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| author | priyanka | 2015-06-24 15:03:17 +0530 |
|---|---|---|
| committer | priyanka | 2015-06-24 15:03:17 +0530 |
| commit | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (patch) | |
| tree | ab291cffc65280e58ac82470ba63fbcca7805165 /536/CH10/EX10.5 | |
| download | Scilab-TBC-Uploads-b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b.tar.gz Scilab-TBC-Uploads-b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b.tar.bz2 Scilab-TBC-Uploads-b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b.zip | |
initial commit / add all books
Diffstat (limited to '536/CH10/EX10.5')
| -rwxr-xr-x | 536/CH10/EX10.5/Example_10_5.sce | 20 |
1 files changed, 20 insertions, 0 deletions
diff --git a/536/CH10/EX10.5/Example_10_5.sce b/536/CH10/EX10.5/Example_10_5.sce new file mode 100755 index 000000000..d97d91f47 --- /dev/null +++ b/536/CH10/EX10.5/Example_10_5.sce @@ -0,0 +1,20 @@ +clear;
+clc;
+
+printf("Example 10.5\n");
+
+N_dot=50; //Initial maas transfer rate
+D=1.8e-9; //Diffusivity of gas in liquid phase
+
+C_bg=(1/22.4)*(273/293); //bulk gas concentration
+N_C=N_dot*C_bg; //Initial maas transfer rate in terms of cocentration
+h=N_C/0.04;// Effective Mass transfer coefficient
+R=1/h;//Equivalent resistance
+printf("\n Equivalent resistance = %.4f s/m",R);
+R_l=R*9; //Liquid phase resistance
+h_l=1/R_l; //Liquid phase coefficient
+
+//From equation 10.113 and using liquid phase resistance
+t=R_l^2/(%pi/D);
+
+printf("\n The required time is = %.2f *10^-11s",t*1e11)
\ No newline at end of file |