Mathematical modeling of microwave-assisted inert medium fluidized bed drying of cylindrical carrot samples

被引:51
作者
Souraki, B. Abbasi [1 ]
Andres, A. [2 ]
Mowla, D. [3 ]
机构
[1] Guilan Univ, Fac Engn, Dept Chem Engn, Rasht, Iran
[2] Univ Politecn Valencia, Inst Food Engn Dev, E-46071 Valencia, Spain
[3] Shiraz Univ, Dept Chem Engn, Shiraz, Iran
关键词
Fluidization; Heat and mass transfer; Glass beads; Penetration depth; Temperature and moisture distribution; TRANSFER-COEFFICIENTS; MASS-TRANSFER; HEAT; SHRINKAGE; DIMENSIONS; SIMULATION; DENSITY;
D O I
10.1016/j.cep.2008.04.005
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Drying behavior of cylindrical samples of carrot was investigated in a microwave-assisted fluidized bed of inert particles. A pilot-scale microwave-assisted fluidized bed dryer was set up for this purpose. Glass beads particles were used as inert materials. Based on the simultaneous heat and mass transfer, a mathematical model was proposed for predicting the temperature and moisture distribution in the drying sample. Considering the carrot radiuses and the penetration depth of the electromagnetic waves, a uniform electric field strength distribution within the drying material was assumed in the proposed model. The heat loss due to surface evaporative cooling was also considered at the external boundaries. A numerical solution was developed for the proposed model using an implicit finite difference method in one-dimensional system. The model was validated by comparing the predicted data with the experimental data, obtained from different cylindrical carrot samples during drying. The effects of microwave power density and also drying air temperature on the moisture and temperature profiles were investigated. (c) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:296 / 305
页数:10
相关论文
共 43 条
[21]  
HATAMIPOUR MS, 2006, T ICHEME, V84, P1
[22]  
Holman J., 2002, HEAT TRANSFER
[23]   MODEL FOR OXIDATIVE THERMAL DECOMPOSITION OF STARCH IN A FLUIDIZED REACTOR [J].
JARIWALA, SL ;
HOELSCHE.HE .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1970, 9 (02) :278-&
[24]   Modelling and simulation of continuous and intermittent radio frequency-assisted fluidized bed drying of grains [J].
Jumah, R .
FOOD AND BIOPRODUCTS PROCESSING, 2005, 83 (C3) :203-210
[25]   Microwave and air drying I. Fundamental considerations and assumptions for the simplified thermal calculations of volumetric power absorption [J].
Khraisheh, MAM ;
Cooper, TJR ;
Magee, TRA .
JOURNAL OF FOOD ENGINEERING, 1997, 33 (1-2) :207-219
[26]   EQUILIBRIUM MOISTURE-CONTENT AND HEAT OF DESORPTION OF SOME VEGETABLES [J].
KIRANOUDIS, CT ;
MAROULIS, ZB ;
TSAMI, E ;
MARINOSKOURIS, D .
JOURNAL OF FOOD ENGINEERING, 1993, 20 (01) :55-74
[27]   DETERMINATION OF TRANSFER-COEFFICIENTS BY PSYCHROMETRY [J].
KONDJOYAN, A ;
DAUDIN, JD .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1993, 36 (07) :1807-1818
[28]  
Lee DH, 1999, CHEM ENG TECHNOL, V22, P443, DOI 10.1002/(SICI)1521-4125(199905)22:5<443::AID-CEAT443>3.0.CO
[29]  
2-L
[30]  
LEE DH, 1993, CHEM ENG TECHNOL, V16, P263