METHOD AND APPARATUS FOR EXTRACTING CARBON DIOXIDE FROM AIR

• US 20110203174A1
• Filed: 08/11/2009
• Published: 08/25/2011
• Est. Priority Date: 08/11/2008
• Status: Abandoned Application

• Current Assignee: Carbon Sink, Inc.
• Original Assignee: Carbon Sink, Inc.
• Inventors: Lackner, Klaus S.
• Application Number:
  US13/058,812
• Publication Number:
  US 20110203174A1
• Time in Patent Office: Days
• US Class Current: 47/58.1R
• CPC Class Codes: A01G 7/02 Treatment of plants with carbon dioxide
• CPC Class Codes: A01G 9/18 Greenhouses for treating plants with carbon dioxide or the like
• CPC Class Codes: B01D 2256/22 Carbon dioxide
• CPC Class Codes: B01D 53/04 with stationary adsorbents B01D53/025 takes precedence
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02P 60/20 Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2

Abstract

A method and apparatus for extracting CO₂ from air, and for delivering that extracted CO₂ to controlled environments, such as a greenhouse, or to open-air agricultural fields. The present disclosure allows the delivery of CO₂ to be made at times of highest demand. The present disclosure contemplates several geometric configurations to enhance the CO₂ extraction process. The present disclosure also provides a method of delivering the CO₂ to the controlled environment in response to demand, such as for example, by using a secondary sorbent as a buffer to store extracted CO₂.

Claims

1. A process for removing carbon dioxide from air, comprising passing ambient air in contact with a sorbent to absorb carbon dioxide from the air, delivering the carbon dioxide to a controlled environment, and removing excess carbon dioxide from an exhaust stream exiting the controlled environment.

2. The process of claim 1, wherein removing excess carbon dioxide from an exhaust stream includes passing the exhaust through a heat exchange loop, the heat exchange loop comprising cooling the exhaust to condense moisture from the exhaust in a first part of the loop, using heat from the first part of the loop to reheat the dry exhaust in a second part of the loop, and bringing the exhaust in contact with a sorbent to absorb carbon dioxide from the exhaust.

3. An apparatus for adding carbon dioxide to a controlled environment, comprising an extractor for extracting carbon dioxide from ambient air outside of the controlled environment and delivering the carbon dioxide into the controlled environment, wherein the extractor further comprises an ion exchange material in a solid frame that forms a partial enclosure having at least two openings to allow air to enter and exit the extractor.

4. The apparatus of claim 3, wherein the frame comprises a plurality of horizontal containers having baffled openings at each end.

5. The apparatus of claim 3, wherein the solid frame comprises a tower, and wherein the at least two openings include baffles, at least one of the openings being located in an upper portion of the tower and at least one of the openings is located in a lower portion of the tower, the ion exchange material being located between said upper portion and said lower portion.

6. The apparatus of claim 5, wherein air flow through the tower is characterized by one of the following:

(a) wherein the air flow through the tower is driven in an upward vertical direction by pressure differences between the upper and lower portions of the tower;

(b) wherein air flow through the tower is driven in an upward vertical direction by solar heat which impinges on the sides of the tower to heat the air as it rises through the tower;

(c) wherein moisture is added to the air having an evaporative cooling effect, and thereby driving the air in a downward vertical direction; and

wherein the tower includes one or more fans for driving the air through the tower.

7. The apparatus of claim 5, wherein the tower is connected to the controlled environment by a set of pipes.

8. An apparatus for adding carbon dioxide to a controlled environment which comprises an extractor for extracting carbon dioxide from air outside of the controlled environment and delivering the extracted carbon dioxide into the controlled environment, wherein the extractor includes a plurality of moveable filters comprised of a carbon dioxide capture material that are placed in contact with ambient air to capture carbon dioxide and moved on a track into an enclosure to release the extracted carbon dioxide.

9. The apparatus of claim 8, wherein the air inside the controlled environment has a greater absolute humidity than the air outside the controlled environment, and further including a device for moving the moveable filters into or adjacent to the controlled environment to release carbon dioxide into the controlled environment.

10. The apparatus of claim 8, wherein the moveable filters are attached to the track.

11. The apparatus of claim 8, wherein the filters are placed on a moveable wheel that turns with the prevailing wind to optimize the flow of ambient air over the filters.

12. A method for delivering carbon dioxide to a controlled environment, comprising capturing carbon dioxide from ambient air using a plurality of moveable filters, the moveable filters having a strong humidity function;

storing the filters until needed; and

exposing the moveable filters to warm, humid air of the controlled environment to release the carbon dioxide when desired.

13. A process for removing carbon dioxide from ambient air and for delivering carbon dioxide to a controlled environment wherein the temperature of the ambient air is substantially lower than the air within the controlled environment to which the carbon dioxide is to be delivered, comprising the steps of heating the ambient air, passing the heated air in contact with a sorbent to absorb carbon dioxide from the air, and delivering the carbon dioxide to a controlled environment.

14. The process of claim 13, wherein the carbon dioxide is delivered to the controlled environment by placing the sorbent in contact within the controlled environment, whereupon the sorbent releases the carbon dioxide as a result of a humidity swing.

