06 Mejoramiento Calidad Catodica Planta San Francisco

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    IMPROVING CATHODE QUALITYAT HIGH CURRENT DENSITY ATSAN FRANCISCO EW PLANT

    1

    J. Flores; K. Muoz & G. Zrate

    XIII Seminario Tcnico Cytec 2010

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    IMPROVING CATHODE QUALITY AT HIGH CURRENTDENSITY AT SAN FRANCISCO EW PLANT

    2

    Julio Flores: Cathodes Plants SuperintendentKatherine Muoz: Chief Operations SX-EW

    Gabriel Zrate: Metallurgist Senior Corporative

    Seminario Tcnico Cytec 2010

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    CONTENTS

    GENERAL INFORMATIONSELE

    CATHODE QUALITY

    3

    NEW GUAR REAGENT

    TESTWORK

    RESULTS

    CONCLUSIONS

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    GENERAL INFORMATION

    The plant produces about 37 Kton/year of cathode in San Francisco and

    around 10 Kton/year of cathode in Los Bronces EW Plant.

    4

    In addition, the unit is equipped with a copper sulphate pentahydrate

    equivalents to 3 Kton/year of fine copper.

    ROM ore is dumped with grades below the cut-off grade for the

    concetrator: 0.15 0.75%Cu tot and 80% chalcopyrite (bioleaching

    process)

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    7

    200 m3/h

    COPPER SULPHATE

    SULPHATEPLANT

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    8

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    SELE (SELECTIVE ENHANCED EW)

    Tecnologies developed by New Tech CopperCorporation

    San Francisco Plant is the first plant that has

    9

    mp emen e s c ean ecno ogy nnova on

    Kind of basket that is introduced in the

    electrolyte cell about EW process

    Fiberglass Reinforced Plastic (FRP) structure

    Allows electrodes to maintain a fix position,

    avoiding short-circuits, that improves process

    efficiency and quality

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    CATHODE QUALITY BACKGROUND

    Current Density (A/m2), I (A) vs Period

    350

    400

    450

    500

    (A/m2)

    45

    50

    55

    60

    65

    10

    100

    150

    200

    250

    300

    2002 2003 2004 2005 2006 2007 2008 2009 2010

    Curr.Den

    s.

    15

    20

    25

    30

    35

    40 I(A)

    |

    Period 2002 2003 2004 2005 2006 2007 2008 2009 2010

    I (A) 22,3 36,1 37,9 44,3 48,5 51,4 48,4 54,2 58,0

    Curr. Dens. (A/m2) 183 296 311 363 393 406 384 430 460

    Prod. (t) 11,7 16,8 21,7 27,1 30,5 34,1 33,2 36,6 2,9

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    CATHODE QUALITYUP TO FEBRUARY 2010

    Ao %Off grade Curr.Dens. (A/m2)

    2005 19 363

    2006 27 393

    2007 28 406

    2008 53 384

    2009 60 430

    11

    Higher %off grade is due to much higher cathode weight than required, specially

    at the highest current density

    Have an ambicious action plan

    Improve and implement best practices operational and housekeeping EW plant

    Cathode plant and Metallurgical Department, decided to test a new guar reagent

    (C) in order to improve cathode quality

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    Parameters to Keep Quality San Francisco Plant

    Temperature of Washing Water to Cathodes [C] > 75

    Temperature of Washing Water Chamber to Cathodes [C] > 70

    Temperature Hot Water Tank [C] > 40

    Temperature Electrolyte Income Cell [C] > 55

    Poor Electrolyte Cu+2 [gpl] > 39

    12

    Poor Electrolyte H+ [gpl] 165 to 180

    pH of Washing Water Chamber to Cathodes > 6

    Pressure of Washing Water Cathodes [Psi] > 80

    Especific Flow Rate to Cells [m3/hr/m2] > 0.2

    Weight Laminate to Harvest [Kg] 33 to 37

    Frecuency to Cleaning Same Cell [month] max 12

    Dosification Guar Reagent [gr/t Cu fine] > 90 % Curr.Density

    Dosification Cobalt Sulphate [ppm] > 80 % Curr.Density

    Poor Electrolyte Cl [ppm] 10 to 20

    Poor Electrolyte Mn [ppm] max 90

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    COMPARISON DIFFERENTS REAGENTS"A" "B" "C"

