FCC counter-current regenerator with a regenerator riser

Patent metadata

Field	Value
Publication number	US-10751684-B2
Application number	US-201715828232-A
Country	US
Kind code	B2
Filing date	Nov 30, 2017
Priority date	Dec 27, 2016
Publication date	Aug 25, 2020
Grant date	Aug 25, 2020

Abstract

A counter-current catalyst regenerator with at least two stages of counter-current contact along with a regenerator riser is proposed. Each stage may comprise a permeable barrier that allows upward passage of oxygen-containing gas and downward passage of coked catalyst into each stage, but inhibits upward movement of catalyst to mitigate back mixing and approximate true counter-current contact and efficient combustion of coke from catalyst. The regenerator riser may provide a passage to transport the catalyst and may serve as a secondary stage for coke combustion to provide the regenerated catalyst.

First claim

The invention claimed is:

1. A regenerator vessel for combusting coke from coked catalyst, the regenerator vessel comprising:
(a) a regeneration section and a separation section, the regeneration section is a fluid tight containment vessel having one or more windows to permit the passage of the coked catalyst from the separation section to the regeneration section;
(b) a regenerator riser comprising:
(i) an inlet in a bottom of the regenerator riser in downstream communication with a spent catalyst standpipe for feeding the coked catalyst; and
(ii) an outlet for discharging catalyst from the regenerator riser;

(c) a one or more stages located above the inlet of the regenerator riser and below the outlet of the regenerator riser, each of the one or more stages comprising a permeable barrier comprising openings sized to permit the catalyst to pass through downwardly, the permeable barriers extending laterally across the regenerator vessel;
(d) a combustion gas distributor for passing a primary stream of oxygen-containing gas upwardly through the one or more stages in counter-current contact with the catalyst to combust coke from the coked catalyst to provide a regenerated catalyst and a flue gas;
(e) a regenerated catalyst outlet, the regenerated catalyst outlet located below the one or more stages;
(f) one or more cyclone separators for separating catalyst from the flue gas; and
(g) a flue gas outlet in the regenerator vessel.

2. The regenerator vessel of claim 1 , wherein the regeneration section located below the separation section and separated by a wall.

3. The regenerator vessel of claim 1 , wherein one or more stages are present in the regeneration section.

4. The regenerator vessel of claim 1 , wherein the outlet of the regenerator riser is located in the separation section above the one or more stages.

5. The regenerator vessel of claim 1 , wherein the inlet of the regenerator riser is located below the regeneration vessel.

6. The regenerator vessel of claim 1 , wherein the inlet is a spent catalyst inlet and the regenerator riser further comprises a regenerated catalyst inlet in communication with the regeneration vessel via a regenerator riser conduit extending from the regeneration vessel to the regenerated catalyst inlet of the regenerator riser.

7. The regenerator vessel of claim 1 , wherein regeneration vessel comprises at least two stages comprising:
a first permeable barrier below the outlet, the first permeable barrier extending laterally across the regenerator vessel;
a second permeable barrier below the first permeable barrier to define a second stage, the second permeable barrier extending laterally across the regenerator vessel; and
the regeneration catalyst outlet below the second permeable barrier.

8. The regenerator vessel of claim 7 wherein the second permeable barrier is spaced below the first permeable barrier.

9. The regenerator vessel of claim 7 further comprising a third permeable barrier below the second permeable barrier and above the regenerator catalyst outlet, the third permeable barrier extending laterally across the regenerator vessel.

10. A regenerator vessel for combusting coke from coked catalyst, the regenerator vessel comprising:
(a) a regenerator riser extending upwardly through the regenerator vessel comprising:
(i) an inlet in a bottom of the regenerator riser in downstream communication with a spent catalyst standpipe for feeding the coked catalyst; and
(ii) an outlet for discharging catalyst from the regenerator riser;

(b) a one or more stages located above the inlet of the regenerator riser and below the outlet of the regenerator riser, each of the one or more stages comprising a permeable barrier comprising openings sized to permit the catalyst to pass through downwardly, the permeable barriers extending laterally across the regenerator vessel;
(c) a combustion gas distributor for passing a primary stream of oxygen-containing gas upwardly through the one or more stages in counter-current contact with the catalyst to combust coke from the coked catalyst to provide a regenerated catalyst and a flue gas;
(d) a regenerated catalyst outlet, the regenerated catalyst outlet located below the one or more stages;
(e) one or more cyclone separators for separating catalyst from the flue gas; and
(f) a flue gas outlet in the regenerator vessel.

11. The regenerator vessel of claim 10 , wherein the regenerator vessel comprises a regeneration section and a separation section, the regeneration section located below the separation section and separated by a wall.

12. The regenerator vessel of claim 11 , wherein the regeneration section is a fluid tight containment vessel with one or windows to permit the passage of catalyst from the separation section to the regeneration section.

13. The regenerator vessel of claim 10 , wherein one or more stages are present in the regeneration section.

14. The regenerator vessel of claim 10 , wherein the outlet of the regenerator riser is located in the separation section above the one or more stages.

15. The regenerator vessel of claim 10 , wherein the inlet of the regenerator riser is located below the regeneration vessel.

16. The regenerator vessel of claim 10 , wherein the inlet is a spent catalyst inlet and the regenerator riser further comprises a regenerated catalyst inlet in communication with the regeneration vessel via a regenerator riser conduit extending from the regeneration vessel to the regenerated catalyst inlet of the regenerator riser.

17. The regenerator vessel of claim 10 , wherein regeneration vessel comprises at least two stages comprising:
a first permeable barrier below the catalyst inlet, the first permeable barrier extending laterally across the regenerator vessel;
a second permeable barrier below the first permeable barrier to define a second stage, the second permeable barrier extending laterally across the regenerator vessel; and
the regeneration catalyst outlet below the second permeable barrier.

18. The regenerator vessel of claim 17 wherein the second permeable barrier is spaced below the first permeable barrier.

19. The regenerator vessel of claim 17 further comprising a third permeable barrier below the second permeable barrier and above the regenerator catalyst outlet, the third permeable barrier extending laterally across the regenerator vessel.

Assignees

• Uop Llc

Inventors

• Davydov Lev
• Sandacz Michael S
• Palmas Paolo
• Fei Zhihao
• Lippmann Matthew

Classifications

• F23C2206/10

  Circulating fluidised bed · CPC title

• F23C10/00

  Fluidised bed combustion apparatus · CPC title

• F23G2203/50

  Fluidised bed furnace · CPC title

• B01J8/1881

  with particles moving downwards while fluidised · CPC title

• B01J8/12

  moved by gravity in a downward flow · CPC title