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

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Anode recycling (α SPG1 )<br />

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

There are several reasons for using anode recycling. First <strong>of</strong> all it supplies<br />

water for the pre reformer. But it also means that more the <strong>fuel</strong> is used,<br />

since some <strong>of</strong> the <strong>fuel</strong> that didn’t react the first time through the SOFC<br />

will react next time. This way more <strong>of</strong> the <strong>fuel</strong> will be used even though<br />

the <strong>fuel</strong> utilization factor from the SOFC point <strong>of</strong> view remains constant<br />

at U f =0,7 (it just means that every time the <strong>fuel</strong> is sent through the cell<br />

70% <strong>of</strong> it will be used in the electrochemical reaction).<br />

There is, however, a downside by the anode recycling. The<br />

concentration <strong>of</strong> the species CO, CO 2 , H 2 , <strong>and</strong> H 2 O is affected by the<br />

recycling . Generally the concentration <strong>of</strong> the reaction products are<br />

increased, which makes both the Nernst potential <strong>and</strong> the cell voltage<br />

decreases when the anode cycling fraction is increased (grey <strong>and</strong> brown<br />

curve in figure 5.17B).<br />

Figure 5.17: A+B The OC ratio (green) should be above 2 to avoid carbon depositing, so the<br />

recycling fraction should not be below 0,6.<br />

From figure 5.17A it can be seen that the increased use <strong>of</strong> the <strong>fuel</strong> in<br />

the SOFC more than compensates for the drop in cell voltages, so elec-<br />

129

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