Effect of Ultrasound-Assisted Osmotic Dehydration Pretreatment on Drying Kinetics and Effective Moisture Diffusivity of Mirabelle Plum

2015 ◽  
Vol 39 (6) ◽  
pp. 2710-2717 ◽  
Author(s):  
Jalal Dehghannya ◽  
Rasoul Gorbani ◽  
Babak Ghanbarzadeh
Keyword(s):  
Osmotic Dehydration ◽  
Moisture Diffusivity ◽  
Drying Kinetics ◽  
Effective Moisture Diffusivity ◽  
Effective Moisture ◽  
Ultrasound Assisted

scholarly journals Mathematical modelling of diced konjac corms drying in a fluidised bed dryer

2020 ◽  
Vol 24 (5 Part A) ◽  
pp. 2833-2843
Author(s):  
Montree Montreepila ◽  
Nattapol Poomsa-Ad ◽  
Lamul Wiset
Keyword(s):  
Fluidized Bed ◽  
Native Species ◽  
Linear Regression Analysis ◽  
Moisture Diffusivity ◽  
Drying Kinetics ◽  
Moisture Loss ◽  
Effective Moisture Diffusivity ◽  
Fluidised Bed ◽  
Effective Moisture ◽  
Kinetics Of

Konjac glucomannan (KGM) can be obtained from tubers (called corms) of various species within the Amorphophallus genus. Among the most popular species for use in food industry is Buk Nuea Sai (Amorphophallus muelleri), a native species in Thailand. Drying process can be helpful in preserving KGM during long storage periods. However, the existing drying systems are often slow and lead to drying delays and subsequently quality reduction of the dried product. Given the economic importance of KGM, new, more efficient drying systems, have to be developed. The present study focuses on the drying kinetics of konjac dices in a fluidized bed, operating at a constant air velocity of 2.5 m/s and air temperatures of 50, 60, and 70?C. Six empirical mathematical models were selected to describe and compare the drying characteristics of konjac dices subjected to these conditions. The model coefficients were determined by non-linear regression analysis. Among the tested models used to describe the drying kinetics of konjac dices, the two-term model was found as the best one. The moisture loss from the dice was described by the Fick?s diffusion equation, and based on the obtained results the effective moisture diffusivity was estimated, getting a value in the range between 9.60526 ? 10?9 m2/s and 1.2006 ? 10?7 m2/s. The relationship between the temperature and the effective moisture diffusivity was described adequately by means of Arrhenius-type equation. An activation energy value between 8.65 kJ/mol and 61.28 kJ/mol was obtained. The findings allow the successful simulation of konjac dice drying in a fluidized bed between 50 and 70?C, 30-60 mm bed height and 6-15 mm dice thickness.

An Experimental Study on the Drying Kinetics of Castor Bean Fruits (Ricinus communis L., “Brs Energia” Variety)

2016 ◽  
Vol 369 ◽  
pp. 119-124
Author(s):  
E.M.A. Pereira ◽  
J.V. Silva ◽  
J.P.S. Santos ◽  
T.H.F. Andrade ◽  
A.G. Barbosa de Lima
Keyword(s):  
Experimental Study ◽  
Castor Bean ◽  
Moisture Diffusivity ◽  
Drying Kinetics ◽  
Effective Moisture Diffusivity ◽  
Effective Moisture ◽  
Air Temperatures ◽  
Thin Layer Drying ◽  
Drying Behavior ◽  
Kinetics Of

This work aims to conduct an experimental study of the drying kinetics of castor bean fruits (Ricinuscommunis L., “BRS Energia” variety). Experiments were conducted using an oven at air temperatures 50 and 70°C and air relative humidity values 16.34 and 6.24%, respectively. The castor bean fruits were considered as a triaxial spheroid. The experimental moisture content data as a function of time were fitted to different lumped models (namely Henderson and Pabis, Page, Midilli and two-term exponential models) available in the literature.The values of the effective moisture diffusivity were obtained from the Fick's diffusion model. Results shows that the two-term drying model could adequately describe the thin layer drying behavior of castor bean fruit, and that the effective moisture diffusivity increases with increasing drying air temperature.

