Given that; the turbine is running under steady state condition.At inlet: P1 = 3MPa; T1 = 350°C; mf = 1 kg/sec; V1 = 50 m/s; Z1=2m At exit: P2 = 10kPa; x = 0.95; Z2 = 5 m; V2 = 120 m/s Heat exchanged during expansion = Q = – 5 kJ/sec From superheat steam table, at 3MPa and 350ºC h1 = 3115.25 kJ/kgh2 = hf2 + xhfg2 From saturated steam table; at 10kPa h2 = 191.81 + 0.95(2392.82) = 2464.99 kJ/kg
From steady flow energy equation:
Q – Ws = mf [(h2 – h1)+ 1/2(V22 – V12) + g(z2– z1)]
– 5 – WS = 1x [ (2464.99 – 3115.25) + { (120)2 – (50)2}/2 × 1000
+ 9.8 (5 – 2 )/1000] – WS = – 639.28 kJ/sec
WS = 639.28 kJ/sec
If the changes in potential and kinetic energies are neglected; then SFEE as; Q – Ws = mf (h2 – h1) – 5 – 1W2 = 1 × (2464.99 – 3115.25) 1W2
= 645.26 KJ/sec
% Error introduced if the kinetic energy and potential energy terms are ignored:
% Error = [(Ws – 1W2)/Ws ] × 100
= [(639.28 – 645.26)/639.28] x 100
= – 0.935%
So Error is = 0.935%