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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 /2762/CH1/EX1.6.5 | |
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initial commit / add all books
Diffstat (limited to '2762/CH1/EX1.6.5')
-rwxr-xr-x | 2762/CH1/EX1.6.5/1_6_5.sce | 11 |
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diff --git a/2762/CH1/EX1.6.5/1_6_5.sce b/2762/CH1/EX1.6.5/1_6_5.sce new file mode 100755 index 000000000..5cea8b264 --- /dev/null +++ b/2762/CH1/EX1.6.5/1_6_5.sce @@ -0,0 +1,11 @@ +//Transport Processes and Seperation Process Principles
+//Chapter 1
+//Example 1.6-5
+//Introduction to engineering principles and units
+//given data
+//heat of formation at 298K for methane is -74.848x10^3 kJ/kg mol, water is 285.840x10^3 kJ/kg mol ,CO is -110.523x10^3 kJ/kg mol,H2 is 0x10^3 kJ/kg mol
+//basis: 1 kg mol of methane at 101.325 kPa and 298K: CH4 + H20 -> CO+ H2
+//std heat of reaction=(sum of heat of formation of pdts)-(sum of heat of formation of pdts)
+H=(-110.523*10^3-3*0)-(-74.848*10^3-285.840*10^3);
+mprintf("the std heat of reaction in is %f kJ/kgmol",H)
+//end
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