Anode for oxygen evolution

Claim 2

A process for producing an anode for oxygen evoution in an alkaline electrolyte wherein the process comprises a. coating an adherent, porous layer comprising nickel upon an electrically conductive support surface, said porous layer having a thickness of about 25 to about 275 micrometers and having a density of about 50%, b. placing the coated support surface into an aqueous nickel nitrate solution, and c. applying cathodic current to coated support surface, for a time sufficient to coat Ni(OH) 2 molecules upon the surface and pores of the porous layer and to provide a Ni(OH) 2 loading of up to about 10 mg/cm 2 of support surface.

Claim 3

The process of claim 1, wherein the cathodic current is applied while the coated substrate is immersed in the nickel nitrate solution.

Claim 4

The process of claim 1, wherein the anode is then washed in water, and then dried.

Claim 5

The process of claim 1, wherein the porous metal layer upon the support surface is sintered nickel upon a substrate material selected from the group consisting of mild steel, nickel, a nickel alloy, and stainless steel.

Claim 6

The process of claim 2, wherein the nickel nitrate solution is about 0.05 to about 4 molar.

Claim 7

The process of claim 5, wherein the solution is about 0.1 to about 0.3 molar.

Claim 8

The process of claim 1, wherein the cathodic current density is about 1 up to about 200 mA/cm 2 .

Claim 9

The process of claim 1, wherein the cathodic current is about 7 mA/cm 2 and the nickel nitrate solution is about 0.2 molar.

Claim 10

A process for the electrolytic production of oxygen comprising passing an electric current through an alkaline solution containing therein an anode and cathode, wherein the anode prior to anodic actions comprises a. an electrically conductive support surface, b. a porous layer comprising nickel adhered to at least part of said support surface, said porous layer having a thickness of about 25 to about 275 micrometers and a density of about 50%, and c. Ni(OH) 2 deposited upon the surface and within the pores of the porous layer, the loading of said Ni(OH) 2 being a small but effective amount to reduce the overpotential for O 2 evolution ranging up to about 10 mg/cm 2 of support surface.

Claim 11

A process for the electrolytic production of oxygen comprising passing an electric current through an alkaline solution containing therein an anode and cathode, wherein the anode prior to anodic actions comprises a. an electrically conductive support surface, b. a porous layer comprising nickel adhered to at least part of said support surface, said porous layer having a thickness of about 25 to about 275 micrometers and a density of about 50%, and c. Ni(OH) 2 deposited upon the surface and within the pores of the porous layer, the loading of said Ni(OH) 2 being a small but effective amount to reduce the overpotential for O 2 evolution ranging up to about 10 mg/cm 2 of support surface.

Claim 12

The process of claim 9, wherein the Ni(OH) 2 loading on the porous layer is up to about 20% of theoretical maximum value.

Claim 13

The process of claim 10, wherein the Ni(OH) 2 loading is about 6% to about 15% of theoretical maximum value.

Claim 14

The process of claim 9, wherein the cathode and anode are of substantially the same compositions.

Claim 15

An anode for oxygen evolution in alkaline electrolyte, said anode prior to anodic actions comprising a. an electrically conductive support surface, b. a porous layer comprising nickel adhered to at least part of said support surface, said porous layer being about 50% dense and having a thickness of about 25 to about 275 micrometers, and c. Ni(OH) 2 deposited upon the surface and within the pores of the porous layer, the loading of said Ni(OH) 2 being a small but effective amount to reduce the overpotential for O 2 evolution ranging up to about 10 mg/cm 2 of support surface, said porous layer bearing said deposit having a porosity of less than about 50%.

Claim 16

An anode for oxygen evolution in alkaline electrolyte, said anode prior to anodic actions comprising a. an electrically conductive support surface, b. a porous layer comprising nickel adhered to at least part of said support surface, said porous layer being about 50% dense and having a thickness of about 25 to about 275 micrometers, and c. Ni(OH) 2 deposited upon the surface and within the pores of the porous layer, the loading of said Ni(OH) 2 being a small but effective amount to reduce the overpotential for O 2 evolution ranging up to about 10 mg/cm 2 of support surface, said porous layer bearing said deposit having a porosity of less than about 50%.

Claim 17

An anode of claim 13, wherein the support surface is steel, nickel or nickel alloy.

Claim 18

An anode of claim 13, wherein the support surface is deposited on a substrate.

Claim 19

The anode of claim 15, wherein the substrate is steel and the support surface is nickel plated on said steel substrate.

Claim 20

The anode of claim 13, wherein the porous layer comprises nickel or a nickel-iron alloy.

Claim 21

An anode of claim 13, wherein the Ni(OH) 2 is substantially converted to nickel oxyhydroxide by placing into an aqueous alkaline solution and applying anodic current.

Claim 22

An anode of claim 13, wherein the porous layer deposited on the support surface has a thickness of up to about 125 micrometers.

Claim 23

An anode of claim 17, wherein the porous layer is deposited as a powder in an aqueous medium.

Claim 24

An anode of claim 13, wherein the Ni(OH) 2 loading on the porous layer is about 1 to about 6 mg/cm 2 .

Claim 25

An anode of claim 13, wherein the Ni(OH) 2 loading on the porous layer is greater than about 1 mg/cm 2 .

Claim 26

An anode of claim 13, wherein the Ni(OH) 2 loading on the porous layer is up to about 20% of the theoretical maximum value.

Claim 27

An anode of claim 13, wherein the Ni(OH) 2 loading on the porous layer is about 6% to about 15% of the theoretical maximum value.

Claim 28

An electrode for gas evolution in alkaline electrolytes, said electrode comprising a. an electrically conductive support surface, b. a porous layer comprising nickel adhered to at least part of said support surface, said porous layer being about 50% dense and having a thickness of about 25 to about 275 micrometers, and c. Ni(OH) 2 deposited upon the surface and within the pores of the porous layer, the loading of said Ni(OH) 2 deposit being less than about 10 mg/cm 2 of support surface.

Claim 29

An electrode for gas evolution in alkaline electrolytes, said electrode comprising a. an electrically conductive support surface, b. a porous layer comprising nickel adhered to at least part of said support surface, said porous layer being about 50% dense and having a thickness of about 25 to about 275 micrometers, and c. Ni(OH) 2 deposited upon the surface and within the pores of the porous layer, the loading of said Ni(OH) 2 deposit being less than about 10 mg/cm 2 of support surface.

Claim 30

An electrode of claim 25, wherein said electrode is used as an anode.

Claim 31

An electrode of claim 25, wherein said electrode is used as a cathode.