At state 1:P1 = 0.75 bar and T1 = 150°C Applying SF’EE to the control volume Q – Ws = mf [(h2 – h1)+ 1/2(V22 – V12) + g(z2 – z1)] neglecting the changes in kinetic and potential energies.i.e.;
Ws = 1/2(V22 – V12) = g(z2 – z1) = 0 i.e.; Q = m [(h2 – h1)]
From super heat steam table at P1 = 0.75 bar and T1 = 150°C
We have(75 – 50)/(100 – 50) = (h1 – 2780.08)/(2776.38 – 2780.08) h1 = 2778.23 KJ/kg
Also, entropy at state (1) (75 – 50)/(100 – 50) = (s1 – 7.94)/(7.6133 – 7.94)
s1 = 7.77665 KJ/kgK at state (2), the condition is saturated liquid.
From saturated steam table h2 = hf = 384.36 kJ/kg s2 = sf = 1.2129 kJ/kgK
Q = 384.36 – 2778.23 = –2393.87kJ/kg-ve sign shows that heat is rejected by system Total heat rejected
= 5 × 2393.87 = 11.9693 MJ similarly, total change in entropy
= m(s2 – s1) = 5(l.2129 – 7.7767) = – 32.819 kJ/K.