Water is the working fluid in a reheat-regenerative Rankine cycle with one closed feedwater heater and one open feedwater heater. Steam enters the turbine at 1400 lbf/in.2 and 1000°F and expands to 500 lbf/in.2, where some of the steam is extracted and diverted to the closed feedwater heater. Condensate exiting the closed feedwater heater as saturated liquid at 500 lbf/in.2 undergoes a throttling process to 120 lbf/in.² as it passes through a trap into the open feedwater heater. The feedwater leaves the closed feedwater heater at 1400 lbf/in.² and a temperature equal to the saturation temperature at 500 lbf/in.2 The remaining steam is reheated to 900°F before entering the second-stage turbine, where it expands to 120 lbf/in.² Some of the steam is extracted and diverted to the open feedwater heater operating at 120 lbf/in.² Saturated liquid exits the open feedwater heater at 120 lbf/in.² The remaining steam expands through the third-stage turbine to the condenser pressure of 2 lbf/in.2 The turbine stages and the pumps each operate adiabatically with isentropic efficiencies of 85%. Flow through the condenser, closed feedwater heater, open feedwater heater, steam generator, and reheater is at constant pressure. The net power output of the cycle is 1.5 x 10° Btu/h. Let To = 60°F. Po = 14.7 lbf/in.2 The table below provides steady-state operating data for the cycle. State h (Btu/lb) s (Btu/lb-ºR) 1 2 1493 1375 1.609 1.627

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12. determine: a. the mass flow rate of steam entering the first stage of the turbine, in lb/h b. the rate of energy input, in Btu/h, to the working fluid passing through the steam generator. c. the magnitude of the exergy output, in Btu/h, of the net power output. d. the magnitude of the energy loss in the condenser, in Btu/h e. the exergy destroyed in the turbine, in Btu/h f. the exergy destroyed in the open feedwater heater, in Btu/h.
Water is the working fluid in a reheat-regenerative Rankine cycle with one closed feedwater heater and one open feedwater heater.
Steam enters the turbine at 1400 lbf/in.² and 1000°F and expands to 500 lbf/in.2, where some of the steam is extracted and diverted
to the closed feedwater heater. Condensate exiting the closed feedwater heater as saturated liquid at 500 lbf/in.2 undergoes a
throttling process to 120 lbf/in.² as it passes through a trap into the open feedwater heater.
The feedwater leaves the closed feedwater heater at 1400 lbf/in.² and a temperature equal to the saturation temperature at 500
lbf/in.2 The remaining steam is reheated to 900°F before entering the second-stage turbine, where it expands to 120 lbf/in.² Some of
the steam is extracted and diverted to the open feedwater heater operating at 120 lbf/in.² Saturated liquid exits the open feedwater
heater at 120 lbf/in.²
The remaining steam expands through the third-stage turbine to the condenser pressure of 2 lbf/in.2 The turbine stages and the
pumps each operate adiabatically with isentropic efficiencies of 85%. Flow through the condenser, closed feedwater heater, open
feedwater heater, steam generator, and reheater is at constant pressure. The net power output of the cycle is 1.5 x 10⁹ Btu/h. Let To =
60°F, Po= 14.7 lbf/in.2 The table below provides steady-state operating data for the cycle.
State h (Btu/lb) s (Btu/lb-ºR)
1493
1
2
1375
1.609
1.627
Transcribed Image Text:Water is the working fluid in a reheat-regenerative Rankine cycle with one closed feedwater heater and one open feedwater heater. Steam enters the turbine at 1400 lbf/in.² and 1000°F and expands to 500 lbf/in.2, where some of the steam is extracted and diverted to the closed feedwater heater. Condensate exiting the closed feedwater heater as saturated liquid at 500 lbf/in.2 undergoes a throttling process to 120 lbf/in.² as it passes through a trap into the open feedwater heater. The feedwater leaves the closed feedwater heater at 1400 lbf/in.² and a temperature equal to the saturation temperature at 500 lbf/in.2 The remaining steam is reheated to 900°F before entering the second-stage turbine, where it expands to 120 lbf/in.² Some of the steam is extracted and diverted to the open feedwater heater operating at 120 lbf/in.² Saturated liquid exits the open feedwater heater at 120 lbf/in.² The remaining steam expands through the third-stage turbine to the condenser pressure of 2 lbf/in.2 The turbine stages and the pumps each operate adiabatically with isentropic efficiencies of 85%. Flow through the condenser, closed feedwater heater, open feedwater heater, steam generator, and reheater is at constant pressure. The net power output of the cycle is 1.5 x 10⁹ Btu/h. Let To = 60°F, Po= 14.7 lbf/in.2 The table below provides steady-state operating data for the cycle. State h (Btu/lb) s (Btu/lb-ºR) 1493 1 2 1375 1.609 1.627
1
2
3
4
5
6
7
8
9
10
11
12
13
1493
1375
1375
1466
1315
1049
94.12
94.54
312.5
317.5
449.6
449.6
449.6
1.609
1.627
1.627
1.698
1.725
1.805
0.1751
0.1758
0.4917
0.4979
0.6491
0.6491
0.663
Transcribed Image Text:1 2 3 4 5 6 7 8 9 10 11 12 13 1493 1375 1375 1466 1315 1049 94.12 94.54 312.5 317.5 449.6 449.6 449.6 1.609 1.627 1.627 1.698 1.725 1.805 0.1751 0.1758 0.4917 0.4979 0.6491 0.6491 0.663
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