System and method of CO2 thermal swing adsorption with wet regeneration and hot drying
AssigneeEnhanced Energy Group LLC
InventorPaul M. Dunn
Life of this patent
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Abstract
A carbon capture system for carbon dioxide (CO2)-thermal swing adsorption (TSA) includes an engine configured to produce a hot exhaust; a plurality of capture vessels that are configured to be respectively cycled through a plurality of stages of a CO2-TSA process; an N2 heat exchanger configured to receive the hot exhaust; and an N2 turbocharger coupled to the N2 heat exchanger. The N2 turbocharger is configured to receive N2 gas from a first capture vessel, heat the N2 gas via the N2 heat exchanger through a thermal exchange with the hot exhaust to produce a heated N2 gas, and provide the heated N2 gas to a second capture vessel in order to dry capture media of the second capture vessel.
Claims21
A carbon capture system for carbon dioxide (CO2)-thermal swing adsorption (TSA), the carbon capture system comprising:
- an engine configured to produce a hot exhaust;
- an adsorption inlet arranged downstream from the engine and configured to receive a cold exhaust comprising a mixture of CO2 and nitrogen (N2), wherein the cold exhaust is derived from the hot exhaust using one or more first heat exchangers;
- a plurality of capture vessels that are configured to be respectively cycled through a plurality of stages of a CO2-TSA process, including a CO2 capture stage, a regeneration stage, a drying stage, and a cooling stage, wherein the plurality of capture vessels are respectively coupled to the adsorption inlet for receiving the cold exhaust during the CO2 capture stage,
- wherein, while a first capture vessel of the plurality of capture vessels is configured in the drying stage, a second capture vessel of the plurality of capture vessels is configured in the CO2 capture stage, and
- wherein the second capture vessel is configured to, during the CO2 capture stage, receive the cold exhaust and absorb CO2 from the cold exhaust to produce a first N2 gas;
- an N2 heat exchanger configured to receive the hot exhaust;
- and
- an N2 turbocharger coupled to the N2 heat exchanger,
- wherein the N2 turbocharger is configured to, while the second capture vessel is configured in the CO2 capture stage and the first capture vessel is configured in the drying stage, receive the first N2 gas from the second capture vessel, heat the first N2 gas via the N2 heat exchanger through a thermal exchange with the hot exhaust to produce a first heated N2 gas, and provide the first heated N2 gas to the first capture vessel, and
- wherein, while the first capture vessel is configured in the drying stage, capture media of the first capture vessel are dried via the first heated N2 gas.
A carbon capture system for carbon dioxide (CO2)-thermal swing adsorption (TSA), the carbon capture system comprising:
- an engine configured to produce a hot exhaust;
- an adoption inlet arranged downstream from the engine and configured to receive a cold exhaust comprising a mixture of CO2 and nitrogen (N2), wherein the cold exhaust is derived from the hot exhaust using one or more first heat exchangers;
- a plurality of capture vessels that are configured to be respectively cycled through a plurality of stages of a CO2-TSA process, including a CO2 capture stage, a regeneration stage, a drying stage, and a cooling stage, wherein the plurality of capture vessels are coupled to the adoption inlet for receiving the cold exhaust during the CO2 capture stage;
- and
- a CO2 evaporative cooler configured to add water vapor to a CO2 stream,
- wherein the CO2 evaporative cooler is configured to receive the CO2 stream from a capture vessel of the plurality of capture vessels configured in the regeneration stage, add water vapor to the CO2 stream to produce a mixed stream of CO2 and water vapor, and provide the mixed stream of CO2 and water vapor to the capture vessel configured in the regeneration stage from which the CO2 stream was received.
Dependencies are inferred from the claim text.