Temperature-vacuum swing adsorption process for capture of CO2

Patent metadata

Field	Value
Publication number	US-11148092-B2
Application number	US-201916454972-A
Country	US
Kind code	B2
Filing date	Jun 27, 2019
Priority date	Jun 27, 2018
Publication date	Oct 19, 2021
Grant date	Oct 19, 2021

Abstract

Methods and systems for capture of CO 2 from a hydrated gaseous stream are described. Systems can be utilized for direct air capture of CO 2 and incorporate a low energy temperature-vacuum swing adsorption (TVSA) process. A TVSA process can include a multi-step CO 2 capture bed regeneration process that includes depressurization of the bed, heating of the bed, venting and purging of the bed, and cooling of the bed. Multiple beds can be cycled between CO 2 capture and regeneration, during which captured CO 2 is recovered. Off-gas from a CO 2 capture bed can be used in regenerating a parallel bed for increased efficiency.

First claim

What is claimed is:

1. A method for separating CO 2 from a gaseous stream comprising CO 2 and H 2 O vapor, the method comprising:
providing a flow of a feed stream to a first desiccant bed to form a dry gaseous stream;
providing the dry gaseous stream thus formed to a first CO 2 capture bed to form a dry, low CO 2 content gas stream;
providing a first portion of the dry, low CO 2 content gas stream to a second desiccant bed, the dry, low CO 2 content gas thus provided removing H 2 O from the second desiccant bed and regenerating the second desiccant bed;
providing a second portion of the dry, low CO 2 content gas stream to a second CO 2 capture bed as a purge gas; and
regenerating the second CO 2 capture bed according to a regeneration process that comprises depressurizing the second CO 2 capture bed, heating the second CO 2 capture bed following the depressurization, venting the second CO 2 capture bed following the heating, purging the second CO 2 capture bed by use of the purge gas, and cooling the second CO 2 capture bed.

2. The method of claim 1 , wherein following purging of the second CO 2 capture bed, at least a portion of the purge gas is provided to the second desiccant bed.

3. The method of claim 1 , further comprising switching the flow of the feed stream from the first desiccant bed to the second desiccant bed, and upon the switch, regenerating the first desiccant bed and the first CO 2 capture bed.

4. The method of claim 1 , further comprising collecting CO 2 removed from the second CO 2 capture bed during the regeneration of the second CO 2 capture bed.

5. The method of claim 4 , comprising delivery of the collected CO 2 to a cultivation area.

6. The method of claim 5 , wherein the cultivation area is an algal cultivation pond.

7. The method of claim 6 , wherein the collected CO 2 is delivered semi-continuously over the course of a day.

8. The method of claim 1 , further comprising providing a third portion of the dry, low CO 2 content gas stream as a diluent to a high CO 2 content gas stream.

9. The method of claim 1 , wherein the depressurization of the second CO 2 capture bed comprises a countercurrent depressurization.

10. The method of claim 1 , wherein the second CO 2 capture bed is vented and purged in a countercurrent flow.

11. The method of claim 1 , wherein the regeneration of the second CO 2 capture bed comprises one or more idle steps.

12. The method of claim 1 , wherein the regeneration of the second CO 2 capture bed comprises a first idle step, a countercurrent depressurization step, an idle heating step, a hot vent step, a hot purge step, a cooling purge step, and a second idle step.

13. A system for capturing CO 2 from a feed gas, the system comprising:
a first desiccant bed;
a first CO 2 capture bed, wherein a light product end of the first desiccant bed is in controllable communication with a heavy product end of the first CO 2 capture bed;
a second desiccant bed, wherein a light product end of the first CO 2 capture bed is in controllable fluid communication with a light product end of the second desiccant bed for countercurrent flow through the second desiccant bed;
a second CO 2 capture bed, wherein the light product end of the first CO 2 capture bed is also in controllable fluid communication with a light product end of the second CO 2 capture bed for countercurrent flow through the second CO 2 capture bed, and wherein
the light product end of the second desiccant bed is in controllable fluid communication with a heavy product end of the second CO 2 capture bed,
the light product end of the second CO 2 capture bed is in controllable fluid communication with the light product end of the first desiccant bed for countercurrent flow through the first desiccant bed, and
the light product end of the second CO 2 capture bed is also in controllable fluid communication with the light product end of the first CO 2 capture bed for countercurrent flow through the first CO 2 capture bed.

14. The system of claim 13 , further comprising a CO 2 storage tank in controllable fluid communication with a heavy product end of the first CO 2 capture bed and also in controllable fluid communication with a heavy product end of the second CO 2 capture bed.

15. The system of claim 13 , further comprising a first vacuum pump in fluid communication with a heavy product end of the first CO 2 capture bed.

16. The system of claim 15 , further comprising a second vacuum pump in fluid communication with a heavy product end of the second CO 2 capture bed.

17. The system of claim 13 , further comprising a first heater in thermal communication with the first CO 2 capture bed and a second heater in thermal communication with the second CO 2 capture bed.

18. The system of claim 17 , wherein the first and second heaters comprise electric heaters.

19. The system of claim 18 , wherein the first heater comprises a series of heaters along a length of the first CO 2 capture bed and the second heater comprises a series of heaters along a length of the second CO 2 capture bed.

20. The system of claim 13 , wherein the first and second CO 2 capture beds are in fluid communication with a cultivation area.

Assignees

• Univ South Carolina

Inventors

• Ritter James A
• Ebner Armin D
• Holland Charles E

Classifications

• Y02P60/20

  Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2 · CPC title

• B01D2259/40052

  Recycled product or process gas · CPC title

• B01D2259/40013

  Pressurization · CPC title

• B01D2259/40081

  Counter-current · CPC title

• B01D2259/4002

  Production · CPC title