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integration of solid oxide fuel cells and ... - Ea Energianalyse

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3. COMPONENT DESCRIPTION<br />

is not in direct contact there will be a temperature difference (over<br />

the tubes), <strong>and</strong> the outlet temperature <strong>of</strong> the fluid will be higher<br />

than for the Wet Cooling Tower.<br />

In this project only the Dry Cooling Tower <strong>and</strong> the Wet Cooling<br />

Tower will be investigated <strong>and</strong> modeled since they constitute the two<br />

extremities.<br />

3.14.1 Dry Cooling Tower - TOWERd<br />

The heat transmission <strong>of</strong> the dry tower works exactly as the general heat<br />

exchanger component (see section 3.8 page 57). The only new thing is<br />

that the cold fluid is humid air with a humidity at the inlet equal to that<br />

<strong>of</strong> the ambient air, while the outlet air has the same absolute humidity as<br />

inlet air (i.e. the relative humidity changes).<br />

T [° C ]<br />

T w ,o<br />

T w ,i<br />

ΔT min ,w , i<br />

ΔT min ,w , o<br />

T air , o<br />

T air ,i<br />

TOWERd<br />

˙Q[kW ]<br />

Figure 3.17: Dry Tower: ∆T min,w,o (left side) specifies how much larger the water outlet<br />

temperature is than the (ambient) air inlet temperature. ∆T min,w,i (right side) specifies how<br />

much colder the outlet air is relative to the water inlet temperature<br />

.<br />

The electricity consumption <strong>of</strong> the fan in the tower is calculated by<br />

the volume flow <strong>of</strong> the air times the (explicitly given) pressure loss in the<br />

72

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