Consider a regenerative vapor power cycle using an open and a closed feedwater heater similar in design to that shown in the figure below. Steam enters the turbine at 14MPa,560?C, state 1 , and expands isentropically in three stages to a condenser pressure of 45 kPa, state 4. Saturated liquid exiting the condenser at state 5 is pumped isentropically to state 6 and enters the open feedwater heater. Between the first and second turbine stages, some steam is extracted at 1MPa, state 2 , and diverted to the closed feedwater heater. The diverted steam leaves the closed feedwater heater as saturated liquid at 1MPa, state 10 , undergoes a throttling process to 0.2 MPa, state 11, and enters the open feedwater heater. Steam is also extracted between the second and third turbine stages at 0.2MPa, state 3 , and diverted to the open feedwater heater. Saturated liquid at 0.2 MPa exiting the open feedwater heater at state 7 is pumped isentropically to state 8 and enters the closed feedwater heater. Feedwater exits the closed feedwater heater at 14MPa,170?C, state 9 , and then enters the steam generator. Each turbine stage and the pumps have an isentropic efficiency of 83%.
If the net power developed by the cycle is 300MW, determine: (a) the percent cycle thermal efficiency. (b) the mass flow rate into the first turbine stage, in kg/s. (c) the magnitude of the rate of heat transfer from the working fluid as it passes through the condenser, in MW.