diff options
Diffstat (limited to '797/CH8/EX8.8.s/8_08_solution.sce')
-rw-r--r-- | 797/CH8/EX8.8.s/8_08_solution.sce | 34 |
1 files changed, 34 insertions, 0 deletions
diff --git a/797/CH8/EX8.8.s/8_08_solution.sce b/797/CH8/EX8.8.s/8_08_solution.sce new file mode 100644 index 000000000..f600b8ce0 --- /dev/null +++ b/797/CH8/EX8.8.s/8_08_solution.sce @@ -0,0 +1,34 @@ +//Solution 8-08 +WD=get_absolute_file_path('8_08_solution.sce'); +datafile=WD+filesep()+'8_08_example.sci'; +clc; +exec(datafile) +//function to evaluate friction factor using Colebrook's equation +function [f] = colebrook(epsilon, D, Re) + f = 1; + fnew = (-1.8 * log10(6.9/Re + (epsilon/D/3.7)**1.11))**(-2); //Haaland equation + err = 0.0001; //maximum allowable error + //using fixed point iteration + while abs(fnew - f) > err + f = fnew; + fnew = (-2.0 * log10(epsilon/ D/3.7 + 2.51 / Re/sqrt(f)))**(-2); + end + return f; +endfunction +//unit conversion +D = D / 100; //from [cm] to [m] +Vdot = Vdot * 10**-3; //from [L/s] to [m^3/s] +A_c = %pi / 4 * D**2; // +V = Vdot / A_c; +Re = rho * V * D / mu; //Reynold's number +if Re < 4000 then + printf("As Re < 4000 flow is turbulent"); +end +funcprot(0); +f = colebrook(epsilon, D, Re); //friction factor +sumK_L = K_Lentrance + 2 * K_Lelbow + K_Lvalve + K_Lexit; +h_minor = sumK_L * V**2 / (2 * g); +h_major = f* L/D * V**2 / (2 * g); +h_L = h_minor + h_major; +z1 = z2 + h_L; //from energy equation between 1 and 2 +printf("Free surface of first reservoir must be %1.2f m above the ground level to ensure water flow between two reservoirs at 6 L/s", z1);
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