Applying the Exergy Balance: Closed Systems
Figure P7.96 shows liquid water at 80 lbf/in.2, 300oF entering a flash chamber through a valve at the rate of 22 lb/s. At the valve exit, the pressure is 42 lbf/in.2 Saturated liquid at 40 lbf/in.2 exits from the bottom of the flash chamber and saturated vapor at 40 lbf/in.2 exits from near the top. The vapor stream is fed to a steam turbine having an isentropic efficiency of 90% and an exit pressure of 2 lbf/in.2 For steady-state operation, negligible heat transfer with the surroundings, and no significant effects of motion and gravity, perform a full exergy accounting, in Btu/s, of the net rate at which exergy is supplied:
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