Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
EGBC National Exam — Mining and Mineral Processing Engineering, 09-MMP-A3 Mineral Processing, 2018-Dec. 3 hours duration, closed book; only an approved Casio or Sharp calculator permitted. Four questions constitute a complete exam paper (100 marks total).
Reference texts: Wills & Finch, Wills' Mineral Processing Technology, 8th ed. (comminution, crushers and mills – Ch. 6; classification, hydrocyclones and partition curves – Ch. 9; gravity concentration – Ch. 10; froth flotation, cells, reagents and flotation columns – Ch. 12; metallurgical balances, recovery/enrichment ratio – Ch. 1 & 12; solid-liquid separation, thickening and filtration – Ch. 15); SME Mining Engineering Handbook, 3rd ed. (porphyry copper mill flowsheets); BC Health, Safety and Reclamation Code for Mines, and the MEND/GARD Guide (Global Acid Rock Drainage Guide) for acid mine drainage prediction and control in the Canadian regulatory context.
Find. (1) Ball mill power rating, $P$ (kW). (2) Total ore flowrate through the ball mill, i.e. fresh feed plus circulating load (t/h).
Check – two assumptions bridge the given data: (i) the magnetic separator does not change particle size, so the ball mill circuit's feed size is the rod mill's own discharge size, $F_{80}=2500\ \mu\text{m}$; (ii) the hydrocyclone classifies by size only (not by magnetic content), so its overflow grade (45% Fe) equals the magnetic concentrate's own grade, which is the figure needed to mass-balance the magnetic separator.
Approach. Mass-balance the magnetic separator (two-product formula) to find the ball mill circuit's fresh feed rate; apply Bond's Third Theory of Comminution to that fresh feed rate for the power rating (250% is Bond's own standard test circulating load, so no correction factor is needed); then scale the fresh feed rate up by the circulating load for the total mill throughput.
Magnetic separator mass balance. Treat the separator as a two-product split of the 100 t/h, 35% Fe rod-mill product into a magnetic concentrate (grade $c$, by assumption (ii) equal to the hydrocyclone overflow grade, 45% Fe) and non-magnetic waste (5% Fe):
$$C=F\cdot\frac{f-t}{c-t}=100\times\frac{35-5}{45-5}=100\times\frac{30}{40}=\boxed{75.0\ \text{t/h}}$$
This magnetic concentrate is the ball mill circuit's fresh feed rate. (Non-magnetic waste $=100-75=25.0$ t/h, for the record.)
Specific grinding energy (Bond's Third Theory). With $F_{80}=2500\ \mu\text{m}$ (assumption (i)), $P_{80}=150\ \mu\text{m}$ and $W_i=11.5\ \text{kWh/t}$:
$$E=10\,W_i\left(\frac{1}{\sqrt{P_{80}}}-\frac{1}{\sqrt{F_{80}}}\right)=10(11.5)\left(\frac{1}{\sqrt{150}}-\frac{1}{\sqrt{2500}}\right)$$
$$E=115\left(0.08165-0.02000\right)=115\times0.06165=\boxed{7.090\ \text{kWh/t}}$$
Ball mill power rating. Bond's specific energy is per tonne of new (fresh) feed to the circuit – not per tonne of total mill throughput – and the given 250% circulating load is exactly Bond's own standard closed-circuit test condition, so $E$ applies directly with no correction factor:
$$P=E\times C=7.090\times75.0=\boxed{531.7\ \text{kW}}$$
Total ore flowrate through the ball mill (Part 2). The mill itself processes the fresh feed plus the circulating load returned by the hydrocyclone underflow:
$$Q_{\text{mill}}=C\,(1+CLR)=75.0\times(1+2.50)=75.0\times3.50=\boxed{262.5\ \text{t/h}}$$
Quantity
Value
Magnetic concentrate (ball mill fresh feed), $C$
75.0 t/h
Non-magnetic waste rejected
25.0 t/h
Specific grinding energy, $E$
7.09 kWh/t
(1) Ball mill power rating, $P$
531.7 kW
(2) Total ore flowrate through ball mill, $Q_{\text{mill}}$