15. The process of claim 13, further comprising the step of removing excess carbon dioxide from an exhaust stream exiting the controlled environment.

16. The process of claim 14, further comprising recovering some of the heat from the resin as it leaves the controlled environment.

17. An apparatus for managing heat in a controlled environment without producing excess carbon dioxide, comprising at least two thermally insulated reservoirs located adjacent to the controlled environment, wherein a first reservoir is maintained at an elevated temperature and a second reservoir is maintained at a lower temperature.

18. The apparatus of claim 17, wherein the first reservoir is maintained at or near a temperature comparable to the day time high temperature of ambient air, and wherein the second reservoir is maintained at or near a temperature comparable to the night time low temperature of ambient air.

19. The apparatus of claim 17, further comprising one or more pipes for carrying a heat exchange fluid between the reservoirs, and at least one pump for circulating the heat exchange fluid in the pipes.

20. The apparatus of claim 17, wherein the reservoirs contain either water or a eutectic solution.

21. A process for capturing carbon dioxide and delivering the captured carbon dioxide to a controlled environment, comprising the steps of capturing carbon dioxide from the air of a livestock facility and delivering the captured carbon dioxide to a controlled environment.

22. A method for managing a carbon dioxide level in a controlled environment, comprising using a primary sorbent to collect carbon dioxide, transferring at least a part of the collected carbon dioxide to a secondary sorbent, storing the collected carbon dioxide in the secondary sorbent, and releasing the stored carbon dioxide as desired for operation of the controlled environment.

23. The method of claim 22, wherein the secondary sorbent undergoes a load swing depending on a concentration of carbon dioxide.

24. The method of claim 23, wherein the secondary sorbent undergoes a load swing between carbon dioxide concentrations of 0.1% and 10%.

25. The method of claim 22, wherein the secondary sorbent is selected from a group consisting of:

a carbonate brine, a liquid amine, a zeolite, activated carbon, and a non-engineered sorbent.

26. The method of claim 22, wherein the secondary sorbent is used to regenerate the primary sorbent directly.

27. The method of claim 22, wherein the secondary sorbent is maintained near 35°

C.

28. The method of claim 22, wherein the carbon dioxide is transferred directly from the primary sorbent to the controlled environment at times of highest demand.

29. The method of claim 22, wherein the secondary sorbent is heated to aid in release of carbon dioxide to the controlled environment.

30. An apparatus for managing the level of carbon dioxide in a controlled environment, comprising:

a primary sorbent for capturing carbon dioxide from an air stream;

an enclosure in which carbon dioxide from the primary sorbent may be released;

at least two gas-liquid interfaces for recapturing the carbon dioxide on a secondary sorbent; and

at least one container for storing the secondary sorbent.

31. A method for carbon dioxide fertilization of open agricultural fields, comprising capturing carbon dioxide from air adjacent the field and releasing the carbon dioxide in a manner that will raise the carbon dioxide concentration near the plants in the field.

32. The method of claim 31, wherein the capture of carbon dioxide is captured at a time when the plants on the field are not photosynthetically active.

33. The method of claim 31, wherein the carbon dioxide is captured downwind from the field to be fertilized.

34. The method of claim 33, wherein the collectors are moved upwind prior to be transformed into carbon dioxide releasing units.

35. The method of claim 34, where the collectors are installed on a track.

36. The method of claim 34 where the collectors are truck mounted.

37. The method of claim 33, wherein the collectors use the captured carbon dioxide to enrich a gas stream that is pumped upstream and released at locations in the field that can be optimized with regard to carbon dioxide retention in the field and carbon dioxide exposure of the plants.

38. The method of claim 31, where the capture medium is sensitive to a humidity or moisture swing and releases carbon dioxide if brought in contact with excess moisture.

39. The method of claim 38, where humidity or moisture is provided from the field'"'"'s irrigation supply.

40. The method of claim 38, where the humidity or moisture is provided from stored rain water.

41. The method of claim 38, wherein recovery from the humidity swing is accelerated using solar heat to dry the capture medium.

42. The method of claim 31, where the capture medium is heat sensitive and carbon dioxide is released by exposing the material to elevated temperatures.

43. The method of claim 42, wherein the temperature swing is partially or completely brought about with solar heat that increases the temperature during the release cycle.

44. The method of claim 42, wherein the temperature swing is at least partially brought about by evaporative cooling during an uptake phase of the collecting unit.

45. The method of claim 31, wherein the carbon dioxide release is accomplished at the capture site and the carbon dioxide enriched gas is pumped upstream of the field prior to its distribution.

46. A method for determining the amount of fossil carbon that has been incorporated into a controlled environment containing plants, comprising measuring the carbon-14 content of the plants.

47. The method of claim 46, wherein the controlled environment is a greenhouse.

48. The method of claim 47, wherein the atmosphere in the greenhouse is enriched at least in part with carbon dioxide from the burning of fossil fuels.

49. The method of claim 48, wherein the atmosphere is further enriched with carbon dioxide from an air capture device.