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 1200°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 1100°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 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.

Elements Of Electromagnetics
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ISBN:9780190698614
Author:Sadiku, Matthew N. O.
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State h (Btu/lb) s (Btu/lb-R)
1
1611
2
3
4
5
6
7
8
9
10
11
12
13
1473
1473
1575
1398
1099
94.12
94.54
312.5
317.5
449.6
449.6
449.6
1.685
1.703
1.703
1.773
1.8
1.89
0.1751
0.1758
0.4917
0.4979
0.6491
0.6491
0.663
Determine for the cycle:
(a) the mass flow rate of steam entering the first stage of the turbine, in lb/h.
(b) the rate of exergy 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 exergy loss in the condenser, in Btu/h.
(c) the exergy destroyed in the tubine, in Btu/h.
(f) the exergy destroyed in the open feedwater heater, in Btu/h.
Transcribed Image Text:State h (Btu/lb) s (Btu/lb-R) 1 1611 2 3 4 5 6 7 8 9 10 11 12 13 1473 1473 1575 1398 1099 94.12 94.54 312.5 317.5 449.6 449.6 449.6 1.685 1.703 1.703 1.773 1.8 1.89 0.1751 0.1758 0.4917 0.4979 0.6491 0.6491 0.663 Determine for the cycle: (a) the mass flow rate of steam entering the first stage of the turbine, in lb/h. (b) the rate of exergy 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 exergy loss in the condenser, in Btu/h. (c) the exergy destroyed in the tubine, 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 1200°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 1100°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 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.
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 1200°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 1100°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 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.
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