NivaarExam PrepOfficial exam papers ↗

04-BS-7 · May 2014

Question 9 of 13: Pipe Sizing from the Moody Chart

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

04-BS-7 Mechanics of Fluids — National Examinations, May 2014. Three (3) hours, closed book. Section A: Calculative (9 questions, do 7); Section B: Analytical/Graphical (4 questions, do 3). Ten questions constitute a complete paper (50 marks). Every printed question is solved below, including the two "extra" questions in each Section beyond the minimum required.

Reference texts: White, Fluid Mechanics, 8th ed. (fluid statics & capillarity Ch.2; Bernoulli/energy equation Ch.3; pipe friction & the Moody chart Ch.6; drag on immersed bodies Ch.7; buoyancy Ch.2; momentum & jet propulsion Ch.3).

Question 9 — Pipe Sizing from the Moody Chart (5 marks)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given.

QuantityValue
Pipe roughness, e0.06 mm
Pipe length, L500 m
Oil density, ρ800 kg/m³
Oil viscosity, μ0.048 Ns/m²
Flow rate, Q0.3 m³/s
Available head, hf190−120 = 70 m

Find. A pipe diameter (0.2–0.4 m range) that delivers 0.3 m³/s under the available 70 m head.

Approach. Write f and Re as functions of trial D, evaluate two or three trial diameters against the Moody chart (equivalent here to the Colebrook equation the chart plots), and interpolate for the D whose (Re, e/D) point gives an f that satisfies the Darcy–Weisbach head-loss equation with the required 70 m.

  1. Express f and Re in terms of D. With V=4Q/(πD²): $$Re = \frac{{\rho VD}}{{\mu}} = \frac{{4\rho Q}}{{\pi\mu D}} = \frac{{4(800)(0.3)}}{{\pi(0.048)D}} = \frac{{6366}}{{D}}$$ $$h_f = f\frac{{L}}{{D}}\frac{{V^2}}{{2g}} \;\Rightarrow\; f = \frac{{h_f\, D\, 2g}}{{L\,V^2}} = \frac{{h_f\, 2g\, \pi^2D^5}}{{16\,L\,Q^2}}$$
  2. Trial diameters (bracketing the required point, as the chart method asks). At D=0.30 m: Re≈21,200, e/D=0.0002, chart f≈0.026, giving hf≈39.8 m (too low — pipe too large). At D=0.25 m: Re≈25,500, e/D=0.00024, chart f≈0.025, giving hf above 70 m (pipe too small). The required point lies between these trials.
  3. Solve the Colebrook/Darcy–Weisbach system directly (equivalent to reading the intersection of the plotted line through the trial points with the D-implied f–Re curve on the Moody chart): $$\boxed{{D \approx 0.267\text{{ m (267 mm)}}}},\quad V=5.38\text{{ m/s}},\quad Re=2.39\times10^4,\quad f=0.0253$$
QuantityResult
Selected diameter, D≈267 mm (specify next standard size ≥ 267 mm, e.g. NPS 250–300 mm)
Velocity5.38 m/s
Reynolds number2.39×10⁴
Friction factor, f0.0253
Check: the printed Moody chart itself could not be plotted on in this format; the diameter above was obtained by solving the same f(Re, e/D) relationship the chart encodes (Colebrook equation) directly, which reproduces the graphical trial-and-error result the hint describes. Transfer the two trial points (D=0.25 m and D=0.30 m above) onto the actual attachment and draw the connecting line as instructed.