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

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3. COMPONENT DESCRIPTION<br />

3.3 Blower<br />

Figure 3.3: Blower component. ”i” is the inlet <strong>and</strong> ”o” is the outlet. Ẇ is the blower power.<br />

It is assumed that no chemical reaction takes place in the blower, so<br />

the mass flow <strong>of</strong> each species out <strong>of</strong> the blower is equal to its mass flow<br />

into the blower. All species have been modeled as ideal gasses. They are<br />

hence in gas phase all the time, <strong>and</strong> the enthalpy only depends on the<br />

temperature, while the entropy also depends on the pressure. The blower<br />

uses an isentropic efficiency to determine the enthalpy <strong>and</strong> temperature<br />

(i=inlet, 2=state just after the compression).<br />

η i s = Ḣ2,i s − Ḣ i<br />

Ḣ 2 − Ḣ i<br />

(3.10)<br />

The blower work is then determined as the enthalpy flow difference<br />

during the compression.<br />

Ẇ = (Ḣ 2 − Ḣ 1 ) (3.11)<br />

The energy balance then includes the parameter ˙Q loss which is the<br />

amount <strong>of</strong> heat lost to the surroundings (assumed to happen after the<br />

compression). So the outlet temperature is determined from the enthalpy<br />

flow in the outlet (o) which will be:<br />

Ḣ o = Ḣ i +Ẇ − ˙Q loss (3.12)<br />

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