Answer:
Qh = 372.24 MW
Explanation:
Solution:-
- Determine the state properties for working fluid water ( Rankine Cycle ):
- We are to assume ideal rankine cycle.
- The mass flow ( m^ ) = 150 kg/s
Turbine Inlet - ( Saturated Vapor ) -
P2 = P3 = 12 MPa, Tsat = 324.68°C
h3 = hg = 2685.4 KJ/kg , s3 = sg = 5.4939 KJ/kg.K
Condenser Inlet/Turbine exit - ( Liquid-vapor )
P4 = P1 = 10 KPa , Tsat = 45.8056°C , s4 = s3 = 5.4939 KJ/kg.K
sf = 0.64919 KJ / kg.K , sfg = 7.49961 KJ / kg.K
hf = 191.81 KJ/kg , hfg = 2392.09 KJ/kg
h4 = 1737.0762 KJ/kg
- Evaluate the quality "x" of liquid vapor mixture of H2O at condenser inlet:
x = ( s4 - sf ) / sfg
x = ( 5.4939 - 0.64919 ) / 7.49961
x = 0.64599 ;
- The enthalpy at this state:
h4 = hf + x*hfg
h4 = 191.81 + 0.64599*2392.09
h4 = 1737.0762 KJ/kg
- The work input by the pump, win,p = 12 KJ/kg
Pump Inlet - ( Saturated liquid ) -
P1 = 10 KPa, Tsat = 45.8056°C
h1 = hf = 191.81 KJ/kg , s1 = sf = 0.64919 KJ / kg.K
Boiler Inlet / Pump exit
P2 = 12 MPa, Tsat = 324.68°C , s2 = s1 = 0.64919 KJ / kg.K
h2 ?
- The isentropic compression process by the pump can be modeled by applying the first law of thermodynamic law for the work done by pump. Assuming steady state conditions of flow and ideal operation of pump at 100% efficiency:
Win,p = mass flow ( m^ ) * [ h2 - h1 ]
mass flow ( m^ ) * win,p = mass flow ( m^ ) * [ h2 - h1 ]
h2 = win,p + h1
h2 = 12 + 191.81
h2 = 203.81 KJ/kg
- The rate of heat transferred from boiler to the working fluid (Qh) is determined by applying steady state first law of thermodynamic on the boiler and water system:
Qh = mass flow ( m^ ) * [ h3 - h2 ]
Qh = 150 * [ 2685.4 - 203.81 ]
Qh = 372238.5 MW / 1000
Qh = 372.24 MW