Methods for reducing flue gas emissions from fluid catalytic cracking unit regenerators

Patent metadata

Field	Value
Publication number	US-10246645-B2
Application number	US-201715473162-A
Country	US
Kind code	B2
Filing date	Mar 29, 2017
Priority date	Sep 29, 2014
Publication date	Apr 2, 2019
Grant date	Apr 2, 2019

Abstract

Methods for reducing flue gas particulate emissions from fluid catalytic cracking unit regenerators are provided. In one embodiment, a method for reducing flue gas particulate emissions from an FCC unit regenerator includes the steps of combining biochar with a hydrocarbon feedstock to generate a biochar-containing feedstock and contacting the biochar-containing feedstock with an FCC catalyst. In another embodiment, a method for reducing flue gas particulate emissions from a FCC unit regenerator includes the steps of fluidizing catalyst fines and biochar particles in a fluidizing gas and adhering a portion of the catalyst fines to the biochar particles while in the fluidizing gas.

First claim

The invention claimed is:

1. A method for reducing flue gas particulate emissions from a fluid catalytic cracking (FCC) unit regenerator comprising the steps of:
combining biochar with a hydrocarbon feedstock to generate a biochar-containing feedstock, wherein said biochar is derived from rapid thermal processing of biomass;
contacting the biochar-containing feedstock with an FCC catalyst; and
regenerating said FCC catalyst to produce the flue gas.

2. The method of claim 1 , further comprising the step of delivering the biochar-containing feedstock to the FCC unit, wherein combining the biochar with the hydrocarbon feedstock is performed prior to the step of delivering.

3. The method of claim 1 , further comprising the step of delivering the hydrocarbon feedstock to the FCC unit, wherein combining the biochar with the hydrocarbon feedstock is performed subsequent to the step of delivering.

4. The method of claim 1 , wherein combining the biochar with the hydrocarbon feedstock is performed to generate a biochar-containing feedstock having a concentration of biochar from about 0.001 to about 0.2 weight percent with respect to total biochar-containing feedstock.

5. The method of claim 1 , further comprising the step of regenerating the FCC catalyst subsequent to the step of contacting, wherein the step of regenerating produces catalyst fines.

6. The method of claim 5 , wherein the step of contacting the biochar-containing feedstock with the FCC catalyst is performed under catalytic cracking conditions to generate a cracked hydrocarbon product.

7. The method of claim 6 , further comprising separating the FCC catalyst from the biochar and the cracked hydrocarbon product to form an FCC unit product stream comprising the biochar, and the cracked hydrocarbon product.

8. The method of claim 7 , further comprising the step of delivering the FCC unit product stream to a distillation column.

9. The method of claim 8 , further comprising the step of removing the biochar and the catalyst fines from the distillation column as part of a bottom product stream.

10. The method of claim 8 , further comprising the step of separating the cracked hydrocarbon product into one or more of a gasoline product, a naphtha product, a light cycle oil product, and a heavy cycle oil product.

11. The method of claim 1 , wherein the step of contacting with the FCC catalyst comprises contacting with one or more of a zeolite, mordenite, and faujasite catalyst.

12. The method of claim 1 , wherein the step of combining the biochar with the hydrocarbon comprises combining a biomass-derived pyrolysis oil comprising biochar with a conventional hydrocarbon feedstock.

13. A method for reducing flue gas particulate emissions from a fluid catalytic cracking (FCC) unit regenerator comprising the steps of:
fluidizing FCC catalyst, catalyst fines, and biochar particles in a fluidizing gas;
adhering a portion of the catalyst fines to the biochar particles while in the fluidizing gas; and
regenerating said FCC catalyst to produce the flue gas.

14. The method of claim 13 , further comprising the step of fluidizing regenerated FCC catalyst particles along with the catalyst fines and the biochar particles in the fluidizing gas.

15. The method of claim 14 , further comprising the step of collecting spent catalyst particles in a cyclone for subsequent regeneration of the spent catalyst particles.

16. The method of claim 15 , wherein the step of collecting spent catalyst particles further comprises substantially preventing the catalyst fines and biochar particles from being collected in the cyclone.

17. The method of claim 16 , further comprising delivering the collected, spent catalyst particles to a catalyst regenerator.

18. The method of claim 13 , wherein the step of fluidizing catalyst fines with biochar particles comprises fluidizing catalyst fines with biochar particles comprising alkali metal contaminants.

19. A method for reducing flue gas particulate emissions from a fluid catalytic cracking (FCC) unit regenerator comprising the steps of:
mixing regenerated FCC catalyst particles, and catalyst fines with a hydrocarbon feedstock;
contacting the hydrocarbon feedstock with biochar to generate a cracked hydrocarbon product and spent FCC catalyst particles;
separating the spent FCC catalyst particles from the cracked hydrocarbon product, the biochar, and the catalyst fines; and
regenerating said spent FCC catalyst to produce the flue gas.

Assignees

• Uop Llc

Inventors

• Froehle Derek
• Frey Stanley Joseph
• Walker Patrick D
• Novotny Andrew R

Classifications

• C10G2300/80

  Additives · CPC title

• C10G11/182

  Regeneration · CPC title

• C10G11/187

  Controlling or regulating · CPC title

• C10G11/18 Primary

  according to the "fluidised-bed" technique · CPC title