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公开(公告)号:US20240359134A1
公开(公告)日:2024-10-31
申请号:US18640772
申请日:2024-04-19
Applicant: GE Infrastructure Technology LLC
Inventor: Dhinesh THANGANADAR , Murali Krishna KALAGA , Raub Warfield SMITH , Thomas Raymond FARRELL
CPC classification number: B01D53/62 , B01D53/02 , F01K23/10 , H02K7/1823 , B01D2257/504 , B01D2258/0283 , F05D2260/61
Abstract: A combustion system includes a topping cycle that generates a flow of exhaust gas, a bottoming cycle, and a fuel cell. The fuel cell includes an anode side, a cathode side, and an electrolyte. The cathode side receives the flow of exhaust gas from the topping cycle via a cathode inlet line. The cathode side removes a first portion of pollutants from the exhaust gas. A heat recovery steam generator (HRSG) receives the exhaust gases from the cathode side via a cathode outlet line, and the HRSG generates a flow of steam for use in the bottoming cycle. A bypass line extends from the cathode inlet line to the cathode outlet line. The combustion system further includes a carbon capture system that is fluidly coupled to the HRSG via an HRSG outlet line. The carbon capture system removes a second portion of pollutants from the exhaust gas.
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公开(公告)号:US20240335817A1
公开(公告)日:2024-10-10
申请号:US18716333
申请日:2022-12-02
Applicant: CLIMEWORKS AG
Inventor: Visuta ENGKAGUL , Baptiste MONNEY , José Augusto BERROCAL , Christoph WEDER , Angelo VARGAS , Davide ALBANI , Claudio LIMONE
CPC classification number: B01J20/267 , B01D53/04 , B01D53/0462 , B01D53/0476 , B01J20/28004 , B01J20/28019 , B01J20/28059 , B01J20/28061 , B01J20/3425 , B01J20/3466 , C08F8/30 , B01D2253/202 , B01D2253/25 , B01D2253/304 , B01D2253/306 , B01D2253/34 , B01D2257/504 , B01D2258/0283 , B01D2258/05 , B01D2258/06 , B01D2259/4009
Abstract: Method for the preparation of a sorbent material and for use of such a material for separating gaseous carbon dioxide from a gas mixture, preferably for direct air capture, using a temperature, vacuum, or temperature/vacuum swing process, comprising primary amine moieties immobilized on a solid support, wherein the primary amine moieties, in the α-carbon position, are substituted by one hydrogen and one non-hydrogen substituent, wherein the sorbent material is in the form of a monolith, a layer, fibres, or particles, wherein the non-hydrogen substituent is selected from the group consisting of alkyl, alkenyl, arylalkyl, and wherein the solid support of the sorbent material is a porous material. Starting from a precursor of said sorbent material comprising one or multiple keto-groups, said one or multiple keto groups are converted into said primary amine moieties through a reductive amination.
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公开(公告)号:US20240335787A1
公开(公告)日:2024-10-10
申请号:US18575802
申请日:2022-06-30
Applicant: Hans Gude GUDESEN
Inventor: Hans Gude GUDESEN
IPC: B01D53/14
CPC classification number: B01D53/1475 , B01D2252/103 , B01D2257/504 , B01D2258/0283
Abstract: A method for extracting CO2 from a gas mixture comprising CO2 is disclosed. The method comprises dispensing the gas mixture in water in a first water volume, dissolving CO2 in the first water volume resulting in water enriched in dissolved 5CO2, and passing the water enriched in dissolved CO2 through a turbine. A corresponding system is also disclosed.
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公开(公告)号:US20240325974A1
公开(公告)日:2024-10-03
申请号:US18620671
申请日:2024-03-28
Applicant: American Ag Energy, Inc.
