Method and system for capturing carbon dioxide and/or sulfur dioxide from gas stream

1. A system for capturing CO 2 , comprising:

(a) a first chemical reaction vessel comprising an amine and/or amino acid salt, for absorbing the CO 2 to produce an amine-COO compound and/or amino acid-COO compound in a CO 2 -containing solution;

(b) a second chemical reaction vessel comprising an aqueous alkali metal carbonate for extracting the CO 2 from the amine-COO compound and/or amino acid-COO compound in the CO 2 -containing solution to form an alkali metal bicarbonate solid and regenerate the amine and/or amino acid salt; and

(c) a third chemical reaction vessel for thermally regenerating the alkali metal carbonate from the alkali metal bicarbonate.

2. The system of claim 1 , wherein the third chemical reaction vessel further comprises an ammonium catalyst for catalyzing the aqueous alkali metal bicarbonate into the alkali metal carbonate and CO 2 gas.

3. The system of claim 2 , wherein the ammonium catalyst comprises ammonium carbonate, ammonium bicarbonate, ammonium hydroxide, or ammonium carbamate, or a mixture thereof.

4. The system of claim 1 , wherein the third chemical reaction vessel comprises low pressure steam for stripping the CO 2 gas and regenerating the solvent.

5. The system of claim 1 , further comprising a heat exchanger for facilitating energy transfer from high temperature lean solvent to low temperature rich solvent.

6. The system of claim 1 , wherein the first chemical reaction vessel further comprises a water-soluble polymer.

7. The system of claim 6 , wherein the water soluble polymer is PEG or PEI.

8. The system of claim 1 , wherein the first chemical reaction vessel further comprises a water wash system and a condense system, for collection of amine and water from a treated gas stream.

9. The system of claim 1 , wherein the second chemical reaction vessel operates at a temperature in the range of 20° C.˜100° C.

10. The system of claim 1 , wherein the second chemical reaction vessel further comprises apparatus selected from the group consisting of a unit of a rotating filter, a stationary filter, a cyclone, a hydrocyclone, and a sedimentation equipment for separation of the alkali metal bicarbonate.

11. The system of claim 1 , wherein the system is configured such that slurry coming from the second chemical reaction vessel is pumped by a peristaltic slurry pump, or a centrifugal slurry pump.

12. The system of claim 1 , wherein the second reaction vessel is placed right above the third chemical reaction vessel for slurry transfer to the third chemical reaction vessel by gravity.

13. The system of claim 1 , wherein the third chemical reaction vessel produces concentrated alkali metal carbonate solution for amine and/or amino acid regeneration.

14. The system of claim 1 , wherein the third chemical reaction vessel produces alkali metal carbonate solid, which is used for amine and/or amino acid regeneration.

15. The system of claim 1 , wherein the third chemical reaction vessel comprises a heat exchanger.

16. The system of claim 1 , wherein the system is further for capturing SO 2 .

17. The system of claim 16 , further comprising:

a SO 2 absorber comprising an amine and/or amino acid salt, wherein the amine and/or amino acid salt is capable of absorbing the SO 2 to produce a SO 2 -containing solution; and

an amine regenerator comprising an aqueous alkali metal carbonate capable of forming an alkali metal sulfite/sulfate precipitate and regenerating the amine and/or amino acid salt.

18. The system of claim 16 , further comprising: a fourth chemical reaction vessel comprising aqueous alkali metal carbonate, wherein the alkali metal carbonate is capable of absorbing the SO 2 to produce an alkali metal sulfite/sulfate precipitate and CO 2 .

19. The system of claim 1 , wherein two immiscible liquid phases form in the second chemical reaction vessel, an upper phase comprising amine solvent and a lower phase comprising alkali metal carbonate solvent.

20. The system of claim 4 , wherein the third chemical reaction vessel has a temperature in a range from about 80° C. to 200° C., and a pressure in a range from about 100 kPa to 7 MPa.

21. The system of claim 1 , wherein the amine and/or amino acid salt is sterically hindered amine.

22. The system of claim 21 , wherein the sterically hindered amine is selected from the group consisting of 2-amino-2-methyl-1-propanol (AMP), 2-amino-1,3-propandiol, 2-amino-1-propanol, 3-methylmorpholine, 2-methylpyrrolidine, 2-ethylpyrrolidine, and mixtures thereof.

