Skorpion Zinc: Mine-to-metal zinc production via solvent extraction

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Skorpion Zinc: Mine-to-metal zinc production via solvent extraction Kathy Sole Anglo Research, South Africa Herman Fuls, Jürgen Gnoinski Skorpion Zinc, Namibia H

Traditional Zinc Processing Usually present as sulphide Amenable to upgrading Roast-Leach-Electrowin process Oxides and silicates considered untreatable

Skorpion Zinc Oxide/silicate: Zn 10-40% Si 26% Fe 2-3% Some Cl and F First application of Zn SX to primary processing Silicate leaching technology First metal May 2003 150 000 t/a SHG zinc (>99.995% purity)

Overview Electrolyte requirements for Zn EW Skorpion Zinc flowsheet Challenges and process improvements during first 5 years of operation Comparison of design and actual performance

Skorpion Zinc

Skorpion Zinc

Advance Electrolyte Specification Element Concentration Element Concentration (mg/l) (μg/l) Zn > 90 000 Ga 3 Mn 2 000 Ge < 10 Cd < 0.05 As < 10 Co < 0.05 Sn < 1 Ni < 0.05 Sb < 1 Fe < 5 Te < 1 Cl < 0.1 Tl 25 F < 0.02

Simplified Skorpion Flowsheet Zinc silicate oxide ore Comminution H 2 SO 4 CaCO 3 Leach Neutralisatn Fe, Al, Si Thickening Zn SX O/F Base metals, Cl, F H 2 SO 4 Zn EW SHG Zn cathode (>99.995% Zn)

Silicate Leaching High SiO 2 in ore Avoid conditions for silica gel formation Minimise Zn losses in filtration dilute leach liquor (30 g/l Zn) upgrade and purify by SX

Zn Extraction by D2EHPA Extraction (%) 100 80 60 40 20 0 Zn Ca Cd Mn Fe(lll) Cu Co Mg Ni RO O P RO OH 0 1 2 3 4 5 6 7 8 Equilibrium ph

Skorpion Zn SX Circuit SO PLS 6 M HCl LO ScO E3 E2 E1 W1 W2 W3 S1 S2 R1 Raffinate H 2 O Zn EW SE SO > 99.995 % Zn

Selectivity of SX Zn Fe Cu Ca Mg Mn K Na Cd Co Ni Sn As Sb Cl F Extraction Wash Scrub Strip/Regen EW From Técnicas Reunidas

Full-Scale SX Process Performance Element Specification Skorpion for AE (mg/l) electrolyte (mg/l) Zn > 90 000 ~ 120 000 Cd < 0.05 0.012 Fe < 5 < 5 Mn < 3000 2500 Co < 0.05 0.07 Ni < 0.05 0.07 Ca ~ 50 Cl < 100 56 F < 20 3

Full-Scale SX Process Performance Selectivity matches theory Capacity exceeds design 107 % Zn transfer ***Pic carbon columns

Challenges Organic transfer to EW Solids in PLS Health of organic phase Fire risk single stream: 100% production loss

Process Improvements Minimisation of organic transfer to EW No D2EHPA 5 mg/l D2EHPA

Process Improvements Minimisation of organic transfer to EW Advance electrolyte processed through aftersettler flotation column activated carbon filter/coalescers (lead-lag configuration) < 1 mg/l OE

Process Improvements Deportment of impurities to electrolyte SX Feed Advance electrolyte [M] in PLS (mg/l) 600 400 Cu Ni [M] in AE (ug/l) 900 600 300 Ni Cu 200 Jan Mar Running May time Jul (months) Sep Nov 2007 0 Running Running time time (months)

Electrowinning of Zinc Half-cell reduction E o (V) Cu 2+ + 2 e Cu 0.34 2 H + + 2 e H 2 0.00 Ni 2+ Co 2+ + 2 e Ni 0.26 + 2 e Co 0.28 PbSO 4 + 2 e Pb + SO 2 4 0.35 Cd 2+ + 2 e Cd 0.40 Zn 2+ + 2 e Zn 0.76 Mn 2+ + 2 e Mn 1.18

Solids in PLS ~100 mg/l TSS (target <10 mg/l TSS) excessive crud formation Linked to excursions of Ni, Co High organic consumption Process Improvements Deportment of impurities to electrolyte

Process Improvements Control of solids deportment to SX Original design thickener clarifier sand filters Process improvements PLS ponds avoid colloidal silica formation ph control of leach avoid leach plant downtime reduce mixer air entrainment Roymec pinned-bed clarifier

Process Improvements Control of solids deportment to SX Pinned-bed clarifier <10 mg/l TSS 300 PLS in PLS out TSS (mg/l) 200 100 0 1 5 9 13 17 21 25 29 Running time (days)

PLS and Electrolyte Composition Element PLS (mg/l) AE (mg/l) Design Actual Design Actual Al 300 82 190 Ca 650 660 50 Cd 100 330 <0.05 0.01 Cl 5000 1030 <100 50 Co 100 18 <0.05 0.02 Cu 700 500 <0.05 0.09 F 200 40 <20 7 Fe 5 1.5 <5 <5 Mg 200 1040 Mn 500 2120 3000 2200 Ni 800 330 <0.05 0.08 Si 40 70 Zn 30 000 38 000 90 000 117 000

Advantages of Zn SX High Si in ore Dilute leach solution to avoid silica gel Minimise soluble zinc losses in filtrate

Advantages of Zn SX High Si in ore EW very sensitive to impurities Reject Cu, Ni, Co, Cd, Mn, Mg Reject F, Cl Reject Ca

Advantages of Zn SX High Si in ore EW very sensitive to impurities Upgrade 30 g/l Zn in PLS > 100 g/l Zn in AE

Advantages of Zn SX High Si in ore EW very sensitive to impurities Upgrade SHG Zn > 99.995 % purity

SHG Zinc Cathode Element SHG spec.* Skorpion (ppm) (ppm) Cd 30 0 Cu 10 7 Fe 20 3 Pb 30 25 Sn 2 2 Zn 999950 999963 * British standard, 1996

Product Quality 150 000 t/a >99.995% Zn SHG Zn

Conclusions Breakthrough technology for zinc oxide treatment untreatable ore First mine-to-metal operation Robust technology SX process considered a technical success Consistent production of 150 000 t/a SHG Zn Amongst world s highest quality and lowest cost zinc producers (2007 C1 US 32/lb Zn)

Acknowledgements Skorpion Zinc Anglo Base Metals Sole 2001, Proceedings 6 th World Congress Chemical Engineering, Melbourne Fuls et al. 2005, Proceedings ISEC 2005, Beijing Gnoinski et al. 2005, Proceedings Lead-Zinc 2005, Osaka Sole et al. 2008, Proceedings ISEC 2008, Tucson, AZ