Device and method for CO2 capture through circumscribed hollow membranes

1. A device for carbon dioxide capture, comprising:

a hollow membrane unit, comprising:

an inner conduit closed at one end, the inner conduit comprising a vapor membrane;

an outer conduit having an outside surface exposed to an atmosphere and an inside surface circumscribing the inner conduit forming a lumen between the inner conduit and the inside surface of the outer conduit, the outer conduit comprising a CO 2 pump membrane, the lumen comprising a CO 2 -rich gas and a water vapor, the water vapor being substantially saturated; and

a light-absorbing material;

a water supply in fluid communication with the inside of the inner conduit;

a mechanical pump in fluid communication with the lumen, the mechanical pump maintaining a pressure differential of at least one atmosphere between the lumen and the atmosphere and providing a product stream comprising the CO 2 -rich gas; and

a cold trap coupled to the hollow membrane unit and the mechanical pump such that the mechanical pump is in fluid communication with the lumen of the hollow membrane unit through the cold trap;

wherein the vapor membrane contains liquid water provided by the water supply, the vapor membrane being sufficiently hydrophobic and porous to contain the liquid water received while also allowing water vapor to pass through the vapor membrane into the lumen, the water vapor formed by the evaporation of the liquid water;

wherein the CO 2 pump membrane is CO 2 -permeable and wherein, as water vapor passes from the lumen to the atmosphere through the CO 2 pump membrane, a carbon concentration gradient is formed and maintained across the CO 2 pump membrane with a first concentration at the outside surface that is higher than a second concentration at the inside surface, said carbon concentration gradient actively pumping CO 2 out of the atmosphere and into the lumen; and

wherein the liquid water inside the inner conduit is heated by sunlight absorbed by the light-absorbing material to a temperature that is above an ambient temperature, thereby facilitating the evaporation of the liquid water to introduce water vapor into the lumen.

2. The device of claim 1 , wherein the mechanical pump removes CO 2 -rich gas and water vapor from within the lumen at substantially the same rate as CO 2 and water vapor are introduced to the lumen through the water vapor membrane and the CO 2 pump membranes.

3. The device of claim 1 , further comprising a plurality of hollow membrane units coupled to a manifold, the inner conduit of each hollow membrane unit in fluid communication with the water supply, the lumen of each hollow membrane unit in fluid communication with the mechanical pump through the manifold.

4. A device for carbon dioxide capture, comprising:

a hollow membrane unit, comprising:

an inner conduit closed at one end, the inner conduit comprising a vapor membrane; and

an outer conduit having an outside surface exposed to an atmosphere and an inside surface circumscribing the inner conduit forming a lumen between the inner conduit and the inside surface of the outer conduit, the outer conduit comprising a CO 2 pump membrane, the lumen comprising a CO 2 -rich gas and a water vapor;

a water supply in fluid communication with the inside of the inner conduit; and

a mechanical pump in fluid communication with the lumen, the mechanical pump maintaining a pressure differential between the lumen and the atmosphere and providing a product stream comprising the CO 2 -rich gas;

wherein the vapor membrane contains liquid water provided by the water supply, the vapor membrane being sufficiently hydrophobic and porous to contain the liquid water received while also allowing water vapor to pass through the vapor membrane into the lumen, the water vapor formed by the evaporation of the liquid water; and

wherein the CO 2 pump membrane is CO 2 -permeable and wherein, as water vapor passes from the lumen to the atmosphere through the CO 2 pump membrane, a carbon concentration gradient is formed and maintained across the CO 2 pump membrane with a first concentration at the outside surface that is higher than a second concentration at the inside surface, said carbon concentration gradient actively pumping CO 2 out of the atmosphere and into the lumen.

5. The device of claim 4 , further comprising a cold trap coupled to the hollow membrane unit and the mechanical pump such that the mechanical pump is in fluid communication with the lumen of the hollow membrane unit through the cold trap.

6. The device of claim 4 , wherein the liquid water inside the inner conduit is heated to a temperature that is above an ambient temperature, thereby facilitating the evaporation of the liquid water to introduce water vapor into the lumen.

7. The device of claim 6 , wherein the hollow membrane unit comprises a light-absorbing material and wherein the liquid water inside the inner conduit is heated by sunlight absorbed by the light-absorbing material.

8. The device of claim 4 , wherein the mechanical pump removes CO 2 -rich gas and water vapor from within the lumen at substantially the same rate as CO 2 and water vapor are introduced to the lumen through the vapor membrane and the CO 2 pump membranes.

9. The device of claim 4 , wherein the water vapor within the lumen is substantially saturated.

10. The device of claim 4 , further comprising a plurality of hollow membrane units coupled to a manifold, the inner conduit of each hollow membrane unit in fluid communication with the water supply, the lumen of each hollow membrane unit in fluid communication with the mechanical pump through the manifold.

11. A method for carbon dioxide capture, comprising:

filling an inner conduit with liquid water from a water supply in fluid communication with the inside of the inner conduit, the inner conduit comprising a vapor membrane and circumscribed within an outer conduit having an outside surface exposed to an atmosphere and an inside surface facing the inner conduit forming a lumen between the inner conduit and the inside surface of the outer conduit, the lumen running the length of the outer conduit, the outer conduit comprising a CO 2 pump membrane that is CO 2 -permeable;

introducing a water vapor into the lumen by allowing the liquid water inside the inner conduit to evaporate and pass through the vapor membrane, the vapor membrane being sufficiently hydrophobic and porous to contain the liquid water while also allowing water vapor to pass through the vapor membrane into the lumen;

forming and maintaining a carbon concentration gradient across the CO 2 pump membrane by allowing water vapor to pass from the lumen to the atmosphere through the CO 2 pump membrane, the carbon concentration gradient having a first concentration at the outside surface that is higher than a second concentration at the inside surface, said carbon concentration gradient actively pumping CO 2 out of the atmosphere and into the lumen as a CO 2 -rich gas; and

removing CO 2 -rich gas and water vapor from the lumen with a mechanical pump that is in fluid communication with the lumen, the mechanical pump maintaining a pressure differential between the lumen and the atmosphere and providing a product stream comprising the CO 2 -rich gas.

12. The method of claim 11 , further comprising substantially evacuating the lumen before introducing the water vapor into the lumen.

13. The method of claim 11 , further comprising condensing the water vapor at it is removed from the lumen with the CO 2 -rich gas, the water vapor condensed with a cold trap coupled to the lumen and the mechanical pump such that the mechanical pump is in fluid communication with the lumen of the hollow membrane unit through the cold trap.

14. The method of claim 11 , further comprising heating the liquid water to a temperature that is above an ambient temperature to facilitate the evaporation of the liquid water while inside the inner conduit to introduce water vapor into the lumen.

15. The method of claim 14 , wherein the liquid water is heated by sunlight absorbed by a light-absorbing material in thermal contact with the inner conduit.

16. The method of claim 11 , wherein the CO 2 -rich gas and water vapor is removed from within the lumen at substantially the same rate as CO 2 and water vapor are introduced to the lumen through the vapor membrane and the CO 2 pump membranes.

17. The method of claim 16 , wherein the water vapor within the lumen is substantially saturated.