Refrigerant 134a enters the compressor of a vapor-compression heat pump at 15 lbf/in.2, 0°F and is compressed adiabatically to 160 lbf/in.2, 160°F. Liquid enters the expansion valve at 160 lbf/in.², 95°F. At the valve exit, the pressure is 15 lbf/in.² (a) Determine the isentropic compressor efficiency, in percent. (b) Determine the coefficient of performance. (c) Determine the magnitude of the compressor power input, in Btu per lb of refrigerant flowing.

Elements Of Electromagnetics
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Thermodynamics 1 Pls asap Po thankyou
Refrigerant 134a enters the compressor
of a vapor-compression heat pump at 15
lbf/in.2, 0°F and is compressed
adiabatically to 160 lbf/in.², 160°F. Liquid
enters the expansion valve at 160 lbf/in.²,
95°F. At the valve exit, the pressure is 15
lbf/in.²
(a) Determine the isentropic compressor
efficiency, in percent.
(b) Determine the coefficient of
performance.
(c) Determine the magnitude of the
compressor power input, in Btu per lb of
refrigerant flowing.
(d) Determine the exergy destruction for
the compressor, in Btu per lb of refrigerant
flowing.
(e) Determine the exergy destruction for
the expansion valve, in Btu per lb of
refrigerant flowing.
(f) Determine the magnitude of the exergy
flow accompanying heat transfer for the
evaporator, in Btu per lb of refrigerant
flowing.
(g) Determine the magnitude of the exergy
flow accomanying heat transfer for the
condenser, in Btu per lb of refrigerant
flowing.
Let To = 480°R
Transcribed Image Text:Refrigerant 134a enters the compressor of a vapor-compression heat pump at 15 lbf/in.2, 0°F and is compressed adiabatically to 160 lbf/in.², 160°F. Liquid enters the expansion valve at 160 lbf/in.², 95°F. At the valve exit, the pressure is 15 lbf/in.² (a) Determine the isentropic compressor efficiency, in percent. (b) Determine the coefficient of performance. (c) Determine the magnitude of the compressor power input, in Btu per lb of refrigerant flowing. (d) Determine the exergy destruction for the compressor, in Btu per lb of refrigerant flowing. (e) Determine the exergy destruction for the expansion valve, in Btu per lb of refrigerant flowing. (f) Determine the magnitude of the exergy flow accompanying heat transfer for the evaporator, in Btu per lb of refrigerant flowing. (g) Determine the magnitude of the exergy flow accomanying heat transfer for the condenser, in Btu per lb of refrigerant flowing. Let To = 480°R
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