04-BS-7 · May 2014
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
04-BS-7 Mechanics of Fluids — National Examinations, May 2014. Three (3) hours, closed book. Section A: Calculative (9 questions, do 7); Section B: Analytical/Graphical (4 questions, do 3). Ten questions constitute a complete paper (50 marks). Every printed question is solved below, including the two "extra" questions in each Section beyond the minimum required.
Reference texts: White, Fluid Mechanics, 8th ed. (fluid statics & capillarity Ch.2; Bernoulli/energy equation Ch.3; pipe friction & the Moody chart Ch.6; drag on immersed bodies Ch.7; buoyancy Ch.2; momentum & jet propulsion Ch.3).
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.
| Quantity | Value |
|---|---|
| Pipe roughness, e | 0.06 mm |
| Pipe length, L | 500 m |
| Oil density, ρ | 800 kg/m³ |
| Oil viscosity, μ | 0.048 Ns/m² |
| Flow rate, Q | 0.3 m³/s |
| Available head, hf | 190−120 = 70 m |
Find. A pipe diameter (0.2–0.4 m range) that delivers 0.3 m³/s under the available 70 m head.
Approach. Write f and Re as functions of trial D, evaluate two or three trial diameters against the Moody chart (equivalent here to the Colebrook equation the chart plots), and interpolate for the D whose (Re, e/D) point gives an f that satisfies the Darcy–Weisbach head-loss equation with the required 70 m.
V=4Q/(πD²):
$$Re = \frac{{\rho VD}}{{\mu}} = \frac{{4\rho Q}}{{\pi\mu D}} = \frac{{4(800)(0.3)}}{{\pi(0.048)D}} = \frac{{6366}}{{D}}$$
$$h_f = f\frac{{L}}{{D}}\frac{{V^2}}{{2g}} \;\Rightarrow\; f = \frac{{h_f\, D\, 2g}}{{L\,V^2}} = \frac{{h_f\, 2g\, \pi^2D^5}}{{16\,L\,Q^2}}$$
| Quantity | Result |
|---|---|
| Selected diameter, D | ≈267 mm (specify next standard size ≥ 267 mm, e.g. NPS 250–300 mm) |
| Velocity | 5.38 m/s |
| Reynolds number | 2.39×10⁴ |
| Friction factor, f | 0.0253 |