Rankine cycle with reheat
- Water is used as working fluid;
- Pressure at the outlet of the low pressure turbine of 10 kPa;
- Pressure at the outlet of the high pressure turbine of 200 kPa;
- Pressure at the pump outlet of 1000 kPa;
- Temperatures after leaving the boiler of 250 °C;
- The pump has an isentropic efficiency of 90%;
- The turbines have an isentropic efficiency of 80%.
using CycleSolver
@solve begin
st3.T = 250 + 273
st5.T = 250 + 273
st3.p = 1000
st5.p = 200
st1.p = 10
newCycle[]
pump(st1, st2, 90)
boiler(st2, st3)
turbine(st3, st4, 80)
boiler(st4, st5)
turbine(st5, st6, 80)
condenser(st6, st1)
end
PrintResults()
Output:
1- CYCLE [water]
State Name |
T [K] | P [kPa] | h [kJ/kg] | s [kJ/kg.K] | x | ṁ [kg/s] | Mass-flux fraction |
---|---|---|---|---|---|---|---|
st1 | 318.956 | 10.0 | 191.806 | 0.6492 | 0.0 | 1.0 | |
st2 | 319.016 | 1000.0 | 192.917 | 0.6495 | 1.0 | ||
st3 | 523.0 | 1000.0 | 2942.79 | 6.9258 | 1.0 | ||
st4 | 393.36 | 200.0 | 2690.28 | 7.0863 | 0.9928 | 1.0 | |
st5 | 523.0 | 200.0 | 2970.91 | 7.7094 | 1.0 | ||
st6 | 318.956 | 10.0 | 2549.14 | 8.04 | 0.9855 | 1.0 |
Cycle Properties:
Total | Component | Value | |
---|---|---|---|
qin Q̇in |
3030.508 kJ/kg 0.0 kW |
boiler: st2 >> st3 boiler: st4 >> st5 |
2749.8738 kJ/kg 280.6342 kJ/kg |
qout Q̇out |
2357.3323 kJ/kg 0.0 kW |
condenser: st6 >> st1 |
2357.3323 kJ/kg |
win Ẇin |
1.1111 kJ/kg 0.0 kW |
pump: st1 >> st2 |
1.1111 kJ/kg |
wout Ẇout |
674.2868 kJ/kg 0.0 kW |
turbine: st3 >> st4 turbine: st5 >> st6 |
252.5148 kJ/kg 421.772 kJ/kg |