Concurrent O
A device for the concurrent oxygen generation and control of carbon dioxide for life support system involves two stages, where a first stage removes CO 2 from an exhalent side of a ventilation loop and a second stage employs Ceramic Oxygen Generators (COGs) to convert CO 2 into carbon and O 2 . The first stage includes a plurality of chambers and means to switch the ventilation loop through at least one of the chambers, where CO 2 removal is carried out before discharge of the CO 2 depleted gas to an inhalant side of the ventilation loop, and to exclude the ventilation loop from the remaining chambers of the first stage, where these chambers are placed in communication with the second stage. The second stage has two portions separated by the COGs such that CO 2 and the formed carbon remain on an intake portion from the O 2 rich atmosphere on the exhaust side, which is plumbed via a metering valve to introduce the O 2 rich atmosphere to the inhalant side of the ventilation loop.
1. A device for continuous conversion of CO 2 to O 2 providing a breathable atmosphere, comprising:
at least one first stage comprising at least one inlet, at least one outlet, a plurality of sorption bed chambers, each chamber comprising at least one CO 2 sorption bed, a means to direct a gas flow to and from said chambers, and a means to actuate said means to direct; and
at least one second stage comprising at least one ceramic oxygen generator (COG) unit comprising a catalytic carbon deposition layer (CCDL) on a cathode of said COG, at least one CO 2 intake, at least one O 2 exhaust, and a means to control said exhaust from said second stage into said outlet of said first stage.
2. The device of claim 1 , wherein said means to direct said gas flow comprises a first valve between said inlet and said bed and a second valve between said bed and said outlet, wherein when said first valve is in an open position said gas flow is directed to said chamber and said second valve is positioned to direct said gas flow to said outlet, and wherein when said first valve is in a closed position said gas flow is restricted from said chamber and said second valve is positioned to provide communication between said chamber and said intake of said second stage.
3. The device of claim 1 , wherein said means to control said exhaust comprises a metering valve.
4. The device of claim 1 , further comprising at least one CO 2 sensor in said outlet or at least one CO 2 sensor in each of said chambers, wherein said sensor provides a signal to each of said means to actuate when a level of CO 2 in said gas flow exceeds a predetermined level of CO 2 wherein said first and second valves of said plurality of said chambers are positioned to direct said gas flow to at least one, but not all, of said chambers and restrict gas flow to all other of said chambers.
5. The device of claim 1 , further comprising at least one CO sensor in said second stage wherein said sensor provides a signal to an alarm when a predetermined level of CO is exceeded.
6. The device of claim 1 , wherein said CCDL further comprises metal containing particles on a support.
7. The device of claim 1 , wherein said CCDL further comprises metal containing particles on a support, wherein said metal comprises Fe, Ni, Co, alloys thereof, or oxides thereof.
8. The device of claim 1 , wherein said CCDL further comprises metal containing particles on a support, wherein said metal comprises Fe, Ni, Co, alloys thereof, or oxides thereof, and wherein said particles are from about 10 to about 50 nm in size.
9. The device of claim 1 , wherein said CCDL further comprises metal containing particles on a support, wherein said support is a Ni comprising wire mesh or a SiO 2 comprising fiber cloth.
10. The device of claim 1 , wherein said bed comprises polyethyleneimine deposited on mesoporous molecular sieves.
11. The device of claim 1 , further comprising one or more heat exchangers.
12. A method of providing a breathable gas for life support, comprising the steps of:
adsorbing CO 2 from an exhaled gas flow in at least one first stage of a device, wherein said first stage comprises at least one inlet, at least one outlet, a plurality of sorption bed chambers, each chamber comprising at least one CO 2 sorption bed where said gas is depleted of CO 2 , a means to direct a gas flow to and from said chambers or restrict flow from said chamber and place said chamber into communication with at least one second stage, and a means to actuate said means to direct;
directing said CO 2 depleted gas from said chamber to an inhalable gas flow;
converting said CO 2 to C and O 2 in said second stages of said device, wherein said second stage comprises at least one ceramic oxygen generator (COG) units comprising a catalytic carbon deposition layer (CCDL) on a cathode of said COG, at least one CO 2 intake, at least one O 2 exhaust, and a means to control said exhaust from said second stage; and
directing said O 2 from said exhaust to said inhalable gas flow.
