04-BS-7 · December 2019
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
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 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 diameter, D | 1 m |
| Pipe length, L | 10 km |
| Elevation drop (available head), Δz | 40 m |
| Absolute roughness, ε | 1 mm |
| Kinematic viscosity of water | 1.0×10⁻&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.
| Quantity | Value |
|---|---|
| Converged velocity, V | 1.99 m/s |
| Reynolds number | 1.99×10⁶ |
| Friction factor, f | 0.0198 |
| Flow rate, Q | 1.56 m³/s |