<p>The extraction of zinc from zinc oxide concentrates was paramount in addressing the issue of zinc oxide ore stockpiles and promoting the efficient utilization of zinc resources. In this work, a new process for the extraction of zinc from mixed zinc oxide concentrates was proposed. Thermodynamic calculations showed that all the physical phases in the concentrate could spontaneously react with concentrated H<sub>2</sub>SO<sub>4</sub> to form ZnSO<sub>4</sub>·H<sub>2</sub>O, PbSO<sub>4</sub>, CaSO<sub>4,</sub> and Fe<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub> in the curing product. The curing experiments indicated that the zinc-containing minerals could be converted to ZnSO<sub>4</sub>·H<sub>2</sub>O and thus extracted under the conditions of a curing temperature of 200 ℃, curing time of 1&#xa0;h, and acid-to-material ratio of 1:1 (g/g). The systematic leaching experiments demonstrated that the leaching rate of zinc could reach 98.99%, iron was 34.31%, calcium was 9.70% and lead was 0.49% under optimal leaching conditions. Furthermore, the mechanism analysis revealed that only ZnSO<sub>4</sub> and Fe<sub>2</sub>(SO<sub>4</sub>)<sub>3</sub> were selectively leached into the solution. The leaching residues were mainly PbSO<sub>4</sub>, CaSO<sub>4,</sub> and SiO<sub>2</sub>, which can be used for thermal lead extraction. The process proposed in this paper avoided the bubbling phenomenon caused by direct acid leaching, reduced acid consumption, and improved the leaching rate of zinc.</p> Graphical Abstract <p></p>

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A Novel Approach for Recovering Zinc from Mixed Zinc Oxide Concentrate by Low Temperature Curing–Water Leaching

  • Yan Xue,
  • Baozhong Ma,
  • Weiwei Zhang,
  • Yubo Liu,
  • Zhihe Cao,
  • Yongqiang Chen,
  • Chengyan Wang

摘要

The extraction of zinc from zinc oxide concentrates was paramount in addressing the issue of zinc oxide ore stockpiles and promoting the efficient utilization of zinc resources. In this work, a new process for the extraction of zinc from mixed zinc oxide concentrates was proposed. Thermodynamic calculations showed that all the physical phases in the concentrate could spontaneously react with concentrated H2SO4 to form ZnSO4·H2O, PbSO4, CaSO4, and Fe2(SO4)3 in the curing product. The curing experiments indicated that the zinc-containing minerals could be converted to ZnSO4·H2O and thus extracted under the conditions of a curing temperature of 200 ℃, curing time of 1 h, and acid-to-material ratio of 1:1 (g/g). The systematic leaching experiments demonstrated that the leaching rate of zinc could reach 98.99%, iron was 34.31%, calcium was 9.70% and lead was 0.49% under optimal leaching conditions. Furthermore, the mechanism analysis revealed that only ZnSO4 and Fe2(SO4)3 were selectively leached into the solution. The leaching residues were mainly PbSO4, CaSO4, and SiO2, which can be used for thermal lead extraction. The process proposed in this paper avoided the bubbling phenomenon caused by direct acid leaching, reduced acid consumption, and improved the leaching rate of zinc.

Graphical Abstract