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3.6. Desorber - DES<br />

3.6 Desorber - DES<br />

In the desorber the weak water-LiBr solution enters (either sub cooled or<br />

saturated liquid) <strong>and</strong> is mixed with the solution in the desorber, which<br />

is heated up by the heating water circuit. Hereby the refrigerant (water)<br />

is evaporated, <strong>and</strong> strong solution LiBr (which is saturated) is returned<br />

towards the absorber. See figure 3.7.<br />

Figure 3.7: Desorber component. Weak solution (ws,i) enters the desorber <strong>and</strong> is heated by the<br />

heating water (h,i <strong>and</strong> h,o). Refrigerant in gas phase (r,o) is sent out through an outlet at the<br />

top, while the strong solution (ss,o) leaves at the bottom <strong>of</strong> the desorber.<br />

The desorber is made up by a reservoir <strong>of</strong> solution in which some<br />

heat exchanger tubes with the warm heating water run. On top there is a<br />

gas phase <strong>of</strong> refrigerant. In the model it is assumed that the temperature<br />

is the same throughout the liquid phase <strong>and</strong> the gas phase. So when<br />

the weak LiBr solution enters the reservoir, it instantly becomes perfectly<br />

mixed with the rest <strong>of</strong> the liquid phase.<br />

It is also assumed that the outlet temperature <strong>of</strong> the refrigerant<br />

(superheated steam) is the same as the outlet temperature <strong>of</strong> the solution,<br />

after all, the water has been evaporated from the solution (at which point<br />

they must have the same temperature), <strong>and</strong> no heating or cooling is<br />

assumed to happen to the gas after the evaporation (hence T ss,o = T r,o ),<br />

see figure 3.8.<br />

Since it is assumed that the temperature <strong>of</strong> the solution is the same<br />

throughout the desorber, only the heating water changes temperature.<br />

Hence the closest approach temperature difference appears between<br />

the outlet temperature <strong>of</strong> the heating water (T h,o ) <strong>and</strong> the mutual<br />

temperature <strong>of</strong> the refrigerant <strong>and</strong> solution (T ss,o = T r,o ):<br />

∆T minr,o = T h,o − T ss,o (3.29)<br />

Since only the heating water changes temperature during the heat<br />

exchange process, the effectiveness will be based on the heating water<br />

53

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