diff options
Diffstat (limited to '797/CH8/EX8.3.s')
-rw-r--r-- | 797/CH8/EX8.3.s/8_03_solution.sce | 34 |
1 files changed, 34 insertions, 0 deletions
diff --git a/797/CH8/EX8.3.s/8_03_solution.sce b/797/CH8/EX8.3.s/8_03_solution.sce new file mode 100644 index 000000000..21f9b3267 --- /dev/null +++ b/797/CH8/EX8.3.s/8_03_solution.sce @@ -0,0 +1,34 @@ +//Solution 8-03 +WD=get_absolute_file_path('8_03_solution.sce'); +datafile=WD+filesep()+'8_03_example.sci'; +clc; +exec(datafile) +function [f] = colebrook(epsilon, D, Re) + f = 1; + //Haaland equation + fnew = (-1.8 * log10(6.9/Re + (epsilon/D/3.7)**1.11))**(-2); + 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 + f = fnew; + return f; +endfunction +//unit conversions +D = D / 100; //[cm] to [m] +A_c = %pi / 4 * D**2; //cross sectional area of pipe +V = Vdot / A_c; //average velocity in pipe +Re = rho * V * D / mu; //Reynold's number +if Re > 4000 then + epsilon = 0.002; //roughness for steel pipe [mm] +end +epsilon = epsilon / 1000; //unit conversion from [mm] to [m] +f = colebrook(epsilon, D, Re); +deltaP = f * L * rho * V**2 / (2 * D); +h_L = deltaP / rho / g; +Wdot_pump = Vdot * deltaP; +printf("Pressure drop in pipe is %1.2f kPa", deltaP / 1000); +printf("\nHead loss in pipe is %1.2f m", h_L); +printf("\nPumping power required is %1.0f W", Wdot_pump);
\ No newline at end of file |