Zinc chloride electrolysis

• US 4,292,147 A
• Filed: 06/20/1980
• Issued: 09/29/1981
• Est. Priority Date: 06/22/1979
• Status: Expired due to Term

• Current Assignee: Derek John Fray
• Original Assignee: National Research Development Corporation
• Inventors: Fray, Derek J., Thomas, Bernard K.
• Primary Examiner(s): Andrews, R. L.
• Application Number:
  US06/161,644
• Time in Patent Office: 466 Days
• Field of Search: 204/117, 204/118, 204/114
• US Class Current: 205/342
• CPC Class Codes: C25C 1/16 of zinc, cadmium or mercury

Abstract

Electrolysing an aqueous solution of zinc chloride or cadmium chloride of a concentration of 15-35 weight % at pH 2-3.5 below 35 C with gas agitation at a current density exceeding 1000 A/m², whereby coherent zinc or cadmium is yielded at the cathode.

Claims

1. A process for electrolysing an aqueous solution of zinc chloride having a concentration of 15-35 weight %, the solution arising from leaching a zinc-containing material using an aqueous substantially saturated chlorine solution, the electrolysis proceeding at pH 2-3.5 below 35°

C. with gas agitation at a current density exceeding 1000 A/m², thereby yielding coherent zinc at the cathode.

2. Electrolysing according to claim 1, wherein the leaching was conducted in the presence of chlorine hydrate.

3. Electrolysing according to claim 1, wherein the solution being electrolysed contains up to 20 weight % of the chloride salts of Group I or of ammonia.

4. Electrolysing according to claim 1, wherein the concentration of the zinc chloride in the aqueous solution is from 20 to 30 weight %.

5. Electrolysing according to claim 4, wherein the said concentration is from 24 to 26 weight %.

6. Electrolysing according to claim 1, wherein the current density exceeds 2500 A/m².

7. Electrolysing according to claim 1, wherein the current is intermittently reversed.

8. Electrolysing according to claim 1, at a temperature not below 0°

C.

9. Electrolysing according to claim 1, at a temperature not exceeding 9°

C.

10. Electrolysing according to claim 9, at a temperature of 5°

-9°

C.

11. Electrolysing according to claim 9, wherein chlorine hydrate formed at the anode is sent to leach zinc from a zinc-containing material.