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Thermal Food Processing

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148 <strong>Thermal</strong> <strong>Food</strong> <strong>Processing</strong>: New Technologies and Quality Issues<br />

engineering, but have been applied to an ever-increasing list of industrial situations,<br />

including food and bioprocessing applications. In thermal processing, CFD<br />

packages can be used not only to analyze an existing process, but also to optimize<br />

the process and to explore scenarios of new, more effective operations. There is<br />

no question that food processing problems are complex and also, in most situations,<br />

involve transient, three-dimensional conditions. Analytical approximation<br />

and solutions may no longer be appropriate, and the CFD approach combined<br />

with chemical or biochemical kinetics equations is necessary. So far, only very<br />

limited thermal processing problems have been investigated using CFD, so there<br />

is a scope of further development that will no doubt be beneficial for the improvement<br />

and modernization of the current food industry to make it safer for consumers.<br />

Though powerful in many ways, in using the CFD approach, it is always<br />

necessary to be able to understand the underlined physics and chemistry in simple<br />

terms and indeed to conduct appropriate experiments to validate the calculations<br />

for the situations of interest.<br />

NOMENCLATURE<br />

A Preexponential factor (sec –1 )<br />

c Concentration (mol·m –3 or kg·m –3 )<br />

Cp Specific heat capacity (J·kg –1 ·K –1 )<br />

d Diameter or characteristic dimension (m)<br />

DT Decimal reduction time at temperature T (min)<br />

D Diffusion coefficient (m2 ·sec –1 )<br />

E Activation energy (J·mol –1 )<br />

F <strong>Thermal</strong> death time (min)<br />

Gr Grashof number,<br />

g Gravity acceleration (m·sec –2 )<br />

H Height of the can (m)<br />

h Heat transfer coefficient (W· m –2 · K –1 )<br />

k <strong>Thermal</strong> conductivity (W·m –1 ·K –1 )<br />

Nu Nusselt number,<br />

p Pressure (N·m –2 or Pa)<br />

Pr Prandtl number,<br />

r Radius or radial coordinate (m)<br />

R Radius (m) or the universal gas constant (J·mol –1 ·K –1 d3ρ2gβ⋅∆T Gr =<br />

µ 2<br />

Nu = h d<br />

k<br />

)<br />

T Temperature (°C)<br />

⋅<br />

Cp<br />

⋅<br />

Pr =<br />

k<br />

µ

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