IP Library Granted Patent US 8,277,769
Granted Patent B2
US 8,277,769 · App. 13/273,391 · Granted Oct 2, 2012

Process for treating carbon dioxide containing gas

Assignee: CO2 Solutions Inc.
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,277,769
App. No.
13/273,391
Granted
Oct 2, 2012
Kind
B2
Abstract

A process is disclosed for recycling carbon dioxide emissions from a fossil-fuel power plant into useful carbonated species The process primarily comprises the steps of: a) burning the fossil fuel, thereby generating heat and a hot exhaust gas containing CO 2 ; and b) converting the heat into energy. The process is characterized in that it further comprises the steps of: c) cooling the exhaust gas; and d) biologically transforming the CO 2 contained in the cooled exhaust gas into carbonated species, thereby obtaining a low CO 2 exhaust gas and producing useful carbonated species. The low CO 2 exhaust gas obtained in step d) can be released in the atmosphere without increasing the problem of greenhouse effect.

Claims (47)

1. A process comprising:

a) combustion of a fossil fuel, thereby generating heat and a hot exhaust gas containing CO 2 ;

b) converting said heat into energy;

c) cooling at least a portion of said exhaust gas to produce a cooled exhaust gas; and

d) reducing the amount of CO 2 contained in the cooled exhaust gas by biologically removing said CO 2 ; thereby obtaining a low CO 2 exhaust gas, wherein step d) comprises:

contacting an aqueous liquid phase with the cooled exhaust gas to cause at least a portion of the CO 2 to dissolve into the aqueous liquid phase and catalyzing the hydration of at least a portion of the dissolved CO 2 and producing a solution containing hydrogen ions and bicarbonate ions; and wherein said hydration is catalyzed by the enzyme carbonic anhydrase or an analogue thereof.

2. The process of claim 1 , wherein the enzyme carbonic anhydrase or the analogue thereof is free in the aqueous liquid phase.

3. The process of claim 2 , wherein in step c) the temperature to which the exhaust gas is cooled avoids a given denaturing of free carbonic anhydrase or the analogue thereof.

4. The process of claim 1 , wherein the enzyme carbonic anhydrase or the analogue thereof is immobilised on a support which is in suspension in the aqueous liquid phase.

5. The process of claim 4 , wherein in step c) the temperature to which the exhaust gas is cooled avoids a given denaturing of immobilized carbonic anhydrase.

6. The process of claim 1 , wherein the enzyme carbonic anhydrase or the analogue thereof is entrapped inside a matrix which is in suspension in the aqueous liquid phase.

7. The process of claim 1 , wherein the enzyme carbonic anhydrase or the analogue thereof is entrapped inside a matrix or immobilized on supports which are mounted within a reactor.

8. The process of claim 1 , wherein step d) comprises adding cations to the solution and adjusting the pH of the solution to precipitate a carbonated species of the cation.

9. The process of claim 8 , wherein the cations are selected from the group consisting of calcium, barium, magnesium and sodium ions.

10. A process comprising:

cooling at least a portion of a CO 2 containing gas to produce a cooled CO 2 containing gas; and

reducing the amount of CO 2 contained in the cooled CO 2 containing gas by biologically removing the CO 2 ; thereby obtaining a low CO 2 gas, comprising contacting an aqueous liquid phase with the cooled CO 2 containing gas to cause at least a portion of the CO 2 to dissolve into the aqueous liquid phase and catalyzing the hydration of at least a portion of the dissolved CO 2 and producing a solution containing hydrogen ions and bicarbonate ions; and wherein the hydration is catalyzed by the enzyme carbonic anhydrase or an analogue thereof.

11. The process of claim 10 , wherein the enzyme carbonic anhydrase or the analogue thereof is free in the aqueous liquid phase.

12. The process of claim 11 , wherein the temperature to which the exhaust gas is cooled avoids a given denaturing of free carbonic anhydrase or the analogue thereof.

13. The process of claim 10 , wherein the enzyme carbonic anhydrase or the analogue thereof is immobilised on a support which is in suspension in the aqueous liquid phase.

14. The process of claim 13 , wherein the temperature to which the exhaust gas is cooled avoids a given denaturing of immobilized carbonic anhydrase.

15. The process of claim 10 , wherein the enzyme carbonic anhydrase or the analogue thereof is entrapped inside a matrix which is in suspension in the aqueous liquid phase.

16. The process of claim 10 , wherein the enzyme carbonic anhydrase or the analogue thereof is entrapped inside a matrix or immobilized on supports which are mounted within a reactor.

