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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 /1943/CH2/EX2.8 | |
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initial commit / add all books
Diffstat (limited to '1943/CH2/EX2.8')
-rwxr-xr-x | 1943/CH2/EX2.8/Ex2_8.sce | 37 |
1 files changed, 37 insertions, 0 deletions
diff --git a/1943/CH2/EX2.8/Ex2_8.sce b/1943/CH2/EX2.8/Ex2_8.sce new file mode 100755 index 000000000..2786b5b6b --- /dev/null +++ b/1943/CH2/EX2.8/Ex2_8.sce @@ -0,0 +1,37 @@ + +clc
+clear
+//Input data
+Pl=5.6//Power load in MW
+Hl=1.163//Heat load in MW
+p1=40//Pressure in bar
+T1=500+273//Temperature in K
+p2=0.06//Pressure in bar
+p3=2//Pressure in bar
+CV=25//Calorific value in MJ/kg
+n=88//Boiler efficiency in percent
+T=6//Temperature rise in degree C
+
+//Calculations
+h1=3445.3//Enthalpy in kJ/kg
+s1=7.0901//Entropy in kJ/kg.K
+s2=s1//Entropy in kJ/kg.K
+s3=s1//Entropy in kJ/kg.K
+x2=(s2-1.5301)/5.5970//Dryness fraction
+h2=2706.7//Enthalpy in kJ/kg
+h26=2201.9//Difference in enthalpy in kJ/kg
+w=(Hl*10^3)/h26//Rate of steam extraction in kg/h
+x3=(s1-0.52)/7.815//Dryness fraction
+h3=(149.79+x3*2416)//Enthalpy in kJ/kg
+h4=149.79//Enthalpy in kJ/kg
+ws=((Pl*10^3+(w*(h2-h3)))/((h1-h2)+(h2-h3)))//Steam generation capacity in kg/s
+ws1=(ws*3600)/1000//Steam generation capacity in t/h
+h7=(504.7+(1.061*10^-3*(p1-p3)*100))//Enthalpy in kJ/kg
+h5=(149.79+(1.006*100*p1*10^-3))//Enthalpy in kJ/kg
+Q1=(((ws-w)*(h1-h5))+(w*(h1-h7)))//Heat input in kW
+wf=((Q1/1000)/((n/100)*CV))*(3600/1000)//Fuel burning rate in t/h
+Q2=((ws-w)*(h3-h4))//Heat rejected to the condensor in kW
+wc=(Q2/(4.187*T))/1000//Rate of flow of cooling water in m^3/s
+
+//Output
+printf('(a) the steam generation capacity of the bolier is %3.2f t/h \n (b) the heat input to the boiler is %3.1f kW \n (c) the fuel burning rate of the bolier is %3.3f t/h \n (d) the heat rejected to the condensor is %3.0f kW \n (e) the rate of flow of cooling water in the condensor is %3.3f m^3/s',ws1,Q1,wf,Q2,wc)
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