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Thermal Food Processing

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

than one of these mechanisms is involved. In some processes, both heat and mass<br />

transfers occur simultaneously. It is important to understand the heat and mass<br />

transfer mechanism for the improvement of existing food thermal processes and<br />

for the development of new and better processes.<br />

The physical laws of heat and mass transfer have widely been used to describe<br />

food thermal processes, producing a large number of mathematical models. Some<br />

assumptions, such as simplified geometrical shape, constant thermal physical properties,<br />

constant surface heat, and mass transfer coefficients, and no volume change<br />

during processing, were widely used in modeling. However, more research should<br />

be conducted to justify the acceptability of those assumptions and to improve the<br />

accuracy of models by finding more information on surface heat and mass transfer<br />

coefficients, food properties, and shrinkage during processing. Before heat and mass<br />

transfer models can become a quantitative tool for correctly analyzing thermal<br />

processes, determination of thermal physical propensities and surface mass and<br />

heat transfer coefficients remains an important area to be studied.<br />

NOMENCLATURE<br />

A Area (m2 )<br />

C Concentration (kg/m3 or kmol/m3 )<br />

c Specific heat capacity (kJ/kg K)<br />

C * Concentration in equilibrium with the bulk gas partial<br />

pressure (kg/m3 or kmol/m3 )<br />

d Diameter (m)<br />

D Mass diffusivity (m2 /sec)<br />

D0 Preexponential factor in Arrhenius equation (m2 /sec)<br />

Dg Mass diffusivity in the gas phase (kmol/N m sec)<br />

Dl Mass diffusivity in the liquid phase (m2 /sec)<br />

E Electrical field strength (V/m)<br />

e Emissivity (–)<br />

Ea Activation energy (J/kg mol)<br />

F12 View factor, fraction of radiation leaving surface 1 and<br />

arriving at surface 2 (–)<br />

g Acceleration due to gravity (m/sec2 )<br />

H Enthalpy (J/kg) or Henry’s constant (J/kmol)<br />

h Heat transfer coefficient (W/m2 K)<br />

hb Boiling heat transfer coefficient (W/m2 K)<br />

hc Convection heat transfer coefficient (W/m2 K)<br />

hcd Condensation heat transfer coefficient (W/m2 K)<br />

hr Radiation heat transfer coefficient (W/m2 K)<br />

J Diffusive flow rate (kg/m2 sec or kmol/m2 sec)<br />

k <strong>Thermal</strong> conductivity (W/mK)<br />

Kg Gas mass transfer coefficient (kmol/N sec)

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