(i) Process on T-s and p-h diagrams :
The processes on T-s and p-h diagrams are shown in


(ii) Mass of refrigerant circulated per minute :
The value of enthalpies and specific volume read from p-h diagram are as under :
h2 = 352 kJ/kg ; h3 = 374 kJ/kg
h4 = h1 = 221 kJ/kg ; v2 = 0.08 m3/kg
Refrigerants effect per kg = h2 – h1 = 352 – 221 = 131 kJ/kg
Volume of refrigerant admitted per min.
= \(\cfrac{\pi}4\) D2L × r.p.m. × 2 × ηvol, for twin cylinder, single acting
= \(\cfrac{\pi}4\) (0.2)2 × 0.15 × 500 × 2 × 0.85 = 4 m3/min
Mass of refrigerant per min = \(\cfrac{4}{0.08}\) = 50 kg/min.
(iii) Cooling capacity in tonnes of refrigeration :
Cooling capacity = 50(h2 – h1) = 50 × 131
= 6550 kJ/min or 393000 kJ/h
= \(\cfrac{393000}{14000}\) = 28.07 TR.
\(\because\) 1 tonne of refrigeration TR = 14000 kJ/h)
(iv) Work per kg = (h2 – h1) = 374 – 352 = 22 kJ/kg
C.O.P. = \(\cfrac{131}{22}\) = 5.95