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04-BS-7 · May 2015

Question 8 of 13: Head Loss in an Annular Duct

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 8: Head Loss in an Annular 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
Duct length, L5 m
Outer diameter, Do25 mm
Inner diameter, Di18 mm
Flow rate, Q0.5 L/s
Materialcopper drawn tubing, ε = 0.0015 mm

Find. The head loss over the 5 m annulus.

Dₒ=25 mmDᵢ=18 mmcopper drawn tubing, water flow ⊥ pageh_L = 4.61 m over the length
Fig. Q8 — for a concentric annulus the hydraulic diameter reduces to Dh = Do − Di, and the Moody chart applies exactly as for a circular pipe of that diameter.

Approach. Replace the true diameter with the hydraulic diameter Dh = 4A/P (which reduces to Do−Di for a concentric annulus), then apply the same Colebrook/Darcy–Weisbach procedure as Question 7.

  1. Flow area and hydraulic diameter: $$A=\frac{\pi}{4}(D_o^2-D_i^2)=\frac{\pi}{4}(0.025^2-0.018^2)=2.364\times10^{-4}\ \text{m}^2, \qquad D_h=D_o-D_i=0.007\ \text{m}$$
  2. Velocity and Reynolds number: $$V=\frac{Q}{A}=\frac{0.0005}{2.364\times10^{-4}}=\boxed{2.12\ \text{m/s}}, \qquad Re=\frac{VD_h}{\nu}=\frac{2.12(0.007)}{1.0\times10^{-6}}=1.48\times10^4$$
  3. Relative roughness and friction factor (drawn tubing, ε = 0.0015 mm, very smooth): $$\frac{\epsilon}{D_h}=\frac{0.0000015}{0.007}=2.14\times10^{-4}, \qquad f\approx0.0283\ \text{(Colebrook at this Re, }\epsilon/D_h\text{)}$$
  4. Head loss: $$h_L=f\frac{L}{D_h}\frac{V^2}{2g}=0.0283\left(\frac{5}{0.007}\right)\frac{2.12^2}{2(9.81)}=\boxed{4.61\ \text{m}}$$
QuantityResult
Hydraulic diameter Dh7 mm
Velocity2.12 m/s
Reynolds number1.48×10⁴
Friction factor0.0283
Head loss4.61 m