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7/28/2019 Yanacocha GOLD MILL
1/19
July 13, 2005
YANACOCHA GOLD MILL
7/28/2019 Yanacocha GOLD MILL
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July 13, 2005
PROJECT IS STRATEGICALLY IMPORTANT TO
YANACOHA OPERATION
Project is economically attractive.
Ores are becoming more complex. Gold
Mill is an alternative process to treat these
materials.
Gold Mill Facility provides the basefacilities and skills for future complex ores
at Yanacocha.
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RESOURCE SUMMARY FOR GOLD MILL
Total Tonnes
41.5 million tonnes
Average Ore Grade
Au 3.92 g/t Ag 24.37 g/t
Contained Ounces Au 5.2 Moz Ag 32.5 Moz
Recoverable Ounces
Au 4.15 Moz Ag 14.2 Moz
Deep Transition Reserves Ounces (Contained)
Au 980 Koz
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PROCESS
Stockpile
Agglomeration
Primary Crusher
Counter Current
Decantation (CCD)
Acidification, Volatilization,
Re-adsorption (AVR)
Sulfidization, Acidification,
Recirculation & Thickening (SART)
Leach Circuit
24 Hrs
Electrical
Substation
Area
Grinding
circuit
Video
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GOLD MILL PROCESS FLOWSHEET
Crusher Feed Bin
Jaw
Crusher
Stockpile Feed Conveyor
Crushed Ore Stockpile
(11 hr S torage)
Mill Feed Conveyor
SAG Mill (625tph)Ball Mill
(11.5MW)
Cyclones
Linear Trash
Screen
Sump & Pumps
Pre-Leach
Thickener
Process Water Tank
Lime &
Cyanide
Tailings Disposal atLa Quinua Leach Pad
Flocculant
NaHS &
H2SO4
Flocculant
Flocculant
Lime
Carbon Treatment
At La QuinuaH2SO4
NaOH
Recovered NaCN
To Mill Circuit
Flocculant
CONCENTRATE SALES
Feeder & Vibrating
Grizzly
EXISTING ATAGGLOMERATOR
Leach Circuit
(6 Tanks @ 24 hrs)
Dilution Water
SART Precip Thickener
SART NeutralizationTanks (4 Stages)
GypsumThickener
Gypsum
Recycle
Carbon
Return
Stripping Columns
(5 Installed)
Adsorption Columns
(5 Installed)
Stripped Solution Tank
Barren
Solution
La Quinua Carbon
Adsorption Circuit
Barren Solution
To Leach Pad
CCD Wash Solution
(LQ Barren)
Barren Solution
To CCD Wash
CARBON COLUMNSAVR CIRCUIT
SART CIRCUIT
GOLD LEACH
PRIMARY CRUSHER
(Existing)
Lime &
Cyanide
CCD CIRCUIT
5 Stages
Precip Filter and
Bagging Plant Gypsum Recycle
To Mill
SAG & BALL
MILLING
CRUSHED ORE STOCKPILE
Flocculant
PRE-LEACH
THICKENER
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CRUSHING
Use existing agglomeration Crusher
1500 TPH
~9.5 h/d operation
Feed Stockpile
~11 hours live capacity in stockpile
Consumables
Power and Steel liners
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MILLING
New SAG and Ball Mill
D-26 Krebbs Hydrocyclones
Classify ground ore (80% -75 m)
Consumables
Power, steel balls, mill liners
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PRE-LEACH THICKENING
Objective
Recover process water for grinding circuit
Thicken pulp for subsequent leaching to
optimize leach residence time
Consumables Flocculent, anti-scalent, and power
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GOLD LEACH
Slurry is mixed in large agitated tanks
with the objectives:
Leach gold and silver from ore copper is
leached as a by-product
Consumables
Power, cyanide, lime, low pressure air
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CCD THICKENING AND WASHING
Purpose
Solids/liquid separation to produce metal/cyanide rich
solution for recovery of gold, silver, copper andcyanide
Solids routed to mill sands
5 Stages of Thickeners- 28 30 metersdiameter
Approx 600 m3/h of wash solution 1.2:1 was
ratio for >99% solute recovery
Final thickener is also a high density mill sands
thickener deeper cone
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SART SOLUTION TREATMENT
Sulfidization, Acidification, Recycle, and
Thickening.
1st CCD thickener overflow is treated in aSART process to remove Cu and Ag
Precipitation of (WAD) metal cyanide
complexes Ag, Cu, Zn
Cu and Ag sulfides sold as a concentrate
Neutralization with lime for gypsum removal Au recovery via 7 stage CIC
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SART SOLUTION TREATMENT
Batu Hijau Copper Sulfide
Precipitation Filter Press
Copper Sulfide product
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CARBON ELUTION / REGENERATION
Will be performed in existing plants at La Quinua
Final Au recovery in existing Merrill Crowe
plant/refinery at Yanacocha NorteObjective
Acid wash carbonate and organic material from
carbon Concentrate gold from carbon to an enriched solution
Regenerate carbon activity
Return sized barren carbon to leach circuitConsumables
Carbon, power, caustic, cyanide, anti-scalent, diesel
fuel, hydrochloric acid
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AVR CYANIDE RECOVERY
Acidification, Volatilization, and Recovery
Excess cyanide used in the mill will berecovered and reused in the mill to maintain
cyanide balance
Only in years where transition ores containinghigh copper values are treated
Solution contacted with air in packed bed towers HCN is stripped from the solution to the gas phase
Recycled cyanide is returned to the mill.
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NEW REAGENT FACILITIES
Cyanide
Lime
Caustic Soda
Carbon
FlocculantDiesel Fuel
Anti-Scalent
Sulfuric Acid
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MILL SANDS DISPOSAL
High compression thickened mill sands.
Dispose mill sands on the south section of theLQ pad.
Mill sands disposal area has same foundation
preparation and liner system as La Quinuaheap leach.
Heap leach and mill sands drainage systems
are continuous.Continuos monitoring program.
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MILL SANDS CROSS SECTION
LA QUINUA PAD
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PROJECT MILESTONE DATES
Submit AFE March 2005
Start EIS Workshops March 2005
Submit EIS January 2006
Start Detail Engineering Plant. November 2005
Start Bulk Earthworks Const. August 2006
EIS Approval January 2007
Start Mechanical/Elect. Const. March 2007
Mechanically complete November 2007
Startup Plant January 2008
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IMPORTANT RISKS
Manageable Risks
Expenditure schedule controlled by social
acceptance/permit progress.
Other Risks Considered Political (Elections).
Social acceptance.
Metal prices.
Reagents & Consumable prices.
Escalation.