IP Library › Granted Patent US 12,194,411
Granted Patent B2
US 12,194,411 · App. 17/193,381 · Granted Jan 14, 2025

Acidic gas absorbent, acidic gas removal method and acidic gas removal apparatus

Inventors: Akiko Suzuki (Ota, JP); Yoshihiko Nakano (Yokohama, JP); Reiko Yoshimura (Kawasaki, JP); Asato Kondo (Yokohama, JP); Kenji Sano (Inagi, JP); Toshihiro Imada (Kawasaki, JP); Shinji Murai (Sagamihara, JP); Mitsuru Udatsu (Kawasaki, JP)
Assignees: KABUSHIKI KAISHA TOSHIBA; TOSHIBA ENERGY SYSTEMS & SOLUTIONS CORPORATION
B01D53/1493B01D53/1425B01D53/1475B01D53/18B01D53/62B01D53/78B01D2252/20405B01D2252/20431B01D2252/20489B01D2252/60B01D2257/504
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Quick Facts
Patent No.
US 12,194,411
App. No.
17/193,381
Granted
Jan 14, 2025
Kind
B2
Abstract

The embodiments provide an acidic gas absorbent having low diffusibility, an acidic gas removal method employing the acidic gas absorbent, and also an acidic gas removal apparatus employing the absorbent. The acidic gas absorbent according to the embodiment comprises: a particular tertiary amine compound, such as, an alkyl dialkanol amine or a hydroxyalkyl piperazine; a halogen-free ionic surfactant; and an aqueous solvent. The embodiments provide not only the acidic gas absorbent but also an acidic gas removal method and apparatus employing the acidic gas absorbent.

Claims (68)

1. An acidic gas absorbent suitable for absorbing carbon dioxide, comprising:

an aqueous solvent;

a halogen-free ionic surfactant; and

an amine compound comprising

a first amine compound selected from the group consisting of (1-1) to (1-8):

 and/or

a second amine compound selected from the group consisting of (2-1) to (2-6):

wherein the halogen-free ionic surfactant is present in a range of from 0.1 to 40 ppm, based on total acidic gas absorbent weight,

wherein the halogen-free ionic surfactant has an ionic group selected from the group consisting of carboxy group, sulfo group, phosphate group, amino group, and ammonium group,

wherein the amine compound is present in a range of from 5 to 75 wt. %, based on the total acidic gas absorbent weight, and

wherein a sum of the first and the second amine compound is in a range of from 10 to 100 wt. % of total amine compound.

2. The acidic gas absorbent of claim 1 , which has a surface tension of 40 mN/m or more at 25° C. before carbon dioxide is introduced thereinto.

3. The acidic gas absorbent of claim 1 , which has a viscosity of 1 to 200 mPa·s at 25° C.

4. An acidic gas removal method, comprising:

contacting an acidic gas-containing gas with the acidic gas absorbent of claim 1 so as to remove acidic gas from the acidic gas-containing gas.

5. The acidic gas absorbent of claim 1 , wherein the amine compound has any one of formula (1-1) to (1-8).

6. The acidic gas absorbent of claim 1 , wherein the amine compound has any one of formula (2-1) to (2-6).

7. The acidic gas absorbent of claim 1 , wherein the halogen-free ionic surfactant is present in a range of from 0.1 to 30 ppm, based on the total acidic gas absorbent.

8. The acidic gas absorbent of claim 1 , wherein the halogen-free ionic surfactant is present in a range of from 2 to 20 ppm, based on the total acidic gas absorbent.

9. The method of claim 4 , wherein the acidic gas is CO 2 .

10. The acidic gas absorbent of claim 1 , wherein the sum of the first and the second amine compound is in a range of from 30 to 75 wt. % of the amine compound.

11. The acidic gas absorbent of claim 1 , wherein the amine compound consists of the first and the second amine compound.

12. The acidic gas absorbent of claim 1 , which has a surface tension in a range of from 40 to 66 mN/m at 25° C. before carbon dioxide is introduced thereinto.

13. An adsorbent system solution, comprising:

the acidic gas absorbent of claim 1 ; and

industrial exhaust fumes of CO 2 gas.

14. The acidic gas absorbent of claim 1 , wherein the amine compound is present in a range of from 45 to 75 wt. %, based on the total acidic gas absorbent weight.

15. The acidic gas absorbent of claim 1 , wherein the acidic gas absorbent does not comprise a metal or comprise solely sodium as metal.

