Moving bed temperature swing adsorption process

Patent metadata

Field	Value
Publication number	US-9527028-B2
Application number	US-201414575563-A
Country	US
Kind code	B2
Filing date	Dec 18, 2014
Priority date	Dec 18, 2014
Publication date	Dec 27, 2016
Grant date	Dec 27, 2016

Abstract

Process for adsorbing a species from a feed gas stream. Feed gas stream is introduced to an adsorption zone having a sorbent. Species from the feed gas stream is adsorbed onto the sorbent at an adsorbing temperature to enrich the sorbent with the species and deplete the species from the feed gas stream. Species-lean product gas stream is output. Species-rich sorbent from the adsorption zone is passed to a regeneration zone. Regenerant gas at a regenerating temperature greater than the adsorbing temperature is introduced into the regeneration zone to strip the species from the species-rich sorbent. Regenerated sorbent from the regeneration zone passes to a cooling zone disposed below the regeneration zone. Regenerated sorbent is cooled at a cooling temperature below the regenerating temperature. Cooled sorbent is transferred to the adsorbent zone.

First claim

What is claimed is:

1. A gas phase adsorption process for adsorbing a species from a feed gas stream, the process comprising:
introducing the feed gas stream to an adsorption zone having a sorbent;
adsorbing the species from the feed gas stream onto the sorbent in the adsorption zone at an adsorbing temperature to enrich the sorbent with the species to provide species-rich sorbent and deplete the species from the feed gas stream to provide a species-lean gas stream;
outputting the species-lean product gas stream;
passing the species-rich sorbent from the adsorption zone to a regeneration zone disposed below the adsorption zone;
introducing a regenerant gas at a regenerating temperature into the regeneration zone to strip the species from the species-rich sorbent and provide a regenerated sorbent, the regenerating temperature being greater than the adsorbing temperature;
passing the regenerated sorbent from the regeneration zone to a cooling zone disposed below the regeneration zone;
cooling the regenerated sorbent at a cooling temperature that is below the regenerating temperature;
transferring the cooled sorbent to the adsorption zone;
heating a cooling zone vent gas to the regenerating temperature and passing the heated cooling zone vent gas to the regeneration zone;
condensing a regeneration zone vent gas; and
passing the condensed regeneration zone vent gas to the cooling zone at the cooling temperature.

2. The process of claim 1 , wherein the adsorption zone, the regeneration zone, and the cooling zone are disposed within a vessel.

3. The process of claim 1 , wherein said passing the species-rich sorbent from the adsorption zone to the regeneration zone comprises causing the species-rich sorbent to flow by gravity to the regeneration zone.

4. The process of claim 3 , wherein said passing the regenerated sorbent from the regeneration zone to the cooling zone comprises causing the regenerated sorbent to flow by gravity to the cooling zone.

5. The process of claim 1 , wherein said transferring the cooled sorbent to the adsorbent zone comprises transferring the cooled sorbent from the cooling zone to a surge zone disposed above the adsorption zone; and
causing the cooled sorbent to flow by gravity from the surge zone to the adsorption zone.

6. The process of claim 5 , wherein said transferring comprises:
controlling a flow of the cooled sorbent from the cooling zone to the surge zone.

7. The process of claim 5 , wherein said transferring further comprises transferring the cooled sorbent via transport by a carrier gas.

8. The process of claim 1 , wherein the species comprises less than 50% by volume of the feed gas stream.

9. The process of claim 1 , further comprising:
separating the species from the condensed regeneration vent gas before said passing to the cooling zone.

10. The process of claim 1 , wherein the feed gas stream comprises a stream taken from the group consisting of hydrocarbon streams, inert gas streams, and aqueous streams.

11. The process of claim 1 , wherein the sorbent is selected from the group consisting of aluminas and zeolitic materials.

