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    Improving copper recoveryat Xstrata Coppers Ernest

    Henry Concentrator by

    changing the grindingchemistry

    Chris Greet, Jessica Kinal, John Twomey and Matthew Peatey

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    Flow sheet

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    2002-2004: Ian Wark Research Institute conducted tests on site

    with the Magotteaux Mill, but encountered problems with

    copper activated pyrite.

    September 2004: A SAG mill feed sample tested successfully.

    April 2005: Confirmation study on new SAG feed sample.

    April 2006: Further confirmation study on new SAG feed sample.

    April 2008: Pilot plant trial.

    November 2009: Plant trail commences.

    Project History

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    Laboratory results:

    Pulp chemistry

    Media pH Eh, mV (SHE) DO, ppm EDTA Fe, % EDTA Cu, %

    Forged18% Cr30% Cr

    10.910.910.9

    -2393110

    0.00.40.6

    1.60.20.2

    0.080.100.09

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    10.0

    12.0

    14.0

    16.0

    18.0

    20.0

    22.0

    24.0

    65.0 70.0 75.0 80.0 85.0 90.0 95.0 100.0

    Cu recovery, %

    Cugrade,

    %

    Forged 18% Cr 30% Cr

    TestRecovery, % Dilutent grade

    Cu Au Au, ppm Mo, ppm IS, % NSG, %

    Forged18% Cr30% Cr

    85.688.887.2

    65.770.465.3

    5.45.25.5

    143615521528

    18.314.47.6

    38.442.349.1

    Laboratory results:

    Cu/Au metallurgy

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    Cu rougher

    cel ls 1 and 2

    Cu rougher

    cel ls 3 and 4

    Cu rougher

    cel ls 1 and 2

    Cu rougher

    cel ls 3 and 4

    HiCr pi lot plant bal l mi l l in

    closed circui t with cyclone

    Main plant

    Cu rougher cells 5 to 8 Cu rougher cells 9 to 12

    Cu rougher cells 5 to 8 Cu rougher cells 9 to 12

    Reagents

    Reagents

    Forged pi lot plant bal l mi l l

    in closed circui t with

    cyc lone

    SAG mil l discharge

    Rougher tai l ing

    Cu rougher concentrate

    Rougher tai l ing

    Cu rougher concentrate

    Surge

    tank

    Surge

    tank

    Pilot plant study:

    Pilot plant flow sheet

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    Media Parameters

    pH Eh, mV (SHE) DO, ppm EDTA Fe, % EDTA Cu, %

    Forged18% Cr

    10.310.1

    -8354

    0.030.02

    0.050.03

    0.10.1

    Pilot plant study:

    Pulp chemistry

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    Pilot plant study:

    Metallurgical improvement

    Statistical analysis of the 65 surveys of the pilot plant indicated:

    2.81.8 percent increase in Cu recovery (>99 percent confidence)

    1.30.8 percent increase in Cu grade (>95 percent confidence)

    3.42.2 percent increase in Au recovery (>99 percent confidence)

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    Do nothing.

    Convert the ball mill to high chrome grinding media:

    Dump and replace with an initial charge of high chrome

    Realise benefits earlier

    On/off trial

    Logistical nightmare for a mill of this size

    Media delivery at end of year

    Purge by top-up

    Nominally 8 months to purge the mill

    Compare before and after

    Supply earlier

    Plant trial:

    The options

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    Plant trial:

    Dumping a mill without a hatch!

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    Media Parameters

    pH Eh, mV (SHE) DO, ppm EDTA Fe, % EDTA Cu, %

    Forged18% Cr

    11.511.2

    7598

    0.61.9

    0.640.27

    0.660.26

    Plant trial:

    Pulp chemistry

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    Plant trial:

    Cu recovery improvement

    75

    7779

    81

    83

    85

    87

    89

    91

    93

    95

    0.05 0.10 0.15 0.20 0.25 0.30 0.35

    Feed copper grade, %

    Copperrecovery,

    %

    Forged Chrome Linear (Forged) Linear (Chrome)

    0

    10

    20

    30

    40

    50

    10 100 1000

    Size, micron

    CuD

    istributioninFinalTailing,

    %

    Forged 18% Cr

    The copper recovery increased by 2.4 0.8 percent, with greater than 99percent confidence, which would increase the potential metal value by

    $12,941,000 USD per annum.

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    Conclusions

    The experimental approach adopted was designed to minimise risk to the

    plant. In all three phases of the work it was noted that a change fromforged steel to high chrome grinding media resulted in:

    A shift in the ball mill discharge Eh to more oxidising pulp potentials;

    An increase in the dissolved oxygen content of the pulp; and

    A reduction in the percentage of EDTA extractable iron.

    The pulp chemical changes were due to the change in grinding media can

    be directly linked to improved copper and gold recoveries in the

    laboratory and pilot plant studies.

    In the plant trial the improvement in the copper recoveries was at least1.6 percent due to improved fine chalcopyrite recovery.

    The work demonstrates that using a robust laboratory schedule such as

    the Magotteaux Mill can be used effectively to predict plant performance.