Oxidation of Fe(II) in a synthetic nickel laterite leach liquor with SO2/air |
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| Authors: | Wensheng Zhang David Muir |
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| Affiliation: | 1. Alyssum Ventures Ltd, Isle of Man;2. Brazilian Nickel Ltd, London, UK;3. Scientific Associate of the Natural History Museum, London, UK;1. Department of Metallurgy and Material, Universitas Indonesia, Depok 16424, Indonesia;2. Research Unit for Mineral Technology, Indonesian Institute of Sciences, South Lampung 35361, Indonesia;1. Department of Materials Science & Nanotechnology Engineering, Abdullah Gul University, Kayseri 38100, Turkey;2. Department of Metallurgical Engineering, Faculty of Mining and Petroleum Engineering, Institut Teknologi Bandung, Bandung 40132, Indonesia;3. Division of Mineral Processing, Department of Mining Engineering, Eskisehir Osmangazi University, Eskisehir 26480, Turkey |
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| Abstract: | Under specific controlled conditions, the addition of SO2 to oxygen or air produces the peroxy-monosulphate free radical in solution, which is a stronger oxidant than oxygen alone. In this study, the practical strategies required to optimise the oxidation of Fe(II) with SO2/air was investigated at 75 °C as part of a process to remove iron as Fe(III) oxides from a synthetic nickel laterite high pressure acid leach solution containing 5 g/L Fe(II), 1 g/L Fe(III), 8 g/L Ni, 30 g/L Mg in sea water at pH about 2. The rate of Fe(II) oxidation was optimised in the pH range of 1.2–2.0 with respect to SO2/air ratio and gas flow rates for minimum production of H2SO4 and maximum utilisation of SO2. In order to minimise the air flow rates into the reactor vessel, the maximum rate of SO2 addition that could be employed with air was established whilst maintaining oxidising conditions. The results provide strategies for commercial applications of the SO2/air oxidising system and indicate important factors for reactor design. |
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