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Experimental and Numerical Analysis of a PCM-Supported ...

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The apparent heat capacity method is adopted in this study, since the temperature<br />

field is the primary dependent variable that can be derived directly from the solution.<br />

The apparent heat capacity assumes that the phase change occurs over a small<br />

temperature interval rather than at a sharp melting temperature. However, in the<br />

present study, all the three types <strong>of</strong> <strong>PCM</strong> packing media have a melting temperature<br />

interval <strong>of</strong> 2°C around the specified melting points according to the manufacturer’s<br />

data. Civan <strong>and</strong> Sliepcevich [18] have formulated the energy equation for a twophase<br />

system <strong>of</strong> a pure substancea in a semi-infinite media undergoing phase<br />

change, as depicted in figure (4.7), as follows:<br />

<br />

<br />

h <br />

h <br />

h <br />

<br />

2<br />

<br />

T<br />

2<br />

hV h V <br />

k<br />

k<br />

k<br />

<br />

T<br />

0<br />

1<br />

<br />

<br />

<br />

<br />

1<br />

1<br />

1<br />

T<br />

2<br />

1<br />

2<br />

<br />

2<br />

2<br />

T<br />

2<br />

2<br />

<br />

1<br />

<br />

<br />

1<br />

<br />

2<br />

h h<br />

1<br />

1<br />

1<br />

2<br />

2<br />

d1<br />

<br />

T<br />

<br />

<br />

dT <br />

t<br />

Dp<br />

Dt<br />

(4.60)<br />

The energy equation in the<br />

form <strong>of</strong> equation (4.60) is<br />

called an apparent heat<br />

capacity formulation in which<br />

the quantities enclosed in the<br />

braces preceding T/t<br />

represent an "apparent"<br />

volumetric heat capacity.<br />

Since the volumetric latent<br />

heat effect <strong>of</strong> phase change,<br />

(ρ 1 h 1 –ρ 2 h 2 ), is included in the<br />

apparent volumetric heat<br />

capacity definition, this<br />

formulation allows for a<br />

continuous treatment <strong>of</strong> a system involving phase transfer. In addition, it doesn’t<br />

require the solution <strong>of</strong> separate, single-phase equations for each <strong>of</strong> the phases.<br />

For simplification Civan <strong>and</strong> Sliepcevich [18] assumed that the pressure is<br />

constant, the phases are isotropic <strong>and</strong> homogeneous, the phase densities are equal,<br />

<strong>and</strong> there is no motion in either <strong>of</strong> the phases. Accordingly, equation (4.60) reduces<br />

to:<br />

in which<br />

Figure 4.7: Schematic <strong>of</strong> a semi-infinite<br />

domain undergoing phase change<br />

T<br />

<br />

T<br />

<br />

c<br />

k<br />

<br />

(4.61)<br />

t<br />

x<br />

<br />

x<br />

<br />

90

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