P1=150kPa
x1=0.9
x2=1 (At the end,state is saturated vapour)
V1=V2 (Vapour is in enclosure,so the volume remains constant)
From tables;
At P1=150kPa
hf=467.13kJ/kg
hg=2693.1kJ/kg
vf=0.001053m3/kg
vg=1.1594m3/kg
So,at state point 1;
v1=vf+x1(vg−vf)
v1=0.001053+0.9(1.1594−0.001053)=1.0436m3/kg
And;
h1=hf+x(hg−hf)
h1=467.13+0.9(2693.1−476.13)=2470.503kJ/kg
But;
v1=v2=1.0436m3/kg
Also;
x2=1
Hence;
P2 can be given by linear interpolation between 150kPa and 175kPa;
From the tables,at 175kPa;
vg=1.0037m3/kg
hg=2700.2kJ/kg
Hence;
P2=150+1.0037−1.15941.0436−1.1594(175−150)=168.59kPaAnd;
h2=2693.1+1.0037−1.15941.0436−1.1594(2700.2−2693.1)=2698.38kJ/kg
Heat addition in the process;
Q12=m(u2−u1)
Q12=m(h2−h1)−m(p2v2−p1v1)
By direct substitution;
Q12=5(2698.38−2470.503)−5(168.59×1.0436−150×1.0436)=1042.54kJ
Answers;
P2=168.59kPa
Q=1042.54kJ
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