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24-MMP-A3 Mineral Processing · December 2018

Question 2 of 4: Iron Ore Grinding Circuit

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.

Question 2: Iron Ore Grinding Circuit (20 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.

Grinding circuit operating data
StageParameterValue
Rod millFeed rate, $F$100 t/h
Rod millFeed grade, $f$35% Fe
Rod millDischarge size, $F_{80}$2500 µm (80% passing)
Magnetic separatorNon-magnetic waste grade, $t$5% Fe
HydrocycloneOverflow grade45% Fe
Ball millCirculating load, $CLR$250%
Ball millProduct size, $P_{80}$150 µm (80% passing)
Ball millBond work index, $W_i$11.5 kWh/t

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.

  1. 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.)
  2. Specific grinding energy (Bond's Third Theory). With $F_{80}=2500\ \mu\text{m}$ (assumption (i)), $P_{80}=150\ \mu\text{m}$ and $W_i=11.5\ \text{kWh/t}$: $$E=10\,W_i\left(\frac{1}{\sqrt{P_{80}}}-\frac{1}{\sqrt{F_{80}}}\right)=10(11.5)\left(\frac{1}{\sqrt{150}}-\frac{1}{\sqrt{2500}}\right)$$ $$E=115\left(0.08165-0.02000\right)=115\times0.06165=\boxed{7.090\ \text{kWh/t}}$$
  3. 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: $$P=E\times C=7.090\times75.0=\boxed{531.7\ \text{kW}}$$
  4. 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: $$Q_{\text{mill}}=C\,(1+CLR)=75.0\times(1+2.50)=75.0\times3.50=\boxed{262.5\ \text{t/h}}$$
QuantityValue
Magnetic concentrate (ball mill fresh feed), $C$75.0 t/h
Non-magnetic waste rejected25.0 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}}$262.5 t/h