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It is required to evaluate the effects of changing surface condenser size on power plant performance. Consider for simplicity an ideal rankine cycle without feed water heaters. the turbine inlet steam is saturated at 1000 psia and has a mass flow rate of 5 x 10^6 lbm/h. Condenser cooling water is available at 60F. For a condenser heat transfer area of 402467 ft^2 and overall heat transfer coefficient of 435 Btu/h*ft^2, the condenser operates at 1 psia. Now consider that the same plant operates with a condenser that has 15 percent more tubes and 15 percent more cooling water flow. Calculate (a) the new exit water temperature in degrees Fahrenheit (b) the new condenser pressure in pounds per square inch absolute and (c) the new plant power in megawatts and efficiency. Assume that the overall heat transfer coefficient is unchanged.
a gas contained within a piston-cylinder assembly undergoes three processes in series taking the gas from state 1
Steam enters a diffuser operating at steady state with a pressure of 14.7 psi, a temperature of 300F, and a velocity of 500ft/s. Steam exits the diffuser as a saturated vapor with negligible kinetic energy. Heat transfer occurs from the steam to its ..
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Air enters an adiabatic compressor at 100 kPa and 27°C and leaves at 600kPa and 177°C at a rate of 1800kg/h. Determine the volume flow rate of the air at the inlet in m³/s. Determine the power input to the compressor.
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Construct the homogeneous solution in terms of four constant that could be determined from initial conditions and show the equations of motion
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