Experimental study and numerical modelling of drying characteristics of apple slices

Abstract The purpose of this work is to quantify the energetic interest of convective and intermittent drying process of natural products. This drying mode has been achieved within a climatic tunnel blower. This laboratory device permitted us to achieve several tests for different conditions of the apple slices drying. In the intermittent case, a variation of the air temperature and air velocity values permitted us to find the most economic velocities for the drying of the apple thin slices. The numerical simulations in the intermittent tests, give us more information on what really happens to the product during periods of interruption. The drying kinetics at the resumption increases with the air temperature. Then, we gain in energy and in overall drying time. These studies show the considerable advantages of the intermittent drying of agricultural products and confirm the preservation of their qualities and the reduction of the drying time.

[1]  Mohamed Sassi,et al.  Modelling of heat and mass transfer in a tunnel dryer , 2006 .

[2]  Frank P. Incropera,et al.  Fundamentals of Heat and Mass Transfer , 1981 .

[3]  L. Bennamoun,et al.  Numerical simulation of drying under variable external conditions: Application to solar drying of seedless grapes , 2006 .

[4]  S. Patankar Numerical Heat Transfer and Fluid Flow , 2018, Lecture Notes in Mechanical Engineering.

[5]  A. Mujumdar Handbook of Industrial Drying , 2020 .

[6]  I. Białobrzewski Simulation of changes in the density of an apple slab during drying , 2006 .

[7]  K. Vafai,et al.  Analysis of Energy and Momentum Transport for Fluid Flow Through a Porous Bed , 1990 .

[8]  Chris T. Kiranoudis,et al.  Heat and mass transfer model building in drying with multiresponse data , 1995 .

[9]  J. Brakel Mass Transfer in Convective Drying , 1980 .

[10]  S. Ben Mabrouk,et al.  Simulation and design of a tunnel drier , 1994 .

[11]  E. Akpinar Determination of suitable thin layer drying curve model for some vegetables and fruits , 2006 .

[12]  C. Geankoplis Transport processes and unit operations , 1978 .

[13]  D. Meel,et al.  Adiabatic convection batch drying with recirculation of air , 1958 .

[14]  G. Crapiste,et al.  DETERMINATION of HEAT TRANSFER COEFFICIENTS DURING DRYING of FOODSTUFFS , 1995 .

[15]  S. Whitaker Simultaneous Heat, Mass, and Momentum Transfer in Porous Media: A Theory of Drying , 1977 .

[16]  Hakan F. Oztop,et al.  Numerical and experimental analysis of moisture transfer for convective drying of some products , 2008 .

[17]  M. Hawlader,et al.  Mathematical modelling and experimental investigation of tropical fruits drying , 2005 .

[18]  Ibrahim Dincer,et al.  Numerical modeling of heat and mass transfer during forced convection drying of rectangular moist objects , 2006 .

[19]  K. Saçılık,et al.  Mathematical modelling of solar tunnel drying of thin layer organic tomato , 2006 .

[20]  Arun S. Mujumdar,et al.  Solar drying of foods: Modeling and numerical simulation , 1997 .

[21]  Dong Sun Lee,et al.  OPTIMIZATION OF OPERATING CONDITIONS IN TUNNEL DRYING OF FOOD , 1993 .

[22]  F. W. Bakker-Arkema,et al.  Drying cereal grains , 1974 .

[23]  F. Zagrouba,et al.  Shrinkage, vitamin C degradation and aroma losses during infra-red drying of apple slices , 2007 .

[24]  C. Ertekin,et al.  Mathematical modeling of thin layer solar drying of sultana grapes , 2001 .

[25]  A. Bejan,et al.  Convection in Porous Media , 1992 .

[26]  A. Bellagi,et al.  Transfer Phenomena During the Drying of a Shrinkable Product: Modeling and Simulation , 2004 .

[27]  Siaw Kiang Chou,et al.  PH—Postharvest Technology: Modelling the Moisture and Temperature Distribution within an Agricultural Product undergoing Time-varying Drying Schemes , 2002 .

[28]  A. Belghith,et al.  Numerical Simulation of the Drying of a Deformable Material : Evaluation of the Diffusion Coefficient , 1995 .

[29]  B. K. Bala,et al.  Drying of hot chilli using solar tunnel drier , 2007 .

[30]  Ibrahim Dincer,et al.  Two-dimensional heat and moisture transfer analysis of a cylindrical moist object subjected to drying: A finite-difference approach , 2003 .

[31]  M. A. Garcı́a,et al.  MATHEMATICAL MODELING FOR FIXED-BED DRYING CONSIDERING HEAT AND MASS TRANSFER AND INTERFACIAL PHENOMENA* , 2001 .

[32]  Zacharias B. Maroulis,et al.  DENSITIES, SHRINKAGE AND POROSITY OF SOME VEGETABLES DURING AIR DRYING , 1994 .