Initial pressure of steam,
p1=7bar=7×105N/m2
Dryness fraction,
x1=0.98
Law of expansion,
pv1.1=constant
Final pressure of steam,
p2=0.34bar=0.34×105N/m2
At 7 bar :
vg=0.273m3/kgv1=x1vg=0.98×0.273=0.267m3/kgp1v1n=p2v2nv1v2=(p2p1)n10.267u2=(0.347)1.11
or
v2=0.267(0.347)1.11=4.174m3/kg
(i) Work done by the steam during the process :
W=n−1p1v1−p2v2=(1.1−1)7×105×0.267−0.34×105×4.174=0.1105(1.869−1.419)=105×4.5Nm/kg
Work done =103105×4.5=450kJ/kg.
At 0.34 bar : vg=4.65m3/kg , therefore, steam is wet at state 2 (sincev2<vg) .
Now, v2=x2vg , where x2= dryness fraction at pressure p2(0.34bar)
4.174=x2×4.65
or
x2=4.654.174=0.897
The expansion is shown on a p-v diagram in Fig., the area under 1-2 represents the work done per kg of steam.
(ii) Heat transferred :
Internal energy of steam at initial state 1 per kg,
u1=(1−x1)uf+x1ug=(1−0.98)696+0.98×2573=2535.46kJ/kg
Internal energy of steam at final state 2 per kg,
u2=(1−x2)uf+x2ug=(1−0.897)302+0.897×2472=2248.49kJ/kg
Using the non-flow energy equation,
Q=(u2−u1)+W=(2248.49−2535.46)+450=163.03kJ/kg
Heat supplied = 163.03 kJ/kg.
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