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+
+clear;
+clc;
+printf("\t Example 5.5\n");
+
+//part(i)
+y_bar=.0183; //kg water vapour/kg dry air
+printf("\n we get humidity as(from chart) :%f kg of water/kg dry air",y_bar);
+printf("\n we get saturation humidity as(from chart) :%d percent",67);
+Ma=18; //molecular weight
+Mb=28.84; //molecular weight
+Tg=30; //temperature of mixture
+rh=(pa/pa2)*100; //relative humidity in pecentage
+pt=1.013*10^5; //total pressure in pascal
+VH=8315*[(1/Mb)+(y_bar/Ma)]*[(Tg+273)/pt]; //humid volume in m^3mixture/kg of dry air
+printf("\n we get humid volume as \t:%f m^3/kg dry air",VH);
+
+//part(ii)
+Ca=1005;
+Cb=1884;
+Cs=Ca+Cb*y_bar; //humid heat in j/kg dry air degree celcius
+printf("\n we get humid heat as \t\t :%f j/kg dry air degree celcius ",Cs);
+
+//part(iii)
+d=2502300; //latent heat in j/kg
+H=Cs*(Tg-0)+y_bar*d; //enthalpy for refrence temperature of 0 degree
+printf("\n we get Enthalpy H as \t\t:%f j/kg dry air",H);
+
+//part(iv)
+dewpoint=23.5; //dew point temperature in degree celcius
+printf("\n the dew point temperature \t :%f degree celcius",dewpoint);
+
+//end \ No newline at end of file