Carbon capture systems

1. A carbon capture system, comprising:

a plurality of thermal swing adsorption (TSA) beds, including at least:

a first TSA bed configured to capture CO 2 within a capture temperature range and to regenerate captured CO 2 at a regeneration temperature range above the capture temperature range;

a second TSA bed configured to capture CO 2 within the capture temperature range and to regenerate captured CO 2 at the regeneration temperature range; and

a third TSA bed configured to capture CO 2 within the capture temperature range and to regenerate captured CO 2 at the regeneration temperature range above the capture temperature range;

a plurality of valves and associated flow paths configured to allow switching operational modes of each of the first TSA bed, the second TSA bed, and the third TSA bed; and

a control module configured to control the plurality of valves to provide continuous operation such that, simultaneously, at least one of the plurality of TSA beds is operated in a capture mode to remove CO 2 from an exhaust flow and to output a nitrogen flow, at least one of the plurality of TSA beds is used in a heated regeneration mode to release CO 2 into a production flow, and at least one of the one of the plurality of TSA beds is operated in a cooling mode to be cooled by a cooling flow.

2. The carbon capture system of claim 1 , wherein the carbon capture system is configured to be connected to a semi-closed cycle engine system to receive engine exhaust therefrom.

3. The carbon capture system of claim 1 , further comprising:

a production stream circulator subsystem selectively connected to each TSA bed and configured to circulate the production flow through a respective TSA bed in regeneration mode to regenerate additional CO2 from the TSA bed to increase CO2 concentration in the production flow.

4. The carbon capture system of claim 3 , wherein the production stream circulator subsystem includes a heat source configured to add heat to the production flow sufficient to heat the respective TSA bed operated in regeneration mode to within the regeneration temperature range.

5. The carbon capture system of claim 3 , wherein the production stream circulator subsystem includes a motive source configured to move the production flow within the production stream circulator subsystem.

6. The carbon capture system of claim 3 , wherein the production stream circulator subsystem is in fluid communication with a CO 2 output subsystem.

7. The carbon capture system of claim 3 ,

wherein the production stream circulator subsystem includes a heat source and a motive source,

wherein the heat source is a waste heat exchanger configured to be in thermal communication with the exhaust flow downstream of an engine,

wherein the motive source is a compressor connected to a turbine, and

wherein the waste heat exchanger is in fluid communication between the compressor and the turbine such that waste heat drives the turbine to power the compressor.

8. The carbon capture system of claim 1 , further comprising:

a flow mover configured to provide motive flow to the exhaust flow to flow through the carbon capture system to a respective TSA bed operated in the capture mode.

9. The carbon capture system of claim 8 , further comprising:

a dehydration subsystem downstream of the flow mover and upstream of at least one of the first TSA bed, the second TSA bed, or the third TSA bed to remove water upstream of at least one of the first TSA bed, the second TSA bed, or the third TSA bed operating in the capture mode.

10. The carbon capture system of claim 9 ,

wherein the dehydration subsystem includes at least two dehydration TSAs and associated valves,

wherein the at least two dehydration TSAs include a first dehydration TSA and a second dehydration TSA, and

wherein the control module is further configured to operate the at least two dehydration TSAs such that the first dehydration TSA is operated in a water capture mode to output dry exhaust to at least one of the plurality of TSA beds and the second dehydration TSA is operated in a water regeneration mode using the nitrogen flow from the plurality of TSA beds that has been heated or in a cooling mode using the nitrogen flow from the plurality of TSA beds that has been cooled.

11. The carbon capture system of claim 1 , further comprising:

a dehydration subsystem integrated with each of the first TSA bed, the second TSA bed, and the third TSA to remove water and CO 2 in same location.

12. The carbon capture system of claim 1 , further comprising:

a nitrogen recirculation system having a nitrogen flow mover configured to recirculate nitrogen output by a respective TSA bed in the capture mode in order to increase cooling effect of the first TSA bed, the second TSA bed, and the third TSA bed when operated in the cooling mode.

13. The carbon capture system of claim 1 , further comprising:

a dehydration subsystem downstream of at least one of the first TSA bed, the second TSA bed, or the third TSA bed when operated in production mode to remove water downstream of at least one of the first TSA bed, the second TSA bed, or the third TSA bed operating in the production mode.

14. A carbon capture system, comprising:

a plurality of thermal swing adsorption (TSA) beds that include a TSA bed configured to capture CO 2 within a capture temperature range and to regenerate captured CO 2 at a regeneration temperature range above the capture temperature range;

a control module configured to control switching operational modes, associated with flow paths, such that, simultaneously, at least one of the plurality of TSA beds is operated in a capture mode to remove CO 2 from an exhaust flow and to output a nitrogen flow, at least one of the plurality of TSA beds is used in a heated regeneration mode to release CO 2 into a production flow, and at least one of the one of the plurality of TSA beds is operated in a cooling mode to be cooled by a cooling flow; and

a production stream circulator subsystem selectively connected to the TSA bed and configured to circulate the production flow to regenerate additional CO 2 from the TSA bed to increase CO 2 concentration in the production flow.

15. The carbon capture system of claim 14 , wherein the production stream circulator subsystem includes a heat source configured to add heat to the production flow sufficient to heat the TSA bed to within the regeneration temperature range.

16. The carbon capture system of claim 14 , wherein the production stream circulator subsystem includes a motive source configured to move the production flow within the production stream circulator subsystem.

17. The carbon capture system of claim 14 , wherein the production stream circulator subsystem is in fluid communication with a CO 2 output subsystem.

18. A method, comprising:

capturing, using at least one of a plurality of thermal swing adsorption (TSA) beds, CO 2 within a capture temperature range;

regenerating, using at least one of the plurality of TSA beds, captured CO 2 at a regeneration temperature range above the capture temperature range; and

controlling a plurality of valves and associated flow paths to provide continuous operation such that, simultaneously, at least one of the plurality of TSA beds is operated in a capture mode to remove CO 2 from an exhaust flow and to output a nitrogen flow, at least one of the plurality of TSA beds is used in a heated regeneration mode to release CO 2 into a production flow, and at least one of the one of the plurality of TSA beds is operated in a cooling mode to be cooled by a cooling flow.

19. The method of claim 18 , further comprising,

using engine waste heat to heat the production flow and to provide motive force to the production flow.

20. The method of claim 18 , further comprising:

circulating the production flow through a TSA bed, of the plurality of TSA beds, in regeneration mode to regenerate additional CO2 from the TSA bed to increase CO2 concentration in the production flow.