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+//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