Inventor: Allison Nicole CHOI , Adam John STROHM , Richard Herbert ROSEN , Wei Han LIM
CPC classification number: B01D53/8628 , B01D53/226 , B01D53/229 , B01D53/8696 , E21B41/0064 , B01D2251/2062 , B01D2251/2067 , B01D2255/1021 , B01D2255/20738 , B01D2255/20761 , B01D2255/50 , B01D2257/102 , B01D2257/404 , B01D2257/504 , B01D2257/80 , B01D2258/0283
Abstract: Provided are systems and methods for obtaining nitrogen and carbon dioxide gases from a flue gas. A method according to some embodiments comprises receiving a flue gas at an inlet of a selective catalytic reduction system, wherein the flue gas comprises one or more NOx gases; reducing the one or more NOx gases to N2 gas in the selective catalytic reduction system; receiving an output gas from the selective catalytic reduction system at an inlet of a gas separation membrane; and separating the output gas into a retentate and a permeate using the gas separation membrane, wherein the retentate comprises N2 gas.
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公开(公告)号:US20240269656A1
公开(公告)日:2024-08-15
申请号:US18040748
申请日:2022-06-17
Applicant: LOWCARBON CO., LTD
Inventor: Cheol LEE
IPC: B01J23/889 , B01D53/86 , B01J29/076 , B01J37/00 , B01J37/03 , B01J37/04
CPC classification number: B01J23/8892 , B01D53/8671 , B01J29/076 , B01J37/0036 , B01J37/035 , B01J37/04 , B01D2255/2022 , B01D2255/2025 , B01D2255/2027 , B01D2255/2045 , B01D2255/2047 , B01D2255/20707 , B01D2255/2073 , B01D2255/20738 , B01D2255/20746 , B01D2255/20753 , B01D2255/20761 , B01D2255/20784 , B01D2255/20792 , B01D2255/2092 , B01D2255/30 , B01D2257/504 , B01D2258/0283
Abstract: Proposed is a method for manufacturing a catalyst for capture and conversion of carbon dioxide capable of removing carbon dioxide and converting carbon dioxide into other useful materials at the same time by capturing and converting carbon dioxide in flue gas generated during fossil fuel combustion into a carbon resource and a catalyst for capture and conversion of carbon dioxide manufactured by the method of the same. The catalyst for capture and conversion of carbon dioxide according to the present disclosure can reduce carbon dioxide by capturing carbon dioxide in flue gas generated during fossil fuel combustion. It is possible to convert the captured carbon dioxide into other useful materials by converting the collected carbon dioxide into sodium carbonate or sodium hydrogen carbonate as carbon resources.
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公开(公告)号:US20240269643A1
公开(公告)日:2024-08-15
申请号:US18566941
申请日:2022-06-09
Applicant: Catator AB
Inventor: Fredrik SILVERSAND
CPC classification number: B01J19/249 , B01D53/864 , B01D53/885 , B01J35/54 , F23C13/08 , B01D2257/502 , B01D2257/702 , B01D2257/708 , B01D2258/0283 , B01J2219/246 , B01J2219/247 , B01J2219/2479 , F23C2900/13001
Abstract: A catalytic reactor (22) comprising a central axis (A) and a stack of catalytically active sheets (10), wherein the catalytically active sheets (10) are stacked in the axial direction. Each of the catalytically active sheets (10) comprises a central opening (17) and at least some of the catalytically active sheets (10) comprise an axially extending flange (18) arranged at least partially around said central opening (17), wherein the flange (18) of one catalytically active sheet (10) extends into the central opening (17) of an adjacent catalytically active sheet (10). Disclosed is also a method for providing a catalytic reaction.
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公开(公告)号:US12042765B2
公开(公告)日:2024-07-23
申请号:US17722036
申请日:2022-04-15
Applicant: The Regents of the University of California
Inventor: Dante Simonetti , David Jassby , Gaurav Sant , Yenwen Tseng
CPC classification number: B01D53/965 , B01D15/363 , B01D53/62 , B01D53/78 , B01D2252/20447 , B01D2252/20484 , B01D2257/504 , B01D2258/0283 , B01D2258/06
Abstract: Disclosed herein are methods of electrochemically enhanced amine-based CO2 capture and systems for performing the methods of amine-based CO2 capture. The present methods and systems advantageously may be carried out at ambient temperatures and allow for reusing the amine through multiple cycles.
