<p>Zinc oxide dust, as an important secondary zinc resource, has significant recycling value. The presence of zinc ferrite (ZnFe<sub>2</sub>O<sub>4</sub>) and zinc sulfide (ZnS) in the dust is the main factor affecting zinc recovery. In this paper, the dissolution behavior of iron minerals and ZnS under different influencing factors was investigated. The study found that the factors affecting the dissolution of iron minerals, in descending order, are initial H<sub>2</sub>SO<sub>4</sub> concentration, liquid–solid ratio and reaction time, and iron mineral dissolution can provide Fe<sup>3+</sup> oxidant for the leaching system. The dissolution extent of ZnS is directly proportional to the concentration of Fe<sup>3+</sup> in the solution. The initial H<sub>2</sub>SO<sub>4</sub> concentration, liquid–solid ratio and reaction time can indirectly affect the dissolution of ZnS by affecting the dissolution of iron minerals in the raw materials. Increasing oxygen flow rate is beneficial to the conversion of Fe<sup>2+</sup> to Fe<sup>3+</sup>, thereby indirectly accelerating the dissolution of ZnS. By increasing the initial Fe<sup>3+</sup> concentration and oxygen flow rate, the content of zinc in the leaching residue can be reduced to 2.16%, and the zinc leaching efficiency reaches 99.51%. This work has important practical value for the treatment of ZnS in zinc oxide dust under an atmospheric pressure-sulfuric acid leaching system and the efficient recovery of zinc.</p>

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Oxidation Behavior of Iron During Atmospheric Oxygen-Enriched Leaching of Zinc Oxide Dust

  • Nian Liu,
  • Xuantong Zhou,
  • Zhigan Deng,
  • Zhanqing Lu,
  • Chang Wei,
  • Xingbin Li

摘要

Zinc oxide dust, as an important secondary zinc resource, has significant recycling value. The presence of zinc ferrite (ZnFe2O4) and zinc sulfide (ZnS) in the dust is the main factor affecting zinc recovery. In this paper, the dissolution behavior of iron minerals and ZnS under different influencing factors was investigated. The study found that the factors affecting the dissolution of iron minerals, in descending order, are initial H2SO4 concentration, liquid–solid ratio and reaction time, and iron mineral dissolution can provide Fe3+ oxidant for the leaching system. The dissolution extent of ZnS is directly proportional to the concentration of Fe3+ in the solution. The initial H2SO4 concentration, liquid–solid ratio and reaction time can indirectly affect the dissolution of ZnS by affecting the dissolution of iron minerals in the raw materials. Increasing oxygen flow rate is beneficial to the conversion of Fe2+ to Fe3+, thereby indirectly accelerating the dissolution of ZnS. By increasing the initial Fe3+ concentration and oxygen flow rate, the content of zinc in the leaching residue can be reduced to 2.16%, and the zinc leaching efficiency reaches 99.51%. This work has important practical value for the treatment of ZnS in zinc oxide dust under an atmospheric pressure-sulfuric acid leaching system and the efficient recovery of zinc.