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+
+clear;
+clc;
+printf("\t Example 2.18\n");
+pa1=0.418*10^5; //partial pressure initially
+pa2=0; //partial pressure of pure air
+r=10/2; //radius of tank in which benzene is stored
+T=(350); //temperature in kelvin
+pt=1*1.013*10^5; //total pressure in pascal
+z=2*10^-3; //gas film thickness in m
+Dab=.2*10^-4; //diffusion coefficient in m^2/s
+R=8314; //universal gas constant
+r=0.2/2; //radius of open bowl is 0.2
+//when air layer is assumed to be stagnant of thickness 2mm
+
+Na=Dab*pt*log((pt-pa2)/(pt-pa1))/(z*R*T); //diffusion flux in kmol/m^2*s
+rate=Na*(3.14*r^2)*18; //rate of loss of evaporation
+printf("\n diffusion rate loss of evaporation :%f *10^-4 kg/s ",rate/10^-4);
+//end \ No newline at end of file