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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 /905/CH1/EX1.14/1_14.sce | |
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Diffstat (limited to '905/CH1/EX1.14/1_14.sce')
-rwxr-xr-x | 905/CH1/EX1.14/1_14.sce | 23 |
1 files changed, 23 insertions, 0 deletions
diff --git a/905/CH1/EX1.14/1_14.sce b/905/CH1/EX1.14/1_14.sce new file mode 100755 index 000000000..91a82850f --- /dev/null +++ b/905/CH1/EX1.14/1_14.sce @@ -0,0 +1,23 @@ +clear;
+clc;
+
+// Illustration 1.14
+// Page: 39
+
+printf('Illustration 1.14 - Page:39 \n\n');
+// Solution
+
+//*****Data*****
+// Binary gaseous mixture of components A and B
+P = 1; // [bar]
+T = 300; // [K]
+R = 8.314; // [cubic m.Pa/mole.K]
+delta = 1; // [mm]
+y_A1 = 0.7;
+y_A2 = 0.2;
+D_AB = 0.1; // [square cm/s]
+//*****//
+
+// Using equation 1.72
+N_A = (D_AB*10^-4)*(P*10^5)*(y_A1-y_A2)/(R*T*delta*10^-3);
+printf("The molar flux of component A is %f mole/square m.s",N_A);
\ No newline at end of file |