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A vapor compression refrigeration cycle utilizes R-134a as the working fluid. The refrigerant flow rate is 50 g/s. Vapor at 1TABLE B.5 Thermodynamic Properties of R-134a TABLE B.5.1 Saturated R-134a Temp. (°C) Press. (kPa) -70 -65 -60 -55 -50 -45 -40TABLE B.5.1 (continued) Saturated R-134a Entropy, kJ/k-K Evap. Temp. (C) Press. (kPa) Sat. Liquid h Sat. Vapor hg Sat. VaporTABLE B.5.2 Superheated R-134a V u S V u S Temp. (C) (mº/kg) h (kJ/kg) (kJ/kg) 50 kPa (-40.67°C) (kJ/kg-K) (m/kg) h (kJ/kg) (TABLE B.5.2 (continued) Superheated R-134a Temp. (°C) (m?/k) V u S V S h (kJ/kg) (kJ/kg) 300 kPa (0.56°C) (kJ/kg-K) (m/kg) (kTABLE B.5.2 (continued) Superheated R-134a V U S S Temp. (°C) (m/kg) h (kJ/kg) (kJ/kg) 800 kPa (31.30°C) (kJ/kg-K) (mº/kg) (k

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Vapoun compresion repigeration cycle ter 2 400 3 -100 1 4 5. Fig: TS of VCPS diagram Given: Flow Rate mi= 50 g5 = 0.05 kgls.The temperature leaving Pressure 160kPa. . From the saturation Steam tables, value of the evaporator -1567 258k entering complli Co-efficient of Peaformance (COP) Repigeration capacity Power input to Compresor bob 6-787 2:49 = 2.82 (ii) Entropy Gener

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