presented by Şerif kaya prof. dr. yavuz a....
TRANSCRIPT
Presented by Şerif KAYA
Supervisor: Prof. Dr. Yavuz A. TOPKAYA, Middle East Technical UniversityMetallurgical & Materials Engineering Dept. Ankara/Turkey
with the support of Dr. Carsten Dittrich, MEAB Chemie Technik GmbH and META Nikel-Kobalt A.Ş.
Leuven, 20155-7 October
Bauxite Residue Valorisation and Best Practices Conference, Leuven, 5-7 October
Outline
3. Previous Studies and Findings
2. General Overview of MHP Process
1. General Information about Scandium
4. Precipitation Experiments and Behaviour of Scandium
5. Current and Future Studies
7. References
6. Discussion & Conclusion
8. Questions & Answers
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3
Importance of Scandium
• Scandium has been obtained from various ores, tailings and residues of previously exploited mines as a by-product up to now. (e.g.: U, Sn, Ta, Ti, W, etc.)
• The main application areas; high strength and light-weight Al-Sc alloys, lighting, electronics, laser research and solid oxide fuel cells.
• However, the supply of Sc is very scarce (5-12 t/a) and price is very high e.g. 99.9% Sc2O3 2000-3000$, [1]- Riggall 2015.
• The presence of ~50-100 ppm Sc in lateritic Ni-Co deposits seems to be a very prominent source for the extraction of Sc together with Ni & Co.
Leuven, 20155-7 October
Conventional MHP Process (pH controlled precipitation)
How to recover Sc from a MHP Circuit?
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Precipitation Behaviour of Ions wrt pH at 25 °C
5
Fe(III) > Al(III) > Sc(III) > Cr(III) > Cu(II) > Fe(II) > Zn(II) > Ni(II) > Co(II) > Mn(II)
Sc
Leuven, 20155-7 October
Findings presented in ERES 2014 Conference
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Parameters Studied for Sivrihisar Lateritic Nickel Ore
• Sulphuric Acid to Ore Ratio:(160, 180, 200, 220, 240, 260, 270, 285, 300, 325, 350 kg/ton dry ore)
• Temperature:(245, 255, 265, 275 °C)
• Particle Size:(-850, -425, and -74 µm)
• Duration:(30 min., 60 min., 90 min., 120 min., 360 min.)
Optimum Leaching Parameters: 260 kg acid/ton dry ore, 255 °C, -850 µm, 60 min.
[2]- Kaya Ş, Topkaya Y.A., ‘High Pressure Acid Leaching of a Nickel Laterite Ore to Extract Scandium’, 1st European Rare Earth Resources Conference, Milos, Greece, 2014.
Preparation of the Synthetic Solution
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• Composition of the optimum PLS and Synthetic Leach Solution
Element PLS Composition (mg/L) Synthetic Solution (mg/L) Reagent
Nickel 5502 5827 Ni(II) Sulfate Hexahydrate
Cobalt 321 371 Co(II) Sulfate Heptahydrate
Scandium 34 30 Sc(III) Sulfate Octahydrate
Iron 1688 1814 Fe(III) Sulfate Hydrate
Aluminum 3985 4317 Al(III) Sulfate (18.H2O)
Chromium 342 150 Cr(III) Sulfate Hydrate
Manganese 2110 2056 Mn(II) Sulfate Monohydrate
Magnesium 1285 1369 Mg(II) Sulfate Heptahydrate
Copper 28 29 Co(II) Sulfate Pentahydrate
Zinc 73 74 Zn(II) Sulfate Heptahydrate
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Experimental Set-up
Leuven, 20155-7 October
MicropipettepH Meter
CaCO3 Slurry
Hot Plate & Magnetic Stirrer
pH Probe
Contact Thermometer
Condenser
CaCO3 Addition
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Fe-I Removal ExperimentsFe-I Removal Experiments (at 90 °C, 120 minutes)Fe-I Removal Experiments (at 90 °C, 120 minutes)
• Aim is to obtain max. Fe ppt. with min. Ni, Co, Sc ppt losses.
• After the determination of optimum pH, a series of exp. to prepare a stock solution for Fe-II Removal Step was carried out.
Exp-1 Exp-2 Exp-3 Exp-4 Exp-5 Exp-6 Exp-7 Exp-8 Exp-9
pH 2.00 pH 2.50 pH 2.75 pH 3.00 pH 3.25 pH 3.50 pH 4.00 pH 4.50 pH 5.00
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Ni
Co
Sc
Fe
Mn
AlCrCu
Zn
0
20
40
60
80
100
1,75 2,00 2,25 2,50 2,75 3,00 3,25 3,50 3,75 4,00 4,25 4,50 4,75 5,00
% P
reci
pita
tion
pH
Fe- I Precipitation Results
Fe-I Removal Results
Leuven, 20155-7 October
Element PLS (mg/L)
PLS after ppt. @ pH
2.75(mg/L)
Ni 5827 4650
Co 371 268
Sc 30 23
Fe 1814 227
Al 4317 3599
Cr 150 98
Mn 2056 1905
Mg 1369 1211
Cu 29 28
Zn 74 67
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Fe-II Removal Experiments
Fe-II Removal Experiments (at 70 °C, 180 minutes)
• Aim is to precipitate all of the remaining Fe and Sc with min. Ni and Co ppt losses.
• After the determination of optimum pH, a series of exp. was carried out to prepare a stock of Fe-II precipitate for Releaching Step.
