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公开(公告)号：US20180231991A1
公开(公告)日：2018-08-16
申请号：US15431264
申请日：2017-02-13
CPC分类号： G05D7/0652 , F16K31/02 , F16K37/0041
摘要： A system, and a method, are disclosed with a plurality of valves acting as a group. The valves of the group are instructed by a master controller or other device to oscillate more open and more closed around a set point. The system controls the oscillation using an instruction to oscillate in a sine waveform pattern; the valves of the group oscillate so that the sine waveform is a positive phase shift of at least one other valve in the group. The phase shift may be calculated as 360/n degrees, where n represents the number of valves in the group.
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公开(公告)号：US10213731B2
公开(公告)日：2019-02-26
申请号：US15410024
申请日：2017-01-19
申请人： Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
发明人： Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
摘要： A method for continuously removing carbon dioxide vapor from a carrier gas is disclosed. This method includes, first, causing direct contact of the carrier gas with a liquid mixture in a separation chamber, the carrier gas condensing at a lower temperature than the carbon dioxide vapor. A combination of chemical effects cause the carbon dioxide to condense, complex, or both condense and complex with the liquid mixture. The liquid mixture is chosen from the group consisting of: first, a combination of components that can be maintained in a liquid phase at a temperature below the carbon dioxide vapor's condensation point, whereby the carbon dioxide condenses into the liquid mixture; second, a combination of components where at least one component forms a chemical complex with the carbon dioxide vapor and thereby extracts at least a portion of the carbon dioxide vapor from the carrier gas; and third, a combination of components that can both be maintained in a liquid phase at a temperature below the carbon dioxide's condensation point, and wherein at least one component forms a chemical complex with the carbon dioxide vapor and thereby extracts at least a portion of the carbon dioxide vapor from the carrier gas. The liquid mixture is then reconstituted after passing through the separation chamber by a chemical separation process chosen to remove an equivalent amount of the carbon dioxide vapor from the liquid mixture as was removed from the carrier gas. The reconstituted liquid mixture is restored to temperature and pressure through heat exchange, compression, and expansion, as necessary, in preparation for recycling back to the separation chamber. The liquid mixture is then returned to the separation chamber. In this manner, the carrier gas leaving the exchanger has between 1% and 100% of the carbon dioxide vapor removed.
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公开(公告)号：US20180200666A1
公开(公告)日：2018-07-19
申请号：US15410024
申请日：2017-01-19
申请人： Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
发明人： Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
CPC分类号： B01D53/1475 , B01D53/002 , B01D53/1493 , B01D53/62 , B01D2251/302 , B01D2251/306 , B01D2251/402 , B01D2251/404 , B01D2251/80 , B01D2252/102 , B01D2252/103 , B01D2252/202 , B01D2252/2021 , B01D2252/2023 , B01D2252/504 , B01D2257/504 , B01D2258/0283 , C10L3/104 , C10L2290/12 , C10L2290/541 , Y02C10/04 , Y02C10/06 , Y02C10/12
摘要： A method for continuously removing carbon dioxide vapor from a carrier gas is disclosed. This method includes, first, causing direct contact of the carrier gas with a liquid mixture in a separation chamber, the carrier gas condensing at a lower temperature than the carbon dioxide vapor. A combination of chemical effects cause the carbon dioxide to condense, complex, or both condense and complex with the liquid mixture. The liquid mixture is chosen from the group consisting of: first, a combination of components that can be maintained in a liquid phase at a temperature below the carbon dioxide vapor's condensation point, whereby the carbon dioxide condenses into the liquid mixture; second, a combination of components where at least one component forms a chemical complex with the carbon dioxide vapor and thereby extracts at least a portion of the carbon dioxide vapor from the carrier gas; and third, a combination of components that can both be maintained in a liquid phase at a temperature below the carbon dioxide's condensation point, and wherein at least one component forms a chemical complex with the carbon dioxide vapor and thereby extracts at least a portion of the carbon dioxide vapor from the carrier gas. The liquid mixture is then reconstituted after passing through the separation chamber by a chemical separation process chosen to remove an equivalent amount of the carbon dioxide vapor from the liquid mixture as was removed from the carrier gas. The reconstituted liquid mixture is restored to temperature and pressure through heat exchange, compression, and expansion, as necessary, in preparation for recycling back to the separation chamber. The liquid mixture is then returned to the separation chamber. In this manner, the carrier gas leaving the exchanger has between 1% and 100% of the carbon dioxide vapor removed.
