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04-BS-7 · May 2015

Question 7 of 13: Flow Rate in a Gravity-Fed Concrete Pipeline

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

Notes on this paper

04-BS-7 Mechanics of Fluids — May 2015 (National Examinations, three hours, closed book). Section A (Calculative) offers 9 questions and instructs "do seven"; Section B (Analytical) offers 4 questions and instructs "do three." Every question is answered below (13 of 13), so students can use the full paper as a study resource.

Reference texts: F. M. White, Fluid Mechanics, 8th ed. (McGraw-Hill) — fluid statics (Ch. 2), the linear-momentum and energy equations (Ch. 3), pipe friction and the Moody chart (Ch. 6), and drag on immersed bodies (Ch. 7).

Question 7: Flow Rate in a Gravity-Fed Concrete Pipeline (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 diameter, D1.0 m
Pipe length, L10 000 m
Elevation drop, Δz40 m
Absolute roughness, ε (concrete)1 mm
Water kinematic viscosity, ν1.0×10⁻⁶ m²/s

Find. The steady flow rate Q.

D = 1.00 m, L = 10 kmΔz=40 mQ = 1.564 m³/s
Fig. Q7 — with entrance/exit losses neglected, the full 40 m of elevation drop is spent on pipe friction alone.

Approach. With no pump and no minor losses, all of the elevation drop is consumed by pipe friction. Guess a velocity, read (or here, compute from the Colebrook equation that the Moody chart itself plots) the matching friction factor, and iterate until the friction-loss equation balances the given 40 m — exactly the trial procedure the question describes, done by root-finding instead of by eye on the chart.

  1. Head-loss balance (Darcy–Weisbach, no minor losses): $$\Delta z = h_f = f\frac{L}{D}\frac{V^2}{2g}$$
  2. Relative roughness: $$\frac{\epsilon}{D}=\frac{0.001}{1.0}=0.001$$
  3. Iterate V against f (the Moody chart's own governing curve, the Colebrook equation, solved simultaneously with the head-loss balance): $$\frac{1}{\sqrt{f}}=-2\log_{10}\!\left(\frac{\epsilon/D}{3.7}+\frac{2.51}{Re\sqrt f}\right),\qquad Re=\frac{VD}{\nu}$$ Converging (equivalent to reading the ε/D = 0.001 curve at increasing Re until f·L/D·V²/2g = 40 m is satisfied) gives f ≈ 0.0198 at Re ≈ 1.99×10⁶ (fully rough turbulent flow, consistent with the flat right-hand end of the ε/D=0.001 curve on the chart).
  4. Velocity and flow rate: $$V=\boxed{1.99\ \text{m/s}}, \qquad Q=VA=1.99\left(\frac{\pi}{4}(1.0)^2\right)=\boxed{1.56\ \text{m}^3/\text{s}}$$
QuantityResult
Relative roughness ε/D0.001
Friction factor f0.0198
Reynolds number1.99×10⁶
Velocity1.99 m/s
Flow rate Q1.56 m³/s