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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 /611/CH6/EX6.8/Chap6_Ex8_R1.sce | |
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initial commit / add all books
Diffstat (limited to '611/CH6/EX6.8/Chap6_Ex8_R1.sce')
| -rwxr-xr-x | 611/CH6/EX6.8/Chap6_Ex8_R1.sce | 27 |
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diff --git a/611/CH6/EX6.8/Chap6_Ex8_R1.sce b/611/CH6/EX6.8/Chap6_Ex8_R1.sce new file mode 100755 index 000000000..d736a261e --- /dev/null +++ b/611/CH6/EX6.8/Chap6_Ex8_R1.sce @@ -0,0 +1,27 @@ +// Y.V.C.Rao ,1997.Chemical Engineering Thermodynamics.Universities Press,Hyderabad,India.
+
+//Chapter-6,Example 8,Page 220
+//Title: Power output of the turbine
+//================================================================================================================
+clear
+clc
+
+//INPUT
+P=3;//pressure of superheated steam in MPa
+Ti=300;//temperature at which the steam enters the turbine in degree celsius
+m=1;//mass flow rate of steam in kg/s
+Te=60;//temperature of dry saturated steam when it leaves the turbine in degree celsius
+
+//CALCULATION
+//For steam at P and Ti:
+h1=2995.1;//specific entahlpy of steam in kJ/kg
+
+//For saturated steam at Te:
+h2=2609.7;//specific enthalpy of saturated vapour in kJ/kg
+
+Ws=m*(h1-h2);//calculation of the power output of the turbine using Eq.(6.83) in kW
+
+//OUTPUT
+mprintf("\n The power output of the turbine=%0.1f kW\n",Ws);
+
+//===============================================END OF PROGRAM===================================================
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