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04-BS-7 · December 2016

Question 9 of 13: Settling Velocity of Magnetite Slurry Particles (Stokes' Law)

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

Notes on this paper

04-BS-7 Mechanics of Fluids — December 2016 (National Examinations, three hours, closed book). Section A (Calculative) offers 9 questions and instructs "do seven"; Section B (Graphical and 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, 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 buoyancy/stability (Ch. 2), Bernoulli and control-volume momentum (Ch. 3), potential (inviscid) flow past a cylinder (Ch. 8), pipe friction and the Moody/Colebrook relation (Ch. 6), open-channel flow (Ch. 10), drag on immersed bodies and Stokes' law (Ch. 7); B. R. Munson et al., Fundamentals of Fluid Mechanics — actuator-disk propeller theory and variable-area tank draining.

Question 9: Settling Velocity of Magnetite Slurry Particles (Stokes' Law) (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
Particle diameter d50 μm = 50×10⁻⁶ m
Particle specific gravity (magnetite)5.0 (ρp=5000 kg/m³)
Carrier fluidwater, ρf=1000 kg/m³, μ=1.0×10⁻³ N·s/m²

Find. Stokes settling velocity, and whether the Stokes assumption is valid for this particle (via its particle Reynolds number).

Approach. Apply Stokes' law (drag-buoyancy-weight balance for a sphere in creeping flow) to get the settling velocity directly from the given data, then compute the particle Reynolds number and compare against the Stokes-law validity range (Re < ~1) implied by the empirical drag-coefficient curve.

  1. Stokes settling velocity. $$v = \frac{2}{9}\frac{(\rho_p-\rho_f)g\,r^2}{\mu} = \frac{2}{9}\frac{(5000-1000)(9.81)(25\times10^{-6})^2}{1.0\times10^{-3}} = \boxed{5.45\ \text{mm/s}}$$
  2. Particle Reynolds number, to check the assumption. $$Re_p = \frac{\rho_f v d}{\mu} = \frac{1000(5.45\times10^{-3})(50\times10^{-6})}{1.0\times10^{-3}} = \boxed{0.27}$$
  3. Compare with the empirical drag curve. The Stokes-law line (CD=24/Re) tracks the measured drag-coefficient curve closely for Re < 1, diverging by only a few percent at Re≈0.27 — well inside the low-Re creeping-flow region of the Drag Diagram for Solid Bodies (spheres). Stokes' law was therefore a good assumption for this particle.
QuantityResult
Settling velocity5.45 mm/s
Particle Reynolds number0.27
Stokes' law valid?Yes — Re≈0.27 is within the creeping-flow (CD=24/Re) region of the empirical curve