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公开(公告)号:US20250043438A1
公开(公告)日:2025-02-06
申请号:US18718041
申请日:2022-10-24
Applicant: Siemens Energy Global GmbH & Co. KG
Inventor: Thomas Reichbauer , Günter Schmid , Yashar Musayev
IPC: C25B3/26 , C25B9/15 , C25B9/21 , C25B11/032 , C25B15/08
Abstract: A device for the electrolysis of CO2 and/or CO, with which an effective extraction of a cathode product can be ensured. The device includes a first gas feed, a first ion exchange membrane, an anode space including an anode, an extraction space, an extraction medium incorporated in the extraction space, a first feed for the extraction medium, and a first drain for the extraction medium. A method for carrying out an electrolysis of CO2 and/or CO, with which a corresponding extraction can be achieved with the device.
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公开(公告)号:US20250027217A1
公开(公告)日:2025-01-23
申请号:US18770838
申请日:2024-07-12
Inventor: Norikazu OSADA , Tsuneji KAMEDA
IPC: C25B11/037 , C25B1/04 , C25B1/23 , C25B9/70 , C25B11/032 , C25B11/091
Abstract: A solid oxide cell includes a hydrogen electrode, a solid oxide electrolyte layer, and an oxygen electrode. The hydrogen electrode includes: a first hydrogen electrode layer having a first surface and a second surface, the first surface being in contact with the oxide electrolyte layer, the second surface being opposite to the first surface; and a second hydrogen electrode layer in contact with the second surface. The first hydrogen electrode layer has a first metal particle and a first metal oxide particle. The second hydrogen electrode layer has a second metal oxide particle with a second metal particle supported with the second metal oxide particle.
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公开(公告)号:US20250027215A1
公开(公告)日:2025-01-23
申请号:US18481209
申请日:2023-10-04
Applicant: SHENZHEN INSTITUTES OF ADVANCED TECHNOLOGY , CHINA MERCHANTS. INVESTMENT DEVELOPMENT COMPANY LIMITED
Inventor: XIAOLONG ZHANG , YINGJUN DONG , JUXIA XIONG , HUIMING CHENG
IPC: C25B11/032 , C25B1/23
Abstract: The preparation method of a gas phase diffusion electrode for electrocatalyzing CO2 to reduce and produce CO provided by the present application comprises: mixing a conductive polymer monomer solution with a molar ratio of 100:1˜1:100 with a metal salt solution, and adding a dispersant to form a mixed solution; transferring the mixed solution to a substrate and reacting at a temperature of −30° C.-50° C. for 1-48 hours to obtain a gas phase diffusion electrode. By the method of using metal ions to self-initiate in-situ growth of conductive polymer monomers, the present application forms a metal-conductive polymer gas phase diffusion electrode. Due to the characteristics of the conductive polymer, the gas phase diffusion electrode can provide more nucleation sites, achieving similar catalytic effect while reducing use amount of metal.
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公开(公告)号:US20250027214A1
公开(公告)日:2025-01-23
申请号:US18481205
申请日:2023-10-04
Applicant: SHENZHEN INSTITUTES OF ADVANCED TECHNOLOGY , CHINA MERCHANTS. INVESTMENT DEVELOPMENT COMPANY LIMITED
Inventor: XIAOLONG ZHANG , JUXIA XIONG , YINGJUN DONG , HUIMING CHENG
IPC: C25B11/032 , C25B3/07 , C25B3/26 , C25B11/052 , C25B11/075
Abstract: The present application provides a preparation method of a gas phase diffusion electrode for electrocatalyzing CO2 to reduce and produce formic acid and an application thereof, comprising: obtaining first mixed solution, obtaining second mixed solution, uniformly mixing the first mixed solution and the second mixed solution, coating them onto a surface of a substrate, and then placing them at a temperature of −30° C.-100° C. for 1-48 hours to obtain the gas phase diffusion electrode. In the preparation method, conductive polymer monomer and bismuth or tin based metal component are coated onto the surface of the substrate to form an integrated conductive polymer-catalyst/hydrophobic substrate composite gas phase diffusion electrode, not only can the stability between metal active components and the substrate material be enhanced, but also characteristics such as better conductivity, higher specific surface area, abundant surface chemical reaction sites, and so on are provided.
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公开(公告)号:US20250011950A1
公开(公告)日:2025-01-09
申请号:US18890870
申请日:2024-09-20
Applicant: Mangrove Water Technologies LTD.
Inventor: Saad Dara , Benjamin Zahiri
IPC: C25B9/23 , B01D61/46 , B01D69/02 , C01D15/02 , C01D15/04 , C01D15/08 , C01F5/24 , C01F11/18 , C02F1/461 , C02F1/469 , C02F101/10 , C02F103/08 , C02F103/10 , C25B1/16 , C25B9/19 , C25B9/21 , C25B11/032 , C25B11/046 , C25B11/048 , C25B11/052 , C25B11/053 , C25B13/00 , C25C1/02 , C25C7/02 , C25C7/04
Abstract: In this disclosure, a process of recycling acid, base and the salt reagents required in the Li recovery process is introduced. A membrane electrolysis cell which incorporates an oxygen depolarized cathode is implemented to generate the required chemicals onsite. The system can utilize a portion of the salar brine or other lithium-containing brine or solid waste to generate hydrochloric or sulfuric acid, sodium hydroxide and carbonate salts. Simultaneous generation of acid and base allows for taking advantage of both chemicals during the conventional Li recovery from brines and mineral rocks. The desalinated water can also be used for the washing steps on the recovery process or returned into the evaporation ponds. The method also can be used for the direct conversion of lithium salts to the high value LiOH product. The method does not produce any solid effluent which makes it easy-to-adopt for use in existing industrial Li recovery plants.
