Solution;
Given;
Initial pressure of steam,p1=5.5 bar
Final pressure of steam,p2=0.75 bar
At 5.5 bar;
v1=vg=0.3427m3/kg
Also;
p1v1=p2v2
v2=p2p1v1=0.755.5×0.3427 =2.513m3/kg
At 0.75 bar;
vg=2.217m3/kg
Since v2>vg (At 0.75 bar),the steam is superheated at state 2.
From tables, interpolating,at 0.75 bar,we have;
u2=2510+(2.588−2.2712.513−2.271)(2585−2510)=2567.25kJ/kg
From tables,at 5.5 bar;
u1=ug=2565kJ/kg
Gain in internal energy is;
Δu=u2−u1 =2567.25-2565=2.25kJ/kg
(i)Work done;
W=∫v1v2pdv
But pv=c
W=c[logev]v1v2
In which ;
c=p1v1=p2v2
And;
p2p1=v1v2
Hence ;
W=5.5×105×0.3427×loge(0.755.5)
W=375.543kN-m/kg
(ii)Heat flow;
Using non flow energy equation;
Q=(u2−u1)+W
Q=2.25+375.543
Q=377.79kJ/kg
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