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公开(公告)号：US10307709B2
公开(公告)日：2019-06-04
申请号：US15410106
申请日：2017-01-19
申请人： Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
发明人： Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
摘要： A method for continuously removing water vapor from a carrier gas is disclosed. This method includes, first, causing direct contact of the carrier gas with a liquid mixture in a separation chamber, the carrier gas condensing at a lower temperature than the water vapor. A combination of chemical effects cause the water vapor to condense, complex, or both condense and complex with the liquid mixture. The liquid mixture is chosen from the group consisting of: first, a combination of components that can be maintained in a liquid phase at a temperature below the water vapor's condensation point, whereby the water vapor condenses into the liquid mixture; second, a combination of components where at least one component forms a chemical complex with the water vapor and thereby extracts at least a portion of the water vapor from the carrier gas; and third, a combination of components that can both be maintained in a liquid phase at a temperature below the water vapor's condensation point, and wherein at least one component forms a chemical complex with the water vapor and thereby extracts at least a portion of the water vapor from the carrier gas. The liquid mixture is then reconstituted after passing through the separation chamber by a chemical separation process chosen to remove an equivalent amount of the water vapor from the liquid mixture as was removed from the carrier gas. The reconstituted liquid mixture is restored to temperature and pressure through heat exchange, compression, and expansion, as necessary, in preparation for recycling back to the separation chamber. The liquid mixture is then returned to the separation chamber. In this manner, the carrier gas leaving the exchanger has between 1% and 100% of the water vapor removed.
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公开(公告)号：US20180200668A1
公开(公告)日：2018-07-19
申请号：US15410106
申请日：2017-01-19
申请人： Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
发明人： Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
CPC分类号： B01D53/263 , B01D5/0027 , B01D5/003 , B01D5/0054 , B01D5/0087 , B01D53/265 , B01D2252/103 , B01D2252/30 , B01D2252/504 , B01D2258/0283 , C10L3/106 , C10L2290/12 , C10L2290/541
摘要： A method for continuously removing water vapor from a carrier gas is disclosed. This method includes, first, causing direct contact of the carrier gas with a liquid mixture in a separation chamber, the carrier gas condensing at a lower temperature than the water vapor. A combination of chemical effects cause the water vapor to condense, complex, or both condense and complex with the liquid mixture. The liquid mixture is chosen from the group consisting of: first, a combination of components that can be maintained in a liquid phase at a temperature below the water vapor's condensation point, whereby the water vapor condenses into the liquid mixture; second, a combination of components where at least one component forms a chemical complex with the water vapor and thereby extracts at least a portion of the water vapor from the carrier gas; and third, a combination of components that can both be maintained in a liquid phase at a temperature below the water vapor's condensation point, and wherein at least one component forms a chemical complex with the water vapor and thereby extracts at least a portion of the water vapor from the carrier gas. The liquid mixture is then reconstituted after passing through the separation chamber by a chemical separation process chosen to remove an equivalent amount of the water vapor from the liquid mixture as was removed from the carrier gas. The reconstituted liquid mixture is restored to temperature and pressure through heat exchange, compression, and expansion, as necessary, in preparation for recycling back to the separation chamber. The liquid mixture is then returned to the separation chamber. In this manner, the carrier gas leaving the exchanger has between 1% and 100% of the water vapor removed.
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