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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 />

54

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