with the collaboration of Iranian Society of Mechanical Engineers (ISME)

Document Type : Research Article

Authors

Department of Mechanics of Agricultural Machinery and Mechanization, Faculty of Agriculture, Shahid Chamran University of Ahvaz, Iran

Abstract

Introduction
Potato (Solanumtuberosum L.) is one of the unique and most potential crops having high productivity, supplementing major food requirement in the world. Drying is generally carried out for two main reasons, one to reduce the water activity which eventually increases the shelf life of food and second to reduce the weight and bulk of food for cheaper transport and storage. The quality evaluation of the dried product was carried out on the basis of response variables such as rehydration ratio, shrinkage percentage, color and the overall acceptability. Drying is the most energy intensive process in food industry. Therefore, new drying techniques and dryers must be designed and studied to minimize the energy cost in drying process. Considering the fact that the highest energy consumption in agriculture is associated with drying operations, different drying methods can be evaluated to determine and compare the energy requirements for drying a particular product. Thermal drying operations are found in almost all industrial sectors and are known, according to various estimates, to consume 10-25% of the national industrial energy in the developed world. Infrared radiation drying has the unique characteristics of energy transfer mechanism. Kantrong et al. (2012) were studied the drying characteristics and quality of shiitake mushroom undergoing microwave-vacuum combined with infrared drying. Motevali et al. (2011) were evaluated energy consumption for drying of mushroom slices using various drying methods including hot air, microwave, vacuum, infrared, microwave-vacuum and hot air-infrared. The objectives of this research were to experimental study of drying kinetics considering quality characteristics including the rehydration and color distribution of potato slices in a vacuum- infrared dryer and also assessment of specific energy consumption and thermal utilization efficiency of potato slices during drying process.
Materials and Methods
A laboratory scale vacuum-infrared dryer, developed at the Agricultural Machinery and Mechanization Engineering Laboratory of Shahid Chamran University of Ahvaz has been used. The dryer consists of a stainless steel drying chamber; a laboratory type piston vacuum pump, which was used to maintain vacuum in the drying chamber; an infrared lamp with power of 250 W which was used to supply thermal radiation to a drying product; and a control system for the infrared radiator.
Sample Preparation
Fresh potatoes were purchased from a local market in Hamadan province. Potatoes were peeled, washed, and cut into sliced with thickness of 1, 2 and 3 mm by a manual slicer. Drying experiments of potato slices were performed in a vacuum chamber with absolute pressure levels of 20, 80, 140 and 760 mmHg; and radiation intensity of infrared lamp was 0.2, 0.3 and 0.4 W cm-2. The mass change of the sample during drying was detected continuously using an electronic weight scale (Lutron, GM- 1500P, Taiwan) with the accuracy of ±0.05 g.
Evaluation of rehydration capacity of dried potato slices
The rehydration tests measured the gain in weight of dehydrated samples (~5 g), dehydrated samples were rehydrated in 200 cc of distilled water at 100°C for 3 minutes.
Evaluation of color
The color of potatoes was measured on five slices selected randomly, and was described by three coordinates in the RGB color space using computer vision.
Evaluation of specific energy consumption
Energy consumption of dying process came from the electrical energy consumed by the operation of the vacuum pump and the infrared lamp. Specific energy consumption was defined as the energy required for removing a unit mass of water in drying the potato slice.
Evaluation of thermal utilization efficiency
Thermal utilization efficiency is defined as the latent heat of vaporization of moisture of sample to the amount of energy required to evaporate moisture from free water. The latent heat of vaporization of water at the evaporating temperature of 100°C was taken as 2257 kJkg-1.
Results and Discussion
The results of the evaluation of rehydration capacity of potato slices during drying process are shown in Table 1. Statistical analysis (ANOVA, post-hoc Duncan) showed that thickness at probability level of 1% had statistically significant influence on rehydration capacity values of dried potato slices. Moisture of dried slice of potato compared to its fresh was obtained nearly 80% in boiling water (at temperature 100°C) for 3 min. The most color changes of slice after drying was related to green color. According to Table 2 and statistical analysis results showed that factor of thickness was not statistically significant on specific energy. The effect of absolute pressure (p<0.05) and radiation intensity (p<0.01) parameters also interaction of absolute pressure and radiation intensity (p<0.05) had statistically significant influence on specific energy of dried potato slices. According to Table 3 and statistical analysis the factor of absolute pressure had statistically significant at probability level of 5% on thermal utilization efficiency. Also the effect of interaction of absolute pressure and radiation intensity had statistically significant at probability level of 5% on thermal utilization efficiency of dried potato slices. The drying efficiency of potato slices varied between 2.13% to 31.01%.
Conclusions
Dried potato slices at a thickness of 1 mm put in boiling water for three minutes; showed the most amount of water absorption ratio that it was able to absorb the value of 86% more than the initial moisture. The lowest rate of color change before and after the drying process is related to the thickness of the thinnest sliced potatoes. Comparison of energy consumption showed that the radiation intensity of 0.4 W cm-2, absolute pressure level of 80 mmHg and slice thickness of 1 mm had shorter drying time in experimental conditions.

