The Relative Activation Energy of Food Materials: Important Parameters to Describe Drying Kinetics

被引:13
作者
Putranto, Aditya [1 ,2 ]
Chen, Xiao Dong [1 ,3 ]
机构
[1] Monash Univ, Dept Chem Engn, Clayton, Vic, Australia
[2] Parahyangan Catholic Univ, Dept Chem Engn, Bandung, Indonesia
[3] Soochow Univ, Sch Chem & Environm Engn, Coll Chem Chem Engn & Mat Sci, Suzhou, Peoples R China
关键词
Drying; Relative activation energy; Reaction engineering approach (REA); Local and global drying rates; REACTION-ENGINEERING APPROACH; MOISTURE TRANSPORT; PARTICULATE; MICROWAVE; CONSTANT; BAKING; MODEL;
D O I
10.1080/10942912.2014.999863
中图分类号
TS2 [食品工业];
学科分类号
0832 ;
摘要
An effective drying model should be accurate and require a small number of experiments to generate the parameters. The relative activation energy of various food materials, important drying kinetic properties used in the reaction engineering approach, is evaluated and summarized. The reaction engineering approach is then implemented to model the global and local drying rates of food materials. By using the relative activation energy, the reaction engineering approach describes the (R-2 higher than 0.99) global drying rate of food materials well. The reaction engineering approach can be coupled with a set of equations of conservation of heat and mass transfer to model the local drying rate of food materials. The relative activation energy is indeed proven to be accurate to model the local drying rate. While the predictions are accurate, the reaction engineering approach is very effective in generating the drying parameters since the relative activation energy can be generated from one accurate drying run. Different drying conditions of the same material with similar initial moisture content would result in the similar relative activation energies. The drying kinetics parameters generated here are readily used for design of new equipment, evaluating the performance of existing dryers, and monitoring the product quality.
引用
收藏
页码:1726 / 1737
页数:12
相关论文
共 28 条
[1]   RETRACTED: EFFECT OF VACUUM, MICROWAVE, AND CONVECTIVE DRYING ON SELECTED PARSLEY QUALITY (Retracted Article) [J].
Akbudak, Nuray ;
Akbudak, Bulent .
INTERNATIONAL JOURNAL OF FOOD PROPERTIES, 2013, 16 (01) :205-215
[2]  
AUDU TOK, 1975, T I CHEM ENG-LOND, V53, P165
[3]   1D and 2D simulations of partially wetted catalyst particles: A focus on heat transfer limitations [J].
Bazer-Bachi, Frederic ;
Augier, Frederic ;
Santos, Bruno .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (09) :1953-1961
[4]  
Bird R B., 2002, Transportphenomena
[5]   Air drying of milk droplet under constant and time-dependent conditions [J].
Chen, XD ;
Lin, SXQ .
AICHE JOURNAL, 2005, 51 (06) :1790-1799
[6]   Fingerprints of the drying behaviour of particulate or thin layer food materials established using a reaction engineering model [J].
Chen, XD ;
Xie, GZ .
FOOD AND BIOPRODUCTS PROCESSING, 1997, 75 (C4) :213-222
[7]   The basics of a reaction engineering approach to modeling air-drying of small droplets or thin-layer materials [J].
Chen, Xiao Dong .
DRYING TECHNOLOGY, 2008, 26 (06) :627-639
[8]   Moisture diffusivity in food and biological materials [J].
Chen, Xiao Dong .
DRYING TECHNOLOGY, 2007, 25 (7-8) :1203-1213
[9]   A mathematical model of the self-heating of spray-dried food powders containing fat, protein, sugar and moisture [J].
Chong, LV ;
Chen, XD .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (19) :4165-4178
[10]   TRANSPORT OF VOLATILE CHLORINATED HYDROCARBONS IN UNSATURATED AGGREGATED MEDIA [J].
GIMMI, T ;
FLUHLER, H ;
STUDER, B ;
RASMUSON, A .
WATER AIR AND SOIL POLLUTION, 1993, 68 (1-2) :291-305