Regeneration vessel adsorption zone and process for adsorbing halogen-containing material and sampling catalyst

Patent metadata

Field	Value
Publication number	US-11724240-B2
Application number	US-202017139616-A
Country	US
Kind code	B2
Filing date	Dec 31, 2020
Priority date	Dec 31, 2020
Publication date	Aug 15, 2023
Grant date	Aug 15, 2023

Abstract

A regenerator vessel for adsorbing halogen-containing material from a regenerator vent gas stream has a plurality of catalyst nozzles disposed at a top portion of the regenerator vessel. A first gas outlet is associated with a chlorination zone, and a second gas outlet associated with a combustion zone. A drying zone is in fluid communication with an air heater and the drying zone located in a bottom portion of the regenerator vessel. The first gas outlet is configured to withdraw a first gas stream from the chlorination zone and the second gas outlet is configured to withdraw a second gas stream from the combustion zone. The top portion of the regenerator vessel has an adsorption zone having a vent gas inlet port, a vent gas outlet port, and a portion of an annular catalyst bed.

First claim

What is claimed is:

1. A regenerator vessel for adsorbing halogen-containing material from a regenerator vent gas stream, the regenerator vessel comprising:
a plurality of catalyst nozzles disposed at a top portion of the regenerator vessel;
a first gas outlet associated with a chlorination zone;
a second gas outlet associated with a combustion zone; and
a drying zone in fluid communication with an air heater, the drying zone located in a bottom portion of the regenerator vessel;
wherein the first gas outlet is configured to withdraw a first gas stream from the chlorination zone;
wherein the second gas outlet is configured to withdraw a second gas stream from the combustion zone;
wherein the top portion of the regenerator vessel comprises an adsorption zone having a vent gas inlet port and a vent gas outlet port, the adsorption zone comprising a portion of an annular catalyst bed.

2. The regenerator vessel of claim 1 , wherein the vent gas inlet port is disposed at a position in the top portion of the regenerator vessel that is radially outward of the vent gas outlet port.

3. The regenerator vessel of claim 1 , wherein the vent gas inlet port is disposed at a position in the top portion of the regenerator vessel having a lower elevation than the vent gas outlet port.

4. The regenerator vessel of claim 1 , wherein the adsorption zone comprises an inlet chamber and an outlet chamber.

5. The regenerator vessel of claim 1 , wherein the regenerator vessel comprises a sample port disposed at a lower elevation that the plurality of catalyst ports and the vent gas inlet port.

6. The regenerator vessel of claim 5 , wherein the sample port is disposed at an angle of about 45 degrees with respect to a vertical outer wall of the regenerator vessel.

7. The regenerator vessel of claim 1 , wherein the regenerator vessel comprises an annular outer baffle and an annular inner baffle disposed in the top portion of the regenerator vessel.

8. The regenerator vessel of claim 7 , wherein the annular outer baffle comprises a vent gas inlet screen, and wherein the annular inner baffle comprises a vent gas outlet screen.

9. The regenerator vessel of claim 1 , wherein the adsorption zone is configured to provide a vent gas flow in relation to a catalyst bed direction that is co-current.

10. A process for regenerating catalyst in a regenerator vessel, the process comprising:
providing the regenerator vessel comprising:
a plurality of catalyst nozzles disposed at a top portion of the regenerator vessel;
a first gas outlet associated with a chlorination zone;
a second gas outlet associated with a combustion zone; and
a drying zone in fluid communication with an air heater located in a bottom portion of the regenerator vessel;
wherein the first gas outlet is configured to withdraw a first gas stream from the chlorination zone;
wherein the second gas outlet is configured to withdraw a second gas stream from the combustion zone;

withdrawing a portion of the second gas stream to form a regenerator vent gas stream;
introducing the regenerator vent gas stream to the top portion of the regenerator vessel at a vent gas inlet port;
contacting the regenerator vent gas stream with catalyst in an adsorption zone disposed in the top portion of the regenerator vessel;
withdrawing a treated regenerator vent gas stream from the top portion of the regenerator vessel at a vent gas outlet port; and
discharging the treated regenerator vent gas stream to the atmosphere.

11. The process of claim 10 , wherein the contacting occurs at a temperature of between about 100 and about 300 degrees Celsius, and wherein at least about 50% of halogen-containing material present in the regenerator vent gas stream is adsorbed onto the catalyst.

12. The process of claim 10 , further comprising sampling the catalyst at an elevation below the vent gas inlet port; and
wherein the step of contacting the regenerator vent gas stream with catalyst in the top portion of the regenerator vessel comprises a vent gas flow in relation to a catalyst bed direction that is counter-current or cross-current.

13. The process of claim 12 , wherein the sampling comprises operating a screw conveyor to withdraw catalyst upward from the adsorption zone of the regenerator vessel.

14. The process of claim 12 , wherein the sampling comprises operating a thief sampling apparatus to withdraw catalyst upward from the adsorption zone of the regenerator vessel, the thief sampling apparatus comprising an elongate member having a plurality of cavities.

15. The process of claim 12 , wherein the sampling comprises operating an eductor sampling apparatus to withdraw catalyst upward from the chloride adsorption zone of the regenerator vessel.

16. A method of retrofitting a head portion of a regenerator vessel, the method comprising:
unloading catalyst from the regenerator vessel;
disconnecting piping associated with the head portion, the piping comprising a chlorination zone outlet, a combustion zone outlet, and catalyst transfer piping;
removing the head portion and a portion of an inner screen;
installing a new head portion having a vent gas inlet port, a vent gas outlet port, an annular outer baffle, and an annular inner baffle;
connecting a vent gas inlet line, a vent gas outlet line, a vent gas cooler, an air preheater, to the new head portion; and
reloading catalyst into the regenerator vessel.

17. The method of claim 16 , further comprising the step of installing a sample port in the new head portion of the regenerator vessel, the sample port disposed radially outward and at a lower elevation with respect to the vent gas inlet port.

18. The method flow of claim 16 , further comprising the step of attaching the annular inner baffle to an annular inner screen and attaching the annular outer baffle to an annular outer screen.

19. The method flow of claim 16 , further comprising the step of installing a purge gas inlet in the new head portion of the regenerator vessel.

20. The method flow of claim 16 , further comprising the step of installing a vent gas inlet screen in the annular outer baffle and installing a vent gas outlet screen in the annular inner baffle.

Assignees

• Uop Llc

Inventors

• Ozmen Jennifer J
• Mudrock Rebecca
• Glover Bryan K
• Lim Hosoo
• Paustian Joel S

Classifications

• B01J2219/00024

  Revamping, retrofitting or modernisation of existing plants · CPC title

• B01J8/26 Primary

  with two or more fluidised beds, e.g. reactor and regeneration installations · CPC title

• B01D53/8659

  Removing halogens or halogen compounds · CPC title

• B01D53/88

  Handling or mounting catalysts · CPC title

• B01J8/001

  Controlling catalytic processes (B01J8/1809 takes precedence) · CPC title