scholarly journals Mathematical modeling and effect of blanching pretreatment on the drying kinetics of Chinese yam (Dioscorea opposita)

2015 ◽  
Vol 21 (4) ◽  
pp. 511-518 ◽  
Author(s):  
Sheng Fang ◽  
Li-Ping Wang ◽  
Ting Wu
Keyword(s):  
Model Performance ◽  
Moisture Diffusivity ◽  
Drying Kinetics ◽  
Effective Moisture Diffusivity ◽  
Diffusivity Coefficient ◽  
Drying Time ◽  
Chinese Yam ◽  
Effective Moisture ◽  
Dioscorea Opposita ◽  
Kinetics Of

The influences of blanching pretreatment on the drying kinetics of Chinese yam (Dioscorea opposita) slices were investigated. Drying experiments were carried out at 60, 70, 80 and 90?C. Six thin layer models were evaluated and the determination of coefficient (R2), chi-square (?2), root means square error (RMSE) were used to analysis the model performance for both raw and blanched samples. The Wang and Singh model gave best results with R2 of 0.9987 and RMSE of 0.0136 for raw yam slices, and R2 of 0.9989 and RMSE of 0.0119 for blanched samples. The effective moisture diffusivity coefficient Deff varied in the range of 0.7295?10-9 to 2.4087?10-9m2 s-1 for raw slices, and 1.3748?10-9 to 3.8524?10-9m2 s-1 for the blanche dones. The activation energy of yam slices drying were 41.149 and 33.499 kJ mol-1 for raw and blanched yam slices, respectively. Results show that blanching pretreatment can reduce the total drying time and improve the effective moisture diffusivity compared with the raw samples.

Drying Kinetics of Grape Stalk

2006 ◽  
Vol 258-260 ◽  
pp. 225-230 ◽  
Author(s):  
J.V. García-Pérez ◽  
M. Blasco ◽  
J.A. Cárcel ◽  
G. Clemente ◽  
A. Mulet
Keyword(s):  
Mass Fraction ◽  
Moisture Diffusivity ◽  
Diffusion Models ◽  
Drying Kinetics ◽  
Effective Moisture Diffusivity ◽  
Effective Moisture ◽  
Mass Load ◽  
Mass Fractions ◽  
The Individual ◽  
Kinetics Of

Grape stalk may be considered as an agro-food byproduct of the wine industry, being considered as a potential source of antioxidant compounds. Actually, before the extraction of antioxidants a previous stage of drying would be necessary. Stalks obtained from a red wine processing (Vitis vinifera var. Bobal) were characterized as a cylinder net with different size ending in spheres. The average diameters and mass fractions of the individual parts of the stalk were measured: spheres (4.4±0.7 mm and 0.352 mass fraction), large cylinders (3.3±0.6 mm and 0.204 mass fraction), intermediate cylinders (2.1±0.4 mm and 0.294 mass fraction) and small cylinders (1.1±0.3 mm and 0.150 mass fraction). Drying kinetics of each one of the parts of the stalk were carried out at 40 °C and 2 m/s using an initial mass load of 30 g. Furthermore, drying experiments of the whole stalk were conducted at the same experimental conditions. Different diffusion models were considered to predict the drying kinetics for each one of the individual parts of the stalk according to the geometry considered. A diffusion model for the whole stalk was developed by adding the individual diffusion models weighed by the corresponding mass fractions. The diffusion models considered fitted properly the drying kinetics of the individual parts considered on the stalk. The figures of the effective moisture diffusivity identified for the different kinds of cylinders were close (1.07-1.78 10-11 m2/s), however, the spheres showed a different behavior characterized by a significantly higher figure of effective moisture diffusivity (3.92 10-8 m2/s). Finally, the usefulness of the model considered to describe the drying kinetics of the whole stalks was shown.

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