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A small, two-stage, vapor-compression refrigeration unit using R-134a produces 15.0 tons of refrigeration with an evaporator pressure of 100. kPa and a condenser pressure of 1200. kPa. The intermediate flash chamber operates at 400. kPa and the isentropic efficiencies of the compressors in each loop are both 89.0%. The following operating specifications have been developed for the stages (loops):
Stage (Loop) A
Station 1A Compressor A inlet
Station 2sA Compressor A outlet
Station 3A Condenser A outlet
Station 4hA Expansion valve A outlet
P1A = 400.kPa
P2sA = 1200.kPa
X3A = 0.00
H4hA = h3A
S2sA = S1A
P3A = 1200.kPa
Stage (Loop) B
Station 1B Compressor B inlet
Station 2sB Compressor B outlet
Station 3B Condenser B outlet
Station 4hB Expansion valve B outlet
X1B = 1.00
P2sB = 400.kPa
X3B = 0.00
H4hB = h3B
P1B = 100.0kPa
S2sB = S1B
P3B = 400.kPa
For this design, determine
a. The mass flow rate of the refrigerant.
b. The system's coefficient of performance.
c. The total power required by the compressor.
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