Oxidation kinetics of tetravalent uranium during sulfuric-acid leaching intensification under in-situ recovery conditions
Abstract
The paper examines how redox phenomena govern the recovery of uranium by in-situ recovery (ISR) technology, with particular emphasis on the role of oxygen and iron in the controlling reactions. A review is presented of the standard electrode potentials of the ionic species participating in the process, followed by a detailed examination of the conversion of Fe(II) to Fe(III) and its effect on uranium dissolution in acidic media. The experimental section addresses the oxygenation of acidic lixiviants through a Venturi-type nozzle. The findings demonstrate that tuning the redox conditions markedly enhances the productivity of ISR. Atmospheric oxygen, owing to its availability and cost efficiency, drives the Fe(II) → Fe(III) transition and thereby raises the solubility of uranium-bearing species. Through experiment, the flow velocity providing the maximum oxygen dissolution was identified. Incorporation of the Venturi nozzle substantially increased the dissolved-oxygen content of the lixiviant, which in turn raised the Fe(III) concentration and improved uranium recovery. The proposed approach yielded a 38.13 % increase in uranium extraction relative to the conventional procedure. The work confirms the importance of redox processes in uranium hydrometallurgy and justifies the need to optimize them for industrial gains. A Venturi nozzle embedded in an acidic recirculation loop, operated without any externally supplied oxidant, sustains an Eh elevation sufficient for the U(IV) → U(VI) transition through enhanced oxidation of Fe2+ to Fe3+. The study quantitatively documents a ~60-70 % rise in dissolved O2, an Eh increment of ~30-80 mV, and a corresponding gain in dissolved uranium.
The work was carried out with the financial support of the Committee of Science of the Ministry of Education and Science of the Republic of Kazakhstan (grant N AP 22685351).
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