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  • 8/13/2019 Ch01 Nikola Anastasijevic

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    JuCaTecJUMBO ELECTRODE TECHNOLOGY

    FOR COPPER ELECTROWINNING

    N. Anastasijevic1, J.-P.Nepper2 and Michael H. Barker3

    Outokumpu Technology GmbH, Ludwig-Erhard-Strasse 21, D-61440 Oberursel, Germany.1 Vice President. R & D, Telephone + 49 6171 96963 255

    [email protected]

    2 Senior Product Manager Copper, Telephone + 49 6171 96963 [email protected]

    3 Senior Research Metallurgist - Electrochemistry

    Outokumpu Research Oy, Kuparitie 10, FIN-28101 Pori, Finland.

    [email protected]

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    JuCaTecAnastasijevic, Nepper, Barker

    * approx. figures

    METAL ELECTROWINNING

    Production* t/y

    7,900,000

    2,800,000

    Major ProcessesZinc

    Copper

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    The cathode size currently used in copper electrowinning is

    driven more by history and product marketing than bytechnological reasons.

    Taken from the copper refinery process

    at the time when SX-EW was introduced (acceptance).

    EW and copper refinery share the same

    development in terms of cell design, size

    and cathode design (permanent cathode),

    handling, stripping etc..

    JuCaTecAnastasijevic, Nepper, Barker

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    0

    0.5

    1

    1.5

    2

    2.5

    3

    3.5

    4

    1900 1920 1940 1960 1980 2000

    Imm

    ersedarea,

    singlec

    athode(m).

    JuCaTecAnastasijevic, Nepper, Barker

    0

    20

    40

    60

    80

    100

    120

    1900 1920 1940 1960 1980 2000

    Cathod

    esperCell Zinc

    Copper

    Increase of cathode size not yet

    implemented in copper

    electrowinning ( )

    Increase in cell and cathode size

    has been used successfully to

    reduce production costs of

    Zn electrowinning(Cathode/bar contact has been

    a bottleneck for enlargement

    of Zinc cathode)

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    JuCaTecAnastasijevic, Nepper, Barker

    Is the Jumbo size cathode feasible

    for Copper electrowinning?

    If yes, does it work?

    Next Step?

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    JuCaTecAnastasijevic, Nepper, Barker

    FEASIBILITY / BASE CASE:

    130 000 t/y copper EW tankhouse in Chile

    Lead anodes and stainless steel cathodes.

    Same electrolyte composition(40 to 37 g/l Copper and 180 to 185 g/l free acid).

    Same assumptions for both plants:average crane velocity, current density (300 A/m) and 95% availability.

    Use of biggest possible commercially available cell

    84 cathodes for state-of-the-art technology and

    114 cathodes/cell for JuCaTec

    (biggest Jumbo cell used in Zinc electrolysis). Stripping machine capacities:

    450 cathodes/hr for the state-of-the-art technology and

    350 for JuCaTec size cathodes/h (conservative approach).

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    JuCaTecAnastasijevic, Nepper, Barker

    FEASIBILITY / BASE CASE (continuation):

    4m vs. 2m immersed cathode area comparison.

    Investment costs included

    equipment (stripping machine(s), storage racks, crane(s)),

    cell area, power supply, electrolyte piping, cell ventilation systems,engineering, transport to the site and packaging.

    Operating costs included

    power consumption, labour and others e.g. chemicals and consumables.

    Impact of plant size consideredrange: 100,000 to 500,000 t/y electrowon copper

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    JuCaTecAnastasijevic, Nepper, Barker

    FEASIBILITY / RESULTS:

    Savings potential with JuCaTec:

    - lower investment costs, up to 20% savings

    - lower operating costs (up to 10%).

    Reasons:

    - more compact tankhouse (smaller tankhouse footprint)

    - shorter crane distances,

    - less handling (means less labour),

    - reduced number of stripping machines and cranes.

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    JuCaTecAnastasijevic, Nepper, Barker

    VERIFICATION:

    Single Electrode Test

    with artificial electrolyte (done)

    Industrial size Prototype cell test

    (pending)

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    JuCaTecAnastasijevic, Nepper, Barker

    Single Cathode Test Conditions:

    Electrode sizes:

    500 x 2105mm cathode (JuCaTec)500 x 1105mm cathode (state-of-the-art height)

    Anode-to-anode

    centre spacing 100 mm

    Electrolyte at inlet:

    40g/l Cu + 150g/l free acid @ 40C

    C.D. 300 A/m

    Manual stripping

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    JuCaTecAnastasijevic, Nepper, Barker

    19

    8

    65

    3

    4

    2 7

    6

    10

    9a

    8a

    K

    A A A AA

    K K

    Electrically both cells connected in series.

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    JuCaTecAnastasijevic, Nepper, Barker

    easy stripping,

    copper was removed as a single rigid panel

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    JuCaTecAnastasijevic, Nepper, Barker

    During the run monitoring of:

    Cell voltage, TINLET/C & TOUTLET/C

    Electrolyte analysisSampled manually from overflow of CuO enrichment tank

    Cathode analysis

    Cathode ID, map & numbering

    Photos of whole cathode

    After stripping, masses & length of 4 parts measured

    Samples punched (2cm discs)Micrographs

    Cathode Chemical analysis

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    JuCaTecAnastasijevic, Nepper, Barker

    MAIN RESULTS OF THE SINGLE ELECTRODE

    VERIFICATION TEST

    Tests with a single jumbo cathode and artificial electrolyte

    successfully performed:

    - Current Efficiencies > 90%

    - Same Cathode Microstructure and impurity level, e.g.same cathode quality as with normal sized EW cathodes

    - Practically same cell voltage

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    JuCaTecAnastasijevic, Nepper, Barker

    Next step:

    Test of a Prototype industrial size cell

    In-plant Verification (SX-EW)