Abstract

The dissolution rate of heazlewoodite in nitric acid solution has been determined. The effects of nitric acid concentration, temperature, particle size, stirring intensity and addition of Cu 2+ ions have been investigated. Solid residues after leaching were examined by SEM, X-ray diffraction and chemical analysis. In the solutions containing less than 2.0 M HNO 3, dissolution was observed to be completely inhibited after 30 min leaching time, and the rate of hydrogen sulphide production was faster than its oxidation to S 0 and HSO 4 −. In 3 M HNO 3, an abrupt increase in dissolution rate of Ni 3S 2 was found. Two different regions of the dissolution of heazlewoodite were observed below and above 50°C. At temperatures below 50°C, the dissolution rate was very slow, even in 3.0 M HNO 3 solution, and H 2S gas was evolved. Above 50°C, the dissolution rate rapidly increased. Over the temperature interval 60–90°C in 3.0 M HNO 3 dissolution followed a linear rate law, and the activation energy was found to be 42.1 kJ mol −1. Most of the oxidized sulphide ion was found in the solution as sulphate. The leaching rate was independent of stirring speed. The rate-controlling step of the Ni 3S 2 dissolution is the oxidation of hydrogen sulphide to elemental sulphur or sulphate ions on the Ni 3S 2 surface. Addition of small amounts of Cu 2+ ions to the nitric acid acted as catalyst for the dissolution of Ni 3S 2. Bubbling air through the leach suspension increased the dissolution rate of Ni 3S 2 in solutions containing less than 2.0 M HNO 3.

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