Process for the recovery of zinc

• US 4,071,421 A
• Filed: 09/17/1976
• Issued: 01/31/1978
• Est. Priority Date: 08/11/1976
• Status: Expired due to Term

• Current Assignee: Sherritt Gordon Mines Limited
• Original Assignee: Sherritt Gordon Mines Limited
• Inventors: Masters, Ian M., Sefton, Verner B., Bolton, Gerald L.
• Primary Examiner(s): Andrews, R. L.
• Application Number:
  US05/724,423
• Time in Patent Office: 501 Days
• Field of Search: 204/96, 204/114, 204/119
• US Class Current: 205/345
• CPC Class Codes: C25B 1/21 Manganese oxides
• CPC Class Codes: C25C 1/16 of zinc, cadmium or mercury
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

A process for recovering zinc and manganese dioxide from material containing zinc and manganese compounds, includes leaching the material to provide an aqueous solution containing manganese and zinc ions, electrolyzing the solution in one electrolytic cell with conditions inhibiting the formation of manganese dioxide and favoring the deposition of zinc, and electrolyzing the solution in another electrolytic cell with conditions favoring the formation of manganese dioxide. Zinc is removed from the one electrolytic cell and manganese dioxide is removed from the other electrolytic cell.

Claims

1. A process for recovering zinc and manganese dioxide from material containing zinc and manganese compounds, including treating the material to provide an aqueous sulphate solution containing manganese and zinc ions, electrolyzing the solution in one electrolytic cell with conditions inhibiting the formation of manganese dioxide and favouring the deposition of zinc, said one electrolytic cell containing from about 5 to about 45 g.p.l. manganese ions, electrolyzing the solution in another electrolytic cell with conditions favouring the formation of manganese dioxide, said other electrolytic cell containing from about 30 to about 100 g.p.l. zinc ions, recovering zinc from said one electrolytic cell, and recovering manganese dioxide from said other electrolytic cell.

2. A process according to claim 1 wherein the zinc and manganese are present in the material in sulphidic form.

3. A process according to claim 2 wherein leaching is carried out in two stages, with solution from the first leachng stage being utilized for subsequent electrolysis in the electrolytic cells, and with leach solution from the second leaching stage being recycled to the first leaching stage.

4. A process according to claim 3 wherein solution is recycled to the second leaching stage after passing through the electrolytic cells.

5. A process according to claim 2 wherein solution is recycled to a leaching step after passing through the electrolytic cells.

6. A process according to claim 1 wherein the formation of manganese dioxide in said one electrolytic cell is inhibited by the use of a preconditioned anode.

7. A process according to claim 6 wherein the anode is of lead containing from about 0.5 to about 1% silver.

8. A process according to claim 1 wherein the formation of manganese dioxide in said other electrolytic cell is favoured by the use of an anode comprising a substrate coated with lead dioxide.

9. A process according to claim 8 wherein the substrate is graphite.

10. A process according to claim 8 wherein the substrate it titanium.

11. A process according to claim 1 wherein said one electrolytic cell contains about 10 to about 20 g.p.l. manganese ions.

12. A process according to claim 1 wherein the formation of manganese dioxide in said other electrolytic cell is favoured by the use of an anode of rolled lead.

13. A process according to claim 1 wherein the solution in said other electrolytic cell contains from about 50 to about 60 g.p.l. zinc ions.

14. A process according to claim 1 wherein zinc is deposited on a cathode in said other electrolytic cell and recovered therefrom.

15. A process according to claim 1 wherein the solution is passed first through said one electrolytic cell and then through said other electrolytic cell.