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+clc;clear;
+//Example 15.4
+
+//given data
+Pprod=100;
+
+//from Table A-1
+Mair=29;
+MC=12;
+MH=2;
+
+//from Table A-4
+Psat=3.1698;
+
+//calculations
+//consedering 100 kmol of dry products
+// xC8H18 + a (O2 + 3.76N2) = 10.02CO2 + 0.88C0 + 84.48N2 + bH20
+//from mass balamces
+a=83.48/3.76;
+x=(0.88+10.02)/8;
+b=18*x/2;
+// 1.36C8H18 + 22.2 (O2 + 3.76N2) = 10.02CO2 + 0.88C0 + 84.48N2 + 12.24H20
+// 1 mol conversion
+// C8H18 + 16.32 (O2 + 3.76N2) = 7.37CO2 + 4.13C0 + 61.38N2 + 9H20
+AF= 16.32*4.76*Mair/(8*MC+9*MH);
+disp(AF,'air-fuel ratio of combustion process in kg air/kg fuel')
+// C8H18 + ath (O2 + 3.76N2) = 8CO2 + 9H2O + 3.76athN2
+ath=8+4.5;
+Pth=16.32/ath*4.76/4.76*100;
+Pth=ceil(Pth);
+disp(Pth,'percentage of theoretical air');
+Nprod=7.37+0.65+4.13+61.98+9;
+// Nv/Nprod = Pv/Pprod
+Pv=Psat;
+Nw= (Nprod*Pv-9*Pprod)/(Pv-Pprod);
+disp(Nw,'the amount of H2O that condenses as the products in kmol')