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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 /2510/CH17/EX17.16/Ex17_16.sce | |
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initial commit / add all books
Diffstat (limited to '2510/CH17/EX17.16/Ex17_16.sce')
-rwxr-xr-x | 2510/CH17/EX17.16/Ex17_16.sce | 31 |
1 files changed, 31 insertions, 0 deletions
diff --git a/2510/CH17/EX17.16/Ex17_16.sce b/2510/CH17/EX17.16/Ex17_16.sce new file mode 100755 index 000000000..d9192b1de --- /dev/null +++ b/2510/CH17/EX17.16/Ex17_16.sce @@ -0,0 +1,31 @@ +//Variable declaration: +Nf = 125 //Array of fins per meter +w = 1 //Length of fin (m) +//From example 17.15: +t = 4/10**3 //Thickness of fin (m) +Do = 50/10**3 //Outside diameter of tube (m) +Af = 7.157*10**-3 //Fin surface area (m^2) +h = 40 //Heat transfer coefficient (W/m^2.K) +DTb = 180 //Excess temperature at the base of the fin (K) +Qf = 50 //Fin heat transfer rate (W) + +//Calculation: +ro = Do/2 //Radius of tube (m) +wb = w-Nf*t //Unfinned exposed base length (m) +Ab = 2*%pi*ro*wb //Area of the base of the fin (m^2) +At = Ab+Nf*Af //Total heat transfer surface area (m^2) +Qw = h*(2*%pi*ro*w)*DTb //Heat rate without fin (W) +Qb = h*Ab*DTb //Heat rate from the base (W) +Qft = Nf*Qf //Heat rate from the fin (W) +Qt = Qb+Qft //Total heat rate (W) +Qm = h*At*DTb //Maximum heat transfer rate (W) +n = Qt/Qm //Overall fin efficiency +E = Qt/Qw //Overall fin effectiveness +Rb = 1/(h*Ab) //Thermal resistance of base ( C/W) +Rf = 1/(h*Nf*Af*n) //Thermal resistance of fin ( C/W) + +//Result: +printf("The rate of heat transfer per unit length of tube is : %.1f W .",Qt) +printf("Or, the rate of heat transfer per unit length of tube is : %.2f kW .",Qt/10**3) +printf("The overall fin efficiency is : %.1f %%",n*100) +printf("The overall fin effectiveness is : %.2f .",E) |