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    Depression of pyrite in porphyry

    co er flotation

    Ian Wark Research InstituteAustralian Research Council Special Research Centre

    For Particle and Material Interfaces

    M. Zanin and S. Farrokhpay

    Case Study

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    High pyrite recovery in Cu/Mo operation

    4800 tphd80 = 150 m

    FINAL TAIL

    SCAVENGER

    FINAL CON

    CLEANERCOLUMNS

    ROUGHERFEED

    2.0 % Cp

    1.6 % PyBall Mills

    SIPX

    grade recovery

    Cp % Py % Cp % Py %

    65-70 10-15 88-90 20-30

    Re-grindVertical Mills

    CLNR SCAV1CLNR SCAV2

    Thio Lime

    Case Study

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    Plant Evidence

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    Rougher Con, pH = 10.5, Eh= 250 mV SHE

    Pyrite reports to the Cu concentrate even at

    high pH

    00

    2020

    4040

    6060

    8080

    100100

    1212101088664422

    Flotationrecovery(%)

    PyPy

    Cp

    Case Study

    Pyrite should not float at high pH (Gaudin,1957):

    Maximum pyrite recovery in the

    intermediate size ranges

    true flotation

    pp

    Xanthate adsorp. density [ ]

    OH

    Xlog

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    Possible mechanisms for pyrite recovery

    Cu 2+

    H O2OH

    -CpCp

    1. Insufficient liberation from

    the copper sulphide

    2. Surface Cu activation

    and genuine flotation

    O2

    grinding

    medium

    pyrite

    Cu-sulphide

    e-

    e-Fe 3+

    OH-

    Galvanic interactions in complex sulphideores (Huang & Grano, 2005)

    yy

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    50

    60

    70

    80

    90

    s[%]

    Pyrite Liberation Data - Survey 5

    Pyrite in the Rougher Con is Liberated

    Pyrite is not recovered

    due to mineralogical

    association with

    90-100%30-90%

    0-30%

    Ro Feed

    Ro Conc

    Cell 9 & 10 Conc

    Ro/Scav Tail

    0

    10

    20

    30

    40Ma

    Liberation

    QEM-Scan analysis Case Study

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    Time-of-Flight Secondary Ion Mass

    Spectrometry: ToF-SIMS

    +++

    No.

    ofCou

    nts

    Ga+ 11 kHzMass resolution ~9000

    in Bunched Mode

    7

    m / z

    Pulsed

    electronflood

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    0.5

    0.6

    Pyrite +SIMSAverage with 95% confidence, N=30

    Sample 1 - Rghr Con

    Sample 2 - Cell 10 Con0.5

    0.6

    s

    Pyrite -SIMSAverage with 95% confidence, N=30

    Sample 1 - Rghr Con

    Sample 2 - Cell 10 Con

    Pyrite in the concentrate is Cu activated

    Copper and collector detected on the surface of pyrite

    More Si, Al, K, Ca and O on the slow-floating pyrite Case Study

    Copper (+)

    Fe-S

    0.0

    0.1

    0.2

    0.3

    0.4

    Normalisedcoun

    ts

    Species

    0.0

    0.1

    0.2

    0.3

    0.4

    Normalisedcount

    Species

    IBX (PA-)

    Fe-S

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    Laboratory Work

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    ROCSS- + SO32- + HSO3

    - + O2

    ROH + 2S2O32- + CO2

    X

    SO32-

    Py[5S0] + 5SO32- Py[S2O3

    2-] + 4S2O32-

    S0

    Na2SO3 and DETA to depress pyrite

    Reduced surface hydrophobicity

    Decomposition ofxanthate

    Pyrite

    Cu

    DETAO2

    Cu (OH)2

    2

    CH2Cu

    CH2

    H2N NH

    CH2 CH2}

    Complexation

    with Cu

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    FEEDO2/

    Condit.SIPX DETA, Na2SO3 frother flotation

    Tail

    Conditioning: O2/air/no gas to control Eh and

    DO level in the pulp

    Flotation Baseline

    Rghr Con (Plant)

    Ore 1

    Con 1, 2, 3, 4

    0-30 mins 2 mins 2 mins 1 min

    Rghr Feed (Lab grind)

    +Thio primary coll.

    Ore 2

    Cu % Fe % Cp % Py %

    Ore 1 0.66 3.4 2.0 1.6

    Ore 2 0.44 4.6 1.2 9.7Feed H/G

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    Depression of pyrite in the rougher

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    60

    80

    100

    ery[%]

    60

    80

    100

    ery[%]

    Limited depression of pyrite with lime

    Flotation tests on plant rougher con (60% Cp, 18% Py) (Ore 1)Pyrite is Cu and

    xanthate activated

    0

    20

    40

    0 4 8 12 16 20

    PyriteReco

    time [min]

    pH 12 with Lime

    baseline (pH 10)

    0

    20

    40

    0 20 40 60 80 100

    PyriteReco

    Chalcopyrite Recovery [%]

    pH 12 with Lime

    baseline (pH 10)

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    60

    80

    100

    [%]

    BaselineO2

    O2+DETA

    O2 +Na2SO3

    60

    80

    100

    [%]

    Depression of pyrite with Na2SO3 and DETA

    After intense

    oxygenationFlotation tests on plant rougher con (60% Cp, 18% Py) (Ore 1)

    pH = 10.5 pH = 10.5

    0

    20

    40

    0 20 40 60 80 100

    PyriteRecover

    Chalcopyrite Recovery [%]

    0

    20

    40

    0 4 8 12 16 20

    PyriteRecover

    time [min]

    Baseline

    O2

    O2+DETA

    O2 +Na2SO3

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    Depression of pyrite in the rougher feed

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    80

    100

    [%]

    Baseline

    Xanth+Na2SO3+Xanth

    Xanth+Na2SO3

    80

    100

    [%]

    Baseline

    Xanth+Na2SO3+Xanth

    Xanth+Na2SO3

    No xanthate

    Chalcopyrite is

    not affected

    Na2SO3 reduces the adsorption of xanthate

    on pyrite in the feedFloat tests on rghr feed ground in the lab (1.2% Cp, 10% Py)(Ore 2)

    pH = 10.5 pH = 10.5

    0

    20

    40

    0 3 6 9 12 15

    PyriteRecovery

    time [min]

    No xanthate

    0

    20

    40

    0 20 40 60 80 100

    PyriteRecovery

    Chalcopyrite Recovery [%]Pyrite re-activates if

    further SIPX is added

    after Na2SO3

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    Conclusions (Case Study)

    Pyrite in the feed was Cu activated, and adsorbed xanthate

    even at high pH (>10.5), becoming highly floatable

    Limited pyrite depression was achieved by increasing the pHwith lime

    2 3

    activation of pyrite in the presence of O2, reducing pyrite

    recovery by 50%.

    However, further addition of xanthate after depression withNa2SO3 re-activated pyrite

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    Conclusions (Generic)

    Xanthate collectors appear not to be very selective versuspyrite

    The use of sodium sulphite (Na2SO3) and similar sulphoxyspecies (Na2S2O5, Na2S2O3) or sulphur dioxide gas (SO2) may

    significantly reduce/reverse xanthate adsorption on pyrite

    Pyrite may re-activate down the bank if furhter xanthate isadded

    For ores containing highly floatable pyrite, the use of moreselective collectors (e.g. thionocarbamates) may be preferable

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    Acknowledgements

    The authors acknowledge the financial support of:

    Australian Research Council (ARC)

    Sponsors of the AMIRA International P260E project

    Thank you!