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THE FIRST LAW OF THERMODYNAMICS
STATE POSTULATE AND SOME PROPERTY RELATIONS
PHYSICAL PROPERTIES OF A PURE SUBSTANCE
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adiabatic air-standard bars Brayton cycle Btu/lb Calculate carbon Carnot Carnot cycle chemical closed system coefficient of performance combustion compression compressor Compute condenser constant pressure constant-volume control volume cooling cycle Determine device dry air entropy change equilibrium evaluate Example exit expansion feedwater heater final pressure final temperature fluid ft/s fuel function given heat engine heat exchanger heat transfer Hence ideal gas initial inlet input interactions internal energy internally reversible irreversible isentropic isothermal kilojoules kinetic kJ/kg macrostate mass flow rate maximum mixture molar molar mass mole nitrogen operates output particles percent piston Prob properties psia pump Pv diagram quantity quasistatic Rankine cycle reaction refrigerant 12 relative humidity reservoir saturated liquid saturated vapor second law shown in Fig Solution specific heat specific volume steady-flow substance Table tank thermal efficiency thermodynamic turbine vapor-compression refrigeration velocity zero