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公开(公告)号:US12037347B1
公开(公告)日:2024-07-16
申请号:US17957183
申请日:2022-09-30
Inventor: Gregory W. Peterson , Thomas H. Epps, III
CPC classification number: C07F1/08 , B01D53/58 , B01D53/62 , B01D67/0079 , B01D69/12 , B01D71/022 , B01D71/82 , B01D2257/406 , B01D2257/504 , B01D2257/93 , B01D2258/0283 , B01D2323/39
Abstract: A composition having the structure of formula I:
[R—Ar—(COOH)2]x[Ar—(COOH)3]2-xM32+ (I)
is provided where M is Mn, Cu, Co, Fe, Zn, Cd, Ni, or Pt; R is a bromine, nitro, a primary amine, C1-C4 alkyl secondary amine, C1-C4 alkyl oxy, Br—(C1-C4 alkyl), NO2—(C1-C4 alkyl), a mercaptan, and reaction products of any of the aforementioned with acyl chlorides of the formulas: CH3(CH2)mC(O)Cl, or CH3(CH(C1-C4 alkyl)CH2)mC(O)Cl, or CH3(CH2)m-Ph-(CH2)pC(O)Cl, where Ph is a C6 phenyl or C6 phenyl with one or more hydrogens replaced with F, C1-C4 fluoroalkyl, or C1-C4 perfluoroalkyl; m is independently in each occurrence an integer of 0 to 12 inclusive; p is an integer of 0 to 36 inclusive, to form an amide, a thioamide, or an ester; Ar is a 1,3,5-modified phenyl, and 1.4>×>0. A process of synthesis thereof and the use to chemically modify a gaseous reactant are also provided.-
公开(公告)号:US12036517B2
公开(公告)日:2024-07-16
申请号:US17897798
申请日:2022-08-29
Inventor: Jungkyu Choi , Kwan Young Lee , Sung-Won Hong
CPC classification number: B01D71/0281 , B01D69/108 , B01D2257/504 , B01D2258/0283 , B01D2311/2626 , B01D2323/08 , B01D2323/12 , B01D2323/24 , B01D2325/02
Abstract: Disclosed are a CHA zeolite membrane and a method of preparing the same, and more particularly, a CHA zeolite membrane having high capacity to separate CO2/N2 and CO2/CH4 even under wet conditions using a membrane produced using a synthetic precursor having a controlled ratio of Si and Al, a method of preparing the same, and a method of capturing and removing carbon dioxide using the membrane.
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公开(公告)号:US12005390B1
公开(公告)日:2024-06-11
申请号:US18509878
申请日:2023-11-15
Applicant: AirMyne, Inc.
Inventor: Bart Ludo Scherpbier , Jun Seon Hong , Derek Chase Popple , Mark Patrick Cyffka , Aryaman Bhartia , Cyndia Aiyun Cao , Arun Suresh Kamath , Sudip Mukhopadhyay
CPC classification number: B01D53/1493 , B01D53/1406 , B01D53/1412 , B01D53/1425 , B01D53/1475 , B01D53/185 , B01D53/62 , B01D53/78 , B01D2251/60 , B01D2251/80 , B01D2252/204 , B01D2252/20494 , B01D2252/504 , B01D2252/602 , B01D2257/504 , B01D2258/0283
Abstract: In a general aspect, a carbon dioxide removal system is presented. In some cases, a gas-liquid contactor is wetted with an alkaline capture solution. A first flow from a first gaseous feed including CO2 from a first source is directed to interact with the alkaline capture solution in the gas-liquid contactor, which forms a first CO2-rich alkaline capture solution. A second flow from a second gaseous feed including CO2 from a second, distinct source is directed to interact with the first CO2-rich alkaline capture solution, which forms a second CO2-rich alkaline capture solution. In some cases, the second flow is independent of the first gaseous feed, and a concentration of CO2 in the second CO2-rich alkaline capture solution is higher than a concentration of CO2 in the first CO2-rich alkaline capture solution. CO2 can be separated from the second CO2-rich alkaline capture solution.
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