Problem 3. A vapor power plant produces 25 kg/s steam at 6 MPa, 500°C, in the boiler. It cools the condenser to an exit of 40°C, and the cycle is shown in the figure. An extraction is done at 800 kPa to an open feedwater heater; in addition, a steam supply of 5 kg/s is taken out and not returned. The missing 5 kg/s water is added to the feedwater heater from a 20°C, 800 kPa source. Assuming the turbines and the pumps to be isentropic, find (a) the needed extraction flow rate to cover both the feedwater heater and the steam supply. (b) the total net power output, (c) the utilization factor of the power plant. 1 | T, %3D 40 С, х 3D0 2 P2 = 800 kPa Boiler T1 E T2 P2 Water resupply FWH 5 P5 = 6 MPa, T, = 500 C 6 P2 = 800 kPa %3D Steam supply %3| 3 X3 = 0 4 PA = 6 MPa 7 P1 Condenser 8 Pg = 800 kPa,T3 = 20 C %3D

Refrigeration and Air Conditioning Technology (MindTap Course List)
8th Edition
ISBN:9781305578296
Author:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson
Publisher:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson
Chapter28: Special Refrigeration Applications
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Problem 19RQ: Two methods used to power refrigeration compressors on a ship are _____and ____.
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Problem 3.
A vapor power plant produces 25 kg/s steam
at 6 MPa, 500°C, in the boiler. It cools the condenser to an exit
of 40°C, and the cycle is shown in the figure. An extraction is
done at 800 kPa to an open feedwater heater; in addition, a
steam supply of 5 kg/s is taken out and not returned. The
missing 5 kg/s water is added to the feedwater heater from a
20°C, 800 kPa source. Assuming the turbines and the pumps
to be isentropic, find (a) the needed extraction flow rate to
cover both the feedwater heater and the steam supply. (b) the
total net power output, (c) the utilization factor of the
plant.
1 T = 40 C, x1 = 0 5 P5 = 6 MPa,T; = 500 C
2 P2 = 800 kPa
3 x3 = 0
4 P4 = 6 MPa
Boiler
4
T1
T2
P2
Water
3+
resupply
8
power
FWH
%3D
%3D
%3D
Steam
6 P2 = 800 kPa
supply
%3D
7
P1
Condenser
8 Pg = 800 kPa, Tg = 20 C
%3D
Transcribed Image Text:Problem 3. A vapor power plant produces 25 kg/s steam at 6 MPa, 500°C, in the boiler. It cools the condenser to an exit of 40°C, and the cycle is shown in the figure. An extraction is done at 800 kPa to an open feedwater heater; in addition, a steam supply of 5 kg/s is taken out and not returned. The missing 5 kg/s water is added to the feedwater heater from a 20°C, 800 kPa source. Assuming the turbines and the pumps to be isentropic, find (a) the needed extraction flow rate to cover both the feedwater heater and the steam supply. (b) the total net power output, (c) the utilization factor of the plant. 1 T = 40 C, x1 = 0 5 P5 = 6 MPa,T; = 500 C 2 P2 = 800 kPa 3 x3 = 0 4 P4 = 6 MPa Boiler 4 T1 T2 P2 Water 3+ resupply 8 power FWH %3D %3D %3D Steam 6 P2 = 800 kPa supply %3D 7 P1 Condenser 8 Pg = 800 kPa, Tg = 20 C %3D
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