13. The method of claim 12 , wherein said means to direct said gas flow comprises a first valve between said inlet and said bed and a second valve between said bed and said outlet, wherein when said first valve is in an open position to direct said gas flow to said bed and said second valve is positioned to direct said gas flow to said outlet, and wherein when said first valve is in a closed position, restricts said gas flow to said bed and said second valve is positioned to provide communication between said chamber and said intake of said second stage.
14. The method of claim 12 , wherein said means to control said exhaust comprises a metering valve.
15. The method of claim 12 , wherein said first stage further comprises at least one CO 2 sensor in said outlet or at least one CO 2 sensor in each of said chambers, wherein said sensor provides a signal to each of said means to actuate when the level of CO 2 in said gas flow exceeds a predetermined level of CO 2 wherein said first and second valves of said plurality of said chambers are positioned to direct said gas flow to at least one, but not all, of said chambers and restrict gas flow to all other of said chambers.
16. The method of claim 12 , wherein said second stage further comprises at least one CO sensor in said second stage wherein said sensor provides a signal to an alarm when a predetermined level of CO is exceeded.
17. The method of claim 12 , wherein said CCDL further comprises metal containing particles on a support.
18. The method of claim 12 , wherein said CCDL further comprises metal containing particles on a support, and wherein said metal particles comprise Fe, Ni, Co, alloys thereof, or oxides thereof.
19. The method of claim 12 , wherein said CCDL further comprises metal containing particles on a support, and wherein said metal particles comprise Fe, Ni, Co, alloys thereof, or oxides thereof, and wherein said particles are from about 10 to about 50 nm in size.
20. The method of claim 12 , wherein said CCDL further comprises metal containing particles on a support, and wherein said support is a Ni comprising wire mesh or a SiO 2 comprising fiber cloth.
21. The method of claim 12 , wherein said bed comprises polyethyleneimine deposited on mesoporous molecular sieves.
22. A device for continuous conversion of CO 2 to O 2 providing a breathable atmosphere, comprising:
at least one first stage comprising at least one inlet, at least one outlet, a plurality of sorption bed chambers, each chamber comprising at least one CO 2 sorption bed, a means to direct a gas flow to and from said chambers, and a means to actuate said means to direct; and
at least one second stage comprising at least one ceramic oxygen generator (COG) unit comprising a graded bilayer electrolyte comprising a layer of cubic-stabilized bismuth oxide and a layer of acceptor-doped ceria between a cathode and an anode, at least one CO 2 intake, at least one O 2 exhaust, and a means to control said exhaust from said second stage into said outlet of said first stage.
23. The device of claim 22 , wherein said means to direct said gas flow comprises a first valve between said inlet and said bed and a second valve between said bed and said outlet, wherein when said first valve is in an open position said gas flow is directed to said chamber and said second valve is positioned to direct said gas flow to said outlet, and wherein when said first valve is in a closed position said gas flow is restricted from said chamber and said second valve is positioned to provide communication between said chamber and said intake of said second stage.
24. The device of claim 22 , wherein said means to control said exhaust comprises a metering valve.
25. The device of claim 22 , further comprising at least one CO 2 sensor in said outlet or at least one CO 2 sensor in each of said chambers, wherein said sensor provides a signal to each of said means to actuate when a level of CO 2 in said gas flow exceeds a predetermined level of CO 2 wherein said first and second valves of said plurality of said chambers are positioned to direct said gas flow to at least one, but not all, of said chambers and restrict gas flow to all other of said chambers.
26. The device of claim 22 , further comprising at least one CO sensor in said second stage wherein said sensor provides a signal to an alarm when a predetermined level of CO is exceeded.
27. The device of claim 22 , wherein said second stage further comprises a catalytic carbon deposition layer (CCDL) on a cathode of said COG.
28. The device of claim 22 , wherein said second stage further comprises a CCDL on a cathode of said COG, and wherein said CCDL comprises metal containing particles on a support.
29. The device of claim 22 , wherein second stage further comprises a CCDL on a cathode of said COG, wherein said CCDL comprises metal containing particles on a support, and wherein said metal particles comprise Fe, Ni, Co, alloys thereof, or oxides thereof.
30. The device of claim 22 , wherein said second stage further comprises a CCDL on a cathode of said COG, wherein said CCDL further comprises metal containing particles on a support, and wherein said metal particles comprise Fe, Ni, Co, alloys thereof, or oxides thereof, and wherein said particles are from about 10 to about 50 nm in size.
31. The device of claim 22 , wherein said second stage further comprises a CCDL on a cathode of said COG, wherein said CCDL further comprises metal containing particles on a support, and wherein said support is a Ni comprising wire mesh or a SiO 2 comprising fiber cloth.
