21-Mat-A3 Structure and Characterization of Materials · Dec-10-Met-A3 2018
Question 2 of 7: Mass Balance (20 marks)
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. National Exams, December 2018 — 10-Met-A3, Metal Extraction Processes. Three hours, closed book, one approved calculator (Casio or Sharp). Seven problems of 20 marks each; the rubric asks for any five, and only the first five in the answer book are marked. All seven are solved here, because this set is a study resource rather than an exam script.
Note on the exam title. The printed exam header reads 10-Met-A3, Metal Extraction Processes. The content is extractive metallurgy — mineral processing, mass and heat balances, pyrometallurgical roasting, copper and aluminum production, and electrometallurgy — and is answered as such.
Reference texts. The answers below are keyed to the works normally recommended for this syllabus code:
F. Habashi, Textbook of Pyrometallurgy — roasting, smelting, mass and heat balances.
T. Rosenqvist, Principles of Extractive Metallurgy, 2nd ed. — ironmaking, non-ferrous smelting, electrometallurgy.
B. A. Wills and J. Finch, Wills' Mineral Processing Technology, 8th ed. — pulp density, comminution, froth flotation.
D. R. Gaskell, Introduction to the Thermodynamics of Materials — heat capacities, reaction enthalpies, electrochemistry.
W. G. Davenport et al., Extractive Metallurgy of Copper, 5th ed. — smelting/converting/refining and SX-EW flowsheets.
ASM Handbook, Vol. 2 (Properties and Selection: Nonferrous Alloys); CIM (Canadian Institute of Mining) practice literature for Canadian smelter/refinery practice (e.g. the historic Cominco smelter at Trail, BC, and Rio Tinto's Kitimat, BC aluminum smelter).
Given. A closed-circuit ball mill/cyclone grinding loop: fresh ore enters the mill at 5 % moisture, dilution water is added at the mill discharge, the cyclone feed is 25 % solids, the cyclone underflow (recycled to the mill) is 80 % solids, and the cyclone overflow (10 t/h dry, product to flotation) is 12.5 % solids.
Given data
Quantity
Symbol
Value
Cyclone overflow, dry solids (= flotation feed)
$O$
10 t/h
Fresh ore moisture (ore bin feed)
—
5 %
Cyclone feed, % solids
$s_{CF}$
25 %
Cyclone underflow, % solids
$s_U$
80 %
Cyclone overflow, % solids
$s_O$
12.5 %
Find. (a) The circulating load (underflow, dry t/h) and (b) the water that must be added to the ball mill discharge stream ahead of the cyclone.
Figure 2.1 — The closed-circuit grinding loop. Underflow recycles to the mill as the circulating load; overflow, fixed by the steady-state solids balance at 10 t/h dry, is the only stream that leaves the loop.
Approach. Convert each stream's percent-solids into a water:solids dilution ratio, then close a water balance first around the cyclone (to get the circulating load $U$) and then around the dilution point ahead of it (to get the water to add). No reagent or solids are lost anywhere in the loop, so both balances are exact.
Set the dilution ratios. For a stream at percent solids $s$, the water-to-solids mass ratio is $\mathrm{dil}(s)=(1-s)/s$:
$$A=\mathrm{dil}(0.25)=\frac{0.75}{0.25}=3.000,\quad B=\mathrm{dil}(0.125)=\frac{0.875}{0.125}=7.000,\quad C=\mathrm{dil}(0.80)=\frac{0.20}{0.80}=0.250$$
($A$ = cyclone feed, $B$ = overflow, $C$ = underflow.) The overflow's dry solids are fixed by the steady-state solids balance around the whole circuit: with no other solids exit, $O=10$ t/h, the fresh feed rate.
Part (a) — water balance around the cyclone to find the circulating load. All solids entering the cyclone (the mill-discharge/cyclone-feed stream, dry mass $CF=O+U$) split into overflow $O$ and underflow $U$; the cyclone itself adds or removes no water, so the water entering equals the water leaving:
$$(O+U)A=OB+UC$$
Solving for $U$,
$$U=\frac{O(B-A)}{A-C}=\frac{10\times(7.000-3.000)}{3.000-0.250}=\frac{40.00}{2.750}$$
$$\boxed{U\approx14.5\ \text{t/h dry (circulating load)}}$$
As a fraction of fresh feed, the circulating-load ratio is $U/O\times100=145.5\ \%$ — the mill sees roughly 2.45 times the fresh feed tonnage once recycle is included, which is a realistic figure for a cyclone closed circuit.
Part (b) — water balance at the dilution point to find the water to add. The cyclone feed stream must carry $CF\!\cdot\!A=(O+U)\times3.000=24.545\times3.000=73.64$ t/h of water. Before any dilution water is added, the ball-mill discharge carries only the water that entered the mill: the fresh ore's own moisture, plus the water already riding on the recycled underflow.
$$\text{fresh ore, wet}=\frac{O}{1-0.05}=\frac{10}{0.95}=10.53\ \text{t/h}\ \Rightarrow\ \text{water}_{fresh}=10.53-10=0.53\ \text{t/h}$$
$$\text{water}_U=U\times C=14.545\times0.250=3.64\ \text{t/h}$$
$$\text{water present before dilution}=0.53+3.64=4.16\ \text{t/h}$$
The dilution water added at the discharge makes up the shortfall to the 73.64 t/h the cyclone feed requires:
$$\text{water to add}=73.64-4.16$$
$$\boxed{\text{water to add}\approx69.5\ \text{t/h}}$$
This is by far the larger of the two water additions in the loop — the closed circuit recycles most of its own water via the underflow, but still needs a substantial fresh water make-up to hit a dilute 25 % cyclone feed.