Figure P8.78 shows a vapor power cycle with reheat and regeneration. The steam generator produces vapor at 1000 lbf.in2 ? 800F. Some of this steam expands through the first turbine stage to 100 lbf/in2 and the remainder is directed to the heat exchanger. The steam exiting the first turbine stage enters the flash chamber. Saturated vapor and saturated liquid at 100 lbf/in2 exit the flash chamber as separated streams. The vapor is reheated in the heat exchanger to 530F before entering the second turbine stage. The open feedwater heater operates at 100 lbf/in2, and the condenser pressure is 1 lbf/in2. Each turbine stage has an isentropic efficiency of 88% and the pumps operate isentropically. For a net power output of 5*109 Btu/h, determine (a) the mass flow rate through the steam generator, in lb/h. (b) the thermal efficiency of the cycle. (c) the rate of heat transfer to the cooling water passing through the condenser, in Btu/h.