Abstract

This work aims to evaluate the performance of a numerical modeling for prediction of food freezing times by comparing numerical with experimental results. A one-dimensional heat diffusion model including temperature dependent thermophysical properties, sudden variations of thermophysical properties during phase change and surface mass transfer was approximated using the finite differences method. The thermophysical properties of foods were modeled as functions of food composition, temperature and phase, using Choi and Okos correlations (Choi & Okos, 1986). Simple geometries such as thin slab, long cylinder and sphere were modeled, and the numerical results were compared with experimental data obtained in a pilot scale freezing tunnel. Numerical simulations were performed for some selected foods, namely sausages, potatoes, hamburger and cheese, in different geometries and sizes. The boundary conditions of the freezing surfaces were of heat and mass convection. The heat transfer coefficients were taken after usual correlations for these geometries. The mass transfer modeling was done using mass convection correlations, considering a known surface wetness. It was found that mass transfer due to moisture evaporation, thermodependency of properties and an accurate estimate for the heat transfer coefficient were crucial elements for the correct prediction of freezing curves. The numerical results were only able to predict the experimental freezing curve by adjusting the theoretical value of the heat transfer coefficient by a factor, varying from 0.7 to 1.3 in most cases, with some outliers up to 2.4. This means that although the heat conduction inside the food itself seemed to generate reasonable food freezing rates, the convection coefficients produced experimentally seemed to vary wildly from the ones predicted in the theoretical relationships. Therefore, one should be very keen of the magnitude of the convection coefficient while performing predictions for a given food freezing application problem. Keywords: Food freezing, Transient heat conduction, Finite difference, Models for food thermal properties

Highlights

  • Food freezing as a conservation process plays an important role in the global food industry

  • Even though it is so widely used, the complexity involved in the process makes it very difficult for one to predict the food freezing times accurately

  • The time of freezing is perhaps the most important variable to know before building a food freezing unit

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Summary

Introduction

Food freezing as a conservation process plays an important role in the global food industry. A major issue when dealing with modeling of food thermal processes is dealing with the wildly varying food thermophysical properties, which are dependent on food temperature and composition These properties experience large and sudden changes during freezing, mainly because the formation of ice crystals. As the use of realistic models for thermophysical properties is a key point to achieve reliable solutions, the use of analytical methods to determine freezing times is highly impaired. Empirical correlations, such as those developed by Plank (apud Stoeker, 2004) and Pham (1986) produce results that might not be much accurate as they do not consider all the mechanisms involved in the process of freezing. The results produced by these two correlations will be compared with the numerical method presented here

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