Fluid catalytic cracking process for cracking multiple feedstocks

Patent metadata

Field	Value
Publication number	US-11214741-B2
Application number	US-202016801019-A
Country	US
Kind code	B2
Filing date	Feb 25, 2020
Priority date	Feb 25, 2020
Publication date	Jan 4, 2022
Grant date	Jan 4, 2022

Abstract

A fluid catalytic cracking (FCC) process for cracking multiple feedstocks in a FCC apparatus comprising a first set of feed distributors having first distributor tips and a second set of feed distributors having second distributor tips is provided. A first feed is injected into the riser from first distributor tips. A second feed is injected into the riser from second distributor tips. The first distributor tips and the second distributor tips are positioned at different radii in the riser. The first feed and the second feed are cracked in the riser in the presence of an FCC catalyst to provide a cracked effluent stream. The first distributor tips and the second distributor tips are located into a region of lower catalyst density and a region of higher catalyst density respectively in the riser.

First claim

The invention claimed is:

1. A fluid catalytic cracking process for cracking multiple feedstocks in a fluid catalytic cracking apparatus comprising:
a riser, the riser comprising a first set of feed distributors having first distributor tips and a second set of feed distributors having second distributor tips positioned around the perimeter of the riser, the process comprising:
injecting from the first distributor tips of the first set of feed distributors, a first feed into the riser;
injecting from the second distributor tips of the second set of feed distributors, a second feed into the riser,
wherein the first distributor tips are positioned at a first radius in the riser and the second distributor tips are positioned at a second radius with respect to a center point of the riser;
wherein the second distributor tips are spaced apart from the first distributor tips at a vertical distance of no more than about an inner diameter of the riser and the first distributor tips are located in a region of a first catalyst density in the riser and the second distributor tips are located in a region of a second catalyst density in the riser, the first catalyst density and the second catalyst density being different; and
cracking the first feed and the second feed in the riser in the presence of a fluid catalytic cracking catalyst to provide a cracked effluent stream.

2. The process of claim 1 , wherein the first distributor tips are located into a region of lower catalyst density in the riser and the second distributor tips are located into a region of higher catalyst density in the riser.

3. The process of claim 2 , wherein the region of lower catalyst density is an inner center region in the riser and the region of higher catalyst density is an outer annular region in the riser.

4. The process of claim 1 , wherein the first radius is smaller than the second radius.

5. The process of claim 1 , wherein the second feed is less crackable than the first feed.

6. The process of claim 1 further comprising a third set of feed distributors having third distributor tips positioned around the perimeter of the riser for injecting a third feed into the riser, wherein the third distributor tips of the third set of feed distributors for injecting the third feed into the riser are positioned at a higher elevation around the perimeter of the riser than the first distributor tips and the second distributor tips.

7. The process of claim 6 , wherein the third feed is selected from one or more of light vacuum gas oil, and unconverted oil.

8. The process of claim 1 further comprising a set of center feed distributors positioned at a lower elevation than the first set of feed distributors and the second set of feed distributors, wherein one or more of heavy cycle oil, main column bottoms, and deasphalted oil is passed through the center feed distributors into the riser.

9. The process of claim 1 , wherein the first feed and the second feed comprise pairs selected from a group consisting of: heavy vacuum gas oil and heavy cycle oil, heavy vacuum gas oil and main column bottoms, heavy vacuum gas oil and deasphalted oil, naphtha and C4 olefins, C5 hydrocarbons and C4 hydrocarbons, and vacuum gas oil and hydrocarbon resid.

10. A fluid catalytic cracking process for cracking multiple feedstocks in a fluid catalytic cracking apparatus comprising a riser, the process comprising:
injecting from first distributor tips of a first set of feed distributors positioned around a perimeter of the riser, a first feed into a region of lower catalyst density in the riser;
injecting from second distributor tips of a second set of feed distributors
positioned around the perimeter of the riser, a second feed into a region of higher catalyst density in the riser,
wherein the second distributor tips are spaced apart from the first distributor tips at a vertical distance of no more than about an inner diameter of the riser; and
cracking the first feed and the second feed in the riser in the presence of a fluid catalytic cracking catalyst to provide a cracked effluent stream.

11. The process of claim 10 , wherein the region of lower catalyst density is an inner center region in the riser and the region of higher catalyst density is an outer annular region in the riser.

12. The process of claim 10 , wherein the first feed and the second feed comprise pairs selected from a group consisting of: heavy vacuum gas oil and heavy cycle oil, heavy vacuum gas oil and main column bottoms, heavy vacuum gas oil and deasphalted oil, naphtha and C4 olefins, C5 hydrocarbons and C4 hydrocarbons, and vacuum gas oil and hydrocarbon resid.

13. The process of claim 10 , wherein the second feed is less crackable than the first feed.

14. The process of claim 10 , wherein the first distributor tips are positioned at a first radius in the riser and the second distributor tips are positioned at a second radius in the riser.

15. The process of claim 14 , wherein the first radius is smaller than the second radius.

16. A fluid catalytic cracking process for cracking multiple feedstocks in a fluid catalytic cracking apparatus comprising:
a riser, the riser comprising a first set of feed distributors having first distributor tips and a second set of feed distributors having second distributor tips positioned around the perimeter of the riser, the process comprising:
injecting from the first distributor tips of the first set of feed distributors, a first feed into the riser;
injecting from the second distributor tips of the second set of feed distributors, a second feed into the riser,
wherein the first distributor tips are positioned at a first radius in the riser and the second distributor tips are positioned at a second radius with respect to a center point of the riser,
wherein the first distributor tips are located in a region of a lower catalyst density in the riser and the second distributor tips are located in a region of a higher catalyst density in the riser; and
cracking the first feed and the second feed in the riser in the presence of a fluid catalytic cracking catalyst to provide a cracked effluent stream.

17. The process of claim 16 , wherein the second distributor tips are spaced apart from the first distributor tips at a vertical distance of no more than about an inner diameter of the riser.

18. The process of claim 16 , wherein the first radius is smaller than the second radius.

19. The process of claim 16 , wherein the second feed is less crackable than the first feed.

20. The process of claim 16 further comprising a third set of feed distributors having a third distributor tips positioned around the perimeter of the riser for injecting a third feed into the riser, wherein the third distributor tips of the third set of feed distributors for injecting the third feed into the riser are positioned at a higher elevation around the perimeter of the riser than the first distributor tips and the second distributor tips.

Assignees

• Uop Llc

Inventors

• Davydov Lev
• Mehlberg Robert
• Wojtowicz Matthew R
• Walker Patrick D
• Durai Sakthivelan Maadasamy
• Kulprathipanja Sathit

Classifications

• C10G2300/1037

  Hydrocarbon fractions · CPC title

• B01J8/085

  Feeding reactive fluids (for solid material, see B01J8/0015) · CPC title

• C10G11/18

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

• B01J8/1818

  Feeding of the fluidising gas (B01J8/44 takes precedence) · CPC title

• C10G2300/701

  Use of spent catalysts · CPC title