Carbon capture systems
AssigneeEnhanced Energy Group LLC
InventorPaul M. Dunn
Life of this patent
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Abstract
A carbon capture system can include a plurality of CO2 thermal swing adsorption (TSA) beds. The plurality of CO2 TSA beds can include at least a first TSA bed, a second TSA bed, and a third TSA bed configured to capture CO2 within a capture temperature range and to regenerate the captured CO2 at a regeneration temperature range above the capture temperature range. The carbon capture system can include a plurality of valves and associated flow paths configured to allow switching operational modes of each of the first, second, and third TSA beds.
Claims20
A carbon capture system, comprising:
- a plurality of thermal swing adsorption (TSA) beds, including at least:
- a first TSA bed configured to capture CO2 within a capture temperature range and to regenerate captured CO2 at a regeneration temperature range above the capture temperature range;
- a second TSA bed configured to capture CO2 within the capture temperature range and to regenerate captured CO2 at the regeneration temperature range;
- and
- a third TSA bed configured to capture CO2 within the capture temperature range and to regenerate captured CO2 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 CO2 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 CO2 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.
A carbon capture system, comprising:
- a plurality of thermal swing adsorption (TSA) beds that include a TSA bed configured to capture CO2 within a capture temperature range and to regenerate captured CO2 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 CO2 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 CO2 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 CO2 from the TSA bed to increase CO2 concentration in the production flow.
A method, comprising:
- capturing, using at least one of a plurality of thermal swing adsorption (TSA) beds, CO2 within a capture temperature range;
- regenerating, using at least one of the plurality of TSA beds, captured CO2 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 CO2 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 CO2 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.
Dependencies are inferred from the claim text.