Abstract
In this study, drying characteristics of pretreated and untreated pumpkin were examined in a hot-air dryer at air temperatures within a range of 40–80 °C and a constant air velocity of 1.5 m/s. The drying was observed to be in the falling-rate drying period and thus liquid diffusion is the main mechanism of moisture movement from the internal regions to the product surface. The experimental drying data for the pumpkin fruits were used to fit Exponential, General exponential, Logarithmic, Page, Midilli-Kucuk and Parabolic model and the statistical validity of models tested were determined by non-linear regression analysis. The Parabolic model had the highest R2 and lowest χ2 and RMSE values. This indicates that the Parabolic model is appropriate to describe the dehydration behavior for the pumpkin.
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Abbreviations
- a:
-
Drying constant
- b:
-
Drying constant
- c:
-
Drying constant
- DR:
-
Drying rate (g water/g dry matter*h)
- k:
-
Drying constant, 1/min
- Me :
-
Equilibrium moisture content (kg water/kg dry matter)
- Mi :
-
Initial moisture content (kg water/kg dry matter)
- MR :
-
Dimensionless moisture ratio
- MR exp,i :
-
Experimental dimensionless moisture ratio
- MR pre,i :
-
Predicted dimensionless moisture ratio
- Mt :
-
Moisture content at any time of drying (kg water/kg dry matter)
- Mt + dt :
-
Moisture content at t + dt (kg water/kg dry matter)
- N:
-
Number of observations
- n:
-
Drying constant, positive integer
- R2 :
-
Coefficient of determination
- t:
-
Time (min)
- W :
-
Amount of evaporated water (g)
- W0:
-
Initial weight of sample (g)
- W1:
-
Sample dry matter mass (g)
- z:
-
Number of constants
- χ2 :
-
Reduced chi-square
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Tunde-Akintunde, T.Y., Ogunlakin, G.O. Mathematical modeling of drying of pretreated and untreated pumpkin. J Food Sci Technol 50, 705–713 (2013). https://doi.org/10.1007/s13197-011-0392-2
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DOI: https://doi.org/10.1007/s13197-011-0392-2