optimisation of magnetite circuit design using isamilltm technology
TRANSCRIPT
3rd Africa Iron Ore Conference 2013 Cape Town, South Africa
OPTIMISING AUSTRALIAN MAGNETITE CIRCUIT DESIGN USING ISAMILL™ TECHNOLOGY
Acknowledge : Barns, Twomey, Walstra
Presented : H de Waal
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Presentation Outline
• IsaMill™ Technology
− Development
− Operating Principles
• Ernest Henry Mine
− Background
− Life Extension
− Magnetite Plant
−Test Work
−Grinding Test Work
−Flow Sheet
• Conclusion
IsaMillTM Technology Development
• Development of IsaMillTM driven by inability to efficiently treat fine grained ore bodies
• Late 1980s, Xstrata required 7µm grind for new Pb/Zn ore bodies in Australia
• Conventional mining technologies previously tested, 1975-1990, but
− Too high power consumption to achieve target size
− Ball/tower mills ineffective below 20-30μm
− Negative influence of steel grinding on flotation
Broken Hill
0 40 micron
Broken Hill
0 40 micron
McArthur River
0 40 micron
McArthur River
0 40 micron
IsaMillTM Technology Development
A technology was found...
• Horizontal Bead Mills
− Technology existed in industries other than mining (Netzsch)
− Small scale
− Batch operation
− Very expensive and exotic media types
• Cross-over from manufacturing into minerals required:
− Much larger scale
− Continuous operation
− Ability to use cheap, local media
Source: AMIRA P336
Horizontal Bead Mill Technology
Other Technology
IsaMillTM Technology Development
• The first 3,000 litre, 1.1 MW IsaMillTM developed in partnership with Netzsch
• Affordable ceramic and local medias such as sand used
• First installed at Mount Isa Mine, 1994
• Enabling technology for McArthur River Mine, 1995
McArthur River Mine
IsaMillTM Technology Development
• Larger mills wanted
− Scale-up to 10,000 litres in 2003 (developed jointly with Anglo Platinum)
− Motor size increased from 1.1 MW to 3.0 MW
− Allows significantly higher throughputs and feed size (F80 up to 300µm)
− Scale up to M50,000 with 8MW motor in development
M10,000 IsaMillTM
IsaMillTM Technology Operating Principle
Media centrifuged to outside of grinding chamber by high centrifugal force (60g) generated inside the mill
Product separator pumps coarse
material back into the grinding
chamber
Discharge End
Multiple Stages of Grinding
Feed End
Coarser particles centrifuged into zone of high media concentration for size reduction before passing to next
stage of processing
Shaft rotating at high speed generating disc tips speeds of between 19–23 m/s
IsaMillTM Grinding Chamber
IsaMillTM Technology Operating Principle
The rotor fingers pump coarse particles and media back towards the feed end
of chamber for further grinding
A volume of slurry, equal to the mill feed flow, passes
through holes in the discharge ring and exits the mill
Material passing through the rotor disc holes moves across the
face of the discharge ring end plate towards the rotor fingers
Rotor Disc
Last Disc
Discharge Ring
Ground slurry passes through holes in the last disc to enter the classification zone
Ernest Henry Mine Background
• 38 km north-east of Cloncurry in the Mount Isa – Cloncurry mineral district of north-west Queensland
• Ore Reserve Estimate as at 30 June 2010
− 88 million tonnes Iron Oxide Cu Au deposit
− 1% Cu as chalcopyrite
− 0.5 g/t Au
− 23% Fe3O4
• Annual production
− 350,000 t Cu concentrate (100,000 t Cu)
− 120,000 ounces Au
− 1.2 Mtpa magnetite after expansion
Ernest Henry Mine Life Extension
• Extend life of EHM to at least 2024
− Transition from open pit to underground and associated magnetite plant through $589 million investment.
− Magnetite Plant
−Numerous studies on magnetite in ore
−Early studies focussed on magnetite removal
−Subsequent studies demonstrated viability of producing high grade magnetite
−Control PSD and liberate valuable material
Ernest Henry Mine AMMTEC Test Work- Grinding Efficiency
• Large tonnage magnetite plants- grinding energy efficiency important
• Test work looked at grinding circuit flow sheet optimisation
− Pilot autogenous primary milling
− Laboratory work (Levin test)
− Pilot secondary ball milling
− Laboratory and limited continuous secondary IsaMill™ testing
− Laboratory tertiary, limited continuous and pilot IsaMill™ test work
Ernest Henry Mine Previous Test Work IsaMill™ Selection
: EHM Tails Tower Mill™ vs IsaMill™ Test Work (Burford & Niva 2008)
Ernest Henry Mine AMMTEC Test Work- Grinding Efficiency
• Primary AG product 420µm
• Magnetic separator gangue rejection 40% of feed
• 2,200 tph feed to secondary grinding stage at a P80 of 770µm (the magnetic fraction coarser than gangue)
• Secondary Ball and IsaMill™ test work
Ernest Henry Mine Test Work- Grinding Efficiency
Section Feed Rate
(t/h)
Specific Energy (kWh/t)
Installed Power (MW)
Annual Media Cost Estimate
($AUD million)
Autogenous Mill 770 µm Product
3800 8.5 40 $0
Single Stage Ball Mill 34 µm Product
2200 47 114 $86
Single Stage IsaMill™ 34 µm Product
2200 34 78 $57
Ball Mill 100 µm Product
IsaMill™ 34 µm Product
Total
2200
1720
12
13
34
24
58
$13
$11
$24
Circuit comparison (David, Larson & Li 2011)
Ernest Henry Mine Grinding Efficiency
• Magnetite plant
−1.2 million tons premium quality magnetite concentrate per annum
−Revenue stream from previous tailings stream
−Reducing amount of tailings
−Construction commenced in July 2010
−First magnetite concentrate produced in December 2010
Conclusion
• IsaMill™ technology has evolved from ultrafine grinding technology to mainstream and regrind technology and has wide acceptance in many metalliferous applications utilising the IsaMill™’s key advantages
− Energy efficiency
− High intensity
− Circuit efficiency
• These advantages have now been transferred to the magnetite beneficiation flow sheet
• Carefully considering the strengths of different technologies and exploiting these strengths has resulted in cost effective, efficient circuit design