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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packing are its heat <strong>and</strong> mass transfer performance, the quality <strong>of</strong> water, pressure<br />
drop, cost <strong>and</strong> durability [149]. Al-Hallaj <strong>and</strong> Selman [2] summarized the main<br />
technical results reported by various research groups. Almost all the investigators<br />
state that the effect <strong>of</strong> water flow rate on the performance <strong>of</strong> the unit is important.<br />
The effect <strong>of</strong> air flow rate on productivity is termed insignificant by all authors except<br />
Younis et al [135]. Also, all researchers express preference for natural convection<br />
since air flow rate has no significant effect on unit productivity. However, forced<br />
circulation could be feasible with another cost-effective source <strong>of</strong> energy such as<br />
wind energy. The effect <strong>of</strong> air flow ate is only noticeable at temperatures around<br />
50 o C, as reported by Al-Hallaj et al [132].<br />
It is concluded that HDH technology has great promise for decentralized small-scale<br />
water production applications, although additional research <strong>and</strong> development is<br />
needed for improving system efficiency <strong>and</strong> reducing capital cost [149]. Al-Hallaj <strong>and</strong><br />
Selman [2] attributed the higher production cost <strong>of</strong> HDH systems compared with<br />
reverse osmosis (RO) <strong>and</strong> multi-stage flash evaporation (MSF) units to three main<br />
reasons:<br />
1. HDH units rely upon natural draft which results in low heat <strong>and</strong> mass transfer<br />
coefficients <strong>and</strong> a large surface area for the humidifier<br />
2. The HDH systems are applied for small desalination capacities <strong>and</strong> scale<br />
economies can not be realized in capital investment<br />
3. Film condensation over tubes is typically used, which is extremely inefficient<br />
when non condensable gases present. Thus, a much larger condenser area<br />
is required, <strong>and</strong> the condenser accounts for the majority <strong>of</strong> the capital cost.<br />
2.8.9 Conclusion <strong>and</strong> spot light<br />
The extensive literature on HDH systems reveals that in spite <strong>of</strong> the large <strong>and</strong><br />
valuable amount <strong>of</strong> research <strong>and</strong> development effort invested, there is still room for<br />
development <strong>and</strong> optimization <strong>of</strong> such systems. To improve the performance <strong>of</strong> HDH<br />
systems, previous studies have investigated various configurations <strong>of</strong> the HDH<br />
cycle. These efforts focused on improving heat <strong>and</strong> mass exchanger designs or<br />
using multi effect humidification <strong>of</strong> air. A multitude <strong>of</strong> alternative water-heated HDH<br />
systems has been presented. However, few interesting approaches focused on<br />
direct air heating compared to direct water heating, which proved to be much more<br />
energy efficient than air heated systems. The multi effects <strong>of</strong> heating/humidification<br />
<strong>of</strong> air which was investigated by Chafik [155], the combination <strong>of</strong> air heating <strong>and</strong><br />
water heating which was presented by Abdel-Monem [145], <strong>and</strong> the hybrid latent<br />
heat storage <strong>and</strong> spray flash evaporation which has been proposed by Miyatake et<br />
al. [141] are approaching the main interest <strong>of</strong> the present work. A novel approach for<br />
the multi effects <strong>of</strong> heating/humidification <strong>of</strong> air <strong>and</strong> improvement <strong>of</strong> the HDH cycle<br />
will be presented in the next chapter.<br />
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