Hydrometallurgy Research & Development at the University ... · Presentation Outline...
Transcript of Hydrometallurgy Research & Development at the University ... · Presentation Outline...
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Hydrometallurgy Research & Developmentat the University of Queensland
http://www.chemeng.uq.edu.au/hydrometallurgy
Associate ProfessorJames Vaughan
https://researchers.uq.edu.au/researcher/2189
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Presentation Outline
• Introduction to UQ / Chem Eng / Metallurgy / Hydrometallurgy
• Background Australian / Brazilian Refineries
• Motivation for Hydrometallurgy Research
• Examples Research Projects
• Alumina• Nickel• Gold
The University of QueenslandBrisbane, Australia
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UQ Snapshot
• Founded in 1909
• UQ ranks in the world’s top 50
universities
• Around 400 degree programs
• Over 50,000 students, 12,000
international students from over 140
countries
• More than 13,500 postgraduate
students
• More than 12,000 PhD graduates
• Almost 7,000 full-time equivalent
staff
• A global network of over 232,000
alumni in more than 160 countries
• #1 school of chemical engineering in
Australia
• Scientia ac Labore
CRICOS Provider Number 00025B
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New Chemical Engineering“Andrew N. Liveris” Building (opening 2021)
https://campuses.uq.edu.au/article/2018/06/andrew-n-liveris-building-construction-project-update
Building Site October 2019
Andrew LiverisCEO of Dow Chemical (~2004-2018)
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Chemical and Metallurgical Engineering
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The dual major in chemical & metallurgical engineering provides the best of both worlds - a foundation in chemical engineering combined with specialisation in extractive metallurgy.
IChemE, AusIMM Accredited
Professor Peter HayesMetallurgy Program Leader
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The treatment of ores, concentrates and othermetal-bearing materials by wet processesusually involving the dissolution of somecomponent, and its subsequent recovery fromthe solution.
PeopleProfessor Peter Hayes – Metallurgy Program LeaderJames Vaughan – Associate ProfessorHong Peng – UQ Amplify Research FellowWilliam Hawker – LecturerWeng Fu – Post Doctoral ResearcherJames Gudgeon – Laboratory ManagerKelly Byrne – Senior Research TechnicianStefan Lakemond – Senior Research TechnicianDavid Mann – Senior Research TechnicianKimiya Bolouri – Senior Research Technician
Research Infrastructure• Comprehensive autoclave facility• Certified radiation facility• Electrowinning / electrorefining / electrochemistry• UV-VIS / TGA / AAS / ICP-OES• FIMS/DMA for Hg• Flow through thin film membrane filtration rig• FIMLAB membrane synthesis / percrystallisation• Single particle optical sensing and laser sizers• Factsage and HSC Chemistry software• Centre for Microscopy and Microanalysis• Brisbane Surface Analysis Facility• Pyrosearch / JKMRC• Bauxite and Alumina Technology Centre
Projects• Refining mixed nickel-cobalt hydroxide precipitate• Synergistic hydro-pyro processing of copper• Separating radionuclides from copper concentrates• Pressure oxidation chemistry• Scandium hydrometallurgy• Ion exchange resin technologies• Inorganic membrane percrystallisation• Nickel agromining• Processing high silica bauxites• Value-added products
CSTR Pilot Plant
Sodium Oxalate Pressure Leaching Solvent Extraction Copper Cathode
Hydrometallurgy
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Hydrometallurgy Research Group
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Examples of Australian Refineries
Australia
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Examples of Brazilian Refineries
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Hydrometallurgy research and development drivers
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Laterite
• Decreasing ore grade
• Increasing ore complexity
• Increase efficiency of mature technologies
• New feed intermediates or secondary (recycled) materials
• Health, safety, environment, community
• Costs of waste disposal and rehabilitation
• Production of advanced / high purity materials / by-products
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Examples of Research & Development Projects
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Laterite
• Alumina• The sandy DeSilication Product (DSP) process concept
• Nickel• Selective acid leaching of nickel from Mixed Ni-Co Hydroxide
Precipitate (MHP)
• Developments in nickel agromining
• Gold• A chemical-thermodynamic model for iron at pressure oxidation (POX)
conditions
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Alumina
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Laterite
Rio Tinto Yarwun Alumina Refinery, Queensland, Australia
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Bayer Process
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Laterite
Bayer Liquor Cycle
Digestion
Clarification
Residue
Precipitation
CalcinationAlumina
Bauxite
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Bayer Process - Digestion
Gibbsite → AluminateAl(OH)3 + NaOH(aq) → NaAl(OH)4(aq) at 110-150°C
Boehmite→ AluminateAlOOH + NaOH(aq) + H2O → NaAl(OH)4(aq) at 180-280°C
Kaolinite (Reactive Silica) → Sodalite DeSilication Product (DSP) 3Al2(OH)4Si2O5 + 8NaOH(aq) → Na8(AlSiO4)6(OH)2.2H2O + 7H2O
DSP is costly in terms of lost NaOH
DSP in residue is an environmental challenge and an impediment to residue reprocessing
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Bauxite Residue (BR) Sinter-Leach
Bayer process: 10 GJ/t-Al2O3 but with BR sinter leach: 40 GJ/t-Al2O3!
