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| author | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
|---|---|---|
| committer | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
| commit | 7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 (patch) | |
| tree | dbb9e3ddb5fc829e7c5c7e6be99b2c4ba356132c /3831/CH15/EX15.4/Ex15_4.sce | |
| parent | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff) | |
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initial commit / add all books
Diffstat (limited to '3831/CH15/EX15.4/Ex15_4.sce')
| -rw-r--r-- | 3831/CH15/EX15.4/Ex15_4.sce | 14 |
1 files changed, 14 insertions, 0 deletions
diff --git a/3831/CH15/EX15.4/Ex15_4.sce b/3831/CH15/EX15.4/Ex15_4.sce new file mode 100644 index 000000000..f0030907e --- /dev/null +++ b/3831/CH15/EX15.4/Ex15_4.sce @@ -0,0 +1,14 @@ +// Example 15_4
+clc;funcprot(0);
+// Given data
+m_H2O=9.00;// moles
+m_m=109;// moles
+p_t=14.7;// The total pressure of the mixture in psia
+
+// Calculation
+X_H2O=m_H2O/m_m;// The mole fraction
+p_H2O=X_H2O*p_t;// psia
+// By interpolation in Table C.1a in Thermodynamic Tables to accompany Modern Engineering Thermodynamics, we find that
+T_DP=108;// °F
+T_DP=(108-32)/1.8;// °C
+printf("\nThus, the exhaust products must be cooled to %3.0f°F(%2.1f°C)or below to condense the water of combustion and have an essentially dry exhaust gas.",(T_DP*1.8+32),T_DP);
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