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Modern Engineering Thermodynamics

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3.8 Quality 75<br />

Although Eq. (3.26) was developed using specific volume, an identical argument can be used to expand it to all<br />

other intensive properties (except pressure and temperature), resulting in equations of the form<br />

x = v − v f<br />

v fg<br />

= u − u f<br />

u fg<br />

= h − h f<br />

h fg<br />

(3.27)<br />

In addition, the term m f /m =1− x represents the relative amount of liquid present in the mixture, called the<br />

moisture of the mixture.<br />

EXAMPLE 3.4<br />

Saturated water at 14.696 psia and 212°F has the following<br />

properties:<br />

v f = 0.01672 ft 3 /lbm v g = 26.80 ft 3 /lbm<br />

u f = 180.1 Btu/lbm u g = 1077.6 Btu/lbm<br />

h f = 180.1 Btu/lbm h g = 1150.5 Btu/lbm<br />

If 0.200 lbm of saturated water at 14.696 psia is put into a<br />

sealed rigid container whose total volume is 3.00 ft 3 (Figure<br />

3.18), determine the following properties of the system:<br />

a. The specific volume v.<br />

FIGURE 3.18<br />

b. The quality, x, and moisture, 1 − x.<br />

Example 3.4.<br />

c. The specific internal energy u.<br />

d. The specific enthalpy h.<br />

e. The mass of water in the liquid and vapor phases, m f and m g .<br />

Solution<br />

The system is a closed rigid container.<br />

∀ = 3.00 ft 3<br />

m = 0.200 lbm<br />

p = 14.696 psia<br />

System<br />

boundary<br />

a. The specific volume can be calculated directly from its definition, Eq. (3.4). as<br />

v = V/m = 3:00/0:200 = 15:0ft 3 /lbm<br />

b. The quality can be calculated from Eq. (3.26) or (3.27) and Eq. (3.25) as<br />

x = v − v f 15:0 − 0:01672<br />

=<br />

v fg 26:80 − 0:01672 = 0:559<br />

or x = 55.9% vapor. Therefore, the amount of moisture present is 1 − x = 0.441, or the mixture consists of 44.1% moisture.<br />

c. The specific internal energy can be obtained by combining Eq. (3.27) with the definition u fg = u g − u f to give u = u f + xu fg =<br />

u f + x(u g − u f ), or<br />

u = 180:1 + ð0:559Þð1077:6 − 180:1Þ = 682 Btu/lbm<br />

d. The specific enthalpy can be obtained by combining Eq. (3.27) with the definition h fg = h g − h f to give h = h f + xh fg =<br />

h f + x(h g − h f ), or<br />

h = 180:1 + ð0:559Þð1150:5 − 180:1Þ = 722 Btu/lbm<br />

e. To obtain the mass of water in the liquid and vapor phases, we can use the original definition of quality given in Eq.<br />

(3.22) to get m g = xm = 0.559(0.2) = 0.112 lbm of saturated water vapor and then m f =(1− x)m = m − m g = 0.088 lbm<br />

of saturated liquid water.<br />

EXAMPLE 3.5<br />

What total mass of saturated water (liquid plus vapor) should be put into a 0.500 ft 3 sealed, rigid container at 14.696 psia so that<br />

the water passes exactly through the critical state when the container is heated? Also, determine the initial quality in the vessel.<br />

Solution<br />

Processes carried out in sealed rigid containers are constant volume (or isochoric) processes. Therefore, the process path on a<br />

p-v diagram is a vertical straight line, as shown in the p-v diagram of Figure 3.19. In this problem, we are given the final<br />

(Continued )

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