04-BS-7 · December 2015
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
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 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 |
|---|---|
| Balloon diameter | 600 mm |
| Balloon (envelope) mass | 80 g |
| Ambient temperature | 15°C |
| ρair (15°C) | 1.21 kg/m³ |
| μair | 1.8×10⁻⁵ N·s/m² |
| Rhelium | 2077 J/kg·K |
Find. Terminal rate of rise V.
Approach. Compute the constant net upward force (buoyancy minus helium weight minus envelope weight); at terminal velocity this equals drag, CD·½ρV²A, but CD itself depends on V through the Reynolds number — so guess trial velocities, compute the required CD and the resulting Re for each, and find where those points meet the sphere drag curve on the attached chart.
| Quantity | Result |
|---|---|
| Net upward force | 0.372 N |
| Reynolds number at terminal velocity | ≈ 8.9×10⁴ |
| Drag coefficient (chart intersection) | ≈ 0.45 |
| Rate of rise | ≈ 2.2 m/s |