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MCS,PHD
Argosy University/ Phoniex University/
Nov-2005 - Oct-2011
Professor
Phoniex University
Oct-2001 - Nov-2016
11.126Â Â An equimolar mixture of O2 and N2 enters a compressor operating at steady state at 10 bar, 220 K with a mass flow rate of 1 kg/s. The mixture exits at 60 bar, 400 K with no significant change in kinetic or potential energy. Stray heat transfer from the compressor can be ignored. Determine for the compressor
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(a)Â Â the power required, in kW.
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(b)Â the rate of entropy production, in kW/K.
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Assume the mixture is modeled as an ideal solution. For the pure components:
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10 bar, 220 K                               60 bar, 400 K
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h (kJ/kg)Â Â Â Â Â Â Â s (kJ/kg ? K)Â Â Â Â Â Â Â Â Â h (kJ/kg)Â Â Â Â Â Â Â s (kJ/kg ? K)
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100 bar,275 K and expands isothermally without irreversibilities to 15 bar. There are no significant changes in kinetic or potential energy. Using data from the generalized fugacity and enthalpy departure charts, determine the power developed and heat transfer, each in kW, for a mass flow rate of 0.5 kg/s.
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