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  • 7/27/2019 Frank Peter Van Der Meer_1

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    PILOT HPGR CAMPAIGN AT

    THE CODELCO EL

    TENIENTE COPPER MINE

    F.P. van der MeerR. DickeP. Morales

    H. Elgueta M.P. Negroni

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    Location: Codelco El Teniente plant, near Rancagua,

    89 km south of Santiago, Chile.

    Plant Capacity: 137,000 tpd.

    Reserves ca. 2.5 billion tons grading ca. 0.84%.Ore Type/Mineralogy: Porphyry copper & molybdenite mineralogy.

    with copper- and sulphide rich breccia

    (Biotite, Tourmaline, Anhydrite).

    UCS 90-140 MPa

    Production: approximately 430,000 t/y refined copper

    Processing Scheme: SAG and conventional milling, followed by

    flotation, thickening and filtration

    CODELCO EL TENIENTE COPPER OPERATION

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    REASONS for ON-SITE PILOT WORK

    1. Variability testing of different ore types

    where representative testing of smaller ore samples abroad is limited,

    and costs for transport and testing for multiple ore samples is high.

    Samples tested included El Teniente, Andina and Chuquicamata ores.

    2. Testing for periods of extended operation

    to provide an impression of the operability of a roller press,

    acquaintance of the operation, and evaluating availability.

    3. Test the operation in a continuous closed circuit

    4. Realistic indication forwear rate on roll surface and cheek plates

    5. Provide a possibility of on-site determination ofdownstream effects

    (such as the reduced ball mill energy input and improved metallurgy)

    6. Confirmation tests of initial small scale results (at KHD laboratories)

    on a semi-production scale.

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    ARRANGEMENT of PILOT HPGR at EL TENIENTE

    Nominal Capacity: 40-60 t/h

    Circulating load : 50-60 %

    Operating gap approximately 32 mm (1)

    6.0 MM

    Closed circuit 6 mm dry screening

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    SUMMARY of PILOT HPGR KEY DATA

    Stud-Lined Rolls

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    GENERALIZED PILOT HPGR SET-UP FLOW SCHEME

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    PILOT HPGR SET-UP at EL TENIENTE

    Feed Chute

    Pilot HPGR

    Discharge

    Conveyor to

    6 mm screen

    Screen OS

    recycle

    conveyor

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    PARAMETERS TO BE RECORDED & MEASURED(1 second interval from data logger):

    Power consumption (kW) , both motors

    Movable roll position; operating gap, left and right

    Hydraulic pressure; left and right

    Feed rate; from weigh-belt feeder or from sample weight and test duration

    SAMPLES TO BE TAKEN

    Fresh feed

    HPGR effective feed including recycle

    HPGR products. Centre and Edge.

    Screen oversize (recycle)

    Screen undersize

    PRODUCT ANALYSES

    Particle size distribution

    Moisture

    Density (SG)

    Bulk density

    Flake size, proportion and strength

    PILOT HPGR TEST DATA COLLECTION

    AUXILIARY MEASUREMENTS

    Roll surface and lateral wall wear, desagglomeration, screen efficiency

    E ll

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    EXAMPLES OF HPGR TEST DATA SERIES

    Codelco Andina Ore

    E ll t

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    EXAMPLE OF TEST RESULTS

    El Teniente and Andina ores

    Effect of Pressure on Specific Energy and Specific Throughput

    E ll t

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    EXAMPLES OF TEST RESULTS

    HPGR Centre Discharge

    with ca. 10 % flakes

    Weak flakes;

    disintegrate upon handling

    Average Feed & Product Size Distributions

    E ll t

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    EXAMPLE OF TEST RESULTS

    El Teniente and Andina ores

    Effect of Pressure on Product Size

    E cellent

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    Projected roll surface wear life

    from wear rate measurements

    indicates

    7,500 to 12,000 operating hours

    for Stud-Plus Lining

    Optimized conditions ensure

    a strong autogenous roll coating

    ROLL SURFACE WEAR

    Excellent

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    OBSERVATIONS ENCOUNTERED

    Gap skew from feed segregation

    and material flow hindrance in feed chute

    Shallow feed chute did appear to

    limit material passage

    at freezing conditions

    A wider chute and insulation

    did achieve better flow conditions

    Mass flow calculations from belt cuts

    difficult to reconcile with actual throughput

    Weigh belt or feeder more reliable

    Sufficient spares, maintenance and

    availability of support personnel essential

    Excellent

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    COMPARISON OF PERFORMANCEAverage Results

    Excellent

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    CRUSHING CIRCUIT SPECIFIC ENERGY COMPARISON

    Ch 2

    Ch 3

    Mda.Bolas

    Conventional Crushing HPGR

    Mda.

    Bolas

    Ch 2

    Ch HPGR

    Courtesy of Codelco

    AND: Additional savings in

    reduced ball mill energyand finished product generated

    in HPGR discharge

    Excellent

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    COMPARISON OF PERFORMANCE

    average results for Andina, El Teniente and Chuquicamata

    with copper ores at similar conditions

    Excellent

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    INDICATION OF FULL SCALE CAPACITIESof average results for Andina and El Teniente ores

    for a specific pressure of 3.0-4.0 N/mm

    Excellent

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    CONCLUSIONS and OBSERVATIONS

    Andina, El Teniente and Chuquicamata ores were amenable to HPGR

    with performance parameters near average of other copper ores

    Andina was slightly harder than El Teniente and Chuquicamata

    with higher energy input and lower specific throughput

    HPGR offers a lower energy consumption in the crushing circuitof average 18 % against SAG milling and 6-10 % against conventional crushing

    No differences were observed in flotation response

    Presently projected or available HPGR unit sizes

    do facilitate maximum unit capacities of up to 3,000-4,000 tons per hour

    Wear rates measured indicate roll surface life of 8,000 to 12,000 operating hours

    Control and arrangement of a homogenous feed supply is essential

    Pilot plant design needs attention equivalent to a production facility

    Preparation in sampling, mass rate measurement, feed supply is critical

    Excellent

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    I THANK YOU FOR YOUR KIND ATTENTION.

    If you have any questions, I would be happy to answer these.