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IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at

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<strong>IEA</strong> SHC Task 38 <strong>Solar</strong> Air Conditioning <strong>and</strong> Refriger<strong>at</strong>ion Subtask C Report, D<strong>at</strong>e: 13.01.2009<br />

3 Wet <strong>Cooling</strong> Tower - Process Calcul<strong>at</strong>ion<br />

The need of special inform<strong>at</strong>ion of wet cooling tower technology begins with the purchase of<br />

a wet cooling tower. The owner <strong>and</strong> l<strong>at</strong>er on the user are interested in the technical behavior<br />

of the cooling tower. Therefore this chapter contains inform<strong>at</strong>ion according the process<br />

calcul<strong>at</strong>ion of wet cooling towers. With the help of these knowledge the commissioning,<br />

adapt<strong>at</strong>ions <strong>and</strong> also changes of the technical fe<strong>at</strong>ures of wet cooling towers can be<br />

executed.<br />

3.1 General aspects<br />

The he<strong>at</strong> transferred from the he<strong>at</strong> sources (solar collectors or other he<strong>at</strong> sources <strong>and</strong> the<br />

air conditioned rooms) to the sorption process have to be rejected to the ambient due to the<br />

requirements of the continuous thermodynamic process.<br />

If a dry he<strong>at</strong> rejection system is used, the return temper<strong>at</strong>ure of the cooling w<strong>at</strong>er will be<br />

about 7 to 10 °C higher than the dry temper<strong>at</strong>ure of the ambient air. This causes cooling<br />

w<strong>at</strong>er temper<strong>at</strong>ures in the Mediterranean countries in the range of 40 to 55 °C. This requires<br />

for the oper<strong>at</strong>ion of sorption cooling machines temper<strong>at</strong>ures of the he<strong>at</strong> source of 110 °C<br />

<strong>and</strong> more, which can not be managed by rel<strong>at</strong>ively cheap fl<strong>at</strong> pl<strong>at</strong>e collectors.<br />

If a wet he<strong>at</strong> rejection system is used, the return temper<strong>at</strong>ure of the cooling w<strong>at</strong>er will be<br />

about 3 to 8 °C lower than the dry temper<strong>at</strong>ure of t he ambient air. In these cases of<br />

applic<strong>at</strong>ion fl<strong>at</strong> pl<strong>at</strong>e collectors can be used.<br />

This calcul<strong>at</strong>ion procedure for a wet cooling tower is used above all for commissioning,<br />

adapt<strong>at</strong>ions <strong>and</strong> changes of the technical fe<strong>at</strong>ures. In addition to this the formulas <strong>and</strong><br />

graphs can be computerized <strong>and</strong> used for several kinds of simul<strong>at</strong>ions of changing the mass<br />

flows of w<strong>at</strong>er <strong>and</strong> air.<br />

M<br />

air<br />

He<strong>at</strong><br />

80/74 °C<br />

Cold<br />

6/12 °C<br />

Absorp. machine<br />

He<strong>at</strong> rejection<br />

28/33 °C<br />

m w<strong>at</strong>er<br />

wet coolig tower<br />

air<br />

fresh w<strong>at</strong>er<br />

drain w<strong>at</strong>er<br />

w<strong>at</strong>er conductivity controlled<br />

Figure 3-1: Principle of a thermal driven cooling with wet he<strong>at</strong> rejection<br />

page 19

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