Drying and Rehydration Behaviors of Convection Drying of Green Peas

被引:58
作者
Doymaz, Ibrahim [1 ]
Kocayigit, Fergun [1 ]
机构
[1] Yildiz Tech Univ, Dept Chem Engn, TR-34210 Istanbul, Turkey
关键词
Activation energy; Drying; Effective diffusivity; Green pea; Pretreatments; Rehydration capacity; AIR-TEMPERATURE; PISUM-SATIVUM; KINETICS; MICROWAVE; PRETREATMENTS; QUALITY; VACUUM; COLOR; DEHYDRATION; SELECTION;
D O I
10.1080/07373937.2011.591713
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The drying behaviors of green peas were examined in a convection dryer for a temperature range of 55-70 degrees C with a constant air velocity of 2.1 m/s. The green peas were pretreated with ethyl oleate and citric acid solutions and blanched with hot water at 85 degrees C before drying. The drying process was continued until sample moisture fell to 0.3 kg water/kg dry matter (dm). The blanched samples dried faster than those in other pretreatments and control conditions. Moreover, rehydration capacities of the pretreatments were higher than control samples. The experimental results illustrated the absence of a constant rate drying period and the drying process took place in the falling rate period. Moisture transfer from green peas was described by applying Fick's diffusion model, and the effective moisture diffusivity was calculated. The calculated effective diffusivity ranged from 8.059 x 10(-11) to 1.973 x 10(-10) m(2)/s for the studied temperature range. The values of activation energy (E-a) were 22.01, 26.86, 30.31, and 30.99 kJ/mol for samples pretreated with citric acid, control samples, samples pretreated with ethyl oleate, and blanched samples, respectively. Drying data were fitted to four thin-layer drying models; namely, Lewis, Henderson and Pabis, logarithmic, and Page. The performance of the models was evaluated by comparing the coefficient of determination (R-2), reduced chi-square (chi(2)), and root mean square error (RMSE). The models that best represented green pea drying were the logarithmic and Page models.
引用
收藏
页码:1273 / 1282
页数:10
相关论文
共 40 条
[31]   Drying kinetics of grape seeds [J].
Roberts, John S. ;
Kidd, David R. ;
Padilla-Zakour, Olga .
JOURNAL OF FOOD ENGINEERING, 2008, 89 (04) :460-465
[32]   Nonisotropic mass transfer model for green bean drying [J].
Rossello, C ;
Simal, S ;
SanJuan, N ;
Mulet, A .
JOURNAL OF AGRICULTURAL AND FOOD CHEMISTRY, 1997, 45 (02) :337-342
[33]  
Sablani S., 2000, DRYING TECHNOLOGY AG
[34]   Drying kinetics of Uryani plum in a convective hot-air dryer [J].
Sacilik, Kamil ;
Elicin, Ahmet Konuralp ;
Unal, Guran .
JOURNAL OF FOOD ENGINEERING, 2006, 76 (03) :362-368
[35]   Drying of Pedro Ximenez Grapes in Chamber at Controlled Temperature and with Dipping Pretreatments. Changes in the Color Fraction [J].
Serratosa, Maria P. ;
Lopez-Toledano, Azahara ;
Medina, Manuel ;
Merida, Julieta .
JOURNAL OF AGRICULTURAL AND FOOD CHEMISTRY, 2008, 56 (22) :10739-10746
[36]   Drying models for green peas [J].
Simal, S ;
Mulet, A ;
Tarrazo, J ;
Rossello, C .
FOOD CHEMISTRY, 1996, 55 (02) :121-128
[37]   Effect of pretreatments on drying and rehydration kinetics and color of sweet potato slices [J].
Singh, Sukhcharn ;
Raina, C. S. ;
Bawa, A. S. ;
Saxena, D. C. .
DRYING TECHNOLOGY, 2006, 24 (11) :1487-1494
[38]   Effect of Pre-Treatment on the Drying Characteristics and Kinetics of Okra (Abelmoschus esculetus (L.) Moench) Slices [J].
Sobukola, Olajide .
INTERNATIONAL JOURNAL OF FOOD ENGINEERING, 2009, 5 (02)
[39]   Selection of chemical and thermal pretreatment combination to reduce the dehydration time of sour cherry (Prunus cerasus L.) [J].
Tarhan, Sefa ;
Ergunes, Gazanfer ;
Taser, O. Faruk .
JOURNAL OF FOOD PROCESS ENGINEERING, 2006, 29 (06) :651-663
[40]   Evaluation of thin-layer models for mushroom (Agaricus bisporus) drying [J].
Xanthopoulos, G. ;
Lambrinos, Gr. ;
Manolopoulou, H. .
DRYING TECHNOLOGY, 2007, 25 (09) :1471-1481