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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/CH4/EX4.8 | |
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initial commit / add all books
Diffstat (limited to '1943/CH4/EX4.8')
-rwxr-xr-x | 1943/CH4/EX4.8/Ex4_8.sce | 31 |
1 files changed, 31 insertions, 0 deletions
diff --git a/1943/CH4/EX4.8/Ex4_8.sce b/1943/CH4/EX4.8/Ex4_8.sce new file mode 100755 index 000000000..65f3383a4 --- /dev/null +++ b/1943/CH4/EX4.8/Ex4_8.sce @@ -0,0 +1,31 @@ + +clc
+clear
+//Input data
+n=6;//Total lancashire boilers in a textile factory
+Ws=6;//Each boiler supplying steam in t/h
+p=16;//Pressure at which steam is supplied in bar
+t=250;//Temperature at which steam is supplied in degree centigrade
+CV=43960;//Calorific value of the fuel oil in kJ/kg
+no=75;//Overall efficiency of the boiler in %
+a=16;//The amount of air required for efficient burning of the fuel inkg
+H=20;//Drought of water gauge required at the base of chimney in mm
+tf=320;//The flue gases leave the boiler in degree centigrade
+ts=300;//The average temperature of the gases in the stack in degree centigrade
+ta=30;//The atmospheric temperature in degree centigrade
+R=0.287;//Real Gas constant in kJ/kgK
+h1=2919.2;//enthalpy at the entrance of the boiler in kJ/kgK
+hf=125.8;//Enthalpy at the feed in kJ/kgK
+pi=3.1412;//Mathematical constant
+g=9.81;//gravitational fore constant in m/s^2
+P=1.013;//Atmospheric pressure in bar
+
+//Calculations
+H1=[(H*R*(273+ta)*(273+ts))]/[P*100*[(273+ts)-(273+ta)]];//The draught produced in m
+Wf=[[(Ws*1000)*6*(h1-hf)]/((no/100)*CV)]/3600;//Air fuel ratio in kg/s
+Wa=a*Wf;//Actual air fuel ratio in kg/s
+Wfg=17*Wf;//Air fuel ratio in kg/s
+D=[[(Wfg*R*(273+ts)*(4/pi))]/[(101.3)*(2*g*H1)^(1/2)]]^(1/2);//Diameter at its base in m
+
+//Output
+printf('(a)The height of the stack H = %3.2f m \n (b)The diameter at its base D = %3.2f m ',H1,D)
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