17. The process of claim 10 , comprising adding cations to the solution and adjusting the pH of the solution to precipitate a carbonated species of the cation.

18. The process of claim 17 , wherein the cations are selected from the group consisting of calcium, barium, magnesium and sodium ions.

19. The process of claim 10 , wherein the CO 2 containing gas comprises hot exhaust gas generated by combustion of fossil fuel.

20. A process comprising:

pre-treating a CO 2 containing gas to remove contaminants and produce a contaminant reduced gas;

reducing the amount of CO 2 contained in the contaminant reduced gas by biologically removing the CO 2 , thereby obtaining a low CO 2 gas, comprising contacting an aqueous liquid phase with the contaminant reduced gas to cause at least a portion of the CO 2 to dissolve into the aqueous liquid phase and catalyzing the hydration of at least a portion of the dissolved CO 2 and producing a solution containing hydrogen ions and bicarbonate ions; and wherein the hydration is catalyzed by the enzyme carbonic anhydrase or an analogue thereof.

21. The process of claim 20 , wherein the contaminants removed are selected from the group consisting of ash, NO x and SO 2 .

22. The process of claim 20 , wherein the pre-treating comprises scrubbing the CO 2 containing gas.

23. The process of claim 22 , wherein the scrubbing is performed while cooling the CO 2 containing gas to produce a cooled CO 2 containing gas with a temperature sufficiently low to allow feeding directly into the step of biologically removing the CO 2 .

24. The process of claim 20 , wherein the CO 2 containing gas is cooled to a temperature sufficiently low so as to maintain a desired catalytic effect of the enzyme carbonic anhydrase or the analog thereof.

25. The process of claim 24 , wherein the temperature to which the CO 2 containing gas is cooled avoids a given denaturing of free carbonic anhydrase.

26. The process of claim 24 , wherein the temperature to which the CO 2 containing gas is cooled avoids a given denaturing of immobilized carbonic anhydrase.

27. The process of claim 20 , wherein the enzyme carbonic anhydrase or the analogue thereof is free in the aqueous liquid phase; immobilised on a support which is in suspension in the aqueous liquid phase; entrapped inside a matrix which is in suspension in the aqueous liquid phase; or entrapped inside a matrix or immobilized on supports which are mounted within a reactor.

28. The process of claim 20 , comprising adding cations to the solution and adjusting the pH of the solution to precipitate a carbonated species of the cation.

29. The process of claim 28 , wherein the cations are selected from the group consisting of calcium, barium, magnesium and sodium ions.

30. The process of claim 20 , wherein the CO 2 containing gas comprises hot exhaust gas generated by combustion of fossil fuel.

31. The process of claim 30 , wherein heat is removed from the hot exhaust gas prior to reducing the amount of CO 2 contained therein and the heat is recycled.

32. A process comprising:

generating a CO 2 containing gas;

ensuring that the CO 2 containing gas is a low temperature CO 2 containing gas having a temperature sufficiently low so as to maintain a desired catalytic effect of carbonic anhydrase or analog thereof;

reducing the amount of CO 2 contained in the low temperature CO 2 containing gas by biologically removing said CO 2 , thereby obtaining a low CO 2 gas, comprising:

contacting an aqueous liquid phase with the low temperature CO 2 containing gas to cause at least a portion of the CO 2 to dissolve into the aqueous liquid phase and catalyzing the hydration of at least a portion of the dissolved CO 2 and producing a solution containing hydrogen ions and bicarbonate ions; and wherein said hydration is catalyzed by the carbonic anhydrase or the analogue thereof.

33. The process of claim 32 , wherein the CO 2 containing gas is cooled to produce the low temperature CO 2 containing gas.

34. The process of claim 33 , wherein the CO 2 containing gas comprises hot exhaust gas generated by combustion of fossil fuel and wherein heat is removed from the hot exhaust gas in a heat exchanger to produce the low temperature CO 2 containing gas.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 2, 2020
From: CO2 SOLUTIONS INC.
To: SAIPEM S.P.A
Reel/Frame 053680/0566 →
CHANGE OF NAME Recorded May 19, 2012
From: CO2 SOLUTION INC.
To: CO2 SOLUTIONS INC.
Reel/Frame 028238/0082 →
Priority Claims (1)
CA 2405635 · Sep 27, 2002 · national
Continuity (3)
Continuation 12586857 · Sep 28, 2009
Continuation 10529168
Related Publication 20120034680A1 · Feb 9, 2012