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

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The enthalpy <strong>and</strong> humidity <strong>of</strong> the saturated air depend on its temperature at constant<br />

pressure <strong>and</strong> can be calculated using the following empirical correlation [132];<br />

3<br />

a<br />

2<br />

a<br />

h 0.00585T<br />

0.497T<br />

19.87T<br />

207.61<br />

(2.10)<br />

a<br />

3<br />

a<br />

2<br />

a<br />

a<br />

6<br />

4<br />

3<br />

w 2.19*10 T 1.85*10<br />

T 7.06*10 T 0.077<br />

(2.11)<br />

a<br />

where T a is the saturated air temperature in ºC.<br />

HDH unit sizing<br />

As a common practice, the number <strong>of</strong> transfer units (NTU) will be used as a measure<br />

for the humidifier size (see appendix D1), while the condenser is assumed to have<br />

the same size as the humidifier for symmetrical design <strong>of</strong> the HDH unit. The NTU<br />

can be related to the performance characteristic (KaV/L) (see appendix D1). Based<br />

on the steady state experimental analysis, Nawayseh et al. [159] has developed the<br />

following correlation for forced convection:<br />

a<br />

0.16<br />

KaV / L 0.52( L/<br />

G)<br />

for forced draft 0.1< L/G

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