Experimental and Numerical Analysis of a PCM-Supported ...
Experimental and Numerical Analysis of a PCM-Supported ...
Experimental and Numerical Analysis of a PCM-Supported ...
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Klausner <strong>and</strong> Mei [136] described a diffusion driven desalination (DDD) process for<br />
mineralized water distillation. The investigations focused on optimization <strong>of</strong> the DDD<br />
system both experimentally <strong>and</strong> numerically. A practical difficulty that arises in film<br />
condensation is that heat transfer is tremendously degraded in the presence <strong>of</strong> noncondensable<br />
gases. In order to overcome this problem, they used a direct contact<br />
condenser. For this application the warm fresh water discharging the direct contact<br />
condenser is chilled in a conventional shell- <strong>and</strong> -tube heat exchanger using cooling<br />
seawater water. A portion <strong>of</strong> the chilled fresh water is directed back to the direct<br />
contact condenser. The distillate is discarded as the fresh water production.<br />
Haddad et al. [140] presented another alternative condensing system for basin type<br />
solar stills as depicted in Figure (2.18). An external condenser, constructed as a<br />
packed bed storage tank filled with sensible heat storage material (rocks), was<br />
integrated with the still. The packed bed condenser was cooled during the night,<br />
using a radiative cooling panel by circulating water into the packed bed condenser<br />
<strong>and</strong> the radiative cooling panel.<br />
The cooling panel utilized the cold effective sky temperature, which normally is 10-<br />
25ºC lower than the ambient temperature, in order to cool the rock domain in the<br />
packed bed storage during the night. The packed bed tank is installed at a higher<br />
level than the solar still level <strong>and</strong> is connected to the solar still by a vertical duct. At<br />
the beginning <strong>of</strong> the day light, the tank temperature was lowered to nearly effective<br />
sky temperature <strong>and</strong> water was evacuated from the storage tank. By buoyancy<br />
forces <strong>and</strong> reduced back pressure created in the condenser, the vapor was sucked<br />
through the duct between the still <strong>and</strong> the condenser.<br />
Several advantages were reported for this system. The heat loss was reduced since<br />
the temperature inside the still was lowered, the low temperature <strong>of</strong> the condenser<br />
enhanced the condensation rate, <strong>and</strong> consequently this lowered the vapor partial<br />
pressure in the still resulting in higher evaporation rate.<br />
When humid air is fed into a dry porous medium which is at a lower temperature, the<br />
humidity condenses <strong>and</strong> the condensate trickles down by gravity. As elapsed time<br />
increases <strong>and</strong> a condensate is formed within the porous medium, the temperature<br />
difference between the humid air <strong>and</strong> porous medium decreases <strong>and</strong> the<br />
condensate flow rate diminishes.<br />
Vafi <strong>and</strong> Sozen [13] developed a model for analyzing the behavior <strong>of</strong> a packed bed<br />
<strong>of</strong> encapsulated phase change material (<strong>PCM</strong>) <strong>and</strong> a condensing flow through it.<br />
Thermal charging <strong>of</strong> the packed bed was analyzed <strong>and</strong> compared for a sensible heat<br />
storage material as well as for different <strong>PCM</strong> storages. It was found that storage <strong>of</strong><br />
thermal energy <strong>of</strong> condensation would be most efficient when a <strong>PCM</strong> with melting<br />
temperature close to the lower limit <strong>of</strong> the operation temperature range chosen. It<br />
was also found that for a given particle size <strong>and</strong> nominal particle Reynolds number,<br />
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