Carbon dioxide recovery from flue gas and the like

• US 20070148069A1
• Filed: 12/23/2005
• Published: 06/28/2007
• Est. Priority Date: 12/23/2005
• Status: Abandoned Application

• Current Assignee: Praxair Technology Incorporated (Linde Plc)
• Original Assignee: Praxair Technology Incorporated (Linde Plc)
• Inventors: Chakravarti, Shrikar, Gupta, Amitabh, Burgers, Kenneth, Williams, William
• Application Number:
  US11/315,019
• Publication Number:
  US 20070148069A1
• Time in Patent Office: Days
• US Class Current: 423/220
• CPC Class Codes: B01D 53/1475 Removing carbon dioxide
• CPC Class Codes: B01D 53/1493 Selection of liquid materials for use as absorbents
• CPC Class Codes: C01B 32/50 Carbon dioxide
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02P 20/151 Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Abstract

Carbon dioxide is recovered in concentrated form from a gas feed stream also containing oxygen by absorbing carbon dioxide and oxygen into an amine solution that also contains another organic component, removing oxygen, and recovering carbon dioxide from the absorbent.

Claims

1. A method for recovering carbon dioxide from a carbon dioxide containing gas comprising:

(A) passing a feed gas comprising carbon dioxide and oxygen in countercurrent contact with an absorbent solution comprising water, an amine component, and an organic component selected from the group consisting of C₁-C₃ alkanols, ethylene glycol, ethylene glycol monomethyl ether, diethylene glycol, propylene glycol, dipropylene glycol, polyethylene glycols and polyethylene glycol ethers of the formula R⁴—

O—

(C₂H₄O)_n—

R⁵ wherein n is 3 to 12, R⁴ is hydrogen or methyl, R⁵ is hydrogen or methyl, or R⁴ is phenyl and R⁵ is hydrogen, polypropylene glycols and polypropylene glycol ethers of the formula R⁶—

O—

(C₃H₆O)_p—

R⁷ wherein n is 3 to 6, R⁶ is hydrogen or methyl, R⁷ is hydrogen or methyl, or R⁶ is phenyl and R⁷ is hydrogen, acetamide which is unsubstituted or N-substituted with one or two alkyl groups containing 1 or 2 carbon atoms, glycerol, sulfolane, dimethylsulfoxide, and mixtures thereof, and transferring carbon dioxide and oxygen from said gas into said absorbent solution to obtain a carbon dioxide and oxygen containing absorbent solution;

(B) separating oxygen from the carbon dioxide and oxygen containing absorbent solution to obtain an oxygen depleted carbon dioxide containing absorbent solution;

(C) heating the oxygen depleted carbon dioxide containing absorbent solution to obtain a heated oxygen depleted carbon dioxide containing absorbent solution; and

(D) separating carbon dioxide from the heated oxygen depleted carbon dioxide containing absorbent solution to obtain a carbon-dioxide-rich stream and a regenerated absorbent solution.

2. The method of claim 1 wherein the organic component is selected from the group consisting of ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, glycerol, and mixtures thereof.

3. The method of claim 1 wherein said amine component is selected from the group consisting of compounds of the formula NR¹R²R³ wherein R¹ is hydroxyethyl, hydroxyisopropyl, or hydroxy-n-propyl, R² is hydrogen, hydroxyethyl, hydroxyisopropyl, or hydroxy-n-propyl, and R³ is hydrogen, methyl, ethyl, hydroxyethyl, hydroxyisopropyl, or hydroxy-n-propyl, or wherein R¹ is 2-(2′

-hydroxyethoxy)-ethyl and both R² and R³ are hydrogen, and mixtures thereof.

4. The method of claim 1 wherein said amine component comprises one or more compounds selected from the group consisting of monoethanolamine, diethanolamine, diisopropanolamine, methyldiethanolamine, and triethanolamine.

5. The method of claim 1 wherein the oxygen depleted carbon dioxide containing absorbent solution is heated in step (C) by indirect heat exchange with the regenerated absorbent solution that is recovered in step (E).

6. The method of claim 1 comprising separating oxygen from the carbon dioxide and oxygen containing absorbent solution in step (B) by feeding the solution to a tank in which the pressure over the solution is subatmospheric.

7. The method of claim 1 comprising separating oxygen from the carbon dioxide and oxygen containing absorbent solution in step (B) by passing scavenging gas through the solution.

8. The method of claim 1 wherein the solution obtained in step (A) is not heated before it is subjected to step (B).

9. The method of claim 1 wherein the temperature of the solution obtained in step (A) is kept below 160°

F. before it is subjected to step (B).

10. The method of claim 1 wherein the absorbent solution obtained in step (D) is recycled to step (A) to comprise at least a portion of the absorbent solution with which feed gas is contacted in step (A).

11. The method of claim 10 wherein the organic component is selected from the group consisting of ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, glycerol, and mixtures thereof.

12. The method of claim 10 wherein said amine component is selected from the group consisting of compounds of the formula NR¹R²R³ wherein R¹ is hydroxyethyl, hydroxyisopropyl, or hydroxy-n-propyl, R² is hydrogen, hydroxyethyl, hydroxyisopropyl, or hydroxy-n-propyl, and R³ is hydrogen, methyl, ethyl, hydroxyethyl, hydroxyisopropyl, or hydroxy-n-propyl, or wherein R¹ is 2-(2′

-hydroxyethoxy)-ethyl and both R² and R³ are hydrogen, and mixtures thereof.

13. The method of claim 10 wherein said amine component comprises one or more compounds selected from the group consisting of monoethanolamine, diethanolamine, diisopropanolamine, methyldiethanolamine, and triethanolamine.

14. The method of claim 10 wherein the oxygen depleted carbon dioxide containing absorbent solution is heated in step (C) by indirect heat exchange with the regenerated absorbent solution that is recovered in step (E).

15. The method of claim 10 comprising separating oxygen from the carbon dioxide and oxygen containing absorbent solution in step (B) by feeding the solution to a tank in which the pressure over the solution is subatmospheric.

16. The method of claim 10 comprising separating oxygen from the carbon dioxide and oxygen containing absorbent solution in step (B) by passing scavenging gas through the solution.

17. The method of claim 10 wherein the solution obtained in step (A) is not heated before it is subjected to step (B).

18. The method of claim 10 wherein the temperature of the solution obtained in step (A) is kept below 160°

F. before it is subjected to step (B).