Dry saturated steam at 100 bar expands isothermally and reversibly to a
pressure of 10 bar. Calculate per kg of steam :
(i) The heat supplied ;
(ii) The work done
Solution;
Given ,
Initial pressure,"p_1=100" bar
Final pressure,"p_2=10" bar
At 100 bar,for saturated steam,from steam tables ,we have;
"s_1=s_g=5.619kJ\/kg"
"t_{s_1}=311\u00b0c"
At 10 bar and 311°c ,the steam is superheated,hence by interpolation;
"s_2=7.124+(\\frac{311-300}{350-300})(7.301-7.124)=7.163kJ\/kgK"
(i)The heat supplied;
"Q=T(s_2-s_1)"
"Q=584(7.163-5.619)"
"Q=901.7kJ\/kg"
(ii)The work done;
Applying non-flow energy equation;
"Q=(u_2-u_1)+W"
"W=Q-(u_2-u_1)"
From steam tables;
At 100 bar,dry saturated steam;
"u_1=u_g=2545kJ\/kg"
At 10 bar,311°c ,by interpolation;
"u_2=2794+(\\frac{311-300}{350-300})(2875-2794)"
"u_2=2811.8kJ\/kg"
"W=901.7-(2811.8-2545)"
"W=634.9kJ\/kg"
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