The Stillwater geothermal power plant in Nevada, which started full commercial operation in 1986, is designed to operate with seven identical units. Each of these seven units consists of a pair of power cycles, labeled Level I and Level II, operating on the simple Rankine cycle using an organic fluid as the working fluid. The heat source for the plant is geothermal water (brine) entering the vaporizer (boiler) of Level I of each unit at 325°F at a rate of 384,286 lbm/h and delivering 22.79 MBtu/h (€œM€ stands for €œmillion€). The organic fluid that enters the vaporizer at 202.2°F at a rate of 157,895 lbm/h leaves it at 282.4°F and 225.8 psia as saturated vapor. This saturated vapor expands in the turbine to 95.8°F and 19.0 psia and produces 1271 kW of electric power. About 200 kW of this power is used by the pumps, the auxiliaries, and the six fans of the condenser. Subsequently, the organic working fluid is condensed in an air-cooled condenser by air that enters the condenser at 55°F at a rate of 4,195,100 lbm/h and leaves at 84.5°F. The working fluid is pumped and then preheated in a preheated to 202.2°F by absorbing 11.14 MBtu/h of heat from the geothermal water (coming from the vaporizer of Level II) entering the preheated at 211.8°F and leaving at 154.0°F. Taking the average specific heat of the geothermal water to be 1.03 Btu/lbm €¢ °F, determine
(a) The exit temperature of the geothermal water from the vaporizer,
(b) The rate of heat rejection from the working fluid to the air in the condenser,
(c) The mass flow rate of the geothermal water at the preheated, and
(d) The thermal efficiency of the Level I cycle of this geothermal power plant.

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Vapor Condenser 8 Air 4 Generator Turbine Fluid pump 6Preheater Vaporizeir Vapor Electricity 7 Working fluid Injection pump Land surfase Production pump Cooler geothermal brine Hot geothermal brine