Given : C.O.P. = 6.5 ; W = 50 kW,
h3′ = 201.45 kJ/kg,
hf4 = h1 = 69.55 kJ/kg ;
h2 = 187.53 kJ/kg
cp = 0.6155 kJ/kg K
Temperature, t3 :
Refrigerating capacity = 50 × C.O.P.
= 50 × 6.5 = 325 kW

Heat extracted per kg of refrigerant
= 187.53 – 69.55 = 117.98 kJ/kg
Refrigerant flow rate = \(\cfrac{325}{117.98}\) = 2.755 kg/s
Compressor power = 50 kW
∴ Heat input per kg = \(\cfrac{50}{2.755}\) = 18.15 kJ/kg
Enthalpy of vapour after compression
= h2 + 18.15 = 187.53 + 18.15
= 205.68 kJ/kg
Superheat = 205.68 – h3′ = 205.68 – 201.45
= 4.23 kJ/kg
But 4.23 = 1 × cp (t3 – t3′)
= 1 × 0.6155 × (t3 – 35)
∴ t3 = \(\cfrac{4.23}{0.6155}\) + 35 = 41.87°C.