Oxygen-consuming electrode which contains carbon nanotubes and method for producing same

Patent metadata

Field	Value
Publication number	US-2017283964-A1
Application number	US-201515510259-A
Country	US
Kind code	A1
Filing date	Aug 28, 2015
Priority date	Sep 12, 2014
Publication date	Oct 5, 2017
Grant date	—

Abstract

The invention relates to an oxygen-consuming electrode, in particular for use in chloralkali electrolysis, comprising a catalyst coating based on carbon nanotubes, and to an electrolysis device. The invention further relates to a method for producing said oxygen-consuming electrode and to the use thereof in chloralkali electrolysis or fuel cell technology.

First claim

1 .- 21 . (canceled)

22 . A process for producing a gas diffusion electrode for the reduction of oxygen, where the gas diffusion electrode has at least one sheet-like electrically conductive support element and a gas diffusion layer applied to the support element and an electrocatalyst, wherein the gas diffusion layer is formed by a mixture of carbon nanotubes and a fluoropolymer, and wherein a mixture of carbon nanotubes and fluoropolymer is applied in powder form to the support element and compacted, with the carbon nanotubes forming the electrocatalyst and being substantially free of nitrogen constituents.

23 . The process as claimed in claim 22 , wherein the carbon nanotubes are in form of an agglomerate, where at least 95% by volume of the agglomerate particles have an external diameter in the range from 30 μm to 5000 μm.

24 . The process as claimed in claim 22 , wherein the fluoropolymer has an average particle size d50 in agglomerated form of from 100 μm to 1 mm.

25 . The process as claimed in claim 22 , wherein the mixture of carbon nanotubes and fluoropolymer is produced by dry mixing.

26 . The process as claimed in claim 25 , wherein the dry mixing is carried out in a first phase until a homogeneous premix is obtained, with the temperature of the material being mixed being not more than 25° C.

27 . The process as claimed in claim 25 , wherein the dry mixing is carried out in a second phase, after obtaining a homogeneous premix from the first phase, using mixing tools, with the temperature of the mixture being more than 30° C.

28 . The process as claimed in claim 22 , wherein compaction is carried out by means of rollers in a roller apparatus, with the linear pressing force exerted by the roller(s) used on the support element and the sprinkled-on powder mixture preferably being from 0.1 to 1 kN/cm.

29 . The process as claimed in claim 22 , wherein rolling is carried out at a constant ambient temperature of the manufacturing rooms, in particular at a temperature of not more than 20° C.

30 . The process as claimed in claim 22 , wherein the mixture of carbon nanotubes and fluoropolymer comprises from 1 to 70% by weight of PTFE and 99-30% of carbon nanotubes.

31 . The process as claimed in claim 22 , wherein the electrically conductive support element is a mesh, nonwoven, foam, woven fabric, braid or expanded metal.

32 . The process as claimed in claim 22 , wherein the support element consists of carbon fibers, nickel, silver or nickel coated with noble metal.

33 . A gas diffusion electrode for the reduction of oxygen, where the gas diffusion electrode has at least one sheet-like electrically conductive support element and a gas diffusion layer and electrocatalyst applied to the support element, wherein the gas diffusion layer consists of a mixture of carbon nanotubes and PTFE, with the carbon nanotubes and fluoropolymer having been applied in powder form to the support element and compacted and the carbon nanotubes forming the electrocatalyst.

34 . The gas diffusion electrode as claimed in claim 33 , wherein the electrode has been produced by a process as claimed in claim 22 .

35 . The gas diffusion electrode as claimed in claim 33 , wherein the mixture of carbon nanotubes and PTFE, contains from 1 to 70% of PTFE and 99-30% of carbon nanotubes.

36 . The gas diffusion electrode as claimed in claim 33 , wherein the electrode has a thickness of from 0.1 to 3 mm.

37 . The gas diffusion electrode as claimed in claim 33 , wherein the gas diffusion layer has been applied on one or both sides to the surfaces of the support element.

38 . The gas diffusion electrode as claimed in claim 33 , wherein the carbon nanotubes have a content of catalyst residues of the catalyst used for producing the carbon nanotubes of less than 1% by weight.

39 . The gas diffusion electrode as claimed in claim 33 , wherein the carbon nanotube powder is present as agglomerate, with at least 95% by weight of the agglomerate particles having an external diameter in the range from 30 μm to 5000 μm.

40 . The gas diffusion electrode as claimed in claim 33 , wherein the proportion of nitrogen in the form of nitrogen chemically bound to the carbon nanotubes is less than 0.5% by weight.

41 . A method comprising utilizing the gas diffusion electrode as claimed in claim 33 as oxygen-depolarized electrode for the reduction of oxygen in an alkaline medium or as electrode in an alkaline fuel cell or as electrode in a metal/air battery.

42 . An electrolysis apparatus comprising a gas diffusion electrode as claimed in claim 33 as oxygen-depolarized cathode.

Assignees

• Covestro Deutschland Ag

Inventors

• Bulan Andreas
• Kintrup Jürgen

Classifications

• H01M8/0234

  Carbonaceous material · CPC title

• H01M12/06

  with one metallic and one gaseous electrode · CPC title

• C02F2001/46166

  Gas diffusion electrodes · CPC title

• H01M8/083

  Alkaline fuel cells · CPC title

• C25B1/46 Primary

  in diaphragm cells · CPC title