Processes and apparatuses for regenerating a catalyst

Patent metadata

Field	Value
Publication number	US-12508563-B2
Application number	US-202218067317-A
Country	US
Kind code	B2
Filing date	Dec 16, 2022
Priority date	Dec 30, 2021
Publication date	Dec 30, 2025
Grant date	Dec 30, 2025

Abstract

Processes and apparatuses for regenerating catalysts used in a hydrocarbon conversion process. The catalyst is separated into a bypass portion and an adsorption portion. The bypass portion is passed to a regeneration zone where coke may be removed. A vent gas from the regeneration zone may include an active additive from the catalyst, like a halogen. The vent gas is sent to an adsorption zone which also receives the adsorption portion. In the adsorption zone, the catalyst will contact and adsorb the active additive and then pass to the regeneration zone. The amount of active additive in the vent gas from the regeneration zone and the adsorption zone is reduced.

First claim

What is claimed is:

1 . A process for regenerating a catalyst, the process comprising:
disengaging catalyst from a lift gas, the catalyst comprising coke and at least one active additive; splitting the catalyst into a bypass portion and an adsorption portion; removing coke from the catalyst of the bypass portion in a regeneration zone, the regeneration zone operated under conditions to remove coke from the catalyst and provide a regenerated catalyst and a vent gas, wherein the vent gas comprises the at least one active additive; adsorbing the at least one active additive from the vent gas with the catalyst from the adsorption portion in an adsorption zone; and, removing coke from the catalyst of the adsorption portion in the regeneration zone, wherein the bypass portion of the catalyst bypasses the adsorption zone.

2 . The process of claim 1 , wherein one or more catalyst transfer pipes are used for the bypass portion.

3 . The process of claim 2 , wherein the one or more catalyst pipes bypass the adsorption zone.

4 . The process of claim 3 , wherein the one or more catalyst transfer pipes for the bypass portion pass through the adsorption zone.

5 . The process of claim 4 , further comprising:
releasing a portion of a seal gas from the one or more catalyst transfer pipes into the adsorption zone while isolating the catalyst of the bypass portion from the vent gas into the adsorption zone.

6 . The process of claim 1 , wherein the adsorption zone produces an adsorption zone vent gas and wherein the process further comprises:
separating, in a separation zone, the adsorption zone vent gas into a water stream and a recycle gas stream, the recycle gas stream being passed to the regeneration zone.

7 . The process of claim 6 , wherein the separation zone comprises a moisture extractor that receives a refinery cooling water.

8 . An apparatus for removing coke from a catalyst, the apparatus comprising:
a disengaging zone, the disengaging zone configured to receive a mixture of catalyst and a lift gas and separate the catalyst from the lift gas, the catalyst comprising coke and at least one additive; a regeneration zone configured to receive a first portion of catalyst from the disengaging zone and wherein the regeneration zone is operated under conditions to remove coke from the catalyst and provide a regenerated catalyst and a vent gas, wherein the vent gas comprises the at least one additive; and, an adsorption zone configured to receive a second portion of catalyst from the disengaging zone and wherein the adsorption zone is operated under conditions to adsorb, with the catalyst from the second portion, the at least one additive in the vent gas; wherein the first portion of the catalyst is isolated from the adsorption zone.

9 . The apparatus of claim 8 , further comprising:
at least one catalyst transfer pipe configured to isolate the first portion of catalyst from the adsorption zone.

10 . The apparatus of claim 9 , wherein the disengaging zone and the adsorption zone are contained in a vessel, and wherein the at least one catalyst transfer pipe is external to the vessel.

11 . The apparatus of claim 9 , wherein the disengaging zone and the adsorption zone are contained in a vessel, and wherein the at least one catalyst transfer pipe is internal to the vessel.

12 . The apparatus of claim 9 , wherein the at least one catalyst transfer pipe comprises a vent opening.

13 . The apparatus of claim 12 , wherein the vent opening comprises a shroud over a concentric pipe.

14 . The apparatus of claim 8 , further comprising a catalyst transfer pipe configured to receive the second portion of the catalyst.

15 . The apparatus of claim 8 , wherein the disengaging zone and the adsorption zone are contained in a vessel, and wherein the vessel further comprises a baffle configured to redistribute catalyst to one or more catalyst transfer pipes.

16 . The apparatus of claim 15 , wherein the baffle comprises a downward concave cone.

17 . The apparatus of claim 16 , wherein the downward concave cone comprises an upper portion of the baffle, and wherein a lower portion of the baffle comprises an upward concave cone.

18 . The apparatus of claim 16 , the baffle is disposed above a boot, the boot comprising the one or more catalyst transfer pipes.

19 . A process for regenerating a catalyst, the process comprising:
disengaging catalyst from a lift gas, the catalyst comprising coke and at least one active additive; splitting the catalyst into a first portion and a second portion; removing coke from the catalyst of the first portion in a regeneration zone, the regeneration zone operated under conditions to remove coke from the catalyst and provide a regenerated catalyst and a vent gas, wherein the vent gas comprises the at least one active additive; adsorbing the at least one active additive from the vent gas with the catalyst from the second portion in an adsorption zone, wherein the adsorption zone produces an adsorption zone vent gas; removing coke from the catalyst of the second portion in the regeneration zone; and, separating, in a separation zone, the adsorption zone vent gas into a water stream and a recycle gas stream, the recycle gas stream being passed to the regeneration zone.

20 . The process of claim 19 , wherein the separation zone comprises a moisture extractor that receives a refinery cooling water.

Assignees

• Uop Llc

Inventors

• Lok Ka L
• Egolf Bryan J
• Zuraski Matthew R
• Jaggi Vikas
• Ozmen Jennifer J

Classifications

• B01D53/8671

  Removing components of defined structure not provided for in B01D53/8603 - B01D53/8668 · CPC title

• B01D2257/80

  Water · CPC title

• B01D2257/20

  Halogens or halogen compounds · CPC title

• B01J2208/00849

  outside the bed, e.g. baffles · CPC title

• B01J2208/00991

  Disengagement zone in fluidised-bed reactors · CPC title