A., O. Aydin and I. Dincer. 2008. Experimental and numerical investigation of heat and mass transfer during drying of Hayward kiwi fruits (Actinidia Deliciosa Planch). Journal of Food Engineering 88(3):323-330. https://doi.org/10.1016/j.jfoodeng.2008.02.017
  11. Keum T. H. and J. W. Rhim. 1994. Effect of Various Pretreatments and Drying Methods on the Quality of Dried Vegetables. Korean journal of food science and technology 26:805-813.
  12. Kumar, D. P., H. H. U. Hebbar and M. N. Ramesh. 2006. Suitability of thin layer models for infrared-hot airdrying of onion slices. LWT-Food Science and Technology 39(6):700-705. https://doi.org/10.1016/j.lwt.2005.03.021
  13. Lee, J. H. and H. J., Kim. 2009. Vacuum drying kinetics of Asian white radish (Raphanus sativus L.) slices. LWT-Food Science and Technology 42(1):180-186. https://doi.org/10.1016/j.lwt.2008.05.017
  14. Madamba, P. S., R. H. Driscoll and K. A. Buckle. 1996. The thin-layer drying characteristics of garlic slices. Journal of Food Engineering, 29, 75-97. https://doi.org/10.1016/0260-8774(95)00062-3
  15. Midilli, A., H. Kucuk and Z. Yapar. 2002. A new model for single-layer drying. Drying technology 20(7):1503-1513. https://doi.org/10.1081/DRT-120005864
  16. Mirzaee, E., S. Rafiee, A. Keyhani and Z. Emam-Djomeh. 2009. Determining of moisture diffusivity and activation energy in drying of apricots. Research in Agricultural Engineering 55(3):114-120. https://doi.org/10.17221/8/2009-RAE
  17. O'Callaghan, J. R., D. J. Menzies and P. H. Bailey. 1971. Digital simulation of agricultural dryer performance. Journal of Agricultural Engineering Research 16:223-244. https://doi.org/10.1016/S0021-8634(71)80016-1
  18. Ozkan, I. A., B. Akbudak and N. Akbudak. 2007. Microwave drying characteristics of spinach. Journal of Food Engineering 78(2):577-583. https://doi.org/10.1016/j.jfoodeng.2005.10.026
  19. Page, G. 1949. Factors influencing the maximum rates of air-drying shelled corn in thin layer. M.S. Thesis. Department of Mechanical Engineering, Purdue University, West Lafayette, IN, USA.
  20. Rhim, J. W. and Lee, J. H. 2011. Drying kinetics of whole and sliced shiitake mushrooms (Lentinus edodes). Food Science and Biotechnology 20(2):419-427. https://doi.org/10.1007/s10068-011-0059-9
  21. Wang, Z., J. Sun, X. Liao, F. Chen, G. Zhao, J. Wu and X. Hu. 2007. Mathematical modeling on hot air drying of thin layer apple pomace. Food Research International 40(1):39-46. https://doi.org/10.1016/j.foodres.2006.07.017
  22. Yagcioglu, A., A. Degirmencioglu and F. Cagatay. 1999. Drying characteristic of laurel leaves under different conditions. In A. Bascetincelik (Ed.), Proceedings of the 7th international congress on agricultural mechanization and energy, 26-27 May, Adana, Turkey (pp.565-569). Faculty of Agriculture, Cukurova University.
  23. Zhu, A. and X. Shen. 2014. The model and mass transfer characteristics of convection drying of peach slices. International Journal of Heat and Mass Transfer 72:345-351. https://doi.org/10.1016/j.ijheatmasstransfer.2014.01.001
  24. Zlatanovic, I., M. Komatina and D. Antonijevic. 2013. Low-temperature convective drying of apple cubes. Applied Thermal Engineering 53(1):114-123. https://doi.org/10.1016/j.applthermaleng.2013.01.012