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AMDREYExtraction of Rare Earths Elements from Acid Mine Drainage
State of Art
Rare Earth / Transition metal Some L/L separation issues
Daniel Meyer
PrometiaScientific SeminarDecember 2016
CSIC (Consejo Superior de Investigaciones Científicas) SpainCarlos Ayora
The University of Huelva (UHU) SpainJose‐Miguel Nieto
The “Institut de Chimie Séparative de Marcoule” FranceStephane Pellet‐Rostaing
University in the Free State. South AfricaEsta van Heerden
Chemec Oy. FinlandLasse Moilanen
AMDREY Partners
ContextWaste from Mine Activity (Pyrite)
Mining Activity
FeS2 + 7/2 O2 + H2O Fe2+ + 2 SO4
2‐ + 2 H+
Acid mine Drainage (AMD)
Waste containing traces of elements : Al, Cu, Zn, As, Cd, Pb, etc.
and interesting metals like Lanthanides and Yttrium
Draining wastepH 2.5 Fe precipitate
Al precipitate
“clean” river pH 6.8Precipitation of metals depending on the pH
Fe precipitates around pH 3
Al precipitates around pH 4,4
AMD SolutionLanthanides (Ln)Yttrium (Y)ppb to some ppm levelOther elements, valuable (VE) unwanted (UE)
Precipitation
DissolutionAs specific as possible
PrecipitatecontainingLn, Y, VE, UE
Solid treatmentLow temperatureWater removing
Solid 1Ln, Y, VE, UE
Solid treatmentHigh temperature
Solid 2Ln, Y, VE, UE
Ln+Y Other
ChemicalSeparation
Concentratesolution
Ln1 Ln2
Ln.. Y
Valuableelements
Fine Chemical Separation
NovelSolutions
NovelSolutions
3. Schwertmannite Fe8O8(OH)6(SO4)∙nH2O2. Hydrobasaluminite Al4(SO4)(OH)10∙15(H2O)1. Unreacted limestone Ca2CO3
using CaCO3
Concentratesolution
General Proposed Approach
Overview of the chemical separation
AMD samples: metalseparation
Direct extractionLiquid‐liquid extraction:
• Caracterisation of aqueous phases
0.001
0.01
0.1
1
10
100
1000
10000
100000
La Nd Gd Yb Y Fe Zr Ca Al Zn Mg Cu As
[M] ppm
Metals concentrations estimated by ICP‐OES
AG
BE
PHPH is the solution which is the mostconcentrated with concentration of
light REE over 1ppm
Very low concentration of REEbut high concentrations in Fe, Al
and Mg
0.0
0.2
Nd1.2
0
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
2 5.2 7.5
[M] ppm
[H2SO4]
La
Nd
Gd
Y
Fe
Ca
Al
AMD samples: metalseparation
Direct extractionLiquid‐liquid extraction:
• Caracterisation of aqueous phases• Solvent Extraction
• Impact of adding H2SO4
We managed to recover up to 1.2ppm Nd in PH solution,
using 7.5M H2SO4
La 20‐30%
Nd 80‐100%
Gd 5‐30%
Y 70‐100%
Fe 0.0095%
Al 0.0053%
Mg 0.0000%
Ca 0.52%
With this condition we are able to recover up to 100% of Nd
and 100% of Y with a very good selectivity toward other
elements.Less than 0.01% of Fe, Al and Mg and less than 1% of Ca
is extracted
AMD samples: metalseparation
Direct extractionLiquid‐liquid extraction:
• Caracterisation of aqueous phases• Solvent Extraction
• Impact of adding H2SO4• Modifications of O/A ratios• Multiple contacts
Multiple contacts help increase the concentration of
recovered metals
Modification of O/A ratios decrease the recovery of REE but increase the selectivitytoward the other elements,
especially Ca
• Shimojo, K.; Kurahashi, K.; Naganawa, H. Extraction Behavior of Lanthanides Using a Diglycolamide Derivative TODGA in Ionic Liquids. Dalton Trans. 2008, No. 37, 5083–5088
Prospects
• Screening of other inorganic acids: HNO3, HCl, H3PO4…• Develop an extraction process for REE without the addition of acid
For exemple with ionic liquids
• Working on concentrated metals• Specific leaching
Al oxydes + REE ?• REE recovery from leaching solution: key step REE / Ca selectivity
• Prospective extractants
CMPO
DMDOHEMA
terpy
BTP
BTBP
Rare Earth / Transition metal Some L/L fundamental separation issues
Extraction and separation of Pd, Ln by diamides from nitric waste
Ln-Pd supramolecular behavior
Aggregation is not a prerequisite for Pd(II) extraction Aggregation is a prerequisite for Nd(III) extraction
" Metal Recognition Driven by Weak Interactions: a Case Study in Solvent Extraction. "R. Poirot, X. Le Goff, O. Diat, D. Bourgeois, D. Meyer; ChemPhysChem , 17(14), 2112, 2016. Pacifichem 2015 Honolulu, dec. 15th, 2015
Weaker coordination of malonamide to La & need for 2 ligands in coordination sphere
Ln-Pd Coordination Behavior
Low pre-organisation (toluene, heptane HNO3 1M)
Nd-Pdhi-loGext = -2 kT
Nd-PdGext)lo Nd-PdGext)hi
Pdd‐metals?
Ln (Nd)
NN
CH3
C7H15C7H15
CH3
O
C5H11
OO
NO3
NdNO3
NO3NO3
NdNO3
NO3
Thermodynamic consideration
Pacifichem 2015 Honolulu, dec. 15th, 2015
High pre-organisation (heptane HNO3 5M)
Acidity and concentration of extractant
Nature of the extractant
Diluant Effect
Pd and RE extraction behaviour in the presence of
other metal
Leading to controlled mixed extraction
Liquid‐Liquid separation Pd, Ln, other M
RE Co Ni Fe Zn
Kinetic can help
3 metal separationKinetic removal Mgreen
(confidential)