Abstract

Iron(III) can be used as an oxidant in the leaching of uranium ore in an acid medium. The oxidation of iron(II) to iron(III) using an SO 2/O 2 gas mixture was investigated in order to provide an iron(III) stream for uranium extraction. The effects of pH, temperature and SO 2/O 2 volumetric ratios were considered. Oxidation of iron(II) by SO 2/O 2 was controlled by diffusion of SO 2 or O 2 at pH 2 and 40 °C. However as the pH decreased below pH 1, the reaction was controlled by a slow chemical step and the reaction rate decreased. Increasing the temperature increased the oxidation rate at pH 0.8, and at 70 °C the rate again became dependent on SO 2 or O 2 diffusion. The oxygen efficiency for a fixed reactor set-up was dependent on the SO 2/O 2 ratio and total flow rate of the gas. In leach tests, the uranium extraction achieved with iron(III) solution prepared by SO 2/O 2 oxidation was the same as that for a standard uranium leach with conventional oxidant.

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