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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storage materials <strong>and</strong> thus it can help to find the optimum thermophysical properties<br />
<strong>of</strong> the storage medium (e.g. optimum melting point range, heat capacity, heat <strong>of</strong><br />
fusion, etc.).<br />
In order to study the<br />
influence <strong>of</strong> the storage<br />
material, one entire year<br />
was simulated <strong>and</strong> weather<br />
data for Al-Arish city was set<br />
as boundary conditions.<br />
Both sensible <strong>and</strong> latent<br />
heat storage media were<br />
simulated, see figure 8.9.<br />
The effect <strong>of</strong> using water as<br />
a sensible heat storage in<br />
the external thermal buffer is<br />
compared with that <strong>of</strong> <strong>PCM</strong><br />
spheres with a melting point<br />
70ºC <strong>and</strong> other<br />
thermophysical properties<br />
indicated in table A.1 in the<br />
appendix.<br />
Figure 8.9: Comparison between water <strong>and</strong><br />
<strong>PCM</strong> as a storage medium<br />
It is evident that the distillate rate using water spheres is typically the same as the<br />
<strong>PCM</strong> storage for small collector area <strong>of</strong> 60 m 2 <strong>and</strong> small storage capacity up to 3m 3 .<br />
Increasing the storage volume beyond the optimum capacity <strong>of</strong> 3m 3 with increasing<br />
the solar collector area, the distillate rate <strong>of</strong> the HDH plant equipped with water<br />
spheres provides more distillate rate than a <strong>PCM</strong> storage.<br />
This behavior is explained as follows. Fixed-bed heat regenerators are usually<br />
cycled between heat storing <strong>and</strong> heat releasing modes. First, a stream containing<br />
charging heat is passed through the bed, where the heat is transferred to the<br />
packing. Later a cold stream is passed through the hot bed in the reverse direction,<br />
thereby heating the stream in the retrieval cycle. In this ideal arrangement, the<br />
packing with the highest temperature in the regenerator contacts the fluid at the exit<br />
from the store. Thus, temperature stratification is always desired to achieve high<br />
thermal performance <strong>of</strong> the cyclic regenerators as it allows the highest attainable<br />
inlet fluid temperature at the interface with the load.<br />
Due to the proposed unidirectional or once-through flow arrangement through the<br />
storage tank, the collector output continuously charges storage <strong>and</strong> energy is<br />
simultaneously withdrawn to h<strong>and</strong>le the dem<strong>and</strong> for the HDH cycle. Under the<br />
transient <strong>and</strong> low solar irradiation intensity at Al-Arish, the daily average inlet hot<br />
water temperature to the storage is relatively low compared to the melting<br />
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