Catalyst and system for methane steam reforming by resistance heating; said catalyst's preparation

Patent metadata

Field	Value
Publication number	US-2021121857-A1
Application number	US-201917059901-A
Country	US
Kind code	A1
Filing date	May 15, 2019
Priority date	May 31, 2018
Publication date	Apr 29, 2021
Grant date	—

Abstract

The invention relates to a structured catalyst for catalyzing steam methane reforming reaction in a given temperature range T upon bringing a hydrocarbon feed gas into contact with the structured catalyst. The structured catalyst comprises a macroscopic structure, which comprises an electrically conductive material and supports a ceramic coating. The macroscopic structure has been manufactured by 3D printing or extrusion and subsequent sintering, wherein the macroscopic structure and the ceramic coating have been sintered in an oxidizing atmosphere in order to form chemical bonds between the ceramic coating and the macroscopic structure. The ceramic coating supports catalytically active material arranged to catalyze the steam methane reforming reaction, wherein the macroscopic structure is arranged to conduct an electrical current to supply an energy flux to the steam methane reforming reaction. The invention moreover relates to methods of manufacturing the structured catalyst and a system using the structured catalyst.

First claim

1 . A structured catalyst for catalyzing steam methane reforming reaction in a given temperature range T upon bringing a hydrocarbon feed gas into contact with said structured catalyst, said structured catalyst comprising a macroscopic structure, said macroscopic structure comprising an electrically conductive material, said macroscopic structure having a resistivity between 10 −5 Ω-m and 10 −7 Ω-m in the given temperature range T, and said macroscopic structure supporting a ceramic coating, wherein the macroscopic structure has been manufactured by extrusion or 3D printing and by subsequent sintering, wherein said macroscopic structure and said ceramic coating have been sintered in an oxidizing atmosphere in order to form chemical bonds between said ceramic coating and said macroscopic structure, wherein said ceramic coating supports catalytically active material, said catalytically active material being arranged to catalyze the steam methane reforming reaction, wherein the macroscopic structure is arranged to conduct an electrical current to supply an energy flux to the steam methane reforming reaction.

2 . (canceled)

3 . A structured catalyst according to claim 1 , wherein the macroscopic structure comprises a plurality of near-parallel or parallel channels.

4 - 6 . (canceled)

7 . A structured catalyst according to claim 1 , wherein the catalytically active material are sub-micron sized particles.

8 . A structured catalyst according to claim 1 , wherein the macroscopic structure has at least one electrically insulating part arranged to increase the principal current path within the macroscopic structure, having a length larger than the largest dimension of the macroscopic structure, and. wherein the structured catalyst is configured for use in a system for carrying out a steam methane reforming reaction, in which system the hydrocarbon feed gas enters into the structured catalyst at a first end and a product gas exits the structured catalyst at a second end, said structured catalyst further being configured to have at least two conductors connected to the structured catalyst at a position closer to said first end than to said second end, wherein said structured catalyst is constructed to, during use, direct an electrical current to run from one conductor substantially to said second end along a longitudinal direction of the structured catalyst and return to a second of the at least two conductors along a longitudinal direction of the structured catalyst, wherein the longitudinal direction extends between the first and second ends.

9 . A structured catalyst according to claim 1 , wherein the resistance and geometry of the material of the macroscopic structure is configured to have a heat generation capacity of 500 to 50000 W/m 2 .

10 . (canceled)

11 . A structured catalyst according to claim 1 , wherein the structured catalyst comprises two or more macroscopic structures.

12 . A method for manufacturing a structured catalyst according to claim 1 , said method comprising the steps of:
a) providing a mixture of powdered metallic particles and a binder, b) extruding said mixture to a structure, c) sintering said structure in a non-oxidizing atmosphere at a first temperature T 1 , where T 1 >1000° C., thereby providing a macroscopic structure, d) providing a ceramic coating onto the macroscopic structure, e) sintering the macroscopic structure and the ceramic coating in an oxidizing atmosphere, at a second temperature T 2 , where T 2 >800° C., in order to form chemical bonds between said ceramic coating and said macroscopic structure, and f) impregnating the ceramic coating with catalytically active material.

13 . A method for manufacturing a structured catalyst according to claim 1 , said method comprising the steps of:
a) providing a mixture of powdered metallic particles and a binder, b) extruding said mixture to a structure, c) sintering said structure in a non-oxidizing atmosphere at a first temperature T 1 , where T 1 >1000° C., thereby providing a macroscopic structure, d) providing a ceramic coating onto the macroscopic structure, wherein the ceramic coating supports catalytically active material, and e) sintering the macroscopic structure and the ceramic coating in an oxidizing atmosphere, at a second temperature T 2 , where T 2 >800° C., in order to form chemical bonds between said ceramic coating and said macroscopic structure.

14 . A method for manufacturing a structured catalyst according to claim 1 , said method comprising the steps of:
a) 3D printing the macroscopic structure with a metal additive manufacturing melting process, b) applying a ceramic coating onto the macroscopic structure, c) sintering the macroscopic structure and the ceramic coating in an oxidizing atmosphere, at a second temperature T 2 , where T 2 >800° C., and d) impregnating the ceramic coating with catalytically active material, thereby providing the structured catalyst.

15 . A method for manufacturing a structured catalyst according to claim 1 , said method comprising the steps of:
a) 3D printing a metal structure with a binder-based metal additive manufacturing process, b) sintering said metal structure in a non-oxidizing atmosphere at a first temperature T 1 , where T 1 >1000° C., thereby providing said macroscopic structure, c) applying a ceramic coating onto the macroscopic structure, d) sintering the macroscopic structure and the ceramic coating in an oxidizing atmosphere, at a second temperature T 2 , where T 2 >800° C., and e) impregnating the ceramic coating with catalytically active material, thereby providing the structured catalyst.

16 . A system for carrying out a steam methane reforming reaction in a given temperature range T between about 200° C. and about 1050° C. or a sub-range thereof upon bringing a hydrocarbon feed gas into contact with a structured catalyst according to claim 1 , said system comprising:
a reactor unit comprising said structured catalyst and at least two conductors electrically connected to said structured catalyst, and
an electrical power supply arranged for being connected to said structured catalyst via the at least two conductors in order to allow an electrical current to run through said structured catalyst during operation of said system.

17 . (canceled)

18 . A system according to claim 16 , wherein the connection between the macroscopic structures of said structured catalyst and said at least two conductors is a mechanical connection, a welded connection, a brazed connection, or a combination of said connections.

19 . (canceled)

20 . A system according to claim 16 , wherein the system comprises a control system arranged to control one or more of the following: the electrical current, the voltage, the heat flux, the space velocity, the temperature, or combinations thereof.

21 . A system according to claim 16 , wherein the hydrocarbon feed gas enters into the structured catalyst at a first end and wherein a product gas exits the structured catalyst at a second end, wherein said at least two conductors are connected to the structured catalyst at a position closer to said first end than to said second end.

22 - 23 . (canceled)

24 . A system according to claim 21 , wherein said structured catalyst is constructed to direct an electrical current to run from one conductor substantially to said second end of the structured catalyst and return to a second of the at least two conductors.

25 . A system according to

Assignees

• Haldor Topsoe As
• Grundfos Holding As

Inventors

• Mortensen Peter Mølgaard
• Bendixen Flemming Buus
• Valler Peter
• Sorea Alexandru

Classifications

• B01J35/45

  Nanoparticles · CPC title

• B01J35/40

  characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title

• B01J35/50

  characterised by their shape or configuration · CPC title

• B01J35/56

  Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths · CPC title

• Y02P10/25

  Process efficiency · CPC title