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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 /1808/CH4/EX4.12/Chapter4_Example12.sce | |
| parent | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff) | |
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initial commit / add all books
Diffstat (limited to '1808/CH4/EX4.12/Chapter4_Example12.sce')
| -rw-r--r-- | 1808/CH4/EX4.12/Chapter4_Example12.sce | 37 |
1 files changed, 37 insertions, 0 deletions
diff --git a/1808/CH4/EX4.12/Chapter4_Example12.sce b/1808/CH4/EX4.12/Chapter4_Example12.sce new file mode 100644 index 000000000..2364593bc --- /dev/null +++ b/1808/CH4/EX4.12/Chapter4_Example12.sce @@ -0,0 +1,37 @@ +clc
+clear
+//INPUT DATA
+p1=5;//pressure in bar
+p2=0.1;//pressure in bar
+m=5;//mass flow rate in kJ/s
+h4=191.8;//Enthalpy in kJ/kg
+h10=2584.7;//Enthalpy in kJ/kg
+S4=0.649;//Entropy in kJ/kg.K
+S10=8.15;//Entropy in kJ/kg.K
+V4=0.001001;//Specific volume in m^3/kg
+h6=640.1;//Enthalpy in kJ/kg
+h9=2747.5;//Enthalpy in kJ/kg
+S6=1.8604;//Entropy in kJ/kg.K
+S9=6.8192;//Entropy in kJ/kg.K
+x2=0.9;//Quality of steam
+Qs=70000;//heat added in boiler in kW
+
+
+//CALCULATIONS
+h2=h6+(x2*(h9-h6));//Enthalpy in kJ/kg
+h5=h4+(V4*(p1-p2));//Enthalpy in kJ/kg
+Wp1=h5-h4;//Pump work in kJ/kg
+mf=((m*(h2-h5))/(h6-h5));//mass flow rate in kJ/s
+h1=((Qs/mf)+h6);//Enthalpy in kJ/kg
+S2=S6+(x2*(S9-S6));//Entropy in kJ/kg.K
+x3=((S2-S4)/(S10-S4));//quality of steam
+h3=h4+(x3*(h10-h4));//Enthalpy in kJ/kg
+Wt=(mf*(h1-h2))+(mf-m)*(h2-h3);//Turbine work in kJ/kg
+nR=((Wt-Wp1)/Qs)*100;//thermal efficiency in percentage
+Wn=Wt-Wp1;//work in kJ/s
+ssc=(mf*3600)/Wn;//specific steam consumption in kg/kW.hr
+R=Wn/Wt;//Work ratio
+
+//OUTPUT
+printf('(i) The Mass flow rate of steam is %3.1f kg/s \n (ii) Thermal efficiency of rankine cycle is %3.1f percentage \n (iii) Specific steam consumption is %3.2f kg/kWhr \n (iv) Work ratio is approximately equal to %f',mf,nR,ssc,R)
+
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