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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 /572/CH13/EX13.13/c13_13.sce | |
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Diffstat (limited to '572/CH13/EX13.13/c13_13.sce')
-rwxr-xr-x | 572/CH13/EX13.13/c13_13.sce | 21 |
1 files changed, 21 insertions, 0 deletions
diff --git a/572/CH13/EX13.13/c13_13.sce b/572/CH13/EX13.13/c13_13.sce new file mode 100755 index 000000000..acc14c9c6 --- /dev/null +++ b/572/CH13/EX13.13/c13_13.sce @@ -0,0 +1,21 @@ +//(13.13) Steam at 5 bar, 240C leaks from a line in a vapor power plant. Evaluate the flow exergy of the steam, in kJ/kg, relative to an environment at 25C, 1 atm in which the mole fraction of water vapor is yeH2O = 0.0303
+
+
+//solution
+Rbar = 8.314 //universal gas constant in SI units
+Tnot = 298 //in kelvin
+//With data from the steam tables
+h = 2939.9 //in kj/kg
+hnot = 104.9 //in kj/kg
+s = 7.2307 //in kj/kg
+snot = .3674 //in kj/kg
+//With data from Table A-25
+gbarH2Oliq = -237180
+gbarH2Ogas = -228590
+yeH2O = .0303
+M =18 //molar mass of steam
+
+ech = (1/M)*(gbarH2Oliq-gbarH2Ogas + Rbar*Tnot*log(1/yeH2O)) //in kj/kg
+
+ef = h-hnot-Tnot*(s-snot) + ech //in kj/kg
+printf(' the flow exergy of the steam, in kJ/k is: %f',ef)
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