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Analysis of convectional drying process of peach

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
In this study the convectional drying process of peach were investigated. Peaches were cut longitudinally into eight similar pieces and were dried in a laboratory air-drier with forced horizontal air flow. Drying experiments were carried out at temperatures of 50, 60, 70oC and for two air velocities: 1.0 and 1.2 m/s. The results are shown graphically on the charts. It was found that a greater effect on increasing the rate of drying is the drying air temperature than the increase in flow velocity. The verification of theoretical models of the first and second drying period indicates that the drying process of peach is determined by internal conditions of heat and mass transfer, therefore to describe the drying process were used models of the second period of drying. Global relative error calculated for the whole process was less than 5%.
Słowa kluczowe
Rocznik
Tom
Strony
333--343
Opis fizyczny
Bibliogr. 24 poz., rys.
Twórcy
autor
  • Faculty of Production Engineering, Warsaw University of Life Sciences
autor
  • Faculty of Production Engineering, Warsaw University of Life Sciences
autor
Bibliografia
  • BOZKIR O. 2006. Thin layer drying and mathematical modeling for washed dry apricots. Journal of Food Engineering, 77(1): 146-151.
  • CONTRERAS C., MARTIN-ESPARZA M.E., CHIRALT A., MARTINEZ-NAVARRETE N. 2008. Influence of microwave application on convective drying: Effects on drying kinetics, and optical and mechanical properties of apple and strawberry. Journal of Food Engineering, 88: 55–64.
  • DANDAMRONGRAK R., MASON R., YOUNG G. 2003. The effect of pretreatments on the drying rate and quality of dried bananas. International Journal of Food Science and Technology, 38: 877–882.
  • DOYMAZ I., PALA M. 2002. The effects of dipping pretreatments on air-drying rates of the seedless grapes. Journal of Food Engineering, 52: 413–417.
  • DOYMAZ I. 2004. Effect of pre-treatments using potassium metabisulphite and alkaline ethyl oleate on the drying kinetics of apricots. Biosystems Engineering, 89: 281–287.
  • GERMER S.P.M., QUEIROZ M.R., AGUIRRE J.M., BERBARI S.A.G., ANJOS V. 2010. Process variables in the osmotic dehydration of sliced peaches. Ciência e Tecnologia de Alimentos. 30(4): 940–948. Online: http://dx.doi.org/10.1590/S0101-20612010000400016 (access: 31.07.2013).
  • GOYAL R.K., KINGSLY A.R.P., MANIKANTAN M.R,. ILYASA S.M. 2007. Mathematical modelling of thin layer drying kinetics of plum in a tunnel dryer. Journal of Food Engineering 79: 176–180.
  • IGUAL M., GARCIA-MARTINEZ E., MARTIN-ESPARZA M.E., MARTINEZ-NAVARRETE N. 2012. Effect of processing on the drying kinetics and functional value of dried apricot. Food Research International 47: 284–290
  • JAROS M. 1999. Kinetyka suszenia warzyw. Rozprawa habilitacyjna. WAR Lublin.
  • KINGSLY R.P., GOYAL R.K., MANIKANTAN M.R., ILYAS S.M. 2007. Effects of pretreatments and drying air temperature on drying behaviour of peach slice. International Journal of Food Science & Technology, 42(1): 65–69.
  • PABIS S. 1982. Teoria konwekcyjnego suszenia produktów rolniczych. PWRiL, Warszawa.
  • PABIS S. 1994. Uogólniony model kinetyki suszenia warzyw i owoców w pierwszym okresie. Zeszyty Problemowe Postępów Nauk Rolniczych, 417: 15–34.
  • PABIS S. 1999. Koncepcja teorii konwekcyjnego suszenia warzyw. In: Konwekcyjne suszenie warzyw teoria i praktyka. Ed. S. Pabis, p. 9–31.
  • PAGE G. 1949. Factors influencing the maximum rates of air-drying shelled corn in thin layers. M.S. Thesis. Lafayette, IN: Purdze University.
  • PEREIRA L.M., FERRARI C.C., MASTRANTONIO S.D.S., RODRIGUES A.C.C., HUBINGER M.D. 2006. Kinetic aspects, texture, and colour evaluation of some tropical fruits during osmotic dehydration. Drying Technology, 24(4): 475–484.
  • SAHARI M.A., SOUTI M., EMAM-JOMEH Z. 2006. Improving the dehydration of dried peach by osmotic method. Journal of Food Technology, 4(3): 189–193.
  • SARSILMAZ C., YALDIZ C., PEHLIVAN D. 2000. Drying of apricots in a rotary column cylindrical dryer (RCCD) supported with solar energy. Renewable Energy, 21: 117–127.
  • SIMAL S., FEMENIA A., GARAU M.C., ROSSELLO C. 2005. Use of exponential, Page’s and difusional models to simulate the drying kinetics of kiwi fruit. Journal of Food Engineering, 60: 323–328.
  • TOGRUL I.T., PEHLIVAN D. 2002. Mathematical modelling of solar drying of apricots in thin layers. Journal of Food Engineering, 55: 209–216.
  • TOGRUL I.T., PEHLIVAN D. 2003. Modelling of drying kinetics of single apricot. Journal of Food Engineering, 58: 23–32.
  • TOGRUL I.T., PEHLIVAN D. 2004. Modelling of thin layer drying kinetics of some fruits dunder open-air sun drying process. Journal of Food Engineering, 65: 413–425.
  • YALDIZ O., ERTEKIN C., UZUN H.I. 2001. Mathematical modeling of thin layer solar drying of sultana grapes. Energy - An International Journal, 26: 457–465.
  • WANG J., SHENG K. 2006. Far-infrared and microwave drying of peach LWT. Food Science and Technology, 39(3): 247–255.
  • PN-A-75101-03:1990. Przetwory owocowe i warzywne. Przygotowanie próbek i metody badań fizykochemicznych. Oznaczanie zawartości suchej masy metodą wagową.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-6cc95de2-3881-4beb-bda7-6ea6ecb9dfdb
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