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High Pressure Acid Leaching of Nickel Laterite Ores: Chemistry and MOC Challenges Mohamed Buarzaiga IAPWS Workshop May 12, 2009.

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Presentation on theme: "High Pressure Acid Leaching of Nickel Laterite Ores: Chemistry and MOC Challenges Mohamed Buarzaiga IAPWS Workshop May 12, 2009."— Presentation transcript:

1 High Pressure Acid Leaching of Nickel Laterite Ores: Chemistry and MOC Challenges Mohamed Buarzaiga IAPWS Workshop May 12, 2009

2 Presentation Outline Overview of laterite ores processing Brief overview of HPAL chemistry Few examples of MOC challenges

3 Background Ni sources: sulfide and oxide ores Ni oxide (laterite) ores found mainly in tropical and subtropical regions (70% of Ni) Depleting Ni sulfide ores Four HPAL plants were built in the last 15 years and others are under construction Vale Inco is building a large plant in New Caledonia (Goro)

4 Autoclave Leaching Primary Neutralization S/L SeparationTailing Neutralization Secondary Neutralization S/L Separation MHP or MSP S/L Separation Lime PLS Barren Solution U/F Intermediate Product CaCO 3 Air Solids to PN Tailings Feed CaCO 3 SO 2 Air Conc. Sulfuric Acid Typical HPAL Flowsheet 240-270  C 250-500 kg acid/t ore

5 Goro Autoclave Circuit H 2 SO 4 92°C 150°C 200°C 92°C 67°C Steam 200°C 270°C Ore slurry Leached slurry Feed Slurry Recycling hot water

6 Goro HPAL Autoclave

7 Goro HPAL Heat Recovery

8 Simplified Autoclave Chemistry MeO + 2 H 2 SO 4  Me 2+ + 2 HSO 4 - + H 2 O H 2 SO 4 = H + + HSO 4 - Goethite  Hematite Conversion 2 FeOOH + 6 H +  2 Fe 3+ + 4 H 2 O 2 Fe 3+ + 3 H 2 O  Fe 2 O 3  + 6 H + Net: 2 FeOOH  Fe 2 O 3  + H 2 O Alunite Formation 6 AlOOH + 9 H 2 SO 4  3 Al 2 (SO 4 ) 3 + 12 H 2 O 3 Al 2 (SO 4 ) 3 + 14 H 2 O  2 (H 3 O)Al 3 (SO 4 ) 2 (OH) 6  + 5 H 2 SO 4 Net: 6 AlOOH + 4 H 2 SO 4 + 2 H 2 O  2 (H 3 O)Al 3 (SO 4 ) 2 (OH) 6  Cr(VI) Formation 3 MnO 2 + 2 Cr 3+ + 2 H 2 O  3 Mn 2+ + 2 HCrO 4 - + 2 H +

9 Sulfate Distribution % Feed Comp 2.0 Ni 0.15 Co 2.1 Al 1.9 Cr 0.99 Mn 39.8 Fe 11.9 SiO 2 2.8 MgO

10 MOC Challenges Harsh service environment High temperature and pressure Jets of high-pressure acidic slurry Abrasive particles Hot acidic slurry for downstream circuits Solution may contain chloride anions

11 MOC Challenges: Autoclave Circuit Ti clad steel for pressure vessels using explosion cladding Base steel: ASTM A516 Gr 70 Cladding Ti material: Gr 1, Gr 11, Gr 17 100-mm steel thickness with 8-mm Ti clad Acid injection into autoclave: Teflon or tantalum lining on titanium dip tubes Block vales

12 Autoclave Valve Erosion M. King JOM, July 2005

13 MOC Challenges: Autoclave Feed Pumps Diaphragm pumps to handle abrasive slurry Temperature limitation on pump  200  C “Drop leg” design for diaphragm protection Specialty elastomers seats for check valves Pulp dilution and implication for downstream circuits

14 Concluding Remarks An overview of a challenging high T process in the mining industry Proper selection of MOC is critical Interactions with universities and other R&D centers have been valuable

15 Thank you!


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