18.01.2015 Views

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

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

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

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

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

When ∆T min,W GHE X 3 is decreased, a bigger amount <strong>of</strong> the energy left<br />

in the exhaust gas can be used to water heating, <strong>and</strong> furthermore the<br />

temperature to which the water can be heated increases (se figure 5.25).<br />

In the investigation ∆T min has been given the same value in both ends<br />

<strong>of</strong> the HEX, but in a real system their relationship will be controlled by<br />

the amount <strong>of</strong> water sent into the HEX (a big water flow means that the<br />

smallest ∆T min will occur at the gas outlet <strong>and</strong> vice versa). So if ∆T min is<br />

e.g. 15 ◦ C the temperature <strong>of</strong> the water doesn’t necessarily have to be 67 ◦ C<br />

as shown in the figure. By sending more water through, ∆T min would be<br />

smallest at the gas outlet end, yielding a smaller water outlet temperature<br />

(e.g. to avoid the guests on a hotel from being burned on the hot water<br />

from the tap).<br />

It can be seen from the red curve, that ideally 40% more hot water<br />

could be produced if there were no losses in the HEX (∆T min = 0 rather<br />

than 15 ◦ C).<br />

141

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!