Pressure and condition of steam, at inlet to the turbine,
p1 = 35 bar, x = 1
Exhaust pressure, p2 = 0.2 bar
Flow rate, m = 9.5 kg/s

From steam tables :
At 35 bar :
h1 = hg1 = 2802 kJ/kg,
sg1 = 6.1228 kJ/kg K
At 0.26 bar :
hf = 251.5 kJ/kg,
hfg = 2358.4 kJ/kg,
vf = 0.001017 m3/kg,
sf = 0.8321 kJ/kg K,
sfg = 7.0773 kJ/kg K.
(i) The pump work :
Pump work = (p4 – p3)
vf = (35 – 0.2) × 105 × 0.001017 J or 3.54 kJ/kg

Now power required to drive the pump
= 9.5 × 3.54 kJ/s or 33.63 kW.
(ii) The turbine work :
s1 = s2 = sf2 + x2 × sfg2
6.1228 = 0.8321 + x2 × 7.0773

h2 = hf2 + x2 hfg2 = 251.5 + 0.747 × 2358.4 = 2013 kJ/kg
Turbine work = m (h1 – h2) = 9.5 (2802 – 2013) = 7495.5 kW
It may be noted that pump work (33.63 kW) is very small as compared to the turbine work (7495.5 kW).
(iii) The Rankine efficiency :

(iv) The condenser heat flow :
The condenser heat flow = m (h2 – hf3 ) = 9.5 (2013 – 251.5) = 16734.25 kW.
(v) The dryness at the end of expansion, x2 :
The dryness at the end of expansion,
x2 = 0.747 or 74.7%.