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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("Example 10.3\n");
+
+P=101.3e3; //pressure of the operating column
+T=295; //Temperature of the operating column
+P_A=7e3; //partial pressure of ammonia
+x=1e-3; //=(y1-y2)Thickness of stationary gas film
+D=2.36e-5; //Diffusivity of ammonia
+
+C_A=(1/22.4)*(273/T)*(P_A/P);//=(C_A1-C_A2)Concentration of ammonia gas
+//X=C_T/C_BM
+X=P*log(P/(P-P_A))/(P-(P-P_A));
+//From equation 10.33
+N_A_=(D/x)*X*(C_A);
+printf("\n The transfer rate per unit area = %.2f *10^-5 kmol/m^2*s",N_A_*1e5) \ No newline at end of file