16. The acidic gas absorbent of claim 1 , wherein the acidic gas absorbent does not comprise a nonionic surfactant.

17. An acidic gas absorbent suitable for absorbing carbon dioxide, the absorbent consisting of:

at least one aqueous solvent having no more than 1 wt. % of organic compound(s);

at least one halogen-free ionic surfactant; and

optionally, an oxidation inhibitor in a range of from 0.01 to 1 wt. %, which is at least one selected from the group consisting of dibutylhydroxytoluene, butylhydroxyanisole, sodium erythorbate, sodium nitrite, sulfur dioxide, 2-mercaptoimidazole and 2-mercaptobenzimidazole;

optionally, a defoaming agent in a range of from 0.00001 to 0.001 wt. %, which is at least one selected from the group consisting of silicone defoaming agent and an organic defoaming agent;

optionally, an anticorrosive agent in a range of from 0.00003 to 0.0008 wt. %, which is at least one selected from the group consisting of a phosphate ester, a tolyltriazole, and a benzotriazole; and

at least one amine compound selected from the group consisting of a first amine compound of formula (1), and a second amine compound of formula (2):

wherein

each R 1a is independently H, a C 1 to C 3 alkyl group, a C 1 to C 3 hydroxyalkyl group a C 1 to C 3 aminoalkyl group, or a C 2 to C 5 alkylaminoalkyl group,

each R 1b is independently H or a C 1 to C 3 alkyl group, and

each R 2 is independently H, a C 1 to C 3 alkyl group, or a C 1 to C 3 hydroxyalkyl group, provided that at least one R 2 is a C 1 to C 3 hydroxyalkyl group,

wherein the acidic gas absorbent does not comprise a metal or comprise solely sodium as metal,

wherein the halogen-free ionic surfactant is present in a range of from 0.1 to 40 ppm, based on total acidic gas absorbent weight, and

wherein the at least one amine compound is present in at least 45 wt. %, based on the total acidic gas absorbent weight.

18. The acidic gas absorbent of claim 17 , wherein the amine compound is present in a range of from 50 to 75 wt. %, based on the total acidic gas absorbent,

wherein the halogen-free ionic surfactant is present in a range of from 0.1 to 30 ppm, based on the total acidic gas absorbent,

wherein the solvent consists of water, and

wherein the at least one amine compound is at least one selected from the group consisting of:

19. An adsorbent system solution, comprising:

the acidic gas absorbent of claim 18 ; and

industrial exhaust fumes of CO 2 gas dissolved in the aqueous solvent.

20. An acidic gas absorbent suitable for absorbing carbon dioxide, comprising:

an aqueous solvent;

a halogen-free ionic surfactant; and

an amine compound comprising a first amine compound of formula (1) and/or a second amine compound of formula (2):

wherein

each R 1a is independently H, a C 1 to C 3 alkyl group, a C 1 to C 3 hydroxyalkyl group a C 1 to C 3 aminoalkyl group, or a C 2 to C 5 alkylaminoalkyl group,

each R 1b is independently H or a C 1 to C 3 alkyl group, and

each R 2 is independently H, a C 1 to C 3 alkyl group, or a C 1 to C 3 hydroxyalkyl group, provided that at least one R 2 is a C 1 to C 3 hydroxyalkyl group,

wherein the halogen-free ionic surfactant is present in a range of from 0.1 to 40 ppm, based on total acidic gas absorbent weight,

wherein the halogen-free ionic surfactant has an ionic group selected from the group consisting of carboxy group, sulfo group, phosphate group, amino group, and ammonium group,

wherein the amine compound is present in a range of from 3 to 80 wt. %, based on the total acidic gas absorbent weight, and

wherein a sum of the first and second amine compound are in a range of from 10 to 100 wt. % of the amine compound, and

wherein (i) the acidic gas absorbent does not comprise a metal or comprise solely sodium as metal and/or (ii) the acidic gas absorbent does not comprise a nonionic surfactant.

21. The acidic gas absorbent of claim 20 , wherein (i) the acidic gas absorbent does not comprise a metal or comprises solely sodium as metal.

22. The acidic gas absorbent of claim 20 , wherein (ii) the acidic gas absorbent does not comprise a nonionic surfactant.

23. The acidic gas absorbent of claim 17 , wherein the amine compound is the second amine compound of formula (2).

24. The acidic gas absorbent of claim 18 , wherein the amine compound has any of formula (2-1) to (2-6).

25. The acidic gas absorbent of claim 20 , wherein the amine compound is the second amine compound of formula (2).

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 13, 2022
From: SUZUKI, AKIKO; NAKANO, YOSHIHIKO; YOSHIMURA, REIKO; KONDO, ASATO; SANO, KENJI; IMADA, TOSHIHIRO; MURAI, SHINJI; UDATSU, MITSURU
To: KABUSHIKI KAISHA TOSHIBA; TOSHIBA ENERGY SYSTEMS & SOLUTIONS CORPORATION
Reel/Frame 058638/0701 →
Priority Claims (1)
JP 2020-154852 · Sep 15, 2020 · national
Continuity (1)
Related Publication 20220080348A1 · Mar 17, 2022
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