Structural catalyst with internal heat transfer system for exothermic and endothermic reactions

Patent metadata

Field	Value
Publication number	US-10737236-B2
Application number	US-201615777732-A
Country	US
Kind code	B2
Filing date	Nov 18, 2016
Priority date	Nov 23, 2015
Publication date	Aug 11, 2020
Grant date	Aug 11, 2020

Abstract

A reactor for efficient control of endothermic and exothermic catalytic reactions, including, for example, Fischer Tropsch reactions. Also disclosed are methods of delivering coolant materials and gasification source materials to the reactor.

First claim

What is claimed is:

1. A reactor having a longitudinal axis, the reactor comprising:
a housing having an outer wall, the outer wall defining at least one gas inlet and at least one coolant inlet;
a frame positioned within the housing, the frame having a longitudinal length and comprising a plurality of interior surfaces and a plurality of exterior surfaces, wherein the plurality of interior surfaces cooperate to define a plurality of interconnected coolant channels within the frame, wherein the plurality of exterior surfaces define a plurality of isolated conduits, each conduit of the plurality of isolated conduits having a respective longitudinal axis that is substantially parallel to the longitudinal axis of the reactor, wherein at least a portion of the at least one exterior surface that defines each respective conduit is coated with at least one catalyst material to position the at least one catalyst material within the conduit,
wherein the plurality of interconnected coolant channels are positioned in fluid communication with the at least one coolant inlet,
wherein the plurality of conduits are positioned in fluid communication with the at least one gas inlet,
wherein within a cross-sectional plane that is perpendicular to the longitudinal axis of the reactor, each coolant channel of the plurality of interconnected coolant channels is fluidly connected with each of the other coolant channels of the plurality of coolant channels,
wherein, within the cross-sectional plane, each respective isolated conduit of the plurality of isolated conduits is defined between intersecting and fluidly connected portions of at least two coolant channels of the plurality of interconnected coolant channels,
wherein, within the cross-sectional plane, at least one isolated conduit of the plurality of isolated conduits is cooperatively defined by the outer wall of the housing and exterior surfaces of the frame, and
wherein the plurality of isolated conduits and the plurality of interconnected coolant channels extend the length of the frame.

2. The reactor of claim 1 , wherein the plurality of interconnected coolant channels of the frame comprise a first plurality of coolant channels and a second plurality of coolant channels, wherein within the cross-sectional plane, the second plurality of coolant channels are oriented substantially perpendicularly to the first plurality of coolant channels to thereby create a grid of coolant channels.

3. The reactor of claim 1 , wherein the plurality of conduits have a substantially rectangular cross-sectional shape.

4. The reactor of claim 1 , wherein the plurality of conduits have a substantially square cross-sectional shape.

5. The reactor of claim 1 , wherein the plurality of conduits have a rounded cross-sectional shape.

6. The reactor of claim 1 , wherein the plurality of interconnected coolant channels of the frame comprise a first plurality of coolant channels and a second plurality of coolant channels, wherein within the cross-sectional plane:
the first plurality of coolant channels have longitudinal axes that extend substantially perpendicularly to the longitudinal axes of the plurality of conduits; and
each coolant channel of the second plurality of coolant channels has a variable profile that extends and is angled relative to the longitudinal axes of the first plurality of coolant channels.

7. The reactor of claim 6 , wherein the variable profile of each coolant channel of the second plurality of coolant channels corresponds to a substantially serpentine pattern extending between and in fluid communication with adjacent coolant channels of the first plurality of coolant channels.

8. The reactor of claim 1 , wherein the reactor has a substantially rectangular cross-sectional shape.

9. The reactor of claim 1 , wherein the reactor has a substantially rounded cross-sectional shape.

10. The reactor of claim 1 , wherein the at least one catalyst material has a thickness ranging from about 10 μm to about 10,000 μm.

11. The reactor of claim 10 , wherein the at least one catalyst material has a thickness ranging from about 40 μm to about 1,000 μm.

12. The reactor of claim 2 , wherein the frame has a diameter, wherein within the cross-sectional plane, each coolant channel of the first plurality of coolant channels extends continuously across the diameter of the frame.

13. The reactor of claim 12 , wherein within the cross-sectional plane, each coolant channel of the first plurality of coolant channels has a respective longitudinal axis extending continuously across the diameter of the frame.

14. The reactor of claim 1 , wherein the at least one gas inlet comprises a first gas inlet, wherein the at least one coolant inlet comprises a first coolant inlet, wherein the first gas inlet and the first coolant inlet are positioned at opposing ends of the housing relative to the longitudinal axis, and wherein the plurality of isolated conduits and the plurality of interconnected coolant channels extend a length of the housing between the first gas inlet and the first coolant inlet.

15. A method comprising:
delivering at least one coolant material to at least one coolant inlet of a reactor, the reactor having a longitudinal axis and comprising:
a housing having an outer wall, the outer wall defining at least one gas inlet and the at least one coolant inlet;
a frame positioned within the housing, the frame having a longitudinal length and comprising a plurality of interior surfaces and a plurality of exterior surfaces, wherein the plurality of interior surfaces cooperate to define a plurality of interconnected coolant channels within the frame, wherein the plurality of exterior surfaces define a plurality of isolated conduits, each conduit of the plurality of isolated conduits having a respective longitudinal axis that is substantially parallel to the longitudinal axis of the reactor, wherein at least a portion of the at least one exterior surface that defines each respective conduit is coated with at least one catalyst material to position the at least one catalyst material within the conduit,
wherein the plurality of interconnected coolant channels are positioned in fluid communication with the at least one coolant inlet,
wherein the plurality of conduits are positioned in fluid communication with the at least one gas inlet,
wherein within a cross-sectional plane that is perpendicular to the longitudinal axis of the reactor, each coolant channel of the plurality of interconnected coolant channels is fluidly connected with each of the other coolant channels of the plurality of coolant channels,
wherein, within the cross-sectional plane, each respective isolated conduit of the plurality of isolated conduits is defined between intersecting and fluidly connected portions of at least two coolant channels of the plurality of interconnected coolant channels,
wherein, within the cross-sectional plane, at least one isolated conduit of the plurality of isolated conduits is cooperatively defined by the outer wall of the housing and exterior surfaces of the frame, and
wherein the plurality of isolated conduits and the plurality of interconnected coolant channels extend the length of the frame; and

delivering at least one gasification source material to the at least one gas inlet of the reactor.

16. The method of claim 15 , wherein the gasification source material is selected from the group consisting of natural gas, biomass, and coal.

17. The method of claim 15 , wherein the chemical reaction produces gaseous hydrocarbons selected from the group consisting of a low

Assignees

• Sabic Global Technologies Bv

Inventors

• Nawaz Zeeshan
• Karim Khalid

Classifications

• B01J2219/2411

  The reactant being in indirect heat exchange with a non reacting heat exchange medium · CPC title

• B01J19/0013

  Controlling the temperature of the process · CPC title

• B01J2219/2428

  Catalysts coated on the surface of the monolith channels · CPC title

• B01J2219/2479

  Catalysts coated on the surface of plates or inserts · CPC title

• B01J19/2485 Primary

  Monolithic reactors · CPC title