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author | priyanka | 2015-06-24 15:03:17 +0530 |
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committer | priyanka | 2015-06-24 15:03:17 +0530 |
commit | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (patch) | |
tree | ab291cffc65280e58ac82470ba63fbcca7805165 /536/CH10/EX10.3/Example_10_3.sce | |
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Diffstat (limited to '536/CH10/EX10.3/Example_10_3.sce')
-rwxr-xr-x | 536/CH10/EX10.3/Example_10_3.sce | 17 |
1 files changed, 17 insertions, 0 deletions
diff --git a/536/CH10/EX10.3/Example_10_3.sce b/536/CH10/EX10.3/Example_10_3.sce new file mode 100755 index 000000000..96665184a --- /dev/null +++ b/536/CH10/EX10.3/Example_10_3.sce @@ -0,0 +1,17 @@ +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 |