Modeling the forced-air cooling process of fresh strawberry packages, Part I: Numerical model

A numerical analysis of the forced-air cooling process of retail packages of strawberries was performed by solving the conservation equations of mass, momentum and energy within the system. The results showed that the heterogeneity of the cooling process is largely influenced by the structure and design of the packaging system (individual clamshell packages and trays). On average 75 ± 2% of the total airflow forced through the system bypassed the clamshells, and 46 ± 5% of the flow rate forced through clamshells bypassed the strawberries. After 1 h of cooling, the average-fruit-temperature per clamshell ranged from 2.4 °C to 8.3 °C between the first and last clamshells along the main flow direction. Within these clamshells, the maximum differences in the volume-average temperature of individual fruits reached 3.5 °C and 5.1 °C, respectively. The results show the potential use of this numerical approach as a design tool to optimize the forced-air cooling process of horticultural products.

[1]  Dennis R. Heldman,et al.  Introduction to food engineering , 1984 .

[2]  Anthony G. Dixon,et al.  CFD study of fluid flow and wall heat transfer in a fixed bed of spheres , 2004 .

[3]  Maria Jose Ferrua Modeling the forced-air cooling process of fresh horticultural products , 2007 .

[4]  J.-P. Emond,et al.  Study of Parameters Affecting Cooling Rate and Temperature Distribution in Forced-air Precooling of Strawberry , 1996 .

[5]  Qian Zou,et al.  A CFD modeling system for airflow and heat transfer in ventilated packaging for fresh foods:: II. Computational solution, software development, and model testing , 2006 .

[6]  R. P. Singh,et al.  A nonintrusive flow measurement technique to validate the simulated laminar fluid flow in a packed container with vented walls. , 2008 .

[7]  R.G.M. van der Sman Prediction of airflow through a vented box by the Darcy–Forchheimer equation , 2002 .

[8]  Florian Huber,et al.  Numerical simulations of single phase reacting flows in randomly packed fixed-bed reactors and experimental validation , 2003 .

[9]  Denis Flick,et al.  Modelling transport phenomena in refrigerated food bulks, packages and stacks: basics and advances , 2006 .

[10]  D. Tanner,et al.  A generalised mathematical modelling methodology for the design of horticultural food packages exposed to refrigerated conditions Part 2. Heat transfer modelling and testing , 2002 .

[11]  Adel A. Kader,et al.  Post Harvest Technology of Horticultural Crops , 1991 .

[12]  F. H. Fockens,et al.  Biophysical properties of horticultural products as related to loss of moisture during cooling down , 1972 .

[13]  R. Paul Singh,et al.  Modeling Airflow through Vented Packages Containing Horticultural Products , 2007 .

[14]  Anthony G. Dixon,et al.  Comparison of CFD simulations to experiment for convective heat transfer in a gas-solid fixed bed , 2001 .

[15]  J. L. Woods Moisture loss from fruits and vegetables. , 1990 .

[16]  Arnab Sarkar,et al.  COMMERCIAL-SCALE FORCED-AIR COOLING OF PACKAGED STRAWBERRIES , 2004 .

[17]  Anthony G. Dixon,et al.  Computational fluid dynamics simulations of fluid flow and heat transfer at the wall-particle contact points in a fixed-bed reactor , 1999 .

[18]  Eduard Egusquiza,et al.  Influence of the turbulence model in CFD modeling of wall-to-fluid heat transfer in packed beds , 2005 .

[19]  Francisco J. Trujillo,et al.  A computational fluid dynamic model of the heat and moisture transfer during beef chilling , 2006 .

[20]  Da-Wen Sun,et al.  Computational fluid dynamics in food processing , 2007 .

[21]  Stephen Whitaker,et al.  ADVANCES IN THEORY OF FLUID MOTION IN POROUS MEDIA , 1969 .

[22]  G. Alvarez,et al.  Analysis of heterogeneous cooling of agricultural products inside bins Part I: aerodynamic study , 1999 .

[23]  A. C Cleland,et al.  Prediction of chilling times of foods in situations where evaporative cooling is significant : Part 2. Experimental testing , 1998 .

[24]  Martine Baelmans,et al.  Effect of process, box and product properties on heat and mass transfer during cooling of horticultural products in pallet boxes , 2001 .

[25]  D. Spalding,et al.  A calculation procedure for heat, mass and momentum transfer in three-dimensional parabolic flows , 1972 .

[26]  A. C Cleland,et al.  Prediction of chilling times of foods in situations where evaporative cooling is significant—Part 1. Method development , 1998 .

[27]  A. C Cleland,et al.  A generalised mathematical modelling methodology for design of horticultural food packages exposed to refrigerated conditions: part 1, formulation , 2002 .

[28]  P. Verboven,et al.  A CONTINUUM MODEL FOR AIRFLOW, HEAT AND MASS TRANSFER IN BULK OF CHICORY ROOTS , 2003 .

[29]  Qian Zou,et al.  A CFD modeling system for airflow and heat transfer in ventilated packaging for fresh foods: I. Initial analysis and development of mathematical models , 2006 .

[30]  Dean Burfoot,et al.  Simulating the bulk storage of foodstuffs , 1999 .

[31]  R. P. Singh,et al.  Modeling the forced-air cooling process of fresh strawberry packages, Part II: Experimental validation of the flow model , 2009 .

[32]  S. Bruin,et al.  Heat and mass transfer during cooling and storage of agricultural products , 1982 .

[33]  Robert E. Wilson,et al.  Fundamentals of momentum, heat, and mass transfer , 1969 .

[34]  J. K. Sherwani,et al.  Land and Water Use , 1963 .

[35]  Denis Flick,et al.  Two-dimensional simulation of turbulent flow and transfer through stacked spheres , 2003 .