Regeneration and activation of catalysts for carbon and syngas production
A method to regenerate and reactivate catalysts used for a carbon and syngas production reaction including a DRM or CARGEN reaction is developed. Carbon dioxide (CO 2 ) is used as the regeneration and activation media. This method of a single step regeneration and activation using CO 2 is more effective than the existing conventional two-step process that includes separate reduction and oxidation steps. This method produces pure carbon monoxide (CO) as a byproduct from the regeneration process by utilizing CO 2 and carbon.
1. A method of regenerating or reactivating a catalyst used in a reforming reaction, the method comprising:
providing the catalyst in a reactor, wherein the catalyst was used in a carbon and syngas production reaction;
providing a first oxidizing gas comprising CO 2 to the reactor for regeneration or reactivation of the catalyst; and
providing to the reactor a second oxidizing gas comprising CO 2 and O 2 for the regeneration or reactivation of the catalyst,
wherein the catalyst is not further reduced for the regeneration or reactivation of the catalyst.
2. The method of claim 1 , wherein the carbon and syngas production reaction is a Dry Reforming of Methane reaction or a CARGEN reaction, and the catalyst comprises solid carbon produced from the Dry Reforming of Methane reaction or the CARGEN reaction.
3. The method of claim 1 , wherein the catalyst comprises nickel as an active metal.
4. The method of claim 1 , wherein the catalyst is deactivated from the carbon and syngas production reaction or has an activity less than that before being used in the carbon and syngas production.
5. The method of claim 1 further comprising producing pure CO from the regeneration or reactivation of the catalyst.
6. The method of claim 1 , wherein the regeneration or reactivation of the catalyst is conducted at a temperature from about 650° C. to about 900° C.
7. The method of claim 5 , wherein the regeneration or reactivation of the catalyst has a duration from about 10 minutes to about 4 hours or until the CO generation diminishes to zero while regeneration or reactivation.
8. A process comprising:
providing a first catalyst in a first reactor for a first carbon and syngas production reaction;
providing a first mixed gas comprising CH 4 and CO 2 in the first reactor for the first carbon and syngas production reaction;
allowing a first reacted gas from the first carbon and syngas production reaction to leave the first reactor; and
providing a first oxidizing gas comprising CO 2 to the first reactor for a first regeneration or reactivation of the first catalyst,
wherein the first catalyst is not further reduced for the first regeneration or reactivation of the first catalyst.
9. The process of claim 8 , wherein the first carbon and syngas production reaction is a first Dry Reforming of Methane reaction or a first CARGEN reaction.
10. The process of claim 8 , further comprising:
providing a second catalyst in a second reactor for a second carbon and syngas production reaction;
providing a second mixed gas comprising CH 4 and CO 2 in the second reactor for the second carbon and syngas production reaction;
allowing a second reacted gas from the second carbon and syngas production reaction to leave the second reactor; and
providing a second oxidizing gas comprising CO 2 to the second reactor for a second regeneration or reactivation of the first catalyst,
wherein the second catalyst is not further reduced for the second regeneration or reactivation of the second catalyst.
11. The process of claim 10 , wherein the second carbon and syngas production reaction is a second Dry Reforming of Methane reaction or a second CARGEN reaction.
12. The process of claim 8 , wherein the first catalyst comprises nickel as an active metal.
13. The method of claim 8 further comprising providing to the first reactor a first additional oxidizing gas comprising CO 2 and O 2 for the first regeneration or reactivation of the first catalyst.
14. The process of claim 8 further comprising producing pure CO from the first regeneration or reactivation of the first catalyst.
15. The process of claim 10 , wherein the second catalyst comprises nickel as an active metal.
16. The process of claim 10 , wherein the second oxidizing gas further comprises O 2 .
17. The method of claim 10 further comprising providing to the second reactor a second additional oxidizing gas comprising CO 2 and O 2 for the second regeneration or reactivation of the second catalyst.
18. The process of claim 10 further comprising producing pure CO from the second regeneration or reactivation of the second catalyst.
19. A process comprising:
providing a first catalyst in a first reactor for a first Dry Reforming of Methane reaction or a first CARGEN reaction;
providing a first mixed gas comprising CH 4 and CO 2 in the first reactor for the first Dry Reforming of Methane reaction or the first CARGEN reaction);
allowing a first reacted gas from the first Dry Reforming of Methane reaction or the first CARGEN reaction to leave the first reactor;
providing a first oxidizing gas comprising CO 2 to the first reactor for a first regeneration or reactivation reaction of the first catalyst;
providing a second catalyst in a second reactor for a second Dry Reforming of Methane reaction or a second CARGEN reaction;
providing a second mixed gas comprising CH 4 and CO 2 in the second reactor for the second Dry Reforming of Methane reaction or the second CARGEN reaction;
allowing a second reacted gas from the second Dry Reforming of Methane reaction or the second CARGEN reaction to leave the second reactor;
providing a second oxidizing gas comprising CO 2 to the second reactor for a second regeneration or reactivation reaction of the second catalyst.
20. The process of claim 19 , wherein the first regeneration reaction of the first catalyst and the second Dry Reforming of Methane reaction or the second CARGEN reaction are about concurrent.