Mathematical modeling of air-impingement cooling of finite slab shaped objects and effect of spatial variation of heat transfer coefficient

Abstract In industrial cooling systems, an important goal is to reduce the temperature of foods as quickly as possible. Heat transfer coefficient ( h -value) is a parameter that to be increased to reduce the cooling time in convective cooling techniques. Higher h -values may be obtained by moving air at high velocities, such as those obtained with impingement systems. The objective of this research was to develop and validate a numerical model to predict the transient time-temperature change during cooling of slab shapes under impinged air conditions and to investigate the spatial variation of h -value over the surface. A three-dimensional explicit finite difference mathematical model was developed to handle the spatial variation, and a plexi-glass slab (16 × 12 × 1 cm), insulated on the bottom surface by polyurethane foam (4 cm in thickness) was used in the validation studies. Type-T 36 gauge thermocouples were inserted into the plexi-glass. Then, the slab was left in an oven until a uniform temperature distribution was obtained and placed under an impinged air jet for cooling. Model validation studies were accomplished at impingement nozzle (1.5 cm in diameter) exit air velocities of 14 and 28 m/s. For all experiments, excellent agreement was obtained between the predictions and the experimental results, and spatial variation of h -value was determined to be an important factor to handle in impingement modeling studies.

[1]  C. E. Walker,et al.  Impingement in food processing , 1998 .

[2]  M. Houška,et al.  Mass transfer experiments on vacuum cooling of selected pre-cooked solid foods , 2002 .

[3]  Mukund V. Karwe,et al.  Fluid Flow and Heat Transfer in Air Jet Impingement in Food Processing , 2004 .

[4]  Coleman duP. Donaldson,et al.  A study of free jet impingement. Part 2. Free jet turbulent structure and impingement heat transfer , 1971, Journal of Fluid Mechanics.

[5]  Josse De Baerdemaeker,et al.  The local surface heat transfer coefficient in thermal food process calculations: A CFD approach , 1997 .

[6]  T. C. Chawla Annual review of numerical fluid mechanics and heat transfer. Volume 1 , 1986 .

[7]  Lp Ketteringham,et al.  The use of high thermal conductivity inserts to improve the cooling of cooked foods , 2000 .

[8]  C. E. Walker,et al.  Cake Baking in Conventional, Impingement and Hybrid Ovens , 1996 .

[9]  B. Nicolai,et al.  Sensitivity analysis with respect to the surface heat transfer coefficient as applied to thermal process calculations , 1996 .

[10]  Khe V. Chau,et al.  A Finite‐Difference Model for Heat and Mass Transfer in Products with Internal Heat Generation and Transpiration , 1990 .

[11]  Hitoshi Fujimoto,et al.  Numerical simulation of convective heat transfer to a radial free surface jet impinging on a hot solid , 1999 .

[12]  K. V. Chau,et al.  Explicit Finite Difference Methods for Heat Transfer Simulation and Thermal Process Design , 1997 .

[13]  Robert Gardon,et al.  Heat Transfer Characteristics of Impinging Two-Dimensional Air Jets , 1966 .

[14]  H. Martin Heat and Mass Transfer between Impinging Gas Jets and Solid Surfaces , 1977 .

[15]  Da-Wen Sun,et al.  Experimental investigation of performance of vacuum cooling for commercial large cooked meat joints , 2004 .

[16]  R. Singh,et al.  Spatial Variation of Convective Heat Transfer Coefficient in Air Impingement Applications , 2003 .

[17]  A. Mujumdar,et al.  NUMERICAL FLOW AND HEAT TRANSFER UNDER IMPINGING JETS: A REVIEW , 1989 .

[18]  Impact of impingement on cooking time and food quality , 2000 .

[19]  Kevin Cronin,et al.  Analysis of random variability in biscuit cooling , 2002 .