Carbon dioxide separation using adsorption with steam regeneration

Patent metadata

Field	Value
Publication number	US-9504955-B2
Application number	US-201414325637-A
Country	US
Kind code	B2
Filing date	Jul 8, 2014
Priority date	Jul 8, 2013
Publication date	Nov 29, 2016
Grant date	Nov 29, 2016

Abstract

A process for separating a carbon dioxide from a gas stream is disclosed. The process can include passing the gas stream over a sorbent that adsorbs the carbon dioxide by concentration swing adsorption and adsorptive displacement. The sorbent can be regenerated and the carbon dioxide recaptured by desorbing the carbon dioxide from the sorbent using concentration swing adsorption and desorptive displacement. A carbon dioxide separation system is also disclosed. Neither the system nor the process rely on temperature swing or pressure swing adsorption.

First claim

We claim:

1. A process for separating CO 2 from a gas stream, comprising
a) passing a gas stream comprising CO 2 over a sorbent to adsorb the CO 2 to the sorbent,
b) recovering the CO 2 by desorbing the CO 2 from the sorbent,
wherein the process does not include pressure swing adsorption or temperature swing adsorption,
wherein step b) includes desorption of the CO 2 from the sorbent by a combination of concentration swing desorption and desorptive displacement, the concentration swing desorption comprising partial pressure purge desorption and the desorptive displacement comprising a process wherein an adsorbed CO 2 molecule is displaced from the sorbent by steam during the desorption step.

2. The process of claim 1 , wherein step a) includes adsorption of CO 2 by concentration swing adsorption and adsorptive displacement.

3. The process of claim 1 , wherein steps a) and b) are conducted at a constant pressure.

4. The process of claim 1 , wherein steps a) and b) are conducted at approximately isothermal conditions.

5. The process of claim 1 , wherein the temperature of the sorbent decreases during step a) by no more than about 20° C.

6. The process of claim 1 , wherein the temperature of the sorbent increases during step b) by no more than about 20° C.

7. The process of claim 1 , wherein the sorbent comprises an alkalized substrate.

8. The process of claim 1 , wherein the sorbent comprises an alkalized alumina.

9. A sorbent based CO 2 adsorption process, comprising the steps of
a) preparing a sorbent comprising an alkalized substrate,
b) passing a gas stream containing CO 2 across the sorbent to adsorb the CO 2 onto the alkalized substrate,
c) recovering the CO 2 from the sorbent by passing steam across the alkalized substrate to displace the carbon dioxide adsorbed on the alkalized substrate with water.

10. The process of claim 9 , wherein the process does not include pressure swing adsorption or temperature swing adsorption.

11. The process of claim 9 , wherein step b) comprises adsorption of CO 2 by concentration swing adsorption and adsorptive displacement.

12. The process of claim 9 , wherein step c) comprises recovering the CO 2 by a combination of concentration swing desorption and desorptive displacement.

13. The process of claim 9 , wherein the alkalized substrate comprises a substrate and at least one alkali or alkaline earth component.

14. The process of claim 9 , wherein the alkalized substrate comprises an alumina component and at least one alkali or alkaline earth component.

15. The process of claim 9 , wherein the alkalized substrate consists essentially of an alumina component and at least one alkali or alkaline earth component.

16. The process of claim 9 , wherein the temperature of the sorbent decreases during step b) by no more than about 20° C.

17. The process of claim 9 , wherein the temperature of the sorbent increases during step c) by no more than about 20° C.

18. A CO 2 separation system, comprising:
a CO 2 feed stream;
a CO 2 adsorption zone;
a CO 2 desorption zone;
one or more CO 2 sorbent beds,
wherein the one or more sorbent beds alternates between the CO 2 adsorption zone and the CO 2 desorption zone, and wherein the one or more sorbent beds adsorbs CO 2 from the CO 2 feed stream in the adsorption zone and desorbs CO 2 in the desorption zone;
wherein the CO 2 separation system does not include a pressure swing or a temperature swing adsorption, and
wherein the desorption zone operates as a concentration swing and a desorptive displacement, the concentration swing comprising partial pressure purge desorption and the desorptive displacement comprising a process wherein an adsorbed CO 2 molecule is displaced from the sorbent by steam during the desorption step.

