US2010105126A1PendingUtilityA1
Method and apparatus for extracting carbon dioxide from air
Est. expiryOct 2, 2026(~0.2 yrs left)· nominal 20-yr term from priority
B01D 2257/504B01J 47/14B01D 53/62B01D 53/04B01J 41/05B01D 2253/206C12M 21/02B01D 2325/38C01B 32/50C12M 29/00Y02T50/678B01D 2252/30C12M 23/36B01D 53/047B01D 53/1493A01G 9/18B01D 2252/10A01G 9/246B01D 53/1425C12M 23/18B01D 2258/06B01D 2252/204A01G 33/00A01G 7/02B01D 53/22Y02A50/20Y02C20/40B01D 50/00B01D 53/02Y02P60/20Y02E50/30Y02P20/151
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Claims
Abstract
A method and apparatus for extracting CO 2 from air comprising an anion exchange material formed in a matrix exposed to a flow of the air, and for delivering that extracted CO 2 to controlled environments. The present invention contemplates the extraction of CO2 from air using conventional extraction methods or by using one of the extraction methods disclosed; e.g., humidity swing or electro dialysis. The present invention also provides delivery of the CO 2 to greenhouses where increased levels of CO 2 will improve conditions for growth. Alternatively, the CO 2 is fed to an algae culture.
Claims
exact text as granted — not AI-modified1 . A process for removing carbon dioxide from ambient air, comprising the steps of passing ambient air in contact with a sorbent to absorb carbon dioxide from the air, and delivering the extracted air to the interior of the greenhouse.
2 . The process of claim 1 , wherein the sorbent comprises an ion exchange resin.
3 . The process of claim 1 , wherein the sorbent has a carbon dioxide holding ability dependent on humidity.
4 . The process of claim 3 , wherein the ion exchange resin is a component of a heterogeneous ion exchange membrane.
5 . The process of claim 4 , including the step of preconditioning the ion exchange membrane by first hydrating and then drying the membrane before use.
6 . The process of claim 1 , wherein a carbon credit is generated for the carbon dioxide removed.
7 - 13 . (canceled)
14 . A method for preconditioning a humidity sensitive ion exchange heterogeneous membrane for use for carbon dioxide extraction from air comprising first hydrating and then drying the material before use.
15 . The method of claim 14 , wherein the ion exchange resin comprises a strong base Type 1 or Type 2 functionality ion exchange resin.
16 . A process for extraction of carbon dioxide from air which comprises providing a first store of a humidity sensitive sorbent,
passing the air in contact with the sorbent under a first H 2 O partial pressure whereupon carbon dioxide is absorbed on the sorbent, and raising the H 2 O partial pressure whereupon carbon dioxide is exhaled by the sorbent.
17 . The process of claim 16 , wherein the sorbent comprises a strong base Type 1 or Type 2 functionality ion exchange resin.
18 . A process for extraction of carbon dioxide from air which comprises providing a first store of a first sorbent;
passing the air in contact with the first sorbent whereupon carbon dioxide is absorbed on the first sorbent; interacting the first sorbent with a second sorbent whereupon carbon dioxide is absorbed onto the second sorbent from the first sorbent; and raising the H 2 O partial pressure whereupon carbon dioxide is exhaled by the second sorbent.
19 . The process of claim 18 , wherein the first sorbent and the second sorbent each comprise a strong base Type 1 or Type 2 functionality ion exchange resin.
20 . The process of claim 18 , wherein the first sorbent and the second sorbent are in a selectively closed loop recirculating system.
21 . An apparatus for extraction of carbon dioxide from the air comprising:
a first store of humidity sensitive sorbent; a second store of humidity sensitive sorbent, and a selectively closed loop recirculation system for selectively recirculating air through the first store and the second store.
22 . The apparatus of claim 21 , including flow valves for controlling recirculation.
23 . The apparatus of claim 21 , wherein the first store of sorbent and second store of sorbent comprise the same ion exchange resin.
24 . The apparatus of claim 23 , wherein the first store of ion exchange resin and the second store of ion exchange resin each comprise a strong base Type 1 or Type 2 functionality ion exchange resin.
25 . A process for removing carbon dioxide from ambient air, comprising the steps of absorbing carbon dioxide from ambient air using a sorbent, and releasing the carbon dioxide from the sorbent to an algae culture.
26 . The process of claim 25 , wherein the sorbent releases the carbon dioxide upon being immersed in the algae culture.
27 . The process of claim 26 , wherein the algae is subsequently immersed in a nutrient solution.
28 . The process of claim 25 , wherein the sorbent comprises a carbonate/bicarbonate brine.
29 . The process of claim 25 , wherein the carbon dioxide is released from the sorbent using an electro-dialysis process.
30 . The process of claim 25 , wherein the carbon dioxide is released from the sorbent using a gas-permeable membrane.
31 . The process of claim 25 , wherein the carbon dioxide is released from the sorbent using an anion-permeable membrane.
32 . The process of claim 25 , wherein the carbon dioxide is released from the sorbent using a humidity swing.
33 . The process of claim 25 , wherein the carbon dioxide is released from the sorbent using a humidity swing.
34 . An apparatus for removing carbon dioxide from ambient air, comprising;
a collector including a sorbent for removing carbon dioxide from air; a separation station for separating the carbon dioxide from the sorbent; and a delivery system for delivering the carbon dioxide from the extractor to a bioreactor containing algae.
35 . The apparatus of claim 34 , wherein the separation station separates the carbon dioxide from the sorbent using a humidity swing.
36 . The apparatus of claim 35 , wherein the bioreactor has a percolating mechanism for bringing the gaseous carbon dioxide released into contact with the algae culture.
37 . The apparatus of claim 35 , wherein the bioreactor has a headspace for bringing the gaseous carbon dioxide released into contact with the algae culture.
38 . The apparatus of claim 34 , wherein the sorbent is sodium carbonate which becomes sodium bicarbonate upon absorbing carbon dioxide.
39 . The apparatus of claim 38 , wherein the separation station is an electrodialytic cell having a first half-cell and a second half-cell.
40 . The apparatus of claim 39 , wherein the delivery system is configured to deliver sodium bicarbonate in substantially equal amounts to each of the first half-cell and the second half-cell.
41 . The apparatus of claim 39 , wherein the delivery system is configured to deliver sodium bicarbonate in substantially equal amounts to each of the first half-cell and the bioreactor.
42 . The apparatus of claim 39 , the first half cell and the second half cell each being divided by an anion permeable membrane
43 . The apparatus of claim 34 , wherein the separation station comprises a membrane cell.
44 . The apparatus of claim 43 , wherein the membrane cell has a gas permeable membrane.
45 . The apparatus of claim 43 , wherein the membrane cell has an anion permeable membrane.
46 . The apparatus of claim 34 , further comprising a harvester for harvesting algae.Cited by (0)
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