Qi, T., Hodge, H., Hawker, W., Hayes, P. and Vaughan, J. (2018). A review of the
bauxite residue sinter-leach process. Alumina2018, Gladstone, QLD, Australia, 9-14
September 2018. Australia: AQW Inc.
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Bauxite Residue and DSP
Bauxite residue is very fine (< 2 µm), DSP cannot be physically separated
Peng, H., Vaughan, J., Staker, W., Wang, J. and Wen, W. (2018). Advanced characterisation of bauxite residue.
Alumina2018, Gladstone, QLD, Australia, 9-14 September 2018. Australia: AQW Inc.
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Growing DSP Particles
We have found conditions where DSP can be grown to > 30 µm
100 µm
Coarse DSP agglomerates
DSP size distribution as a function of reaction time
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The Sandy DSP Process
Vaughan J., Peng H., Seneviratne D., Hodge H., Hawker W., Hayes P., Staker W.
The Sandy Desilication Product Process Concept. JOM (2019)
Bayer Process
DSP Conc.Sinter-Leach
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The Sandy DSP Process
• Lower mass flow to sinter-leach:
Reduces energy requirement (OPEX) and size of the plant (CAPEX)
• Lower gangue mineral concentrations;
Reduces reagent requirement associated with side reactions (OPEX)
Next step: continuous piloting, seeking industry partners
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2020 TMS Annual Meeting & Exhibition: Alumina & Bauxite
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Laterite
Light Metals 2020
This is an excellent opportunity to interact with experts from the Light Metals industryand academia from all over the world and get the latest update on key issues in theindustry. Based on the importance of improving processes, reduce environmentalimpact and the global challenges in aluminum production.
Alumina & Bauxite topics:
Bauxite Ore Characterisation, Bauxite Mining and Processing, Handling and Processing, Separation of Impurities, Sustainability and Environmental Issues, Processing Bauxite Residue
https://www.tms.org/TMS2020
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Nickel
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Laterite
First Quantum MineralsRavensthorpe nickel operationWestern Australia
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Processing nickel laterite ore
Laterite ore
Ferronickel smelting / NPI
Caron process
Acid leaching
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Processing nickel laterite ore
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Laterite ore
Ferronickel smelting / NPI
Caron process
Acid leaching
Direct Solvent eXtraction
Mixed Sulphide Precipitate
Mixed Hydroxide Precipitate
GoroBulong
Moa BayMurrin MurrinCoral BayAmbatovy
CawseRavensthorpeRamuCaldagGoro
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Options for refining MHP
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ConventionalAMMONIA LEACH
- LIX 84I
ConventionalACID LEACH
- C272
NewSELECTIVE ACID
LEACH
Leachreagents
NH3/(NH4)2CO3 H2SO4
H2SO4
Oxidant
MHP leach selectivity
Mn - Mn, Co, Cu
Leach robustness
Sensitive to:MHP ageing; Fe, Al
OxidationSulphate
High High
Co/Ni solvent extraction
Nickel selective Cobalt selective Not needed
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Selective acid leaching of nickel from mixed hydroxide precipitate (MHP)
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MHP
OxidantH2SO4
SelectiveAcidLeach
ConcentratedNickel solution
CobaltConcentrate
40% Ni2% Co
15% Ni15% Co
100 g/L Ni0.005 g/L Co
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MHP oxidizing leach as a function of pH
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0
20
40
60
80
100
1234567
Leach E
xtr
action
(%)
Slurry pH
Cu
Co
Conditions80°C100% Oxidant100 g-Ni/L-Slurry30 min / pH adjust
Mg
Ni
Zn
Mn
Williams C., Hawker W., Vaughan J. Selective leaching of mixed nickel –
cobalt hydroxide. Hydrometallurgy 138, 84-92 (2013)
Ni Selective Leach pH
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Oxidation precipitation diagram (pH = 4.6)
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Williams C., Hawker W., Vaughan J. Selective leaching of mixed nickel –
cobalt hydroxide. Hydrometallurgy 138, 84-92 (2013)
Ni Selective Leach Eh
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Selective acid leach technology licensed to
https://purebatterytech.com/Powering the green energy revolution
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2019 Pilot Plant
MHP(40% Ni, 2% Co)
50 kg NiSO4.6H2O(>99.9% Pure)
10 kg Cobalt Concentrate(15% Co)
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Refinery feasibility study complete
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Nickel agromining
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Nickel agromining is envisaged to be a part of a progressive mining and rehabilitation strategy where local communities farm metals before and after conventional mining operations.
