21-Mat-A3 Structure and Characterization of Materials · December 2014
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 2014 — 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, roasting, refining, hydrometallurgy and aluminum production — 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.
F. Habashi, Textbook of Hydrometallurgy, 2nd ed. — solvent extraction, distribution ratios, phase-ratio effects.
T. Rosenqvist, Principles of Extractive Metallurgy, 2nd ed. — refining, molten-salt electrolysis, vacuum metallurgy.
B. A. Wills and J. Finch, Wills' Mineral Processing Technology, 8th ed. — comminution, classification, flotation, thickening.
D. R. Gaskell, Introduction to the Thermodynamics of Materials — heat capacities, transformation and reaction enthalpies.
W. G. Pfann, Zone Melting, 2nd ed. — zone refining theory and the normal-freezing distribution equation.
ASM Handbook, Vol. 2 (Nonferrous Alloys) and the CIM / Canadian Institute of Mining practice literature for Canadian smelter and refinery practice.
Given. A ball mill runs in closed circuit with a cyclone. Fresh ore (6 % moisture) joins the cyclone underflow recycle ahead of the mill; the mill discharge is diluted with water before the cyclone. The cyclone overflow, at 100 t/h dry solids, is the final product fed to flotation.
Given data
Quantity
Symbol
Value
Dry ore fed to flotation (cyclone overflow, dry)
Os
100 t/h
Moisture in ore-bin feed
—
6 %
Cyclone feed, % solids
f
30 %
Cyclone underflow, % solids
u
75 %
Cyclone overflow, % solids
o
15 %
Find. (a) The circulating load — the dry-solids tonnage in the underflow recycled to the mill; (b) the water that must be added between the mill discharge and the cyclone to dilute the pulp to 30 % solids.
Figure 1 — Closed-circuit grinding: fresh feed and cyclone underflow both enter the ball mill; the discharge is diluted with water before the cyclone splits it into product overflow and recycled underflow.
Approach. Use a solids balance around the whole circuit to fix the fresh-feed rate, then a coupled solids/water balance around the cyclone alone (its three %solids values) to get the circulating underflow tonnage; finally balance water from the ore bin through the mill to the cyclone feed to isolate the dilution water.
Fix the fresh-feed dry-solids rate. At steady state the underflow recycle enters and leaves the mill loop unchanged, so a solids envelope around the whole circuit (ore bin in, cyclone overflow out) gives fresh feed = product:
$$O_s = 100\ \text{t/h dry} \;\Rightarrow\; \text{fresh feed dry solids} = 100\ \text{t/h}$$
Balance total mass and solids across the cyclone. Let $U_s$ and $O_s$ be the dry-solids tonnages in the underflow and overflow. Total (wet) cyclone feed equals underflow plus overflow, and dividing each stream's solids by its own %solids gives its wet tonnage:
$$\frac{U_s+O_s}{f}=\frac{U_s}{u}+\frac{O_s}{o}$$
with $f=0.30$, $u=0.75$, $o=0.15$. This is the standard two-product balance around a classifier.
Solve for the circulating load $U_s$. Substituting the %solids and clearing fractions,
$$0.30\left(\frac{U_s}{0.75}+\frac{O_s}{0.15}\right)=U_s+O_s
\;\Rightarrow\; 0.4\,U_s+2\,O_s = U_s+O_s \;\Rightarrow\; O_s = 0.6\,U_s$$
$$U_s=\frac{O_s}{0.6}=\frac{100}{0.6}$$
$$\boxed{U_s = 166.7\ \text{t/h dry solids (circulating load)}}$$
As a ratio to fresh feed this is a circulating-load ratio of 167 %, well inside the 100–400 % range typical of a ball-mill–cyclone circuit.
Cross-check with the classic %solids ratio formula. The textbook relation for the wet-tonnage ratio underflow/overflow around a cyclone is $U_{\text{wet}}/O_{\text{wet}}=(f-o)/(u-f)=(30-15)/(75-30)=0.333$. Computing $U_{\text{wet}}=U_s/u=222.2$ t/h and $O_{\text{wet}}=O_s/o=666.7$ t/h gives the same ratio, $222.2/666.7=0.333$, confirming step 3.
Build up the water at each point, starting with the fresh ore-bin feed. At 6 % moisture, the wet ore-bin tonnage is
$$\dot m_{NF}=\frac{100}{1-0.06}=106.4\ \text{t/h},\qquad \text{water}_{NF}=106.4-100=6.4\ \text{t/h}$$
Add the water carried by the recycled underflow. At 75 % solids, $U_{\text{wet}}=166.7/0.75=222.2$ t/h, so its water content is $222.2-166.7=55.6$ t/h. The mill neither adds nor removes water (dilution water is added downstream, before the cyclone), so the mill discharge carries the sum of what entered:
$$\text{water}_{\text{disc}} = 6.4+55.6 = 61.9\ \text{t/h},\qquad \dot m_{\text{disc}} = 106.4+222.2 = 328.6\ \text{t/h}\ (81.2\ \%\ \text{solids})$$
Set the cyclone-feed water demand at 30 % solids. The cyclone feed carries the same $266.7$ t/h of solids ($=U_s+O_s$) but must arrive at 30 % solids:
$$\dot m_{CF}=\frac{266.7}{0.30}=888.9\ \text{t/h},\qquad \text{water}_{CF}=888.9-266.7=622.2\ \text{t/h}$$
Take the difference to get the added dilution water.
$$\text{water added} = \text{water}_{CF}-\text{water}_{\text{disc}} = 622.2-61.9$$
$$\boxed{\text{water added} \approx 560.3\ \text{t/h}}$$