Process for adsorbing hydrogen chloride from a regenerator vent gas

Patent metadata

Field	Value
Publication number	US-2016175774-A1
Application number	US-201414575496-A
Country	US
Kind code	A1
Filing date	Dec 18, 2014
Priority date	Dec 18, 2014
Publication date	Jun 23, 2016
Grant date	—

Abstract

A process for adsorbing HCl from a regeneration vent gas. The regeneration vent gas from a regeneration zone is cooled, and the cooled regeneration vent gas is passed to an adsorption zone that is spaced apart from the regeneration zone. A spent catalyst is passed from a reaction zone to the adsorption zone. HCl from the regeneration vent gas is adsorbed onto the spent catalyst in the adsorption zone to enrich the spent catalyst with HCl to provide HCl-rich spent catalyst and deplete HCl from the regeneration vent gas to provide HCl-lean regeneration vent gas. The HCl-lean regeneration vent gas is purged to atmosphere, and the HCl-rich spent catalyst is passed to a regeneration zone disengaging hopper.

First claim

What is claimed is:

1 . A process for adsorbing hydrogen chloride (HCl) from a regeneration vent gas, the process comprising:
cooling the regeneration vent gas from a regeneration zone; passing the cooled regeneration vent gas to an adsorption zone that is spaced apart from the regeneration zone; passing a spent catalyst from a reaction zone to the adsorption zone; adsorbing HCl from the regeneration vent gas onto the spent catalyst in the adsorption zone to enrich the spent catalyst with HCl to provide HCl-rich spent catalyst and deplete HCl from the regeneration vent gas to provide HCl-lean regeneration vent gas; purging the HCl-lean regeneration vent gas to atmosphere; and passing the HCl-rich spent catalyst to a regeneration zone disengaging hopper of the regeneration zone.

2 . The process of claim 1 , wherein said passing the spent catalyst comprises:
passing the spent catalyst to an adsorption zone disengaging hopper that is spaced apart from the regeneration zone; and delivering the spent catalyst from the adsorption zone disengaging hopper to the adsorption zone.

3 . The process of claim 1 , wherein the regeneration zone is disposed within a vessel; and
wherein the adsorption zone is spaced apart from the vessel.

4 . The process of claim 1 , wherein the regeneration vent gas is cooled to a temperature between about 38 C-190 C (100-375 F).

5 . The process of claim 1 , wherein the regeneration zone is in communication with an input of the adsorption zone.

6 . The process of claim 5 , wherein the regeneration zone disengaging hopper is in communication with an output of the adsorption zone.

7 . The process of claim 6 , wherein a pressure within the regeneration zone is greater than a pressure of the adsorption zone.

8 . The process of claim 7 , wherein a pressure of the regeneration zone disengaging hopper is greater than a pressure within the regeneration zone.

9 . The process of claim 1 , further comprising:
introducing a lift gas comprising nitrogen from an elutriation and lift gas system into the adsorption zone.

10 . The process of claim 9 , wherein said passing the spent catalyst comprises:
passing the spent catalyst to an adsorption zone disengaging hopper that is spaced apart from the regeneration zone; and delivering the spent catalyst from the adsorption zone disengaging hopper to the adsorption zone; further comprising: venting gas from the adsorption zone disengaging hopper into the elutriation and lift gas system.

11 . The process of claim 1 , wherein the HCl-rich spent catalyst is passed to the regeneration zone disengaging hopper via a lock hopper.

12 . A process for adsorbing hydrogen chloride (HCl) from a regeneration vent gas, the process comprising:
cooling the regeneration vent gas from a regeneration zone disposed within a vessel; passing the cooled regeneration vent gas to an adsorption zone that is spaced apart from the vessel; passing spent catalyst from a reaction zone into the adsorption zone; adsorbing HCl from the regeneration vent gas onto the spent catalyst in the adsorption zone to enrich the catalyst with HCl to provide an HCl-rich spent catalyst and deplete HCl from the regeneration vent gas to provide an HCl-lean regeneration vent gas; introducing a lift gas from an elutriation and lift gas system into the adsorption zone; returning a vent gas including a portion of the lift gas from the adsorption zone to the elutriation and lift gas system; purging the HCl-lean regeneration vent gas to atmosphere; and passing the HCl-rich spent catalyst to a regeneration zone disengaging hopper.

13 . The process of claim 12 , wherein a pressure in the regeneration zone disengaging hopper is greater than a pressure within the adsorption zone.

14 . The process of claim 12 , wherein a pressure in the regeneration zone disengaging hopper is greater than a pressure within a burn zone of the regeneration zone; and
wherein a pressure within the burn zone is greater than a pressure of the adsorption zone.

15 . The process of claim 14 , wherein the regeneration zone disengaging hopper is in communication with an output of the adsorption zone.

16 . The process of claim 15 , wherein the burn zone is in communication with an input of the adsorption zone.

17 . The process of claim 12 , wherein the adsorption zone comprises at least one module that is spaced apart from the vessel.

18 . The process of claim 12 , wherein the adsorption zone is an axial gas flow zone.

19 . The process of claim 12 , wherein gas in the adsorption zone flows in a radial direction.

20 . A process for adsorbing HCl from a regeneration vent gas, the process comprising:
cooling the regeneration vent gas from a burn zone of a regeneration zone to a temperature of between 38 C-190 C (100 F-375 F), the regeneration zone being disposed within a vessel; passing the cooled regeneration vent gas to an adsorption zone comprising one or more modules that are spaced apart from the vessel, wherein the burn zone is in communication with the adsorption zone; introducing a spent catalyst and a lift gas containing nitrogen to the adsorption zone; adsorbing HCl from the regeneration vent gas onto the spent catalyst in the adsorption zone, said adsorbing enriching the catalyst with HCl to provide an HCl-rich spent catalyst and depleting HCl from the regeneration vent gas to provide an HCl-lean regeneration vent gas; purging the HCl-lean regeneration vent gas to atmosphere; and passing the HCl-rich spent catalyst from an output of the adsorption zone to a regeneration zone disengaging hopper that is in communication with an output of the adsorption zone; wherein a pressure within the regeneration zone disengaging hopper is greater than a pressure within the burn zone; and wherein the pressure within the burn zone is greater than a pressure within the adsorption zone.

Assignees

• Uop Llc

Inventors

• Sadler Clayton C
• Wegerer David A

Classifications

• B01D53/8659 Primary

  Removing halogens or halogen compounds · CPC title

• B01D53/02 Primary

  by adsorption, e.g. preparative gas chromatography {(solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01)} · CPC title

• B01J38/42

  using halogen-containing material · CPC title

• B01D53/86

  Catalytic processes · CPC title

• B01D2257/2045

  Hydrochloric acid · CPC title