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Modern Engineering Thermodynamics

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544 CHAPTER 14: Vapor and Gas Refrigeration Cycles<br />

EXAMPLE 14.3 (Continued )<br />

b. From Table C.9b in Thermodynamic Tables to accompany <strong>Modern</strong> <strong>Engineering</strong> <strong>Thermodynamics</strong>, the thermodynamic data at<br />

the monitoring stations shown in the schematic are<br />

where we have calculated<br />

Station 1<br />

T 1 = − 15:0°C<br />

Station 2s<br />

T 2s = 20:0°C<br />

s 1 = s 2s = 0:89973 kJ/ ðkg.KÞ x 2s = 1:00<br />

x 1 = 0:9395<br />

h 1 = 231:0 kJ/kg<br />

Station 3<br />

T 3 = 20:0°C<br />

x 3 = 0:00<br />

h 2s = 256:5 kJ/kg<br />

s 2s = 0:89973 kJ/ ðkg.KÞ<br />

p 2s = 909:9 kPa<br />

Station 4s<br />

T 4s = T 1 = −15:0°C<br />

h 3 = 68:67 kJ/kg x 4s = 0:1765<br />

s 3 = 0:25899 kJ/ðkg.KÞ<br />

p 3 = p 2 = 909:9 kPa<br />

s 4s = s 3 = 0:25899 kJ/ðkg.KÞ<br />

h 4s = 65:6 kJ/kg<br />

and<br />

x 1 = s 1 − s f 1<br />

s<br />

= s 2s − s f 1<br />

fgx1 s<br />

=<br />

0:89973 − 0:11075<br />

= 0:9395<br />

fg1 0:83977<br />

h 1 = h f 1 + x 1 ðh fg1 Þ = 27:33 + ð0:9395Þð216:79Þ = 231:0 kJ/kg<br />

x 4s = s 3 − s f 4 0:25899 − 0:11075<br />

s<br />

= = 0:1765<br />

fg4 0:83977<br />

h 4s = h f 4 + x 4s ðh fg4 Þ = 27:33 + ð0:1765Þð216:79Þ = 65:59 kJ/kg<br />

Then,<br />

COP isentropic<br />

=<br />

vapor-compression<br />

cycle ðwith expansion<br />

turbineÞ<br />

=<br />

_Q L<br />

h<br />

=<br />

1 − h 4s<br />

_W c − _W t ðh 2s − h 1 Þ − ðh 3 − h 4s Þ<br />

231:0 − 65:59<br />

ð256:5 − 231:0Þ − ð68:67 − 65:59Þ = 7:38<br />

which is identical to the Carnot efficiency of part a, as it should be, because the Rankine and Carnot cycles are identical<br />

in this case (see Figure 14.10).<br />

c. When the isentropic turbine is replaced by an adiabatic, aergonic throttling valve, the process from station 3 to station 4<br />

becomes isenthalpic rather than isentropic, as shown in Figure 14.11.<br />

3 2<br />

4<br />

Throttling<br />

valve<br />

Q H<br />

Condenser<br />

W C<br />

Q L<br />

3<br />

2s<br />

Evaporator<br />

1<br />

T<br />

4h 1<br />

s<br />

FIGURE 14.11<br />

Example 14.3, Solution, part c.

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