From Mollier chart :
h1 = 3250 kJ/kg
h2 = 2170 kJ/kg Heat drop (or work done) = h1 – h2
= 3250 – 2170 = 1080 kJ/kg
Heat supplied = h1 – hf2
= 3250 – 173.9 [hf2 = 173.9 kJ/kg at 0.08 bar]
= 3076.1 kJ/kg
Thermal efficiency = \(\cfrac{Work \,done}{Heat \,supplied}\) = \(\cfrac{1080}{3076.1}\) = 0.351 or 35.1%.
Exhaust steam condition, x2
= 0.83 (From Mollier chart).
Second case. Refer
From Mollier chart :
h1 = 3250 kJ/kg ;
h2 = 2807 kJ/kg ;
h3 = 3263 kJ/kg ;
h4 = 2426 kJ/kg.
Work done = (h1 – h2) + (h3 – h4) = (3250 – 2807) + (3263 – 2426) = 1280 kJ/kg
Heat supplied = (h1 – hf4 ) + (h3 – h2)
= (3250 – 173.9) + (3263 – 2807) = 3532 kJ/kg
Thermal efficiency
Condition of steam at the exhaust,
x4 = 0.935 [From Mollier chart].