Catalytic plate reactors

Patent metadata

Field	Value
Publication number	US-9682357-B2
Application number	US-201314427597-A
Country	US
Kind code	B2
Filing date	Aug 12, 2013
Priority date	Sep 17, 2012
Publication date	Jun 20, 2017
Grant date	Jun 20, 2017

Abstract

A method of controlling the temperature of autothermal microchannel reactors is disclosed. A hierarchical control structure employs a distributed temperature controller including a phase change material and a supervisory control system including the control of one or more inputs into the reactor. The phase change material acts as a fast, distributed controller, and the supervisory controller acts over a longer time horizon to mitigate persistent disturbances. A stochastic optimization method for selecting the phase change layer thickness is employed.

First claim

What is claimed is:

1. An apparatus for processing a first substance, the apparatus comprising:
a first enclosed channel configured to transport the first substance;
a second enclosed channel configured to transport a second substance; and
a solid phase change layer disposed between, and thermally coupled to, the first enclosed channel and the second enclosed channel; wherein the solid phase change layer can transfer thermal energy from the second enclosed channel to the first enclosed channel;
wherein the first enclosed channel further comprises a first catalyst configured to promote the chemical transformation of the first substance; and the second enclosed channel further comprises a second catalyst configured to promote the chemical transformation of the second substance.

2. The apparatus of claim 1 , wherein the chemical transformation of the first substance is endothermic; and the chemical transformation of the second substance is exothermic.

3. The apparatus of claim 2 wherein the phase change layer is configured to change from a solid to a liquid when the exothermic transformation generates more energy than the endothermic transformation requires.

4. The apparatus of claim 2 wherein energy from the exothermic transformation in the second enclosed channel is conducted to the first enclosed channel and is sufficient to enable the endothermic transformation.

5. The apparatus of claim 1 wherein the phase change layer is configured to have a melting temperature above a normal/nominal operating temperature of the apparatus.

6. The apparatus of claim 1 wherein the phase change layer comprises copper.

7. The apparatus of claim 1 wherein the first substance comprises methane and water and the first catalyst comprises platinum.

8. The apparatus of claim 1 wherein the second substance comprises methane and oxygen or methane and air and the second catalyst comprises nickel.

9. The apparatus of claim 1 wherein the first enclosed channel is approximately parallel with the second enclosed channel.

10. The apparatus of claim 1 , wherein the solid phase change layer comprises a metal alloy.

11. A catalytic reactor comprising:
a set of enclosed reforming channels and a set of enclosed combustion channels separated by a solid phase change layer; wherein the solid phase change layer can transfer thermal energy from the combustion channels to the reforming channels;
a reforming catalyst layer disposed in the enclosed reforming channels; and
a combustion catalyst layer disposed in the enclosed combustion channels.

12. The catalytic reactor of claim 11 wherein the reactor is configured to operate in co-current flow mode.

13. The catalytic reactor of claim 11 wherein the reactor is configured to operate in counter-current flow mode.

14. The catalytic reactor of claim 11 wherein the phase change layer has a thermal conductivity greater than 100 W/mK.

15. The catalytic reactor of claim 11 wherein the enclosed reforming channels are configured to catalyze a methane steam reforming reaction and the enclosed combustion channels are configured to catalyze a methane combustion reaction.

16. The catalytic reactor of claim 11 wherein the reforming and/or combustion channels are configured to receive methane derived from a natural gas source.

17. The catalytic reactor of claim 11 , wherein the solid phase change layer comprises a metal alloy.

18. A method of operating a reactor, wherein the reactor comprises:
(i) a first enclosed channel which comprises a reforming catalyst disposed therein;
(ii) a second enclosed channel which comprises a combustion catalyst disposed therein; and
(iii) a solid phase change layer;
wherein the first enclosed channel and second enclosed channel are separated by and in thermal contact with the solid phase change layer;

wherein the method comprises:
(a) flowing a first substance in the first enclosed channel, thereby reacting the first substance on the reforming catalyst disposed in the first enclosed channel; and
(b) flowing a second substance in the second enclosed channel, thereby reacting the second substance on the combustion catalyst disposed in the second enclosed channel;
wherein thermal energy transfers from the second enclosed channel, through the phase change layer, to the first enclosed channel.

19. The method of claim 18 wherein the reforming catalyst supports the endothermic reaction of the first substance; and the combustion catalyst supports the exothermic reaction of the second substance.

20. The method of claim 19 wherein the phase change layer is configured to change from a solid to a liquid when the exothermic reaction generates more energy than the endothermic reaction requires.

21. The method of claim 18 wherein the phase change layer is configured to have a melting temperature above a normal operating temperature of the reactor.

Assignees

• Univ Texas

Inventors

• Baldea Michael
• Pattison Richard Chase

Classifications

• Y02E60/145

  Cross-Sectional Technologies · mapped topic

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• B01J2219/00961

  Temperature · CPC title

• B01J2219/0086

  Dimensions of the flow channels · CPC title

• B01J2219/00995

  Mathematical modeling · CPC title