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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 /587/CH8/EX8.3 | |
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Diffstat (limited to '587/CH8/EX8.3')
-rwxr-xr-x | 587/CH8/EX8.3/example8_3.sce | 38 |
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diff --git a/587/CH8/EX8.3/example8_3.sce b/587/CH8/EX8.3/example8_3.sce new file mode 100755 index 000000000..f1b4e8cd0 --- /dev/null +++ b/587/CH8/EX8.3/example8_3.sce @@ -0,0 +1,38 @@ +clear;
+clc;
+
+//Example8.3[Flow of Oil in a Pipeline through a Lake]
+//Given:-
+Ts=0;//Temp of lake[degree Celcius]
+Ti=20;//Temp of oil[degree Celcius]
+d=0.3;//Diameter[m]
+l=200;//length of pipe[m]
+//At 20 degree Celcius
+rho=888.1;//[kg/m^3]
+nu=9.429*10^(-4);//Kinematic viscosity[m^2/s]
+k=0.145;//[W/m.degree Celcius]
+Cp=1880;//[J/kg.degree Celcius]
+Pr=10863;//Prandtl Number
+v_avg=2;//[m/s]
+//Solution(a)
+Re=v_avg*d/nu;
+disp(ceil(Re),"The Reynolds number is")
+Lt=0.05*Re*Pr*d;//[m]
+disp("m",Lt,"The thermal entry length is")
+Nu=3.66+((0.065*(d/l)*Re*Pr)/(1+(0.04*(((d/l)*Re*Pr)^(2/3)))));
+h=(k*Nu)/d;//[W/m^2.degree Celcius]
+As=%pi*d*l;//[m^2]
+m_=rho*%pi*((d/2)^2)*v_avg;//[kg/s]
+Te=Ts-((Ts-Ti)*exp((-h*As)/(m_*Cp)));//[degree Celcius]
+disp("degree Celcius",Te,"Exit temperature of oil is")
+//Solution(b):-
+ln_del_T=(Ti-Te)/(log((Ts-Te)/(Ts-Ti)));//[degree Celcius]
+disp("degree Celcius",ln_del_T,"The logrithmic mean temperature difference is")
+Q=h*As*ln_del_T;//[W]
+disp("W",Q,"The rate of heat loss from the oil are")
+//Solution(c)
+f=64/Re;//Friction factor is
+del_P=l*rho*(v_avg^2)/(2*d);//[N/m^2]
+disp(del_P);
+W_pump=m_*del_P/rho;//[kW]
+disp("pump just to overcome the friction in the pipe as the oil flows","kW",W_pump/1000,"We need a")
\ No newline at end of file |