23. The system of claim 1 , wherein the amine and/or amino acid salt is a secondary amine.

24. The system of claim 23 , wherein the secondary amine is selected from the group consisting of pyrrolidine, 3-methylpyrrolidine, 3-ethylpyrrolidine, 1-(2-hydroxyethyl)piperazine, 1-(2-aminoethyl)piperazine, 1-methylpiperazine, 1-ethylpiperazine, 1-butylpiperazine, 2-methylpiperazine, 2-ethylpiperazine, 2-butylpiperazine, 2-methylpiperidine, 2-ethylpiperadine, 2-butylpiperidine), and mixtures thereof.

25. The system of claim 1 , wherein the amine and/or amino acid salt is selected from the group consisting of glycine, alanine, lysine, serine, proline, piperazine-2-carboxylic acid, and mixtures thereof.

26. The system of claim 1 , wherein the amine and/or amino acid salt is selected from the group consisting of 1-(2-hydroxyethyl)piperazine, 1-(2-aminoethyl)piperazine, 1-(2-ethoxyethyl)piperazine, 1-(2-methoxyethyl)piperazine, 1-(1,3-dioxolan-2-ylmethyl)piperazine, 1-(1-methyl-4-piperidinyl)piperazine, 1-[2-(2-hydroxyethoxy)ethyl]piperazine, 1-[2-(dimethylamino)ethyl]piperazine, 1-[3-(dimethylamino)propyl]piperazine, 1-methylpiperazine, 1-ethylpiperazine, 1-butylpiperazine, 1-decylpiperazine, 1-(4-hydroxybutyl)piperazine, 1,4-bis(2-hydroxyethyl)piperazine, 1,4-bis(3-aminopropyl)piperazine, 1-amino-4-(2-hydroxyethyl)piperazine, 1-methyl-4-(1-piperidin-4-ylethyl)piperazine, 1,4-bis(methyl)piperazine, 1,4-bis(ethyl)piperazine, 1,4-bis(butyl)piperazine, and mixtures thereof.

27. The system of claim 1 , wherein the first chemical reaction vessel further comprises an absorption rate promoter.

28. The system of claim 27 , wherein the rate promoter is selected from the group consisting of piperazine, 2-amino-2-methylpropanol (AMP), diglycolamine (DGA), ethanolamine (MEA), enzyme carbonic anhydrase, piperazine-2-carboxylic acid salt, amino acid salts from the group comprising glycine, alanine, serine, glutamine, proline, lysine, arginine, or histidine, and mixtures thereof.

29. The system of claim 1 , wherein the first chemical reaction vessel further comprises an antioxidant, a corrosion inhibitor, a flocculation aid, or a mixture thereof.

30. The system of claim 1 , wherein the first chemical reaction vessel is a random packing tower, a structure packing tower, a tray tower, or a spray tower.

31. The system of claim 1 , wherein no precipitate is formed by the chemical reaction in the first chemical reaction vessel.

32. A method of capturing CO 2 from a stream of flue gas, comprising:

(a) reacting CO 2 with an amine and/or amino acid salt to produce an amine-COO and/or amino acid-COO compound in a CO 2 containing solution without forming precipitate;

(b) reacting the amine-COO and/or amino acid-COO compound with an alkali metal carbonate to thereby form an alkali metal bicarbonate precipitate and regenerate the amine and/or amino acid salt in a two-immiscible-aqueous-phase system; and

(c) reacting the alkali metal bicarbonate precipitate in a thermal regeneration reaction to thereby regenerate the alkali metal carbonate and release CO 2 .

33. The method of claim 32 , wherein the reaction in operation (c) comprises reacting the alkali metal bicarbonate with an ammonium-based catalyst.

34. The method of claim 32 , wherein the reaction in operation (a) occurs in a first reaction vessel and operation (b) occurs in a second reaction vessel, and wherein amine and/or amino acid salt regenerated in the second reaction vessel is recycled back to the first reaction vessel.

35. The system of claim 17 , further comprising a fourth reaction vessel for precipitating out the alkali metal sulfite/sulfate precipitate.

36. The system of claim 19 , wherein the upper amine solvent phase is fed to the first chemical reaction vessel, and the lower alkali metal carbonate solvent phase is fed to a fourth chemical reaction vessel for absorbing SO 2 to produce an alkali metal sulfite/sulfate precipitate and CO 2 .