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

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5. SIMULATION AND RESULTS<br />

Figure 5.4: T COND is the condenser temperature (upper x-axis). ∆T COND is the change <strong>of</strong> the<br />

condenser temperature (lower x-axis). w ss <strong>and</strong> w ws is the concentration <strong>of</strong> the strong <strong>and</strong> weak<br />

LiBr-solution on mass basis. p Hi g h <strong>and</strong> p Low is the pressure at the condenser <strong>and</strong> evaporator<br />

respectively (right y-axis)<br />

strong LiBr-solution (w ss ) must decrease in order to keep the solution<br />

at equilibrium, see appendix B.4.2 page 232.<br />

As w ss decreases it approaches w ws as seen in figure 5.4. If T COND<br />

increases to 42 ◦ C the concentration <strong>of</strong> the strong <strong>and</strong> weak solution<br />

becomes equal <strong>and</strong> COP ABS drops rapidly since no refrigerant is sent to<br />

the condenser.<br />

COP ABS has no optimum with respect to ∆T COND within the simulated<br />

range - the condenser temperature should just be as low as possible.<br />

But since the curve is almost flat on the left h<strong>and</strong> side <strong>of</strong> the graph, it<br />

can be concluded that a condenser temperature <strong>of</strong> about 30 to 35 ◦ C is<br />

sufficiently low for the given parameter configuration (<strong>of</strong> the single cycle<br />

configuration).<br />

110

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