32. The device of claim 22 , wherein said cubic-stabilized bismuth oxide comprises an erbia-stabilized bismuth oxide (ESB).
33. The device of claim 22 , wherein said acceptor-doped ceria comprises a samaria- or a gadolinia-doped ceria (SDC or GDC).
34. The device of claim 22 , wherein said cathode comprises a Pt-ceria cermet or a Pd-ceria cermet.
35. The device of claim 22 , wherein said anode comprises a silver-ESB cermet.
36. The device of claim 22 , wherein said bed comprises polyethyleneimine deposited on mesoporous molecular sieves.
37. The device of claim 22 , further comprising one or more heat exchangers.
38. A method of providing a breathable gas for life support, comprising the steps of:
adsorbing CO 2 from an exhaled gas flow in at least one first stage of a device, wherein said first stage comprises at least one inlet, at least one outlet, a plurality of sorption bed chambers, each chamber comprising at least one CO 2 sorption bed where said gas is depleted of CO 2 , a means to direct a gas flow to and from said chamber or restrict flow from said chamber and place said chamber into communication with at least one second stage, and a means to actuate said means to direct;
directing said CO 2 depleted gas from said chamber to an inhalable gas flow;
converting said CO 2 to C and O 2 in said second stages of said device, wherein said second stage comprises at least one ceramic oxygen generator (COG) unit comprising a graded bilayer electrolyte comprising a layer of cubic-stabilized bismuth oxide and a layer of acceptor-doped ceria between a cathode and an anode, at least one CO 2 intake, at least one O 2 exhaust, and a means to control said exhaust from said second stage; and
directing said O 2 from said exhaust to said inhalable gas flow.
39. The method of claim 38 , wherein said means to direct said gas flow comprises a first valve between said inlet and said bed and a second valve between said bed and said outlet, wherein when said first valve is in an open position to direct said gas flow to said bed and said second valve is positioned to direct said gas flow to said outlet, and wherein when said first valve is in a closed position, restricts said gas flow to said bed and said second valve is positioned to provide communication between said chamber and said intake of said second stage.
40. The method of claim 38 , wherein said means to control said exhaust comprises a metering valve.
41. The method of claim 38 , wherein said first stage further comprises at least one CO 2 sensor in said outlet or at least one CO 2 sensor in each of said chambers, wherein said sensor provides a signal to each of said means to actuate when the level of CO 2 in said gas flow exceeds a predetermined level of CO 2 , and wherein said first and second valves of said plurality of said chambers are positioned to direct said gas flow to at least one, but not all, of said chambers and restrict gas flow to all other of said chambers.
42. The method of claim 38 , wherein said second stage further comprises at least one CO sensor in said second stage and wherein said sensor provides a signal to an alarm when a predetermined level of CO is exceeded.
43. The method of claim 38 , wherein said second stage further comprises a catalytic carbon deposition layer (CCDL) on a cathode of said COG.
44. The method of claim 38 , wherein said second stage further comprises a CCDL on a cathode of said COG, and wherein said CCDL further comprises metal containing particles on a support.
45. The method of claim 38 , wherein second stage further comprises a CCDL on a cathode of said COG, and wherein said CCDL further comprises metal containing particles on a support, said metal particles comprising Fe, Ni, Co, alloys thereof, or oxides thereof.
46. The method of claim 38 , wherein wherein second stage further comprises a CCDL on a cathode of said COG, wherein said CCDL further comprises metal containing particles on a support, said metal particles comprising Fe, Ni, Co, alloys thereof, or oxides thereof, and wherein said particles are from about 10 to about 50 nm in size.
47. The method of claim 38 , wherein said second stage further comprises a CCDL on a cathode of said COG, wherein said CCDL further comprises metal containing particles on a support, and wherein said support is a Ni comprising wire mesh or a SiO 2 comprising fiber cloth.
48. The method of claim 38 , wherein said cubic-stabilized bismuth oxide comprises an erbia-stabilized bismuth oxide (ESB).
49. The method of claim 38 , wherein said acceptor-doped ceria comprises a samaria- or a gadolinia-doped ceria (SDC or GDC).
50. The method of claim 38 , wherein said cathode comprises a Pt-ceria cermet or a Pd-ceria cermet.
51. The method of claim 38 , wherein said anode comprises a silver-ESB cermet.
52. The method of claim 38 , wherein said bed comprises polyethyleneimine deposited on mesoporous molecular sieves.