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+clc
+//initialisation of variables
+T= 290 //K
+xa= 0.4
+xb= 0.6
+P= 600 //kPa
+V= 60 //L
+R= 8.314 //J/mol K
+Mp= 44 //kg/kmol
+Mb= 58.12 //kg/kmol
+vp= 0.00171 //m^3/kg
+vb= 0.00166 //m^3/kg
+na= 0.1 //kmol
+nb= 0.15 //kmol
+V1= 0.04000 //m^3
+xa= 0.4
+np= 2
+Vc= 0.1 //m^3
+//CALCULATIONS
+Pasat= %e^(14.435-(2255/T))
+Pbsat= %e^(14.795-(2770/T))
+P1= xa*Pasat+xb*Pbsat
+Na1= P*V/(100*R*T)
+Vp= vp*Mp
+Vb= vb*Mb
+V= na*Vp+nb*Vb
+Vv= V1-V
+nv= P1*Vv/(R*T)
+ya= xa*Pasat/P
+yb=1-ya
+Na= na+ya*nv
+Nb= nb+yb*nv
+//RESULTS
+printf (' initial pressure= %.2f kPa',P1)
+printf (' \n moles of propane= %.5f kmol',Na1)
+printf (' \n initial mole of propane= %.5f kmol',Na)
+printf (' \n initial mole of butane= %.5f kmol',Nb)
+printf (' \n numbar of phases= %.f ',np)
+printf (' \n volume in final state= %.1f m^3',Vc)