19. The system of claim 18 , further comprising an inlet and an outlet for the adsorption zone where the CO 2 feed stream enters the adsorption zone via the inlet and a purified gas stream exits the adsorption zone via the outlet.

20. The system of claim 18 , further comprising an inlet and an outlet for the desorption zone, wherein a stream comprising steam enters the desorption zone via the inlet and a CO 2 enriched stream exits via the outlet.

21. The system of claim 18 , further comprising a purge zone after the desorption zone, wherein the one or more sorbent beds enters the purge stage and is purged via a stripping gas stream.

22. The system of claim 18 , wherein the one or more sorbent beds comprises a sorbent, and the sorbent comprises a substrate and at least one alkali or alkaline earth component.

23. The system of claim 18 , wherein the one or more sorbent beds comprises a sorbent, and the sorbent comprises an alumina component and at least one alkali or alkaline earth component.

24. The system of claim 18 , wherein the adsorption zone operates as a concentration swing and adsorptive displacement.

25. The system of claim 18 , wherein the adsorption zone has an adsorption inlet and an adsorption outlet, the desorption zone has a desorption inlet and a desorption outlet, and the adsorption inlet and adsorption outlet are in opposing positions from the desorption inlet and the desorption outlet, relative to the one or more sorbent beds.

26. The system of claim 18 , wherein the one or more sorbent beds comprises at least two sorbent beds, and the at least two sorbent beds rotate through each of the adsorption and desorption zones.

27. The system of claim 18 , wherein the one or more sorbent beds comprises a plurality of sorbent beds rotating in series through the adsorption zone, desorption zone, and optionally though a purge stage after the desorption zone.

28. A method for purifying a CO 2 gas stream to increase the concentration of the CO 2 in a product stream, comprising the steps of
a) preparing a sorbent bed having an inlet and an outlet,
b) passing a gas stream containing CO 2 across the sorbent bed to adsorb the CO 2 to the sorbent, and
c) recovering a CO 2 -enriched stream by passing steam across the CO 2 containing sorbent,
wherein the method does not include a pressure swing adsorption or temperature swing adsorption process, and
wherein the CO 2 is recovered by a combination of concentration swing desorption and desorptive displacement, the concentration swing desorption comprising partial pressure purge desorption and the desorptive displacement comprising a process wherein an adsorbed CO 2 molecule is displaced from the sorbent by steam during the desorption step.

29. The method of claim 28 , wherein the CO 2 is adsorbed in step b) by a concentration swing adsorption and adsorptive displacement.

30. The method of claim 28 , wherein greater than 80% by volume of the CO 2 has been recovered in the CO 2 -enriched stream.

31. The method of claim 28 , wherein greater than 85% by volume of the CO 2 has been recovered in the CO 2 -enriched stream.

32. The method of claim 28 , wherein greater than 90% by volume of the CO 2 has been recovered in the CO 2 -enriched stream.

33. A method for removing CO 2 to purify a gas stream, comprising the steps of
a) preparing a sorbent bed having an inlet and an outlet,
b) passing a gas stream containing CO 2 across the sorbent bed from inlet to outlet to adsorb

Assignees

• Exxonmobil Res & Eng Co
• Tda Research Inc

Inventors

• Elliott Jeannine Elizabeth
• Copeland Robert James
• Leta Daniel P
• Mccall Patrick P
• Bai Chuansheng
• Derites Bruce A

Classifications

• B01D2259/4065

  using eight beds · CPC title

• B01D2253/1122

  Metals · CPC title

• B01D2259/4009

  using hot gas · CPC title

• B01D2251/30

  Alkali metal compounds · CPC title

• Y02C10/08

  Cross-Sectional Technologies · mapped topic