System and method of CO
A capture vessel is provided that is configured to capture carbon dioxide (CO 2 ) according to a thermal swing adsorption (TSA) process. The capture vessel includes capture media that are configured to adsorb CO 2 from an exhaust gas during a CO 2 capture stage to produce a first N 2 gas that exits the capture vessel, receive a mixed stream of CO 2 and water vapor during a wet regeneration stage, adsorb water from the mixed stream of CO 2 and water vapor and release adsorbed CO 2 during the wet regeneration stage to produce a CO 2 stream, receive a first heated N 2 gas and release adsorbed water due to evaporation caused by the first heated N 2 gas during a drying stage, and receive a cooled gas during a cooling stage such that an absorption capacity of the capture media for CO 2 capture is increased for a next CO 2 capture stage.
1 . A method of performing a carbon dioxide (CO 2 )-thermal swing adsorption (TSA) process for carbon capture, the method comprising:
dynamically configuring a carbon capture system comprising a plurality of capture vessels, arranged in parallel, into different fluid path configurations to perform the CO 2 -TSA process,
wherein the CO 2 -TSA process includes a cyclical sequence for each capture vessel of the plurality of capture vessels, and
wherein the cyclical sequence includes a CO 2 capture stage, followed by a wet regeneration stage, followed by a drying stage, followed by a cooling stage;
performing the CO 2 capture stage for a first capture vessel of the plurality of capture vessels;
performing the wet regeneration stage for a second capture vessel of the plurality of capture vessels in parallel with the CO 2 capture stage of the first capture vessel; and
performing the drying stage for a third capture vessel of the plurality of capture vessels in parallel with the CO 2 capture stage of the first capture vessel.
2 . The method of claim 1 , further comprising:
performing the cooling stage for the third capture vessel in parallel with the CO 2 capture stage of the first capture vessel,
wherein performing the drying stage for the third capture vessel is performed during a first portion of the CO 2 capture stage of the first capture vessel,
wherein performing the cooling stage for the third capture vessel is performed during a second portion of the CO 2 capture stage of the first capture vessel, and
wherein the first portion of the CO 2 capture stage precedes the second portion of the CO 2 capture stage.
3 . The method of claim 2 , wherein performing the CO 2 capture stage for the first capture vessel in parallel with performing the cooling stage for the third capture vessel includes configuring the carbon capture system into a first fluid path configuration such that:
the first capture vessel receives an exhaust gas comprising CO 2 and nitrogen (N 2 ) and converts the exhaust gas into a first N 2 gas by adsorbing CO 2 from the exhaust gas,
the first N 2 gas is cooled via a heat exchange with a coolant to produce a cooled gas, and
the third capture vessel receives the cooled gas, wherein capture media of the third capture vessel is cooled via the cooled gas.
4 . The method of claim 3 , wherein performing the CO 2 capture stage for the first capture vessel in parallel with performing the drying stage for the third capture vessel includes configuring the carbon capture system into a second fluid path configuration such that:
the first capture vessel receives an exhaust gas comprising CO 2 and nitrogen (N 2 ) and converts the exhaust gas into a first N 2 gas by adsorbing CO 2 from the exhaust gas,
the first N 2 gas is heated via a heat exchange with a hot exhaust gas to produce a first heated N 2 gas, and
the third capture vessel receives the first heated N 2 gas, wherein capture media of the third capture vessel is dried via the first heated N 2 gas by expelling adsorbed water from the capture media of the third capture vessel via evaporation.
5 . The method of claim 1 , wherein performing the CO 2 capture stage for the first capture vessel in parallel with performing the drying stage for the third capture vessel includes configuring the carbon capture system into a first fluid path configuration such that:
the first capture vessel receives an exhaust gas comprising CO 2 and nitrogen (N 2 ) and converts the exhaust gas into a first N 2 gas by adsorbing CO 2 from the exhaust gas,
the first N 2 gas is heated via a heat exchange with a hot exhaust gas to produce a first heated N 2 gas, and
the third capture vessel receives the first heated N 2 gas, wherein capture media of the third capture vessel is dried via the first heated N 2 gas by expelling adsorbed water from the capture media of the third capture vessel via evaporation.
6 . The method of claim 5 , wherein configuring the carbon capture system into the first fluid path configuration includes recycling a portion of the first N 2 gas into a stream of the exhaust gas to dilute a CO 2 concentration of the exhaust gas.
7 . The method of claim 5 , wherein the hot exhaust gas is a source of the exhaust gas received by the first capture vessel.
8 . The method of claim 5 , wherein performing the CO 2 capture stage for the first capture vessel in parallel with performing the wet regeneration stage for the second capture vessel includes configuring the carbon capture system into a second fluid path configuration such that:
the second capture vessel produces a CO 2 stream based on a release of adsorbed CO 2 from capture media of the second capture vessel, receives a mixed stream of CO 2 and water vapor derived from the CO 2 stream, adsorbs water from the mixed stream of CO 2 and water vapor to release the adsorbed CO 2 to produce the CO 2 stream, and outputs the CO 2 stream,
wherein the adsorbed CO 2 is adsorbed by the capture media of the second capture vessel during a respective CO 2 capture stage.
9 . The method of claim 1 , wherein performing the CO 2 capture stage for the first capture vessel in parallel with performing the wet regeneration stage for the second capture vessel includes configuring the carbon capture system into a fluid path configuration such that:
the second capture vessel produces a CO 2 stream based on a release of adsorbed CO 2 from capture media of the second capture vessel, receives a mixed stream of CO 2 and water vapor derived from the CO 2 stream, adsorbs water from the mixed stream of CO 2 and water vapor to release the adsorbed CO 2 to produce the CO 2 stream, and outputs the CO 2 stream,
wherein the adsorbed CO 2 is adsorbed by the capture media of the second capture vessel during a respective CO 2 capture stage.
10 . The method of claim 9 , wherein performing the CO 2 capture stage for the first capture vessel in parallel with performing the wet regeneration stage for the second capture vessel includes adding water vapor to the CO 2 stream to produce the mixed stream of CO 2 and water vapor.
11 . The method of claim 9 , wherein performing the wet regeneration stage for the second capture vessel includes:
injecting auxiliary CO 2 into the CO 2 stream during an initial time interval of the wet regeneration stage;
siphoning off a portion of the CO 2 stream during a remaining time interval of the wet regeneration stage; and
storing the portion of the CO 2 stream for a next regeneration stage of the CO 2 -TSA process.