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Modern Engineering Thermodynamics

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14.14 Reversed Brayton Cycle Refrigeration 571<br />

b. In a more realistic analysis, we still assume ideal gas behavior, but now we introduce isentropic compressor and<br />

expander efficiencies of (η s ) c = (η s ) e = 0.650, and use Eq. (14.23), where the coldest temperature in the cycle<br />

is now only<br />

and<br />

Then, Eq. (14.23) gives<br />

T 4 = T 3 − ðT 3 − T 4s Þðη s Þ e<br />

= 540: − ð540: − 443Þð0:650Þ = 477 R = 17:0°F<br />

T 2s = T 1 T 3 /T 4s =<br />

ð530: RÞð540: RÞ<br />

443 R<br />

= 646 R<br />

T<br />

COP reversed<br />

=<br />

1 − T 4<br />

ðT 2s − T 1 Þ/ðη<br />

Brayton cycle<br />

s Þ c<br />

− ðT 3 − T 4s Þðη s Þ e<br />

R=AC<br />

530: − 477<br />

=<br />

½ð646 − 530: Þ/0:650Š− ð540: − 443Þð0:650Þ<br />

= 0:220<br />

The results of part b of this example are much more realistic than those of part a due to the large thermodynamic<br />

irreversibilities (friction, heat loss, etc.) present in early mechanical equipment.<br />

Exercises<br />

28. If Gorrie had found a way to increase the isentropic efficiency of his compressor in Example 14.10 from 65.0% to 75.0%<br />

(but the isentropic efficiency of the expander did not change), determine the new coefficient of performance of the<br />

actual (not ASC) system assuming all the other variables remain unchanged. Answer: COP actual = 0.244.<br />

29. A sudden heat wave causes the compressor inlet temperature in Example 14.10 to increase from 70.0°F to 95.0°F.<br />

Determine the new actual (not ASC) coefficient of performance of the unit. Assume all the other variables remain<br />

unchanged. Answer: COP actual = 0.384.<br />

30. Gorrie found a way to increase the pressure ratio of his compressor in Example 14.10 from 2.00 to 3.00. Determine<br />

the new actual (not ASC) coefficient of performance of the unit. Assume all the other variables remain unchanged.<br />

Answer: COP actual = 0.214.<br />

Like modern Brayton power cycles, modern reversed Brayton refrigeration cycles can be constructed with regeneration<br />

capability (Figure 14.28). Unlike power cycles, however, regeneration in refrigeration cycles does not<br />

improve the cycle’s thermal efficiency; instead, it reduces the COP. However, regeneration does have the advantage<br />

of decreasing the minimum cooling temperature T 4s . Therefore, the purpose of regeneration in refrigeration<br />

cycles is simply to be able to reach lower cooling temperatures.<br />

The use of a modern reversed Brayton refrigeration cycle is illustrated in the following example.<br />

Internal heat<br />

transfer from A to B<br />

Q L<br />

B<br />

Regenerator<br />

A<br />

Cold air<br />

Q H<br />

Hot air<br />

Turbine<br />

Compressor<br />

W c<br />

FIGURE 14.28<br />

A modern reversed Brayton cycle with a regenerator.

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