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+// Display mode
+mode(0);
+// Display warning for floating point exception
+ieee(1);
+clear;
+clc;
+disp("Engineering Thermodynamics by Onkar Singh Chapter 5 Example 2")
+T1=(27+273);//temperature of water in K
+T2=(100+273);//steam temperature of water in K
+m=5;//mass of water in kg
+q=2260;//heat of vaporisation at 100 degree celcius in KJ/kg
+Cp=4.2;//specific heat of water at constant pressure in KJ/kg K
+M=18;//molar mass for water/steam
+R1=8.314;//gas constant in KJ/kg K
+disp("total entropy change=entropy change during water temperature rise(deltaS1)+entropy change during water to steam change(deltaS2)+entropy change during steam temperature rise(deltaS3)")
+disp("deltaS1=Q1/T1,where Q1=m*Cp*deltaT")
+disp("heat added for increasing water temperature from 27 to 100 degree celcius(Q1)in KJ")
+disp("Q1=m*Cp*(T2-T1)")
+Q1=m*Cp*(T2-T1)
+disp("deltaS1=Q1/T1 in KJ/K")
+deltaS1=Q1/T1
+disp("now heat of vaporisation(Q2)=m*q in KJ")
+Q2=m*q
+disp("entropy change during phase transformation(deltaS2)in KJ/K")
+disp("deltaS2=Q2/T2")
+deltaS2=Q2/T2
+disp("entropy change during steam temperature rise(deltaS3)in KJ/K")
+disp("deltaS3=m*Cp_steam*dT/T")
+disp("here Cp_steam=R*(3.5+1.2*T+0.14*T^2)*10^-3 in KJ/kg K")
+disp("R=R1/M in KJ/kg K")
+R=R1/M
+T2=(100+273.15);//steam temperature of water in K
+T3=(400+273.15);//temperature of steam in K
+disp("now deltaS3=(m*R*(3.5+1.2*T+0.14*T^2)*10^-3)*dT/T in KJ/K")
+function y = f(T), y =(m*R*(3.5+1.2*T+0.14*T^2)*10^-3)/T , endfunction
+deltaS3 = intg(T2, T3, f)
+disp("total entropy change(deltaS)=deltaS1+deltaS2+deltaS3 in KJ/K")
+deltaS3=51.84;//approximately
+deltaS=deltaS1+deltaS2+deltaS3
+
+