NivaarExam PrepOfficial exam papers ↗

04-BS-7 · December 2016

Question 7 of 13: Head Loss in an Outhouse Vent Pipe

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

Notes on this paper

04-BS-7 Mechanics of Fluids — December 2016 (National Examinations, three hours, closed book). Section A (Calculative) offers 9 questions and instructs "do seven"; Section B (Graphical and 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, 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 buoyancy/stability (Ch. 2), Bernoulli and control-volume momentum (Ch. 3), potential (inviscid) flow past a cylinder (Ch. 8), pipe friction and the Moody/Colebrook relation (Ch. 6), open-channel flow (Ch. 10), drag on immersed bodies and Stokes' law (Ch. 7); B. R. Munson et al., Fundamentals of Fluid Mechanics — actuator-disk propeller theory and variable-area tank draining.

Question 7: Head Loss in an Outhouse Vent Pipe (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 D100 mm = 0.100 m
Pipe length (vertical + horizontal) L3.0 + 0.5 = 3.5 m
Flow rate Q110 m³/h = 0.03056 m³/s
Fluidair at 20°C, ρ=1.19 kg/m³, μ=1.8×10⁻⁵ N·s/m²
Fittings (Pipe Flow Data table)short-radius elbow K=0.9; square-edged entrance K=0.5; submerged exit K=1.0
Pipe roughness (plastic, smooth)ε ≈ 0

Find. Total head loss in the pipe, expressed as a differential pressure (Pa).

Approach. Compute the mean velocity and Reynolds number, obtain the Moody friction factor for this hydraulically smooth pipe, sum the major (pipe-friction) and minor (entrance/elbow/exit) losses in metres of the flowing fluid (air), then convert to a pressure using the air density.

  1. Velocity and Reynolds number. $$A = \frac{\pi(0.1)^2}{4} = 7.854\times10^{-3}\ \text{m}^2, \qquad V = \frac{Q}{A} = \frac{0.03056}{7.854\times10^{-3}} = 3.89\ \text{m/s}$$ $$Re = \frac{\rho V D}{\mu} = \frac{1.19(3.89)(0.1)}{1.8\times10^{-5}} = \boxed{25{,}720}\ \text{(turbulent)}$$
  2. Friction factor (Moody chart / smooth-pipe correlation, ε/D ≈ 0). Using the Blasius smooth-pipe fit (equivalent to reading the ε/D=0 curve of the Moody diagram at this Re): $$f = \frac{0.316}{Re^{0.25}} = \frac{0.316}{25{,}720^{0.25}} = \boxed{0.0250}$$
  3. Major (friction) head loss. $$h_{f} = f\frac{L}{D}\frac{V^2}{2g} = 0.0250\left(\frac{3.5}{0.1}\right)\frac{3.89^2}{2(9.81)} = 0.675\ \text{m (air)}$$
  4. Minor losses (entrance + elbow + submerged exit). $$\Sigma K = 0.5+0.9+1.0 = 2.4, \qquad h_{minor} = 2.4\frac{V^2}{2g} = 1.852\ \text{m (air)}$$
  5. Total head loss and equivalent differential pressure. $$h_L = h_f + h_{minor} = 0.675+1.852 = 2.53\ \text{m (of air)}$$ $$\Delta p = \rho_{air}\,g\,h_L = 1.19(9.81)(2.53) = \boxed{29.5\ \text{Pa}}$$
QuantityResult
Velocity V3.89 m/s
Reynolds number25,720
Friction factor f0.0250
Total head loss hL2.53 m (air)
Equivalent differential pressure29.5 Pa