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Modern Engineering Thermodynamics

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

T<br />

3<br />

2s<br />

p<br />

3 2s<br />

4h 1<br />

4h<br />

1<br />

s<br />

h<br />

(a) Vapor-compression isentropic refrigeration cycle<br />

with isenthalpic throttling<br />

2s<br />

T<br />

3<br />

1<br />

p<br />

3 2s<br />

4h<br />

4h<br />

1<br />

s<br />

(b) Same as (a) except with superheat<br />

h<br />

FIGURE 14.12<br />

T–s and p–h diagrams for an isentropic vapor-compression cycle.<br />

EXAMPLE 14.4<br />

Repeat part c of Example 14.3 requiring that the evaporator outlet be a saturated vapor at −15.0°C and introduce a compressor<br />

isentropic efficiency of 75.0%.<br />

Solution<br />

First, draw a sketch of the system (Figure 14.13). Since the evaporator outlet is a saturated vapor, the compressor outlet is a<br />

superheated vapor, as shown in the figure.<br />

The thermodynamic data for the four monitoring stations are (see Example 14.3 for details)<br />

Then, from Eq. (14.7),<br />

Station 1<br />

Station 2s<br />

T 1 = −15:0°C<br />

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

x 1 = 1:00<br />

s 2s = s 1 = 0:95052 kJ/ ðkg.KÞ<br />

h 1 = 244:13 kJ/kg h 2s = 271:92 kJ/kgðfrom interpolation in Table C:10bÞ<br />

s 1 = 0:95052 kJ/ ðkg.KÞ T 2s = 39:3°C<br />

Station 3<br />

Station 4h<br />

T 3 = 20:0°C<br />

T 4h = T 1 = −15:0°C<br />

x 3 = 0:00<br />

h 4h = h 3 = 68:67 kJ/kg<br />

h 3 = 68:67 kJ/kg x 4h = 0:1910<br />

s 3 = 0:25899 kJ/ ðkg.KÞ s 4h = 0:27088 kJ/ ðkg.KÞ<br />

Q<br />

COP vapor-compression<br />

= _ L<br />

=<br />

cycle<br />

j _W j<br />

R/AC<br />

c<br />

=<br />

h 1 − h 4h<br />

ðh 2s − h 1 Þ/ ðη s<br />

244:13 − 68:67<br />

ð271:92 − 244:13Þ/0:750 = 4:74<br />

Þ c

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