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24-MMP-B5 Mineral Processing Design and Operations · May 2013

Question 5 of 7: Copper Flotation Circuit – Cumulative Grade and Recovery

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

Notes on this paper

National Exams, 09-MMP-B5 Mill Design & Operations, May 2013, 3 hours, closed book (one Casio or Sharp approved calculator permitted). Answer any five (5) of the seven (7) questions asked – each question is of equal value (20%). Every question (1–7) is answered in full below as a complete study resource.

Reference texts: B.A. Wills & J.A. Finch, Wills' Mineral Processing Technology, 8th ed.; A.L. Mular, D.N. Halbe & D.J. Barratt (eds.), Mineral Processing Plant Design, Practice, and Control (SME, 2002); A.L. Mular & R. Poulin, CAPCOSTS: A Handbook for Estimating Mining and Mineral Processing Equipment Costs (CIM Special Volume 47, 1998); T.J. Napier-Munn, S. Morrell, R.D. Morrison & T. Kojovic, Mineral Comminution Circuits: Their Operation and Optimisation (JKMRC, 1996); R.A. Arterburn, "The Sizing and Selection of Hydrocyclones," in Mular & Bhappu (eds.), Mineral Processing Plant Design; J.A. Finch & G.S. Dobby, Column Flotation (Pergamon, 1990); A.F. Taggart, Handbook of Mineral Dressing.

Question 5: Copper Flotation Circuit – Cumulative Grade and Recovery (20%)

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. All stream %mass/%Cu/%S values above, expressed on a 100-units- of-fresh-feed basis (see table).

Find. Cumulative Cu grade and recovery after each stage of (i) the rougher-scavenger train and (ii) the cleaning train, and the overall final-concentrate grade and recovery.

Approach. Work entirely in "Cu units" = %mass×%Cu/100 (i.e. Cu mass on the 100-units-feed basis), which add directly across streams; close the mass balance at each node first as a check, then accumulate concentrate mass and Cu content stage-by-stage through both the rougher-scavenger train and the cleaner train.

Stream%mass%Cu%S
Feed100.01.433.18
Pri. Rougher conc.5.111.7114.46
Sec. Rougher conc.9.26.057.78
Scavenger conc.12.31.442.53
Scavenger tail (→Final Tails)73.40.111.89
Cleaner-1 conc. (Stream 9)2.629.5331.93
Cleaner-2 conc. (Stream 11)1.330.9032.08
Cleaner-3 conc. (Stream 13)0.430.6632.03
  1. Close the rougher-scavenger mass balance (check). $$100-5.1=94.9\ (\to\text{Sec.Ro feed}),\quad94.9-9.2=85.7\ (\to\text{Scav feed}),\quad 85.7-12.3=\boxed{73.4}$$ matching the given scavenger tail exactly – confirms the rougher-scavenger topology (cascading tails, each stage skimming its own concentrate).
  2. Combined rougher-scavenger concentrate feeding the cleaner train (Stream 8). $$m_8=5.1+9.2+12.3=26.6,\qquad Cu_8=5.1(11.71)/100+9.2(6.05)/100+12.3(1.44)/100=1.331\ \text{Cu units}$$ $$\text{grade}_8=\frac{1.331}{26.6}\times100=\boxed{5.00\%\ \text{Cu}}$$
  3. Cleaner train, stage by stage (feed 26.6 mass / 1.331 Cu units). Cleaner 1: conc(9)=2.6 mass, Cu=2.6(29.53)/100=0.768; tail forward=26.6−2.6=24.0 mass, Cu=1.331−0.768=0.563 (grade 2.35% Cu).
    Cleaner 2: conc(11)=1.3 mass, Cu=1.3(30.90)/100=0.402; tail forward=24.0−1.3=22.7 mass, Cu=0.563−0.402=0.161 (grade 0.71% Cu).
    Cleaner 3: conc(13)=0.4 mass, Cu=0.4(30.66)/100=0.123; tail forward (Stream 14)= 22.7−0.4=22.3 mass, Cu=0.161−0.123=0.0388 (grade 0.17% Cu) – this residual tail joins the scavenger tail as the overall Final Tails.
  4. Final concentrate and final tails. $$m_{FC}=2.6+1.3+0.4=4.3,\quad Cu_{FC}=0.768+0.402+0.123=\boxed{1.292\ \text{Cu units}}$$ $$\text{grade}_{FC}=\frac{1.292}{4.3}\times100=\boxed{30.0\%\ \text{Cu}}$$ $$m_{FT}=73.4+22.3=95.7,\quad Cu_{FT}=73.4(0.11)/100+0.0388=0.1195$$ $$\text{grade}_{FT}=\frac{0.1195}{95.7}\times100=0.125\%\ \text{Cu}$$ Mass check: 4.3+95.7=100.0 ✓. Cu check: 1.292+0.1195=1.412 vs. feed Cu=1.430 (≈1.3% low, attributable to the 2–4-significant-figure rounding of the printed stream assays – see check note).
  5. Overall Cu recovery to final concentrate. $$R=\frac{Cu_{FC}}{Cu_{feed}}\times100=\frac{1.292}{1.430}\times100=\boxed{90.4\%}$$
Feed100, 1.43% CuPri. RougherSec. RougherScavengerFinal Tails95.7, 0.125% CuRegrind Mill+ ThickenerCleaner 1Cleaner 2Cleaner 3Final Conc.4.3, 30.0% Cu90.4% recovery73.4, 0.11%Cu5.1, 11.71%Cu9.2, 6.05%Cu12.3, 1.44%CuStream 8:26.6, 5.00%CuTail 10:24.0, 2.35%CuTail 12:22.7, 0.71%CuTail 14: 22.3, 0.17%CuConc 9:2.6, 29.53%CuConc 11:1.3, 30.90%CuConc 13:0.4, 30.66%Cu
Copper flotation flowsheet mass balance (all figures on a 100-units-fresh-feed basis): rougher-scavenger train at top, regrind/cleaner train below, closing to Final Concentrate and Final Tails.
Stage (cumulative)Mass (% feed)Cu grade (%)Cu recovery (%)
Rougher – Scavenger train
After Primary Rougher5.111.7141.8
After Pri.+Sec. Rougher14.38.0780.7
After Pri.+Sec.+Scavenger26.65.0093.1
Cleaning train
After Cleaner 12.629.5353.7
After Cleaner 1+23.929.9981.8
After Cleaner 1+2+3 (Final Conc.)4.330.090.4
Check: the ≈1.3% shortfall between total Cu accounted for (final conc. + final tails = 1.412 Cu units) and the feed assay (1.430 Cu units) is a normal closure gap from the source's rounded 2–4-significant-figure stream assays, not a modelling error – the rougher-scavenger tail check in Step 1 closes exactly on the mass basis, confirming the flowsheet topology used is correct.