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04-BS-7 · December 2015

Question 9 of 13: Pressure Drop in a Corrugated Aluminum Air Duct

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

Notes on this paper

04-BS-7 Mechanics of Fluids — December 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. Constants used throughout (from the paper's own Constants page): g = 9.81 m/s², ρwater = 1000 kg/m³, ρair = 1.19 kg/m³ (20°C) / 1.21 kg/m³ (15°C), μair = 1.8×10⁻⁵ N·s/m², Rair = 287 J/kg·K, Rhelium = 2077 J/kg·K, patm = 100 kPa.

Reference texts: F. M. White, Fluid Mechanics, 8th ed. (McGraw-Hill) — fluid statics and manometry (Ch. 2), control-volume momentum/energy and propulsion (Ch. 3), potential/inviscid flow around cylinders (Ch. 8), viscosity and Newtonian shear (Ch. 1), pipe friction and the Moody chart (Ch. 6), and drag on immersed bodies (Ch. 7).

Question 9: Pressure Drop in a Corrugated Aluminum Air Duct (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 D150 mm
Corrugation (roughness) height e3 mm
Air flow rate Q0.08 m³/s
ρair (20°C) / μair1.19 kg/m³ / 1.8×10⁻⁵ N·s/m²

Find. Pressure drop per 100 m of straight pipe.

D=150mme=3mme/D = 0.02, Q = 0.08 m³/s
Fig. Q9 — corrugated duct wall gives relative roughness e/D = 3/150 = 0.02, read against the Moody chart at the flow's Reynolds number.

Approach. Compute the mean velocity and Reynolds number, read (or solve via Colebrook) the friction factor at the given relative roughness, then apply the Darcy–Weisbach head-loss formula.

  1. Mean velocity and Reynolds number. $$V = \frac{Q}{A} = \frac{0.08}{\frac{\pi}{4}(0.15)^2} = 4.53\ \text{m/s}, \qquad Re = \frac{\rho VD}{\mu} = \frac{1.19(4.53)(0.15)}{1.8\times10^{-5}} = 4.49\times10^4$$
  2. Relative roughness and friction factor. $$\frac{e}{D} = \frac{0.003}{0.150} = 0.02$$ Reading the Moody chart at Re = 4.5×10⁴ along the e/D=0.02 curve (confirmed by the Colebrook equation): $$f \approx \boxed{0.0495}$$
  3. Darcy–Weisbach head loss per 100 m, converted to a pressure drop. $$\Delta p = f\left(\frac{L}{D}\right)\left(\frac{1}{2}\rho V^2\right) = 0.0495\left(\frac{100}{0.15}\right)\left(\frac{1}{2}(1.19)(4.53)^2\right)$$ $$\Delta p = 0.0495(666.7)(12.19) = \boxed{402\ \text{Pa} = 0.402\ \text{kPa per 100 m}}$$
QuantityResult
Mean velocity4.53 m/s
Reynolds number4.49×10⁴
Friction factor f0.0495
Pressure drop / 100 m402 Pa (0.402 kPa)