an effective new leaching aid
TRANSCRIPT
Mining Solutions
An effective new leaching aid successfully tested with oxide and mixed sulphide copper ores
ATLASAdvanced Technology for Leaching Aids
Jack BenderMining Solutions, BASF Corporation, USA
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Project Status
Copper Oxide or Secondary Sulfide Ore
Copper Lixiviant (e.g. H2SO4)
Fissures with added contact / Copper extraction
Project Progress All leaching aid fundamental lab work
has been completed SX and Biocompatibility laboratory
work has been completed Customer trials have started Production and Registration complete
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Ore procurement Oxide and Secondary Sulfide Ore classified, analyzed and packaged by expert engineering firm - SGS Sample crushed, screened, split into seven test charges
Unloading Crushed ore Screening
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Agglomeration of Size Fractions
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Leaching Aid Requirements
CRITICAL Aspects Must not affect any downstream processes including Solvent Extraction and
Electrowinning Highly water soluble surfactants that are not extracted into kerosene during SX Cannot stay at the aqueous/organic interface, interfering with kinetics and phase
separation Cannot affect downstream or upstream processes even at very high overdose
concentrations or near critical micelle concentration
Other requirements Must be compatible with native bacteria or inoculated archea Stable at pH << 1 at ambient or slightly elevated temperatures (<50°C) for 3-6 month Needs to Reduce surface tension, but dramatic effect is not recommended Effective at low concentrations: typical dosage range has been 25 ppm
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Phase Disengagement
At extremely high concentrations, 10x dosage, there is an effect on the aqueous continuous phase disengagement, although it is still not a dramatic effect.
Therefore, the leaching aid should only be added directly to the raffinate going to leach
Typical Leaching Aid dose of 25 ppm
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Chemical CompatibilityBatch – Standard QC testing with 10 v/v% LIX 984N
Continuous - 1Ex1Ex1S configuration, 10 v/v% LIX 984N, Mine PLS & Synthetic LE
Obviously no negative effects on SX
Assay Barren Organic E30 E300 S30 S300 Net Transfer Phase Sep (s)Blank Cu 1.42 4.72 4.75 1.64 1.63 3.33 95, 75
%E300 99.37% 99.68%20 ppm Atlas Reagent Cu 1.43 4.69 4.73 1.64 1.63 3.3 85, 80
%E300 99.15% 99.68%50 ppm Atlas Reagent Cu 1.42 4.69 4.72 1.65 1.63 3.3 95, 75
%E300 99.36% 99.35%
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Compatibility with ElectrowinningCopper cathode has been previously plated using a rectifier and simple EW system. The effect of adding a leaching aid was similar to that of a smoothing agent.
This is due to the reduction of the surface tension and the attraction of the polar functional groups of the leaching aid to the high charge density of copper cathode dendrites.
In no cases was there any negative impact from the leaching aid
A
C D
B
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Biocompatibility - Subset of Data – 12Bacteria and Archea Tested
Acidithiobacillus ferrivorans (AFER)iron and sulfur oxidizer (tested on iron)
Acidithiobacillus thiooxidans (ATEX) sulfur oxidizer
Ferroplasma acidiphilum (FACID)archea iron oxidizer
Leptospirillum ferriphilum (LFER)iron oxidizer
Acidophilium acidophilum (AA) heterotroph
Acidithiobacillus ferrooxidans (AFEX)iron oxidizer
* Work performed by Universal Biomining
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Laboratory Column Setup - Oxides Ore agglomerated with water and 25% of the total weight of acid
consumption of the ore 16 columns (2 meter) loaded with 90 Kg each of copper oxide ore after
agglomeration Leach rate - 8 ml/min (0.005 gpm) of 10 g/L sulfuric acid Temperature controlled at ~18ºC Trials conducted as “closed circuits” – copper was extracted from PLS
and the raffinate was dosed with leach aid / necessary acid and recycled back to the columns In some cases PLS treated with solvent extraction with the same results Blanks run with each set of columns
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Laboratory Column Testing – 2M Column Each column leached with dilute
sulfuric acid + leach aid at various concentrations. The control columns leached with acid only Each combination tested in
quadruplicate Daily analysis of PLS includes Cu
content, pH, ORP, free acid and surface tension Standard deviation of column
results was less than 1%
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Trial 5 – Oxide Trial 5
Leaching aid added after agglomeration
Approximately 70% leaching of copper achieved in 30 days
391 g total copper in column at 92% leachable 361 g total
leachable copper
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Trial 6 OxideTrial 6
Leaching aid added during agglomeration
Approximately 70-76% leaching of copper achieved in 60 days
391 g total copper in column at 92% leachable 361 g total
leachable copper
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Trial 7 – Customer Mixed Sulfide
Customer Trial involving the recycle of aqueous
63 g of acid soluble copper (60% leached with LA, 49% leached blank) at 110 days
Initial drop in recovery was expected due to the use of bacterial leaching
Trial 7
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Trial 8 – Oxide – “Chilean Conditions”Trial 8
The oxide ore was leached using leaching aid in all cases
Chloride and nitrate was added in some cases
Only at extremely high concentrations of chloride and nitrate is the leaching suppressed
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Production and Toxicity
Toxicity The leaching aid has been assessed a polymer exemption by the
Toxic Substances Control Act (TSCA) Chemical Substance Inventory and the Registration, Evaluation, Authorization and Restriction of Chemicals (REACH). Therefore, it is exempt from the standard toxicity testing required by non-polymer substances
ProductionWe have completed a full scale production run of the leaching aid BASF has sufficient facilities globally to support the mining industry
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Conclusions Leaching Aid has been identified that is compatible with Solvent Extraction,
Electrowinning, and various bacteria/archea
Careful control of column conditions resulted in reproducible results from a four column sample size
Leaching aid concentrations of approximately 25 ppm were optimal while over dosing and under dosing could greatly affect leaching results
The method by which the leaching aid is added to the system can have an influence on the effectiveness of copper leaching
Proceeding with column trials at various customers, a mini-heap trial at one customer and a plant trial at one customer
In the process of providing samples to some customers for testing
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INTERNAL