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

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5.3. Partial optimization <strong>of</strong> st<strong>and</strong>ard parameters<br />

Figure 5.13: A+B In the st<strong>and</strong>ard parameter configuration the temperature <strong>of</strong> the low pressure<br />

desorber is set at the temperature where the strong solutions out <strong>of</strong> DES1 <strong>and</strong> DES2 are equal<br />

(intersection <strong>of</strong> red lines on the right figure). But by removing this equation an giving T DES1<br />

explicitly, this can be changed to see how it affects the performance <strong>of</strong> the system.<br />

5.13B shows that the intersection <strong>of</strong> the two red concentration curves<br />

actually gives a desorber temperature quite close to the optimum for<br />

COP ABS,f uel .<br />

5.3.3 SOFC subsystem<br />

Now some <strong>of</strong> the parameters in the SOFC subsystem are investigated. As<br />

mentioned earlier: the anode <strong>and</strong> cathode side <strong>of</strong> the SOFC has the same<br />

inlet temperature <strong>and</strong> the same outlet temperature.<br />

Changing ∆T SOFC<br />

A high temperature increase over the <strong>fuel</strong> cell (∆T SOFC ) is desirable<br />

for several reasons. One <strong>of</strong> the reasons is that it reduces the required<br />

air flow through the <strong>fuel</strong> cell thereby decreasing the blower power<br />

consumption. But ∆T SOFC can in practice not be too high, since a higher<br />

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