Keywords

1. AOAC. 1990. Official Methods of Analysis. Association of Official Analytical Chemists, Washington, DC. No. 934-06
2. Bhandri, B., and T. Howes. 1999. Implication of glass transition for the drying and stability of dried foods. Journal of Food Engineering 40: 71-79.
3. Darvishi, H. 2012. Energy consumption and mathematical modeling of microwave drying of potato slices. Agricultural Engineering International: CIGR Journal 14 (1): 94-101.
4. Fealehkari, M., R. AmiriChayjan, and J. AmiriParian. 2012. Study of the physical properties (color and shrinkage) of shallot using convective-infrared drying method. 7th National Conference on Agriculture Machinery Engineering and Mechanization, Shiraz.
5. FAO. 2013. Statistical Yearbook 2013 World food and agriculture. http://faostat.fao.org/site/291/default.aspx
6. Francis, F. J. 2000. Encyclopedia of Food Science and Technology. John Wiley & Sons Inc.
7. Garcia, P., N. Sanjuan, J. Bon, J. Carreres, and A. Mulet. 2005. Rehydration process of Boletus edulis mushroom: characteristics and modeling. Journal of the Science of Food and Agriculture 85: 1397-1404.
8. Hoffman, B. 2004. Cancer Threat for Snackers. http://www.freerepublic.com /focus/news/673300/posts/
9. Kantrong, H., A. Tansakul, and G. S. Mittal. 2012. Drying characteristics and quality of shiitake mushroom undergoing microwave-vacuum drying and microwave-vacuum combined with infrared drying. Journal Food Scientists and Technologists.
10. Lee, J. H., and H. J. Kim. 2009. Vacuum drying kinetics of Asian white radish (Raphanussativus L.) slices. LWT – Food Science and Technology 42: 180-186.
11. Lee, K. T., M. Farid, and S. K. Nguang. 2006. The mathematical modeling of the rehydration characteristics of fruit. Journal of Food Engineering 72 (1): 16-23.
12. Leeratanarak, N., S. Devahastin, and N. Chiewchan. 2006. Drying Kinetics and Quality of Potato Chips Undergoing Different Drying Techniques. Journal of Food Engineering 77: 635-43
13. Li, Z., G. S. V. Raghavan, N. Wang, and C. Vigneault. 2011. Drying rate control in the middle stage of microwave drying. Journal of Food Engineering 104: 234-238.
14. Lin, Y. P., T. Y. Lee, J. H. Tsen, and V. A. King. 2006. Dehydration of yam slices using FIR-assisted freeze drying. Journal of Food Engineering 79: 1295-1301.
15. Motevali, A., S. Minaei, M. H. Khoshtaghaza, and H. Amirnejat. 2011. Comparison of energy consumption and Specific Energy Requirements of Different methods for drying mushroom slices. Energy 36: 6433-6441.
16. Prachayawarakorn, S., P. Prachayawasin, and S. Soponronnarit. 2004. Effective diffusivity and kinetics of urease inactivation and color change during processing of soybeans with superheated-steam fluidized bed. Drying Technology 22 (9): 2095-2118.
17. Reyes, A., S. Ceron, R. Zuniga, and P. Moyano. 2007. A comparative study of microwave-assisted air drying of potato slices. Biosystems Engineering 98: 310-318.
18. Singh, K. K. 1994. Development of a small capacity dryer for vegetables. Journal of Food Engineering 21: 19-30.
19. Sharma, G. P., R. C. Verma, and P. B. Pathare. 2005. Thin-layer infrared radiation drying of onion slices. Journal of Food Engineering 67: 361-366.
20. Strumillo, C., and T. Kudra. 1986. drying principles, application and design. Routledge. pp 448.
21. UmeshHebbar, H., K. H. Vishwanathan, and M. N. Ramesh. 2004. Development of combined infrared and hot air dryer for vegetables. Journal Food Engineering 65 (4): 557-563.
CAPTCHA Image