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A refrigerator operating on standard vapour compression cycle has a coefficiency performance of 6.5 and is driven by a 50 kW compressor. The enthalpies of saturated liquid and saturated vapour refrigerant at the operating condensing temperature of 35°C are 62.55 kJ/kg and 201.45 kJ/kg respectively. The saturated refrigerant vapour leaving evaporator has an enthalpy of 187.53 kJ/kg. Find the refrigerant temperature at compressor discharge. The cp of refrigerant vapour may be taken to be 0.6155 kJ/kg°C.

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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.

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