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Modern Engineering Thermodynamics

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9.9 Unsteady State Processes in Open Systems 297<br />

The work transport energy efficiency η W is defined in Chapter 4 for a work producing system (e.g., an engine or<br />

motor) by Eq. (4.72) as<br />

Inserting Eqs. (9.35) and (9.37) gives<br />

ðη W Þ work<br />

producing<br />

W<br />

ðη W Þ work<br />

= _ act<br />

(4.72)<br />

producing<br />

_W rev<br />

= _m½ðh 1 − T b s 1 Þ − ðh 2 − T b s 2 Þ + ðV 1 2 − V 2 2 Þ/ð2g c Þ + ðg/g c ÞðZ 1 − Z 2 ÞŠ − T b<br />

_S P<br />

_m½ðh 1 − T b s 1 Þ − ðh 2 − T b s 2 Þ + ðV 12 − V 22 Þ/ð2g c Þ + ðg/g c ÞðZ 1 − Z 2 ÞŠ<br />

= 1 −<br />

T b<br />

_S P<br />

_m½ðh 1 − T b s 1 Þ − ðh 2 − T b s 2 Þ + ðV 12 − V 22 Þ/ð2g c Þ + ðg/g c ÞðZ 1 − Z 2 ÞŠ<br />

and, for a work absorbing system (pump, compressor, etc.), Eq. (4.71) gives<br />

ðη W Þ work<br />

absorbing<br />

=<br />

(9.38)<br />

_m½ðh 1 − T b s 1 Þ − ðh 2 − T b s 2 Þ + ðV 1 2 − V 2 2 Þ/ð2g c Þ + ðg/g c ÞðZ 1 − Z 2 ÞŠ<br />

_m½ðh 1 − T b s 1 Þ − ðh 2 − T b s 2 Þ + ðV 12 − V 22 Þ/ð2g c Þ + ðg/g c ÞðZ 1 − Z 2 ÞŠ − T b<br />

_S P<br />

(9.39)<br />

EXAMPLE 9.7<br />

Determine the maximum (reversible) power that could be produced by expanding 0.500 kg/s of steam in a shaft work<br />

machine from 8.00 MPa, 300.°C to a saturated vapor at 100.°C. Neglect any kinetic and potential energy effects. The temperature<br />

of the system boundary is T b = 20.0°C<br />

Solution<br />

First, draw a sketch of the system (Figure 9.14).<br />

The unknown is the maximum (reversible) power for this<br />

system. For this open system, we have the following thermodynamic<br />

station data:<br />

Expansion<br />

Station 1 ƒƒƒ ƒ!<br />

p 1 = 8:00 MPa<br />

T 1 = 300:°F<br />

Station 2<br />

x 2 = 1:00<br />

T 2 = 100:°C<br />

m = 0.500 kg/s<br />

1<br />

T b = 20.0°C<br />

2<br />

Station 1 Station 2<br />

p 1 = 8.00 MPa x 2 = 1.00<br />

T 1 = 300.°C T 2 = 100.°C<br />

W max = W rev = ?<br />

Neglecting all kinetic and potential energy effects, Eq. (9.37)<br />

reduces to<br />

_W max = _W rev = _m ½ðh 1 − T b s 1 Þ − ðh 2 − T b s 2 ÞŠ<br />

FIGURE 9.14<br />

Example 9.7.<br />

and, using the values just given, we get<br />

_W max = ð0:50 kg=sÞf½2785:0 − ð20:0 + 273:15Þð5:7914ÞŠ−½2676:0 − ð20 + 273:15Þð7:3557ÞŠg<br />

= 284 kW<br />

Exercises<br />

19. If the mass flow rate of steam in Example 9.7 is increased from 0.500 kg/s to 0.850 kg/s with all the inlet and exit steam<br />

properties remaining constant, what is the maximum (reversible) power output? Answer: _W max = _W rev = 482 kW.<br />

20. Determine the maximum (reversible) power output in Example 9.7 when the steam exits with a quality of 90.0% rather<br />

than 100.%. Answer: _W max = _W rev = 308 kW.<br />

21. Suppose the inlet steam pressure and temperature in Example 9.7 is increased to 10.0 MPa and 800.°C. Determine the<br />

maximum (reversible) power output. Answer: _W max = _W rev = 712 kW.<br />

9.9 UNSTEADY STATE PROCESSES IN OPEN SYSTEMS<br />

In Chapter 6, we analyze the energy transport requirements in the emptying and filling of a rigid container. In<br />

this section, we carry out an entropy analysis of the filling of a rigid container and determine whether it is more<br />

efficient to fill it adiabatically or isothermally.

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