Apparatus for the generation, transmission, distribution and/or the usage of electrical energy, in particular electrical switching device

Patent metadata

Field	Value
Publication number	US-10566159-B2
Application number	US-201816154767-A
Country	US
Kind code	B2
Filing date	Oct 9, 2018
Priority date	Apr 6, 2016
Publication date	Feb 18, 2020
Grant date	Feb 18, 2020

Abstract

The present application relates to an apparatus for the generation, transmission, distribution and/or usage of electrical energy, the apparatus including a housing enclosing an insulation space and an electrically conductive part arranged in the insulation space, wherein the insulating space contains a dielectric fluid including carbon dioxide and oxygen. In the apparatus an oxidation catalyst is arranged that includes noble metal particles coated onto or embedded into a carrier and serves for the catalytic oxidation of carbon monoxide to carbon dioxide.

First claim

The invention claimed is:

1. An apparatus for generation, transmission, distribution and/or the usage of electrical energy, said apparatus comprising:
a housing enclosing an insulation space and an electrically conductive part arranged in the insulation space, wherein said insulating space contains a dielectric fluid comprising carbon dioxide and oxygen, in the apparatus an oxidation catalyst is arranged, a ratio of a molar fraction of carbon dioxide to a molar fraction of oxygen ranges from 50:50 to 100:1 to prevent soot formation during arcing, and the oxidation catalyst is arranged inside the insulation space of the apparatus, further the apparatus being a switching device comprising at least one switching chamber, which comprises at least two arcing contacts movable in relation to each other and defining an arcing region, in which an arc is formed during a current breaking operation, the switching chamber further comprising an exhaust volume, which is fluidly connected to the arcing region to allow the dielectric fluid heated by the arc to flow out of the arcing region in direction towards the exhaust volume,
wherein the oxidation catalyst comprises noble metal particles that are coated onto or are embedded into a carrier and are for a catalytic oxidation of carbon monoxide to carbon dioxide, and the oxidation catalyst is arranged in a high-temperature area of the switching device, said high-temperature area being located, in direction of an outflow of the heated dielectric fluid, between the arcing region and the exhaust volume,
wherein the oxidation catalyst is arranged in the high-temperature area of the apparatus, said high temperature area being designed to maintain a temperature below 500° C. over a duration of an oxidation reaction.

2. The apparatus according to claim 1 , wherein the ratio of the molar fraction of carbon dioxide to the molar fraction of oxygen ranges from 80:20 to 95:5.

3. The apparatus according to claim 1 , wherein the noble metal particles are made of at least one metal selected from a group consisting of: Au, Ru, Rh, Pd, Os, Ir, Pt and mixtures thereof.

4. The apparatus according to claim 1 , wherein the oxidation catalyst is a platinum-group-member catalyst comprising particles of a platinum group member coated onto a ceramic or metal carrier.

5. The apparatus according to claim 1 , wherein the oxidation catalyst is arranged in the high-temperature area of the apparatus, said high-temperature area being designed to maintain a temperature of above 250° C. over the duration of the oxidation reaction.

6. The apparatus according to claim 1 , wherein the oxidation catalyst further comprises a heater designed to generate a temperature of at least 250° C.

7. The apparatus according to claim 1 , wherein the oxidation catalyst is arranged in an intermediate chamber delimited by an intermediate chamber wall and being located, in direction of the outflow of the heated dielectric fluid, between the arcing region and the exhaust volume.

8. The apparatus according to claim 1 , wherein the oxidation catalyst is a gold catalyst comprising gold particles calcinated on a metal oxide carrier.

9. The apparatus according to claim 8 , wherein the gold particles have an average diameter of at most 10 nm at most.

10. The apparatus according to claim 8 , wherein the gold catalyst further comprises a partly reducible oxide, in particular ceria or a transition metal oxide.

11. The apparatus according to claim 1 , which further includes a desiccant contained in the insulation space; and/or that the dielectric fluid comprises one compound selected from a group consisting of: SF 6 , an organofluorine compound, and mixtures thereof.

12. The apparatus according to claim 11 , wherein the organofluorine compound selected from a group consisting of: fluoroethers, fluoroketones perfluoroketones, fluoroolefins, fluoronitriles, and mixtures thereof.

13. The apparatus according to claim 1 , wherein the oxidation catalyst is part of a catalyst system, which apart from the oxidation catalyst further comprises a fan designed to create a flow of the dielectric fluid through the oxidation catalyst.

14. The apparatus according to claim 1 , further comprising a circuit breaker.

15. The apparatus according to claim 1 , wherein the oxidation catalyst is arranged in a manner to allow a direct contact with the insulation fluid contained in the insulation space.

16. The apparatus according to claim 1 , wherein the apparatus is devoid of a reaction vessel separate from the insulation space and designed for the oxidation from carbon monoxide to carbon dioxide to take place.

17. The apparatus according to claim 1 , wherein the oxidation catalyst comprises gold particles calcinated on a carrier based on CeO 2 doped with Fe atoms.

18. The apparatus according to claim 1 , wherein the oxidation catalyst is devoid of an oxidizing agent layer containing Mn, Co, Ni, Cu, Zn, Ti, Fe, V or Cr.

19. The apparatus according to claim 1 , wherein the ratio of the molar fraction of carbon dioxide to the molar fraction of oxygen ranges from 87:13 to less than 90:10.

20. The apparatus of claim 1 , wherein the oxidation catalyst is a gold catalyst comprising gold particles calcinated on a metal oxide carrier defined by an aluminium oxide or an iron oxide carrier.

21. The apparatus according to claim 1 , wherein the dielectric fluid comprises an organofluorine compound.

22. An apparatus for the generation, transmission, distribution and/or usage of electrical energy, said apparatus comprising:
a housing enclosing an insulation space and an electrically conductive part arranged in the insulation space, wherein said insulating space contains a dielectric fluid comprising carbon dioxide and oxygen, in the apparatus an oxidation catalyst is arranged, a ratio of a molar fraction of carbon dioxide to a molar fraction of oxygen ranges from 50:50 to 100:1 to prevent soot formation during arcing, and the oxidation catalyst is arranged inside the insulation space of the apparatus, further the apparatus being a switching device comprising at least one switching chamber, which comprises at least two arcing contacts movable in relation to each other and defining an arcing region, in which an arc is formed during a current breaking operation, the switching chamber further comprising an exhaust volume, which is fluidly connected to the arcing region to allow the dielectric fluid heated by the arc to flow out of the arcing region in direction towards the exhaust volume,
wherein the oxidation catalyst comprises noble metal particles that are coated onto or are embedded into a carrier and are for a catalytic oxidation of carbon monoxide to carbon dioxide, and the oxidation catalyst is arranged in a high-temperature area of the switching device, said high-temperature area being located, in direction of an outflow of the heated dielectric fluid, between the arcing region and the exhaust volume,
and
wherein the oxidation catalyst further comprises a heater designed to generate a temperature of below 500° C.

Assignees

• Abb Schweiz Ag

Inventors

• Mantilla Javier
• Claessens Max
• Anderson Ryan-Gerald

Classifications

• B01J2523/00

  Constitutive chemical elements of heterogeneous catalysts · CPC title

• B01J23/63

  with rare earths or actinides · CPC title

• B01J23/38

  of noble metals · CPC title

• H01H2033/566

  Avoiding the use of SF6 · CPC title

• H01H33/7076 Primary

  characterised by the use of special materials (H01H33/7023 - H01H33/7069 take precedence) · CPC title