Exp-1 Exp-2 Exp-3 Exp-4 Exp-5
pH 4.00 pH 4.25 pH 4.50 pH 4.75 pH 5.00
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Ni Ni
Ni
Co
Co
Sc
Sc ScSc Sc
Fe
Fe
Fe
Fe Fe
MnMn Mn Mn
Mn
AlAl Al
Al Al
Cr
Cr Cr CrCr
Cu
Cu
Cu
Cu Cu
Zn
Zn
Zn
Zn
0
20
40
60
80
100
3,75 4,00 4,25 4,50 4,75 5,00
% P
reci
pita
tion
pH
Fe- II Precipitation Results
Fe-II Removal ResultsElement Initial
PLS (mg/L)
PLS after ppt.
@ pH 4.75(mg/L)
Ni 4650 2819
Co 268 241
Sc 23 0
Fe 227 2
Al 3599 4
Cr 98 <5
Mn 1905 1509
Mg 1211 -
Cu 28 <5
Zn 67 41
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After Fe-II purification a precipitate containing 703 g/ton Sc was obtained.
Initially the ROM contained 106 g/ton Sc. Experiments ac
Exp-1 Exp-2 Exp-3 Exp-4
25 gpl H2SO4 50 gpl H2SO4 75 gpl H2SO4 100 gpl H2SO4
Releaching Exp. of Sc enriched Fe-II Precipitate
Element Solid Comp.(g/ton)
Nickel 4010
Cobalt 36
Scandium 703
Iron 3100
Aluminum 11.6 %
Chromium 1446
Manganese 29
Calcium 14.6 %
Copper 504
Zinc 368
Composition of the solid residue before releaching
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Releaching Results of Sc enriched Fe-II Precipitate
Exp. % Sc Extracted
Ni
(mg/L)
Co
(mg/L)
Sc
(mg/L)
Fe
(mg/L)
Al
(mg/L)
Cr
(mg/L)
Mn
(mg/L)
Cu
(mg/L)
Zn
(mg/L)
25 g/L
H2SO4
42.5 373 4.6 72 220 8180 158 3.8 50 36
50 g/L
H2SO4
72.5 664 6.8 121 507 15925 344 4.4 88 56
75 g/L
H2SO4
82.4 776 7.6 136 617 18683 423 4.8 102 65
100 g/L
H2SO4
91.9 928 8.7 153 659 18848 529 4.6 102 64
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Summary of Fe-I & Fe-II Removal and Releaching Experiments
Fe-I Removal Experiments (at 90 °C, 120 minutes)• Fe-I Purification (at 90 °C, 120 minutes): Aim is max. Fe ppt. with min. Ni, Co, Sc ppt losses.
minutes)• Fe-II Purification (at 70 °C, 180 minutes): Aim is to precipitate all of the remaining Fe and Sc with
min. Ni and Co ppt losses.
• Releach: Aim is to obtain max Sc dissolution during releach.
Re-leaching of Sc rich Fe-II Precipitates (at 60 °C, 60 minutes)
A releach solution containing 153 mg/l Sc was obtained, and this solution was used for Sc recovery!
Exp-1 Exp-2 Exp-3 Exp-4 Exp-5 Exp-6 Exp-7 Exp-8 Exp-9
pH 2.00 pH 2.50 pH 2.75 pH 3.00 pH 3.25 pH 3.50 pH 4.00 pH 4.50 pH 5.00
Exp-1 Exp-2 Exp-3 Exp-4 Exp-5
pH 4.00 pH 4.25 pH 4.50 pH 4.75 pH 5.00
Exp-1 Exp-2 Exp-3 Exp-4
25 gpl H2SO4 50 gpl H2SO4 75 gpl H2SO4 100 gpl H2SO4
Our Scandium Concentrate
16Leuven, 20155-7 October ~15% Sc containing precipitate produced in META R&D Laboratory.
[1]- Riggall, S., ‘Australian scandium supply - A paradigm shift for a strategic metal’, in AeroMat 2015Conference, Long Beach, California, 2015.
[2]- Kaya Ş, Topkaya Y.A., ‘High Pressure Acid Leaching of a Nickel Laterite Ore to Extract Scandium’, in 1st European Rare Earth Resources Conference, Milos, Greece, 2014.
REFERENCES
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THANK YOU for YOUR ATTENTION
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Special Thanks to;
For their endless support to this study.Leuven, 20155-7 October
METU, META and MEAB Collobaration
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Dr. Carsten Dittrich, MEAB
Dr. Bülent Şentürk, META
Prof. Dr. Yavuz A. Topkaya, METU/META
Poor Şerif Kaya :), METU
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Products obtained after Fe-I Removal Exp.
1.Characterization
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Physical Characterization:
• Moisture content: ~14% moisture in as-received ore (-2 mm) • Bulk Density: 1.08 gr/cm3 (as received -2 mm)• Solid Density: 3.51 gr/cm3 (by He pycnometer)• Magnetic Character: Very weak magnetic minerals (no separation)
Chemical Characterization:
Table 1 Chemical analysis of the laterite ore sample Constituent Fe Ni Co Sc (ppm) Al2O3 MnO MgO
Content (wt. %) 46.2 1.54 0.093 106 3.61 1.04 0.71
Constituent Cr2O3 SiO2 CaO Na2O K2O As S
Content (wt. %) 2.25 14.56 0.98 0.02 0.02 0.12 0.02
29 October 2015
1.Characterization
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Mineralogical Characterization:
By X-Ray Analysis:
Major Phases: Hematite, Goethite, QuartzMinor Phases: Kaolinite and Nimite (Clay minerals)
By SEM Analysis:
Nickel is distributed in: Iron oxides and clay mineralsCobalt is distributed in: Clay mineralsScandium is distributed in: No detection. But, strong correlation of Sc distribution with Fe and Clay minerals (Al-Si) in wet screen analysis.
By DTA/TGA Analysis: Presence of the found minerals were counter-checked.
29 October 2015
Mine Site & ~5000 tons of Stock
Li
monitic
Zone
Hematitic
Zone
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