diff options
author | priyanka | 2015-06-24 15:03:17 +0530 |
---|---|---|
committer | priyanka | 2015-06-24 15:03:17 +0530 |
commit | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (patch) | |
tree | ab291cffc65280e58ac82470ba63fbcca7805165 /2417/CH11/EX11.12/Ex11_12.sce | |
download | Scilab-TBC-Uploads-b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b.tar.gz Scilab-TBC-Uploads-b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b.tar.bz2 Scilab-TBC-Uploads-b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b.zip |
initial commit / add all books
Diffstat (limited to '2417/CH11/EX11.12/Ex11_12.sce')
-rwxr-xr-x | 2417/CH11/EX11.12/Ex11_12.sce | 30 |
1 files changed, 30 insertions, 0 deletions
diff --git a/2417/CH11/EX11.12/Ex11_12.sce b/2417/CH11/EX11.12/Ex11_12.sce new file mode 100755 index 000000000..ebe3a6e28 --- /dev/null +++ b/2417/CH11/EX11.12/Ex11_12.sce @@ -0,0 +1,30 @@ +//scilab 5.4.1
+clear;
+clc;
+printf("\t\t\tProblem Number 11.12\n\n\n");
+// Chapter 11 : Heat Transfer
+// Problem 11.12 (page no. 569)
+// Solution
+
+//From problem 11.9,
+//The bare pipe
+r2=3.50; //Outside diameter //Unit:in.
+r1=3.00; //inside diameter //Unit:in.
+Ti=240; //Inside temperature //unit:fahrenheit
+L=5; //Length //Unit:ft
+k=26; //Unit:Btu/(hr*ft*F) //k=proportionality constant //k=thermal conductivity
+Rpipe=log(r2/r1)/(2*%pi*k*L); //the resistance of pipe //Unit:(hr*F)/Btu
+printf("The resistance of pipe is %f (hr*F)/Btu\n",Rpipe);
+
+//Now,in problem 11.12,
+To=70; //Outside temperature //unit:fahrenheit
+deltaT=Ti-To; //Change in temperature //unit:fahrenheit
+h=0.9; //Coefficient of heat transfer //Unit:Btu/(hr*ft^2*F)
+A=(%pi*r2)/12*L; //Area //Unit:ft^2 //1 inch = 1/12 feet //unit:ft^2
+Rconvection=inv(h*A); //The resistance due to natural convection to the surrounding air //Unit:(hr*F)/Btu
+printf("The resistance due to natural convection to the surrounding air is %f (hr*F)/Btu\n",Rconvection);
+
+Rtotal=Rpipe+Rconvection; //The total resistance //unit:(hr*F)/Btu
+printf("The total resistance is %f (hr*F)/Btu\n\n",Rtotal);
+Q=deltaT/Rtotal; //ohm's law (fourier's equation) //The heat transfer from the pipe to the surrounding air //unit:Btu/hr
+printf("The heat transfer from the pipe to the surrounding air is %f Btu/hr\n",Q);
|