Experimental and fundamental critical analysis of diffusion model of airflow drying

被引:23
作者
Nguyen, T. H. [1 ,2 ,4 ]
Lanoiselle, J. -L. [1 ]
Allaf, T. [3 ]
Allaf, K. [2 ]
机构
[1] Univ Bretagne Sud, CNRS, FRE 3744, IRDL, Pontivy, France
[2] Univ La Rochelle, LaSIE, CNRS, UMR 7356, La Rochelle, France
[3] ABCAR DIC Proc, La Rochelle, France
[4] Hanoi Univ Sci & Technol, 1 Dai Co Viet, Hanoi, Vietnam
关键词
Agro-material; critical airflow velocity; drying kinetic model; heat transfer; mass transfer; EFFECTIVE MOISTURE DIFFUSIVITY; PRESSURE-DROP TECHNOLOGY; ENERGY-CONSUMPTION; FORCED-CONVECTION; SIMULTANEOUS HEAT; MASS-TRANSFER; HOT AIR; KINETICS; TEMPERATURE; FRUITS;
D O I
10.1080/07373937.2016.1155052
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Scientific literature of agromaterial drying present contradictory conclusions in terms of the kinetic effect of airflow velocity. Some authors confirmed that it does not trigger any modification of drying, while some articles tried to establish empirical models of the effective diffusivity D-eff versus the airflow velocity, what is fundamentally erroneous. By analyzing internal and external transfer phenomena, this research aimed at recognizing that once air velocity is higher than a critical airflow velocity (CAV), the internal transfers become the limiting phenomenon. CAV depends on the effective diffusivity and the product size. It was calculated in the cases of two studied raw materials (apple and carrot), differently textured by instant controlled pressure drop (DIC). Values of CAV greatly depend on diffusivity of water within the matrix. At temperature T-40 degrees C, they were 1 m/s for untreated carrot and 2.1 m/s for DIC-textured carrot, whose D-eff values were 1.31 and about 3 x 10(-10) m(2)/s, respectively. Also, at temperature T=40 degrees C, they were 2.1 m/s for untreated apple and 3 m/s for DIC-textured apple, whose D-eff were 1.4 and about 10.4. 10(-10) m(2)/s, respectively.
引用
收藏
页码:1884 / 1899
页数:16
相关论文
共 81 条
[1]  
Abbaszadeh A, 2012, IRAN J CHEM CHEM ENG, V31, P75
[2]   Influence of drying conditions on the effective moisture diffusivity, energy of activation and energy consumption during the thin-layer drying of berberis fruit (Berberidaceae) [J].
Aghbashlo, Mortaza ;
Kianmehr, Mohammad H. ;
Samimi-Akhijahani, Hadi .
ENERGY CONVERSION AND MANAGEMENT, 2008, 49 (10) :2865-2871
[3]  
Aghfir M., 2007, JITH 2007, P5
[4]   Caracterisation and modelisation of drying of three tropical products: cassava, ginger and okros [J].
Ahouannou, C ;
Jannot, Y ;
Lips, B ;
Lallemand, A .
SCIENCES DES ALIMENTS, 2000, 20 (4-5) :413-432
[5]   Moisture transfer models for slabs drying [J].
Akpinar, EK ;
Dincer, I .
INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2005, 32 (1-2) :80-93
[6]   Fruits & Vegetables Drying Combining Hot Air, DIC Technology and Microwaves [J].
Al Haddad, M. ;
Mounir, S. ;
Sobolik, V. ;
Allaf, K. .
INTERNATIONAL JOURNAL OF FOOD ENGINEERING, 2008, 4 (06)
[7]   Improving the Drying of Onion Using the Instant Controlled Pressure Drop Technology [J].
Albitar, Nsren ;
Mounir, Sabah ;
Besombes, Colette ;
Allaf, Karim .
DRYING TECHNOLOGY, 2011, 29 (09) :993-1001
[8]  
Allaf K., 1988, FEASIBILITY STUDY NE
[9]  
Allaf K., 1993, ALLAF K, P14
[10]  
Allaf K., 2012, TECHNIQUES INGENIE F, VF3005, P18