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

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4.9. Validation <strong>of</strong> Model<br />

Distribution <strong>of</strong> heat rejection<br />

The heat from the absorption cycle is removed by the condenser <strong>and</strong> the<br />

absorber <strong>and</strong> according to [27] the distribution should be as follows:<br />

˙Q ABSO = 56%<br />

˙Q COND = 44%<br />

For the single cycle at st<strong>and</strong>ard parameter configuration with<br />

additional air pre heat <strong>and</strong> wet tower the heat removed by the absorber<br />

<strong>and</strong> the condenser is ˙Q ABSO = 31,1kW (53%) <strong>and</strong> ˙Q COND = 27,7kW (47%)<br />

respectively.<br />

So in the model a slightly bigger fraction <strong>of</strong> the heat is removed by the<br />

condenser. The reason is the same as described in the previous section<br />

- low condenser/absorber temperature. If this is increased by 5 ◦ C, COP<br />

will drop to about 0,7 <strong>and</strong> the fraction <strong>of</strong> the heat rejected by the absorber<br />

will be 56%.<br />

COP<br />

According to [27], COP ABS should be between 0,70 <strong>and</strong> 0,75 almost independent<br />

<strong>of</strong> the temperatures (<strong>and</strong> load). At the st<strong>and</strong>ard configuration,<br />

the model gives a COP ABS <strong>of</strong> 0,80 which is a little higher than expected.<br />

But this can be due to the assumptions that the heat losses as well as<br />

pressure losses <strong>of</strong> the components have been neglected. Also the low<br />

condenser/absorber temperature will increase the COP ABS .<br />

Taking the above into consideration it is concluded that the temperature<br />

levels <strong>of</strong> the absorption cycle <strong>and</strong> the general behavior <strong>of</strong> the absorption<br />

model seems to be reasonable.<br />

103

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