Solution;
Given;
R=38.9ftlb/lb°R
k=1.4
But ;
778.17ft−lb=1Btu
Hence;
R=0.05Btu/lb°R
(a)
cvcp=k
cp=1.4cv
Also;
cp−cv=R
1.4cv−cv=0.05
cv=0.125Btu/lb°R
Mass =3lb
P1=20psia
T1=140°F= 599.67°R
T2=740°F=1199.67°F
Change in internal energy;
Δu=mcv(T2−T1)
Δu=3×0.125(1199.67−599.67)
Δu=225Btu
Change in enthalpy;
Δh=mcp(T2−T1)
cp=1.4cv=0.175
Δh=3×0.175(1199.67−599.67)
Δh=315Btu
The heat,work
The process is constant volume , hence;
W=0
From first law of thermodynamics ;
Q=Δu=225Btu
(b)
The process is steady flow;
W=v∫dp
W=v(p2−p1)
P2=T1p2×T2=599.6720×1199.67=40.01psia
P2=40.01psia=5761.6lb/ft2
P1v1=mRT1
v1=2880.8053×0.05×599.67=0.0312ft3
W=0.0312(5761.6−2880.805)
W=89.95lb−ft
W=0.1156Btu
Entropy;
Δs=m[cpln(T1T2)−Rln(p1p2)]
Δs=3[0.175ln(599.671199.67)−0.05ln(2880.8055761.6)]
Δs=0.2600Btu/°R
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