12. A temperature swing adsorption process for adsorbing a species from a feed gas stream, the process comprising:
introducing the feed gas stream to an adsorption zone having a sorbent;
adsorbing the species from the feed gas stream onto the sorbent in the adsorption zone at an adsorbing temperature to enrich the adsorbent with the species to provide species-rich sorbent and deplete the species from the feed gas stream to provide a species-lean gas stream;
outputting the species-lean product gas stream;
causing the species-rich sorbent to flow by gravity from the adsorption zone to a regeneration zone disposed below the adsorption zone;
introducing a regenerant gas at a regenerating temperature into the regeneration zone to strip the species from the species-rich sorbent and provide a regenerated sorbent, the regenerating temperature being greater than the adsorbing temperature;
causing the regenerated sorbent from the regeneration zone to flow by gravity to a cooling zone disposed below the regeneration zone;
cooling the regenerated sorbent in the cooling zone at a cooling temperature that is lower than the regenerating temperature;
transferring the cooled sorbent to the adsorbent zone;
heating a cooling zone vent gas to the regenerating temperature and passing the heated cooling zone vent gas to the regeneration zone;
outputting a regenerating zone vent gas having a desorbed species;
separating the desorbed species from the regeneration zone vent gas to provide a regenerant gas; and
recycling the regenerant gas to the cooling zone.

13. The process of claim 12 , further comprising:
outputting a regeneration zone vent gas having a desorbed species as an effluent gas.

14. The process of claim 12 , further comprising:
condensing at least a portion of the desorbed species in the regeneration zone vent gas before the separating the portion of the desorbed species from the regeneration zone vent gas to provide the regenerant gas.

15. The process of claim 12 , further comprising:
condensing the regeneration zone vent gas before the separating the desorbed species from the condensed regeneration zone vent gas;
pressurizing the condensed regeneration vent gas to increase a condensation temperature of the condensed regeneration vent gas;
further condensing and further separating the desorbed species from the pressurized regeneration zone vent gas to provide the regenerant.

16. The process of claim 12 , further comprising:
condensing the regeneration zone vent gas before the separating the desorbed species from the regeneration zone vent gas; wherein the separation is a liquid-liquid separation to provide a liquid regenerant; and
vaporizing the liquid regenerant to provide the regenerant gas.

17. A moving bed temperature swing adsorption process for adsorbing a species from a feed gas stream, the process comprising:
introducing the feed gas stream to an adsorption zone having a sorbent, the adsorption zone being disposed within a vessel;
adsorbing the species from the feed gas stream onto the sorbent in the adsorption zone at an adsorbing temperature to enrich the adsorbent with the species to provide species-rich sorbent and deplete the species from the feed gas stream to provide a species-lean gas stream;
outputting the species-lean product gas stream;
causing the species-rich sorbent to flow by gravity from the adsorption zone to a regeneration zone in the vessel disposed below the adsorption zone;
introducing a regenerant gas at a regenerating temperature into the regeneration zone and contacting the species-rich sorbent with the regenerant gas to strip the species from the species-rich sorbent and provide a regenerated sorbent, the regenerating temperature being greater than the adsorbing temperature;
causing the regenerated sorbent from the regeneration zone to flow by gravity to a cooling zone disposed in the vessel below the regeneration zone;
introducing a cooling gas at a cooling temperature to cool the regenerated sorbent in the cooling zone, the cooling temperature being lower than the regenerating temperature;
transferring the cooled sorbent to a surge zone disposed in the vessel above the adsorbent zone;
causing the cooled sorbent from the surge zone to flow by gravity to the adsorption zone;
heating a cooling zone vent gas to the regenerating temperature and passing the heated cooling zone vent gas to the regeneration zone to introduce the regenerant

Assignees

• Uop Llc

Inventors

• Sadler Clayton C
• Wegerer David A
• Lippmann Matthew

Classifications

• B01D53/0454 Primary

  Controlling adsorption (controlling temperature swing adsorption B01D53/0462, controlling pressure swing adsorption B01D53/047) · CPC title

• B01D2253/108

  Zeolites · CPC title

• B01D53/0462 Primary

  Temperature swing adsorption · CPC title

• B01D2253/104

  Alumina · CPC title

• B01D53/0438

  Cooling or heating systems · CPC title