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21-Mat-B1 Hydrometallurgy and Electrometallurgy · December 2014

Question 3 of 7: Stokes' law particle settling

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

Notes on this paper

Paper format. National Professional Examinations, December 2014 — 10-Met-B1, Mineral Processing. Three hours, closed book, approved Casio/Sharp calculator only. Six numbered Problems (all compulsory except Problem 5) plus a two-mark Bonus Question. Problem 5's rubric asks for any SIX of eleven sketch-and-describe topics; all eleven topics are answered below.

Note on the exam title

Nothing on the paper is a hydrometallurgy (leaching, solvent extraction, electrowinning) or electrometallurgy question; the syllabus actually examined is comminution and grinding-circuit mass balance, particle settling, flotation kinetics, and mineral-processing equipment/terminology — the physical/mechanical beneficiation stage that precedes hydro- or pyro-metallurgical extraction.

Reference texts. The answers below are keyed to the works normally recommended for this syllabus code:


Problem 3 — Stokes' law particle settling (10 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. Stokes' law $V=gd^2(D_s-D_f)/18\mu$; a $d_1=100$-micron particle settles 1 m in $t_1=1.5$ s (same fluid, same solid and fluid densities, so $g,\mu,D_s,D_f$ are all identical between the two particles); target particle $d_2=10$ microns.

Find. (a) the settling time $t_2$ for the 10-micron particle; (b) two limitations of Stokes' law.

Approach. With every term except $d$ held constant, Stokes' law reduces to $V\propto d^2$; since both particles settle the same 1 m distance, $t=1/V\propto1/d^2$, so the ratio of settling times can be found without computing $g,\mu,D_s,D_f$ individually.

  1. Scale settling time with particle size. $V_1/V_2=(d_1/d_2)^2$ and $t=1/V$ (fixed 1 m drop) gives $$\dfrac{t_2}{t_1}=\left(\dfrac{d_1}{d_2}\right)^2=\left(\dfrac{100}{10}\right)^2=100.$$
  2. Solve for $t_2$. $$t_2=100\times t_1=100\times1.5=\boxed{150\ \text{s}}\ (2.5\ \text{minutes}).$$ A ten-fold reduction in diameter increases the settling time by the square, i.e. a hundred-fold — fine particles settle very slowly, which is the practical reason classification and thickening equipment must be sized generously for the fines fraction.
  3. (b) Limitations of Stokes' law. It is valid only in the laminar (viscous) settling regime, $Re_p=\rho_f v d/\mu\lesssim1$ — larger or denser particles settle fast enough to enter the transitional/turbulent regime, where drag no longer scales linearly with velocity and Stokes over-predicts the settling velocity. It also assumes rigid, smooth spheres settling individually in an infinite, quiescent Newtonian fluid: real ore particles are angular (higher drag than an equal-volume sphere), and at the solids concentrations found in an actual slurry, particles interfere with each other's flow field (hindered settling), which further slows the true settling velocity below the Stokes prediction.
QuantityResult
Settling time, 10-micron particle$\boxed{150\ \text{s} = 2.5\ \text{min}}$
Limitation 1Laminar-flow assumption ($Re_p\lesssim1$) fails for coarser/faster particles
Limitation 2Assumes ideal spheres in dilute, quiescent suspension — angularity and hindered settling both violate this
Check. The $d^2$ scaling used here holds only because the problem keeps particle and fluid density fixed between the two cases (an "ore particle" of unspecified but presumably identical mineralogy in both parts) — if the two particles were different minerals, $(D_s-D_f)$ would also differ and the simple ratio would not apply.