Claims
- 1. In a method of electrolyzing brine in an electrolytic cell having a permionic membrane with cathodic electrocatalyst bearing upon one surface of the permionic membrane, which method comprises feeding alkali metal chloride to the cell, imposing an electrical potential across the cell, and evolving hydrogen at the cathode electrocatalyst, the improvement wherein the cathodic electrocatalyst comprises particles consisting essentially of borides of transition metals chosen from the group consisting of borides of titanium, vanadium, niobium, tantalum, and tungsten.
- 2. The method of claim 1 wherein the boride is TiB.sub.2.
- 3. In a method of electrolyzing brine in an electrolytic cell having a permionic membrane with cathodic electrocatalyst bonded to and embedded in one surface of the permionic membrane, which method comprises feeding alkali metal chloride to the cell, and imposing an electrical potential across the cell, the improvement wherein the cathodic electrocatalyst comprises particles consisting essentially of borides of transition metals.
- 4. The method of claim 3 wherein the borides are chosen from the group consisting of borides of titanium, vanadium, niobium, tantalum, chromium, and tungsten.
- 5. The method of claim 4 wherein the boride is TiB.sub.2.
- 6. In an electrolytic cell having a permionic membrane with a cathode bearing upon the cathodic surface thereof, the improvement wherein the cathode comprises particles consisting essentially of borides of transition metals chosen from the group consisting of borides of titanium, vanadium, niobium, tantalum, and tungsten.
- 7. The electrolytic cell of claim 6 wherein the boride is TiB.sub.2.
- 8. In an electrolytic cell having a permionic membrane with a cathode bearing upon the cathodic surface thereof, the improvement wherein the cathode comprises particles consisting essentially of a boride of a transition metal.
- 9. The electrolytic cell of claim 8 wherein the boride is chosen from the group consisting of borides of titanium, vanadium, niobium, tantalum, chromium, and tungsten.
- 10. The electrolytic cell of claim 9 wherein the boride is TiB.sub.2.
- 11. In a method of electrolyzing brine in an electrolytic cell having a permionic membrane with cathodic electrocatalyst bearing upon one surface of the permionic membrane, which method comprises feeding alkali metal chloride to the cell, and imposing an electrical potential across the cell, the improvement wherein the cathodic electrocatalyst comprises particles consisting essentially of a boride of a transition metal.
- 12. The method of claim 11 wherein the boride is chosen from the group consisting of borides of titanium, vanadium, niobium, tantalum, chromium, and tungsten.
- 13. The method of claim 12 wherein the boride is TiB.sub.2.
- 14. In an electrolytic cell having a permionic membrane with a cathode bonded to and embedded in the cathodic surface thereof, the improvement wherein the cathode comprises particles consisting essentially of borides of transition metals.
- 15. The electrolytic cell of claim 14 wherein the borides are chosen from the group consisting of borides of titanium, vanadium, niobium, tantalum, chromium, and tungsten.
- 16. The electrolytic cell of claim 15 wherein the boride is TiB.sub.2.
Parent Case Info
This is a continuation of application Ser. No. 014,465, filed Feb. 23, 1979, now abandoned.
US Referenced Citations (2)
Number |
Name |
Date |
Kind |
3770613 |
Chisholm |
Nov 1973 |
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4191618 |
Coker et al. |
Mar 1980 |
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Continuations (1)
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Number |
Date |
Country |
Parent |
14465 |
Feb 1979 |
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