Initial conditions of steam:
Pressure (p1)=200kPa=0.2MPa
Quality (X)=0.85
From steam table
vf=0.00106 m3/kg
vg=0.88568 m3/kg
initial state specific volume (v1)= vf+X(vg-vf)
=0.00106+0.85x(0.88568-0.00106)=0.7529m3/kg.
Now heat is supplied at constant volume such that temperature of system becomes
Case-(a) :
Temperature T=4000C,specific volume (v2)=(v1)=0.7529 m3/kg
From steam table the critical temperature Tc=373.94
Since T2=400C >Tc, Steam is super heated ,
From superheated steam table at T=400c and v=0.7530m3/kg,
we get following value of P and v at T=400C
P(MPa) v(m3/kg)
0.40 0.77264
0.45 0.68634
therefore pressure (p) at v=0.7539 m3/kg is given by linear interpolation
P2-0.40=[(0.45-0.4)/(0.68634-0.77264)]x(0.7529-0.7739)
P2=0.4121MPa=412.1 kPa
Case-(a) :
Temperature T=140C, The specific volume of saturated steam(vg)=0.50845 m3/kg
The specific volume of system(v2)=v1=0.7529 m3/kg is more than that of saturatred steam at 140 C.
therefore steam is superheated .
From superheated steam table at T=140C
P(MPa) v(m3/kg)
0.24 0.77616
0.26 0.71495
herefore pressure (P2) at v=0.7539 m3/kg is given by linear interpolation
P2-0.24=[(0.26-0.24)/(0.71495-0.77616)]x(0.7529-0.77616)
P2=0.2461MPa=246.1KPa
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