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

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5.5. Total optimization <strong>of</strong> system<br />

eta | COP<br />

St<strong>and</strong>ard vs Optimized parameters<br />

1,2<br />

1,1<br />

1,0<br />

0,9<br />

0,8<br />

0,7<br />

0,6<br />

0,5<br />

0,4<br />

0,3<br />

0,2<br />

0,1<br />

0,0<br />

0,07<br />

0,46<br />

0,03<br />

0,52 0,50<br />

0,03<br />

0,59 0,51<br />

eta_HW<br />

COP_ABS,<strong>fuel</strong><br />

eta_sys,el,net<br />

0,55<br />

St<strong>and</strong>ard Optimized Optimized<br />

ΔT_SOFC=120<br />

Figure 5.32: All bars are for the Double stage with Air Preheat. The right <strong>and</strong> middle columns<br />

are both for the optimized system, where i d has been optimized by aiming for a trade<strong>of</strong>f factor<br />

between cooling <strong>and</strong> electricity <strong>of</strong> 3,4.<br />

With the new ∆T min = 11 ◦ C for the additional air preheat (GGHEX4),<br />

the total gain <strong>of</strong> using air preheat is 14kW (59kW with air preheat vs<br />

45 kW for the same parameters without air preheat (not shown in the<br />

figure)).<br />

5.5.3 Future: ∆T SOFC = 120 ◦ C<br />

It is now investigated what will happen if it in the future becomes<br />

possible to use a 120 ◦ C temperature span over the <strong>fuel</strong> cell (i.e. inlet<br />

temperature is kept constant while outlet temperature is increased from<br />

780 ◦ C to 810 ◦ C).<br />

As seen in figure 5.32 the electricity generation increases 5kW while<br />

the cooling power decreases 8kW 14 . From a cooling perspective this<br />

14 the current density has been adjusted to give the same trade<strong>of</strong>f factor between<br />

153

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