System and methods for CO
View Patent ↗Systems and methods for separating carbon dioxide (CO 2 ) from a gas stream are provided. The system includes a reaction chamber 20 , a pressurization unit 30 , and a desorption unit 40 . The reaction chamber 20 is configured to receive a liquid sorbent stream 14 and the gas stream 12 , to react at least a portion of CO 2 in the gas stream 12 with the liquid sorbent and form an adduct stream 22 . The pressurization unit 30 is configured to contact the adduct stream 22 with a pressurized CO 2 stream 24 and form a pressurized adduct stream 32 that includes a liquid CO 2 adduct. The desorption unit 40 is in fluid communication with the pressurization unit 30 , and is configured to decompose at least a portion of the liquid CO 2 adduct to form a CO 2 stream 42 and a regenerated liquid sorbent stream 44.
1. A method of separating carbon dioxide (CO 2 ) from a gas stream, comprising:
contacting a liquid sorbent stream with the gas stream;
reacting at least a portion of CO 2 in the gas stream with the liquid sorbent stream in a reaction chamber to form an adduct stream comprising a solid CO 2 adduct;
contacting the adduct stream with a pressurized CO 2 stream, thereby liquefying at least a portion of the solid CO 2 adduct and forming a pressurized adduct stream comprising a liquid CO 2 adduct; and
heating the pressurized adduct stream to decompose at least a portion of the liquid CO 2 adduct to form a CO 2 stream and a regenerated liquid sorbent stream.
2. The method of claim 1 , further comprising pressurizing at least a portion of the CO 2 stream in a pressurization unit the pressurized CO 2 stream, and recirculating the pressurized CO 2 stream to the pressurization unit.
3. The method of claim 1 , wherein the pressurized CO 2 stream has a pressure greater than 7 atm.
4. The method of claim 1 , further comprising pre-heating the pressurized adduct stream via heat exchange with the regenerated liquid sorbent stream to form a pre-heated pressurized adduct stream and a cooled regenerated liquid sorbent stream.
5. The method of claim 4 , further comprising recirculating at least a portion of the cooled regenerated liquid sorbent stream to the reaction chamber.
6. The method of claim 1 , wherein the liquid sorbent comprises an amino siloxane compound.
7. The method of claim 6 , wherein the amino siloxane compound has a structure of formula: (NH 2 C 3 H 6 Si(Me) 2 OSiMe 2 C 3 H 6 NH 2 ), wherein “Me” is a methyl group.
8. A method of separating carbon dioxide (CO 2 ) from a gas stream, comprising:
contacting a liquid sorbent stream with the gas stream in a reaction chamber;
reacting at least a portion of CO 2 in the gas stream with the liquid sorbent stream to form an adduct stream comprising a solid CO 2 adduct;
contacting the adduct stream with a pressurized CO 2 stream, thereby liquefying at least a portion of the solid CO 2 adduct and forming a pressurized adduct stream comprising a liquid CO 2 adduct;
pre-heating the pressurized adduct stream via heat exchange with a regenerated liquid sorbent stream to form a pre-heated pressurized adduct stream and a cooled regenerated liquid sorbent stream;
heating the pre-heated pressurized adduct stream to decompose at least a portion of the liquid CO 2 adduct to form a CO 2 stream and the regenerated liquid sorbent stream;
pressurizing at least a portion of the CO 2 stream to form the pressurized CO 2 stream and recirculating the pressurized CO 2 stream for contacting with the adduct stream; and
recirculating at least a portion of the cooled regenerated liquid sorbent stream to the reaction chamber.