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WORKING FLUID SELECTION FOR AN INCREASED EFFICIENCY HYBRIDIZED GEOTHERMAL-SOLAR THERMAL POWER PLANT IN NEWCASTLE, UTAH

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WORKING FLUID SELECTION FOR AN INCREASED EFFICIENCY HYBRIDIZED GEOTHERMAL-SOLAR THERMAL POWER PLANT IN NEWCASTLE, UTAH ( working-fluid-selection-for-an-increased-efficiency-hybridiz )

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In Equation 5 all of the symbols have the same meaning as in Equation 4. ηt is the isentropic efficiency of the turbine and h2s is the enthalpy at the exit conditions of the turbine with the same entropy as in the inlet conditions. If a turbine operated at 100% isentropic efficiency, it would generate the maximum amount of work for the given conditions at the inlet and outlet. After the working fluid exits the turbine, it must be condensed back into the liquid phase in the condenser. By a simplified energy balance the amount of heat energy that will need to be removed from the working fluid per unit mass is the difference in enthalpy at the outlet of the turbine with that of the working fluid in the liquid phase. Equation 6 shows the total cooling load for the condenser. () (6) In this equation Qcond is the rate that heat must be removed from the system, ṁwf is the mass flow rate of the working fluid, h2 is the outlet enthalpy of the turbine and h3 is the enthalpy of the working fluid at saturated liquid conditions. The flow rate of the cooling fluid can be calculated by equating the Qcool terms in Equations 6 and 7 and solving for ṁcool. () (7) In Equation 7 Qcool is the required cooling rate, ṁcool is the mass flow rate of the cooling fluid, Ta is the inlet temperature of the cooling fluid and Tb is the outlet temperature of 27

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WORKING FLUID SELECTION FOR AN INCREASED EFFICIENCY HYBRIDIZED GEOTHERMAL-SOLAR THERMAL POWER PLANT IN NEWCASTLE, UTAH

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