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authorpriyanka2015-06-24 15:03:17 +0530
committerpriyanka2015-06-24 15:03:17 +0530
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+
+clear;
+clc;
+printf("\t Example 5.6\n");
+
+//part(i)
+y=.048; //humidity kmol water vapour/kmol dry air
+y_bar=y*(18/28.84); //(from chart) absolute humidity
+printf("\n we get absolute humidity as :%f kg of water/kg dry air",y_bar);
+printf("\n we get percentage humidity as(from chart) :%f percent",25.5);
+y_bar=y*(18/28.84); //relative humidity
+Ma=18; //molecular weight
+Mb=28.84; //molecular weight
+Tg=55; //temperature of mixture
+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 VH 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 :%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 H as \t :%f j/kg dry air",H);
+
+//end \ No newline at end of file