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Modern Engineering Thermodynamics

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464 CHAPTER 13: Vapor and Gas Power Cycles<br />

efficiencies are in the range of 1%. Also note that the ratio of pump power to engine power in this example<br />

is only<br />

ð0:01672Þð20:0 − 14:7Þð144/778:16Þ Btu=lbm<br />

j _W p / _W pm j =<br />

ð1156:4 − 1133:9Þ − ð0:01672Þð20:0 − 14:7Þð144/778:16Þ Btu=lbm<br />

= 0:00073 = 0:073%<br />

and consequently the pump input power could be safely neglected in comparison to the engine output power<br />

in the thermal efficiency calculation. Even so, for clarity and completeness, the pump power is included in all<br />

subsequent thermal efficiency calculations carried out in the examples given in this chapter.<br />

EXAMPLE 13.4<br />

In 1876, George H. Corliss (1817–1888) built what was then the largest steam engine ever made (Figure 13.12), for the<br />

United States Centennial Exposition in Philadelphia, Pennsylvania. It had two cylinders, each with a 40.0-inch bore and a<br />

10.0 ft stroke. Steam entered the engine as a saturated vapor at 100. psia, producing 1400. hp at only 36.0 rpm. The engine’s<br />

flywheel was 30.0 ft in diameter and weighed 56.0 tons. If the steam was condensed at 14.7 psia, determine the Rankine<br />

cycle thermal efficiency of this engine assuming (a) isentropic prime mover and pump, (b) an engine isentropic efficiency of<br />

55.0% and a pump isentropic efficiency of 65.0%, and (c) the steam mass flow rate required to produce 1400. hp.<br />

FIGURE 13.12<br />

Example 13.4, The Corliss engine.<br />

Solution<br />

a. The thermodynamic states at the four main points around the Rankine cycle for this system are (Figure 13.13)<br />

Station 1—Engine inlet<br />

p 1 = 100: psia<br />

Station 2s—Engine exit<br />

p 2s = 14:7 psia<br />

x 1 = 1:00 s 2s = s 1<br />

h 1 = h g ð100: psiaÞ = 1187:8 Btu/lbm<br />

<br />

.<br />

x 2s = s 2s – s f ð14:7 psiaÞ s fg ð14:7 psiaÞ<br />

.<br />

s 1 = s g ð100: psiaÞ = 1:6036 Btu/lbm . R = ½1:6036 − 0:3122Š 1:4447 = 0:8939<br />

h 2s = h f ð14:7 psiaÞ + x 2s h fg ð14:7 psiaÞ<br />

= 180:1 + 0:8939 ð970:4Þ<br />

= 1047:5 Btu/lbm

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