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04-BS-7 · December 2019

Question 8 of 13: Flow Rate in a Gravity Water Supply Pipeline

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

Notes on this paper

04-BS-7 Mechanics of Fluids — December 2019 (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. Constants used throughout (from the paper's own Constants page): g = 9.81 m/s², patm = 100 kPa, ρwater = 1000 kg/m³, SGglycerine = 1.26, SGmercury = 13.56, ρconcrete = 2400 kg/m³, ρair = 1.19 kg/m³ (20°C) / 1.21 kg/m³ (15°C), μwater = 1.0×10⁻³ N·s/m², μair = 1.8×10⁻⁵ N·s/m², Rair = 287 J/kg·K.

Reference texts: F. M. White, Fluid Mechanics, 8th ed. (McGraw-Hill) — fluid statics and manometry (Ch. 2), hydrostatic forces and the middle-third rule (Ch. 2), buoyancy and equilibrium (Ch. 2), dimensional analysis and drag (Ch. 5, 7), pipe friction and the Moody/Colebrook relation (Ch. 6), control-volume momentum and propeller/actuator-disk theory (Ch. 3, 11); J. D. Anderson, Fundamentals of Aerodynamics — wave/compressibility drag divergence (Ch. 5) for the Boeing 747 wind-tunnel chart used in Question 9.

Question 8: Flow Rate in a Gravity Water Supply 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 m
Pipe length, L10 km
Elevation drop (available head), Δz40 m
Absolute roughness, ε1 mm
Kinematic viscosity of water1.0×10⁻&sup6; m²/s

Find. The steady flow rate Q in the pipeline.

Approach. With entrance/exit losses neglected, the entire 40 m elevation drop is consumed by pipe friction: $\Delta z=f(L/D)(V^2/2g)$. Since $f$ itself depends on $V$ (through $Re$), iterate — guess $V$, compute $Re$ and $\epsilon/D$, read/solve $f$ from the Colebrook relation (the Moody diagram in equation form), compute the resulting head loss, and repeat until it matches the given 40 m.

  1. Relative roughness (fixed for all iterations). $$\frac{\epsilon}{D}=\frac{0.001}{1.0}=0.001$$
  2. Iterate on velocity. A trial $V=2.0$ m/s gives $Re=DV/\nu=1.0(2.0)/10^{-6}=2.0\times10^6$; the Colebrook equation at this $Re$ and $\epsilon/D=0.001$ gives $f\approx0.0198$, and $$h_L=f\frac{L}{D}\frac{V^2}{2g}=(0.0198)\left(\frac{10{,}000}{1.0}\right)\frac{(2.0)^2}{2(9.81)}=40.4\ \text{m}$$ very close to the target 40 m; refining slightly downward converges to $V=1.991$ m/s ($Re=1.99\times10^6$, $f=0.0198$, $h_L=40.0$ m exactly).
  3. Flow rate. $$A=\frac{\pi}{4}D^2=0.7854\ \text{m}^2$$ $$Q=AV=(0.7854)(1.991)=\boxed{1.56\ \text{m}^3\text{/s}}$$
QuantityValue
Converged velocity, V1.99 m/s
Reynolds number1.99×10⁶
Friction factor, f0.0198
Flow rate, Q1.56 m³/s