Multi-stage CO2 removal system and method for processing a flue gas stream

• US 8,182,577 B2
• Filed: 10/21/2008
• Issued: 05/22/2012
• Est. Priority Date: 10/22/2007
• Status: Active Grant

• Current Assignee: General Electric Technology GmbH (GE Vernova, Inc.)
• Original Assignee: Alstom Technology Ltd. (Alstom SA)
• Inventors: Gal, Eli, Bade, Otto M., Laslo, Dennis J., Kozak, Frederic Z., Muraskin, David J., Dopatka, Jurgen
• Primary Examiner(s): Smith, Duane
• Assistant Examiner(s): Patel, Pankti
• Application Number:
  US12/255,104
• Publication Number:
  US 20090101012A1
• Time in Patent Office: 1,309 Days
• Field of Search: 952/25, 952/28
• US Class Current: 95/16
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 53/1406 Multiple stage absorption
• CPC Class Codes: B01D 53/1475 Removing carbon dioxide
• CPC Class Codes: B01D 53/50 Sulfur oxides B01D53/60 takes precedence
• CPC Class Codes: B01D 53/62 Carbon oxides
• CPC Class Codes: B01D 53/78 with gas-liquid contact
• CPC Class Codes: Y02A 50/20 Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
• CPC Class Codes: Y02C 20/40 of CO2

Abstract

An ammonia based CO2 capture system and method is provided in which multiple absorption stages are provided. Each absorption stage delivers an ionic solution at a predetermined temperature and contacts it with a flue gas stream.

Claims

1. A method for removing carbon dioxide from a flue gas stream using a series of absorption stages in which a flue gas stream is contacted with an ionic solution containing ammonia, the series of absorption stages including a first absorption stage and a last absorption stage relative to the flow direction of the flue gas stream, the method comprising:

controlling a temperature and an ammonia-to-CO2 mole ratio of the ionic solution provided to each stage in the series of absorption stages such that the ionic solution provided to the first absorption stage has a higher temperature and a lower ammonia-to-CO2 mole ratio than the ionic solution provided to the last absorption stage.

2. The method of claim 1, wherein the temperature of the ionic solution provided to first absorption stage is between 10°

C. and 20°

C.; and

the temperature of the ionic solution provided to the last absorption stage is between 0°

C. and 10°

C.

3. The method of claim 2 wherein the R of the ionic solution provided to the last absorption stage is in the range of 1.8-2.0.

4. The method of claim 3 wherein the R of the ionic solution provided to the first absorption stage is in the range of 1.4-1.8.

5. The method of claim 1, wherein the series of absorption stages includes an intermediate absorption stage, and wherein the ionic solution provided to each of the first, intermediate, and last stages has a different R value.

6. The method of claim 5, wherein the ionic solution provided to each of the first, intermediate, and last stages has a different temperature.

7. The method of claim 6, wherein the temperature of the ionic solution provided to first absorption stage is between 10°

C. and 20°

C.;

the temperature of the ionic solution provided to the last absorption stage is between 0°

C. and 10°

C.; and

the temperature of the ionic solution provided to the intermediate absorption stage is between 10°

C. and 20°

C.

8. The method of claim 7, wherein the R of the ionic solution provided to the last absorption stage is in the range of 1.8-2.0, and the R of the ionic solution provided to the first absorption stage is in the range of 1.4-1.8.

9. The method of claim 1, wherein the temperature and the R of the ionic solution provided to the first absorption stage is selected to promote the precipitation of ammonia bicarbonate solids in the first stage.

10. The method of claim 9, further comprising:

collecting the ammonia bicarbonate solids in the first stage, and

removing the collected ammonia bicarbonate solids from the first stage.

11. The method of claim 10, further comprising:

separating the removed ammonia bicarbonate solids from the ionic solution in a hydroclone.

12. The method of claim 1, wherein the series of absorption stages are contained in a single absorption vessel.

13. A system for removing carbon dioxide from a flue gas stream, the system comprising:

a series of absorption stages including a first absorption stage and a last absorption stage relative to the flow direction of the flue gas stream, each absorption stage in the series of absorption stages including;

a gas-liquid contact mass transfer device;

a liquid distribution device; and

a solution delivery path configured to deliver a supply of ionic solution to the liquid distribution device, the solution delivery path including a heat exchange device;

wherein

the solution delivery paths for the first and last absorption stages are configured to provide the first absorption stage with an ionic solution having a lower ammonia-to-CO2 mole ratio than an ammonia-to-CO2 mole ratio of the ionic solution provided to the last absorption stage.

14. The system of claim 13, wherein:

the solution delivery path of the first absorption stage is in fluid communication with a rich solution outlet of the first absorption stage, thereby providing for the flow of ionic solution from the rich solution outlet of the first absorption stage to the heat exchange device and the liquid distribution device in the first absorption stage, and

the solution delivery path of the last absorption stage is in fluid communication with the rich solution outlet of the first absorption stage, thereby providing for the flow of ionic solution from the rich solution outlet of the first absorption stage to the heat exchange device and the liquid distribution device in the last absorption stage.

15. The system of claim 14, wherein the solution delivery path of the last absorption stage is also in fluid communication with a rich solution outlet of the last absorption stage, thereby providing for the flow of ionic solution from the rich solution outlet of the last absorption stage to the heat exchange device and the liquid distribution device in the last absorption stage.

16. The system of claim 13, wherein the series of absorption stages includes an intermediate absorption stage, and the solution delivery path for the first, intermediate, and last absorption stages are configured to provide the first, intermediate, and last absorption stages with ionic solution having different R values.

17. The system of claim 16, wherein:

the solution delivery path of the first absorption stage is in fluid communication with a rich solution outlet of the first absorption stage, thereby providing for the flow of ionic solution from the rich solution outlet of the first absorption stage to the heat exchange device and the liquid distribution device of the first absorption stage,

the solution delivery path of the last absorption stage is in fluid communication with the rich solution outlet of the first absorption stage, thereby providing for the flow of ionic solution from the rich solution outlet of the first absorption stage to the heat exchange device and the liquid distribution device of the last absorption stage; and

the solution delivery path of the intermediate absorption stage is in fluid communication with a source of lean ionic solution, thereby providing for the flow of lean ionic solution from the source to the liquid distribution device of the intermediate absorption stage.

18. The system of claim 17, wherein the solution delivery path of the intermediate absorption stage is also in fluid communication with a rich solution outlet of the intermediate absorption stage, thereby providing for the flow of ionic solution from the rich solution outlet of the intermediate absorption stage to the heat exchange device and the liquid distribution device of the intermediate absorption stage.

19. The system of claim 18, wherein the solution delivery path of the last absorption stage is also in fluid communication with a rich solution outlet of the last absorption stage, thereby providing for the flow of ionic solution from the rich solution outlet of the last absorption stage to the heat exchange device and the liquid distribution device of the last absorption stage.

20. The system of claim 16, wherein the series of absorption stages are contained in a single absorption vessel.