    DESCRIPTION Guar Galactomannon PolymerDerivate

    Guar Galactomannon PolymerDerivate

    Low molecular weight

    carbohydrate, dextrin type,

    oligosaccharide group

    SOLVENT Water Water Water

    13

    WATER VOLUMEN FOR 250 GR/TON8 m

    3

    8 m

    3 4 m3

    SOLUBILITY 95% 85% 99%

    DISSOLUTION T > 25C > 25 > 5C

    DISSOLUTION TIME 2 hours 12 hours 0,5 hours

    HIDRATATION 12 hours 12 hours Not required

    AGITATION Mechanical Mechanical Mechanical or Neumatic

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    "A" "B" "C"

    EFFECTOS ON SX None None None

    OPERATIONALS PROBLEMSLow temperatures tend to form

    gel

    Easy form gel to blocks pumps

    and pipesNone

    CATHODE DEPOSIT ESTRUCTURE Columnar Non defined Columnar

    14

    CATHODES NODULATION Ocassional Frequent None

    CATHODE LOOK Opaque Opaque Bright

    ACID MIST DPRESS None None 10%

    CURRENT DENSITY < 400 A/m2 < 350 A/m2 < 500 A/m2

    MEASUREMENT METHOD None None Yes

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    INDUSTRIAL TEST PROCEDURE (430 g/t)

    First week (25%) : 4 kg C + 11 kg A (per shift)

    Second week (50%) : 7.5 kg C + 7.5 kg A (per shift)

    Third week 75% : 11 k C + 4 k A er shift

    15

    Fourth week (100%) : 15 kg C + 0 kg A (per shift)

    Preparation tank : C addes first with water at < 55C, agitation

    for 30 min and then Guar is added

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    RESULTS

    Main parameters were graphed between April and June 22nd of 2010

    Cathode ualit was evaluated usin S content

    16

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    Current Density vs Period

    430

    450

    2)

    17

    350

    370

    390

    Mar-10 Apr-10 May-10 May-10 Jun-10 Jul-10

    Date

    (Amp/

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    Flow Electrolyte Feed Cells vs Period

    1800

    1900

    2000

    18

    1300

    1400

    1500

    1600

    1700

    Mar-10 Apr-10 May-10 May-10 Jun-10 Jul-10

    Date

    (m3/h)

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    Copper in Electrolytes vs Period

    50

    55

    60

    l

    19

    20

    25

    30

    35

    40

    Mar-10 Apr-10 May-10 May-10 Jun-10 Jul-10

    Date

    Cu+2 g

    Cu Poor

    Cu Rich

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    Temperatures in EW Plant vs Period

    70

    80

    90

    20

    30

    40

    50

    60

    Mar-10 Apr-10 May-10 May-10 Jun-10 Jul-10

    Date

    TC

    TRich electrolyte to cells

    TWashing w ater

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    Average Content of Sulfur into Cathodes vs Period

    30

    35

    40

    45

    )

    21

    0

    5

    10

    15

    2025

    Mar-10 Apr-10 May-10 May-10 Jun-10 Jul-10

    Date

    S(pp

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    Cathode Quality Distribution vs Period

    60

    70

    80

    90100

    e(Sppm)

    22

    0

    10

    20

    30

    4050

    Jan-10 Feb-10 Mar-10 Apr-10 May-10 Jun-10

    Date

    %Cathodegra

    %Special %Total Grade A %Of f grade

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    Average week S content before the test was 6.9 and 22.4 ppm and 14

    ppm as median.

    After test avera e S content was 2.9 and 9.3 m and 6.3 as median.

    24

    Tendence of S content into cathode is to get values < 5 ppm

    According to the graphs, current density and electrolyte flowrate

    decreased after started test. They have opposite effects and overall effect

    is neutralized

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    CONCLUSIONS

    Highest current density in copper EW plant, increase off grade quality in

    cathodes and increase possibilty to have unsafe operation

    25

    eep ng opera ona an me a urg ca parame ers, ensurance goo

    quality and safety operation

    Necessary have a metallurgical senior external advisor

    Decision to test a new guar reagent early this year (C), is a good

    complement for help to improve quality cathode, reducing S content

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    In order to validate the results obtained, it has been recommended to

    continue with 100% addition of C to EW plant, and follow so close sulfur

    content and any effect that residual product may have on the SX plant

    26

    Necessary test differents tecnologies to improve cathode quality

    operating high current density

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    Thank you!