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公开(公告)号:US20250011949A1
公开(公告)日:2025-01-09
申请号:US18890121
申请日:2024-09-19
Applicant: Mangrove Water Technologies LTD.
Inventor: Saad Dara , Benjamin Zahiri
IPC: C25B9/23 , B01D61/46 , B01D69/02 , C01D15/02 , C01D15/04 , C01D15/08 , C01F5/24 , C01F11/18 , C02F1/461 , C02F1/469 , C02F101/10 , C02F103/08 , C02F103/10 , C25B1/16 , C25B9/19 , C25B9/21 , C25B11/032 , C25B11/046 , C25B11/048 , C25B11/052 , C25B11/053 , C25B13/00 , C25C1/02 , C25C7/02 , C25C7/04
Abstract: In this disclosure, a process of recycling acid, base and the salt reagents required in the Li recovery process is introduced. A membrane electrolysis cell which incorporates an oxygen depolarized cathode is implemented to generate the required chemicals onsite. The system can utilize a portion of the salar brine or other lithium-containing brine or solid waste to generate hydrochloric or sulfuric acid, sodium hydroxide and carbonate salts. Simultaneous generation of acid and base allows for taking advantage of both chemicals during the conventional Li recovery from brines and mineral rocks. The desalinated water can also be used for the washing steps on the recovery process or returned into the evaporation ponds. The method also can be used for the direct conversion of lithium salts to the high value LiOH product. The method does not produce any solid effluent which makes it easy-to-adopt for use in existing industrial Li recovery plants.
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公开(公告)号:US12180600B2
公开(公告)日:2024-12-31
申请号:US17568594
申请日:2022-01-04
Applicant: UOP LLC
Inventor: Richa Baronia , Jyoti Goel , Sachin Daulatgir Giri , Sagar Sopan Ghadage , Kuldeep Balram Mamtani
IPC: C25B3/26 , C25B3/07 , C25B3/23 , C25B9/17 , C25B11/032 , C25B11/042 , C25B13/00
Abstract: A process for electrochemical conversion of carbon dioxide using a three-compartment cell provides low voltage requirements, high faradaic efficiencies, and high concentration of formic acid in product solutions. The applied voltage between anode and cathode should be less than 3.5V. Carbon dioxide may be converted to an organic acid.
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公开(公告)号:US20240413363A1
公开(公告)日:2024-12-12
申请号:US18709844
申请日:2022-09-27
Applicant: Robert Bosch GmbH
Inventor: Anton Ringel , Juergen Hackenberg , Julia Drillkens , Michael Giuseppe Marino
IPC: H01M8/04225 , C25B9/75 , C25B9/77 , C25B11/032 , C25B11/036 , C25B15/08 , H01M8/10 , H01M8/241 , H01M8/2465
Abstract: Method for conditioning an electrochemical cell unit (53) before putting the electrochemical cell unit (53) into operation for converting electrochemical energy into electrical energy as a fuel cell unit (1) and/or for converting electrical energy into electrochemical energy as an electrolytic cell unit (49) having stacked electrochemical cells (52) and channels for conducting a fuel and/or an electrolyte and channels for conducting an oxidizing agent and/or an electrolyte being formed in the electrochemical cell unit (53), the method having the steps of: providing a conditioning fluid; and conducting the conditioning fluid through the channels (12) for fuel and/or electrolytes and/or conducting the conditioning fluid through the channels (13) for oxidizing agents and/or electrolytes, wherein, during at least 50% of the duration of the method for conditioning the electrochemical cell unit (53), hydrogen is conducted as the conditioning fluid through the channels (13) for oxidizing agents and/or electrolytes.
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公开(公告)号:US12161968B2
公开(公告)日:2024-12-10
申请号:US17627872
申请日:2020-07-27
Applicant: Enapter S.r.l.
Inventor: Jan-Justus Schmidt , Antonio Filpi , Sean Crawford Chapman , Lazarus Diamond , Daniele Procaccio , Alessandro Cappelletti
IPC: B01D53/32 , C25B1/04 , C25B9/23 , C25B9/70 , C25B11/032 , C25B11/075 , G01N27/407 , H01M8/0662
Abstract: An electrochemical cell, or stack thereof, wherein each cell of the stack comprises at least: a membrane electrode assembly (MEA), the MEA comprising at least: an anode, a cathode, and an an-ion exchange membrane therebetween, an inlet to the anodic half-cell for the introduction of hydrogen at a first pressure, and an outlet from the cathodic half-cell for the transfer of hydrogen at a second pressure, and means to provide a required power to the cell. In one embodiment, the purification and compression of hydrogen occurring by utilisation of the following reaction pathway: formula (A) and formula (B).
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公开(公告)号:US20240392445A1
公开(公告)日:2024-11-28
申请号:US18738382
申请日:2024-06-10
Applicant: USA Fortescue IP, INC.
Inventor: Bamdad Bahar , Zhefei Li , Richard Sherrer , Jacob Zerby
IPC: C25B1/02 , C25B9/65 , C25B11/032 , C25B11/093 , C25B13/08
Abstract: An electrochemical oxygen pump moves or pumps oxygen molecules with a unique anion conducting layer comprising an anion conducting polymer. These pumps can either be used as high precision oxygen flow meters or as oxygen filters. The system can be plumbed to have air as the inlet and the pump will selectively pump oxygen out, offering another way to remove oxygen from the air, along with distillation or pressure swing absorption.
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