Alternating fixed and fluidized bed reactor systems and processes

Patent metadata

Field	Value
Publication number	US-12404171-B2
Application number	US-202217683964-A
Country	US
Kind code	B2
Filing date	Mar 1, 2022
Priority date	Mar 1, 2022
Publication date	Sep 2, 2025
Grant date	Sep 2, 2025

Abstract

The present disclosure refers to systems and methods for producing hydrogen among other products. In some embodiments the methods comprise sequentially conducting a cracking step in a fixed bed mode and conducting a flowing step in a fluidized bed mode. Such sequential processes may result in a number of advantages including, for example, regenerating the catalyst during the fluidized bed mode in a manner such that beneficial heat is generated for use in the endothermic cracking step.

First claim

We claim:

1. A process for producing hydrogen and solid carbon comprising:
cracking a light hydrocarbon stream in a reactor in the presence of a catalyst under conditions suitable to produce at least (1) hydrogen and (2) a carbon byproduct deposited on a surface of the catalyst, wherein the light hydrocarbon stream is flowing downward and wherein the reactor is in a fixed bed reactor mode;
flowing a light hydrocarbon gas, a superheated steam, an inert gas, or a mixture thereof upward through the reactor wherein the reactor is in a fluidized reactor mode and wherein the conditions are suitable to detach at least a portion up to all of the deposited carbon byproduct from the surface of the catalyst; and
regenerating the catalyst by reacting an oxidant with the carbon byproduct;
wherein the process further comprises employing at least a portion of the heat from regenerating to the cracking.

2. The process of claim 1 wherein the steps are carried out sequentially.

3. The process of claim 1 wherein the conditions suitable to detach at least a portion up to all of the deposited carbon byproduct from the surface of the catalyst comprise a superficial velocity of from about 0.05 to about 5 meters per second.

4. The process of claim 1 which further comprises employing a second reactor operating in parallel with the first reactor.

5. The process of claim 4 wherein the first reactor operates in a production mode while the second reactor operates in a regeneration mode.

6. The process of claim 4 wherein the first reactor operates in a regeneration mode while the second reactor operates in a production mode.

7. The process of claim 1 which further comprises employing a second reactor and a third reactor wherein each reactor is operating in parallel with the first reactor and wherein at least one of the first, second, and third reactors operates in a regeneration mode while at least one of the remaining first, second, and third reactors operates in a production mode.

8. The process of claim 1 wherein the inert gas is nitrogen.

9. The process of claim 1 wherein the reactor alternates between fixed bed reactor mode and fluidized reactor mode.

10. The process of claim 1 which further comprises separating hydrogen from unreacted light hydrocarbon gas, superheated steam, inert gas, or any mixture thereof.

11. The process of claim 1 which further comprises:
separating hydrogen during the cracking step;
separating detached carbon byproduct during the flowing step; and
separating or capturing at least a portion up to substantially all of any carbon dioxide formed in the regenerating step.

12. The process of claim 7 which further comprises recycling unreacted light hydrocarbon gas, superheated steam, inert gas, or any mixture thereof to an inlet of the reactor.

13. The process of claim 1 which further comprises capturing at least a portion of any carbon dioxide produced.

14. The process of claim 12 further comprising operating a second reactor in parallel with the first reactor wherein the second reactor conducts a cracking step in a fixed bed mode while the first reactor conducts the flowing step.

15. The reactor system of claim 13 further comprising a second reactor operably connected in parallel.

16. The reactor system of claim 13 wherein the reactor vessel comprises a gas disengagement zone.

17. The reactor system of claim 14 wherein the gas disengagement zone comprises a vessel diameter configured to separate gas and solids, reduce catalyst, or both while the reactor vessel is fluidized.

18. The reactor vessel of claim 13 further comprises a separator configured to separate hydrogen from light hydrocarbon, natural gas, or both.

19. The reactor system of claim 13 further comprising a heat exchanger.

20. The reactor system of claim 13 further comprising a second reactor and a third reactor operably connected in parallel.

21. A process for producing hydrogen and solid carbon comprising:
cracking a light hydrocarbon stream in a reactor in the presence of a catalyst under conditions suitable to produce at least (1) hydrogen and (2) a carbon byproduct deposited on a surface of the catalyst, wherein the light hydrocarbon stream is flowing downward and wherein the reactor is in a fixed bed reactor mode;
flowing a light hydrocarbon gas, a superheated steam, an inert gas, or a mixture thereof upward through the reactor wherein the reactor is in a fluidized reactor mode and wherein the conditions are suitable to detach at least a portion up to all of the deposited carbon byproduct from the surface of the catalyst; and
regenerating the catalyst by reacting an oxidant with the carbon byproduct;

wherein the process further comprises pre-treating unreacted light hydrocarbon gas to remove a substantial portion of catalyst poisoning impurities.

22. The process of claim 21 which further comprises employing at least a portion of the heat from regenerating for cracking the light hydrocarbon.

23. A process for producing hydrogen comprising:
(1) sequentially conducting a cracking step in a fixed bed mode and conducting a flowing step in a fluidized bed mode in a first reactor;
wherein the cracking step comprises cracking a light hydrocarbon stream comprising methane in a reactor in the presence of a catalyst under conditions suitable to produce at least (1) hydrogen and (2) a carbon byproduct deposited on a surface of the catalyst, wherein the light hydrocarbon stream comprising methane is flowing downward and wherein the reactor is in a fixed bed reactor mode;
wherein the flowing step comprises flowing a light hydrocarbon gas comprising methane, a superheated steam, an inert gas, or a mixture thereof upward through the reactor wherein the reactor is in a fluidized reactor mode and wherein the superficial velocity of the flowing is sufficient to detach at least a portion up to all of the deposited carbon byproduct from the surface of the catalyst;
and
(2) regenerating the catalyst during the flowing step by reacting an oxidant with the carbon byproduct such that heat is generated for use in the cracking step.

24. A reactor system comprising:
a reactor vessel comprising light hydrocarbon catalyst in a fixed bed configuration;
wherein said reactor vessel is configured to receive light hydrocarbon feed flowing downward to produce hydrogen while allowing carbon byproduct to be deposited on catalyst surface;
wherein said reactor vessel is configured to receive a light hydrocarbon gas, a superheated steam, or an inert gas flowing upward to fluidize the light hydrocarbon catalyst and thereafter receive an oxidizing agent to remove deposited carbon byproduct;
wherein the reactor system is configured to sequentially alternate between a fixed bed reactor mode and a fluidized bed reactor mode.

Assignees

• Chevron Usa Inc

Inventors

• Luo Huping
• Li Lin
• Kuperman Alexander
• Ouyang Xiaoying

Classifications

• C01B3/28 Primary

  using moving solid particles, e.g. fluidised bed technique · CPC title

• B01J19/2445

  placed in parallel · CPC title

• C01B2203/1011

  Packed bed of catalytic structures, e.g. particles, packing elements · CPC title

• C01B2203/1241

  Natural gas or methane · CPC title

• B01J38/72

  including segregation of diverse particles · CPC title