van der Ent A. et al. Agromining: farming for metals in the future? Environmental science & technology (2015)
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Nickel agromining
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Metal unexploited
resources
Industrial
waste
Serpentine
soils
Tailings
Pellets
Ash
Metal compounds are recycled into industry
Acetate
Sulfate
Hyperaccumulator plants are grown
NiNi
Ni
NiNi
Ni
Metals are extracted and translocated to the aerial parts
Ni
Ni
Ni
Ni
Ni
Ni
Biomass in harvested and transformed
J.L. Morel
Metals are extracted and purified
Hydrometallurgy
Agromining chain
Soil prepared for hyperaccumulators’
growth
Amendments
NiNi
NiNi
Ni
Ni
NiNi
NiNi
Ni
Ni
NiNi
Ni
Ni
Ni
Ni
B. Laubie
0.1% Ni2% Ni
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Nickel agromining
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Demonstration farms: Malaysia, Albania, Austria, France, Greece, Spain
300 kg-Ni / (ha*year) production rates achieved
Alyssum MuralePhyllanthus rufuschaneyi
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Element localisation by synchrotron XFM-mXRF (Alyssum murale)
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Example of a process for agromined nickel
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Vaughan J. et al. Characterisation and hydrometallurgical processing of nickel from tropical agromined bio-ore. Hydrometallurgy (2017)
2% Ni
10% Ni
40% Ni(recycledto Ni farm)
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Gold
36
Laterite
Newcrest Lihir Gold Operation, Lihir Island, Papua New Guinea
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Gold
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Laterite
Newcrest-UQ research team (2017)
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Pressure Oxidation (POX)
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Pressure oxidation is used to chemically liberate finely disseminated gold in sulfide minerals, typically pyrite / arsenopyrite.
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Conventional understanding of iron phase stability in POX
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(adapted from Fleming, 2010) (adapted from Babcan, 1971)
Lack of reliable thermodynamic data at elevated temperatures
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UQ HydrometallurgyPOX Autoclave and Rapid Filtration
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Ivana Ambrosia PhD research
2L Ti Autoclave with internalCooling / Sampling Port
Sample Flash Vessel and Pressure Filter
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Solubility of Basic Ferric Sulphate at 220°C
FeHSO4SO40 (a) + H2O(l) ↔ FeOHSO4(s) + HSO4
-(a) + H+(a)
Unpublished results Ivana Ambrosia
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Solubility of Hematite at 220°C
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Unpublished results Ivana Ambrosia
FeHSO4SO40(a) ↔ Fe2O3
Fe(SO4)30(aq) ↔ Fe2O3
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Eh-pH diagram for Fe-S-H2O system at 220°C
Unpublished results Ivana Ambrosia
Using solubility data and simplifying assumptions a self-consistent thermodynamic database was produced providing predictive capabilities at 220°C
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Summary
Sand
y DSP
MHP R
efinin
g
Ni Agr
omining
POX C
hemist
ry
Ore Grade
Ore Complexity
Increase Efficiency
New Feed
HSEC
Waste Management
High Purity Products
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Acknowledgements
Thanks to:
The researchers that contributed to the projects described.
The industry and granting agencies for supporting the projects.
Thanks for inviting me to this wonderful conference on extractive metallurgy.
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Sponsors
46
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Collaborators
47
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