Nickel-based anode for oxygen evolution

Patent metadata

Field	Value
Publication number	US-2024352598-A1
Application number	US-202218713850-A
Country	US
Kind code	A1
Filing date	Dec 15, 2022
Priority date	Dec 16, 2021
Publication date	Oct 24, 2024
Grant date	—

Abstract

An anode for oxygen evolution in electrolytic processes comprising a nickel-based planar substrate having a first side and second side and a porous catalytic coating formed on at least one side of the substrate, wherein the porous catalytic coating exhibits a lamellar morphology made from metallic patches and void patches, the metallic patches being made from a material selected from nickel, nickel oxide, a nickel-aluminium alloy, or combinations thereof. The present invention also concerns a method for the production of such an anode using powder plasma spraying or electric wire-arc spraying.

First claim

1 . An anode for oxygen evolution in electrolytic processes comprising a nickel-based planar substrate having a first side and second side and a porous catalytic coating formed on at least one side of said substrate, wherein said porous catalytic coating exhibits a lamellar morphology made from metallic patches and void patches, said metallic patches being made from a material selected from nickel, nickel oxide, a low-alloy nickel component comprising at least 80 wt. % nickel, or combinations thereof, wherein said metallic patches of said porous coating have a size distribution such that their lengths, measured parallel to the planar substrate, is predominately at least 25 μm.

2 . The anode according to claim 1 , wherein porous catalytic coating has a void ratio within a range from 5 to 50%.

3 . The anode according to claim 1 , wherein said porous catalytic coating has a thickness within a range from 50 μm to 200 μm.

4 . The anode according to claim 3 , wherein said porous catalytic coating formed on at least one side of said planar substrate has a thickness within a range from 100 μm to 180 μm.

5 . The anode according to claim 4 , wherein said porous catalytic coating is formed on both sides of said metal substrate.

6 . The anode according to claim 1 , wherein said metallic patches of said porous catalytic coating comprise 80 to 98 wt. % nickel or nickel oxide and 20 to 2 wt. % aluminium, referring to the metallic elements.

7 . The anode according to claim 6 , wherein said porous catalytic coating comprises 0.1 to 2 vol. % nickel oxide.

8 . The anode according to claim 1 , wherein said porous catalytic coating has a surface area within a range of 5 to 20 m 2 /g (BET).

9 . The anode according to claim 1 , wherein said nickel-based substrate is a nickel mesh having a thickness within the range of 0.2 to 1.5 mm.

10 . The anode according to claim 1 , wherein said porous catalytic coating is obtained by powder plasma spraying or electric wire arc spraying an initial coating comprising a mixture of a first component comprising predominately nickel and a second component comprising predominantly aluminium on at least one side of said substrate and subsequent leaching of aluminium from said initial coating.

11 . A method for the production of an anode for oxygen evolution in electrolytic processes, comprising the following steps:
a) providing a planar nickel-based metal substrate having a first side and a second side; b) providing a first coating material comprising at least 80 wt. % nickel and providing a second coating material comprising at least 80 wt. % aluminium; c) depositing melted droplets from said first coating material and melted droplets from said second coating material on at least one side of said substrate to form an initial coating; d) leaching of aluminium from said initial coating in an alkaline bath to form a porous catalytic coating.

12 . The method of claim 11 , wherein in step b) said first coating material is a nickel powder and said second coating material comprising is an aluminium powder, and in step c) melted droplets of said nickel powder and melted droplets of said aluminium powder are deposited on said substrate via plasma spraying.

13 . The method of claim 11 , wherein in step b) said first coating material is a first consumable metal wire comprising at least nickel and said second coating material is a second consumable wire comprising at least aluminium, and in step c) melted droplets from said first and second metal wires are deposited on said substrate via electric wire-arc spraying.

14 . The method according to claim 11 , wherein in step c), an initial coating is applied to both sides of said substrate.

15 . The method according to claim 11 , wherein step d) is carried out in an aqueous alkaline hydroxide solution at a temperature in the range from 10 and 100° C. for a time period between 10 min and 36 hours.

16 . The anode according to claim 2 , wherein porous catalytic coating has a void ratio within the range from 10 to 25%.

17 . The method according to claim 15 , wherein step d) is carried out for the time period between 2 to 24 hours.

Assignees

• Industrie De Nora Spa

Inventors

• Pino Francesco

Classifications

• C25B1/04 Primary

  by electrolysis of water · CPC title

• C25B11/091

  consisting of at least one catalytic element and at least one catalytic compound; consisting of two or more catalytic elements or catalytic compounds · CPC title

• C25B11/061

  Metal or alloy · CPC title

• Y02E60/36

  Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title

• C23C4/18

  After-treatment · CPC title