Ruthenium coated cathodes

• US 3,974,058 A
• Filed: 09/16/1974
• Issued: 08/10/1976
• Est. Priority Date: 09/16/1974
• Status: Expired due to Term

• Current Assignee: BASF Corporation (BASF SE)
• Original Assignee: BASF Wyandotte Corporation (BASF SE)
• Inventors: Gokhale, Sudarshan D.
• Primary Examiner(s): Mack, John H.
• Assistant Examiner(s): Prescott, A. C.
• Application Number:
  US05/506,510
• Time in Patent Office: 694 Days
• Field of Search: 204/242, 204/252, 204/254, 204/266, 204/278, 204/290 R, 204/290 F, 204/292, 204/98, 204/128
• US Class Current: 204/266
• CPC Class Codes: C25B 11/091 consisting of at least one catalytic element and at least one catalytic compound; consisting of two or more catalytic elements or catalytic compounds

Abstract

Composite cathodes comprising a metal substrate having thereon an intermediate coating of cobalt and an overcoating of ruthenium for use in electrolytic cells for the electrolysis of aqueous alkali metal halide solutions reduces the cell voltage requirements in comparison to the conventional ferrous metal cathodes traditionally used in such cells.

Claims

1. In an electrolytic cell for the production of halogen and caustic from alkali metal halide solutions wherein the cell is equipped with anodes, cathodes, and means separating said anodes from said cathodes, the improvement which comprises a composite cathode comprising a metal substrate having thereon an intermediate coating of cobalt and an overcoating of ruthenium.

2. The electrolytic cell of claim 1 wherein the coatings are on one side of the cathode.

3. The electrolytic cell of claim 1 wherein the coatings are on both sides of the cathode.

4. The electrolytic cell of claim 1 wherein there is a secondary coating between the intermediate coating of cobalt and the said metal substrate selected from the group consisting of nickel, platinum, palladium and rhodium.

5. The electrolytic cell of claim 4 wherein the secondary coating is nickel.

6. The electrolytic cell of claim 4 wherein the ruthenium coating is applied as two separate layers.

7. The electrolytic cell of claim 6 wherein the cathode is heat treated before and after the deposition of the first layer of ruthenium.

8. The electrolytic cell of claim 4 wherein the intermediate layer has a nonuniform thickness so as to increase the surface area.

9. The electrolytic cell of claim 1 wherein said means for separating said anodes from said cathode is a diaphragm.

10. The electrolytic cell of claim 1 wherein said means for separating said anode from said cathode is a membrane.