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Thermal Food Processing

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Heat and Mass Transfer in <strong>Thermal</strong> <strong>Food</strong> <strong>Processing</strong> 59<br />

they are cheap in terms of computation time. Predictions by general codes based<br />

on the k-e model are often very different from experimental data. Because the shape<br />

of many food products is very complex, the experimental determination of heat<br />

transfer coefficients remains at the time quicker and much more reliable than<br />

predictions. The calculation based on the current CFD codes has to be used with<br />

caution, and more research is needed to improve near-wall modeling, particularly<br />

around blunt bodies placed in a turbulent flow. A full treatment of turbulence would<br />

require more complex models, such as large eddy simulations (LESs) and Reynolds<br />

stress models (RSMs). However, LES models require large computing resources<br />

and are not of use as general-purpose tools. Because the RSM accounts for the<br />

effects of streamline curvature, swirl, rotation, and rapid changes in strain rate in<br />

a more rigorous manner than the k-e models, it has greater potential to give accurate<br />

predictions for complex flows. However, the fidelity of RSM predictions is still<br />

limited by the closure assumptions used to model various terms in the exact transport<br />

equations for the Reynolds stresses. The modeling of the pressure strain and<br />

dissipation rate terms is particularly challenging. Therefore, the RSM with additional<br />

computational expense might not always yield results that are clearly superior<br />

to simpler models in all cases of flows. The mathematical expressions of turbulence<br />

models may be quite complicated, and they contain adjustable constants that need<br />

to be determined as best-fit values from experimental data. Therefore, any application<br />

of a turbulence model should not go beyond the data range. Besides, the current<br />

turbulence models can be used to guide the development of other models through<br />

comparative studies.<br />

2.4.2 JUDGMENT OF ASSUMPTIONS IN MODELS<br />

Accurate modeling of a thermal process of foods is complex. For simplification<br />

and saving of computational time, some assumptions made in the modeling are<br />

necessary. Most assumptions come from the geometrical dimension and shape,<br />

surface heat, and mass transfer coefficients, food materials properties, and volume<br />

change during thermal processes. Before simulation, whether or not to use a<br />

model of coupled heat and mass transfer or coupled heat transfer and fluid flow<br />

should also be determined.<br />

Sensitivity analysis can make a judgment for the acceptability of an assumption<br />

in the modeling. Some research has been carried out to investigate the sensitivity<br />

of variables of interest, such as temperature on operating conditions of a thermal<br />

system and thermal properties of foods. 99–107 Findings from the research include<br />

that the time- and location-dependent variations in operating conditions, such as<br />

variable temperature and surface heat transfer coefficient, cause the detachment of<br />

the thermal and geometric centers during processing of foods. 99 For simulating a<br />

thermal process with a low heat transfer coefficient, small deviations in the coefficient<br />

may result in large deviations in the core temperature of foods. 100,107 The<br />

disturbances of different means, but with the same scale of fluctuation in processing<br />

the medium temperature, resulted in comparable center temperature variation. 103<br />

For a typical sterilization process, it was found that thermal-physical properties

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