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公开(公告)号:US20240246885A1
公开(公告)日:2024-07-25
申请号:US18626178
申请日:2024-04-03
Applicant: CANON KABUSHIKI KAISHA
Inventor: Miki Itoh , Hironao Sajiki , Yoshinari Sawama , Miki Niikawa , Kwihwan Park
CPC classification number: C07C1/02 , B01J10/00 , B01J19/0006 , B01J19/18 , B01J19/285 , C07C1/12 , C07C9/04 , B01J2219/00162 , B01J2219/00957 , B01J2219/0286 , B01J2219/30408
Abstract: A hydrocarbon is produced by applying mechanical energy to a metal body containing stainless steel by solid-solid contact so that a contact pressure per unit area is 30 kPa or more, in the presence of a gas containing carbon dioxide and a hydrogen source, thereby adding hydrogen to carbon dioxide. Further, a hydrocarbon is produced by providing a reaction vessel for applying mechanical energy to a metal body by solid-solid contact in the presence of a gas containing carbon dioxide and a hydrogen source, a gas introduction unit for introducing the gas containing carbon dioxide to the reaction vessel, a hydrogen source introduction unit for introducing the hydrogen source to the reaction vessel, and a gas discharge unit for discharging a gas containing the hydrocarbon produced in the reaction vessel, and adding hydrogen to the carbon dioxide in the reaction vessel.
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公开(公告)号:US11981614B2
公开(公告)日:2024-05-14
申请号:US17148407
申请日:2021-01-13
Applicant: CANON KABUSHIKI KAISHA
Inventor: Miki Itoh , Hironao Sajiki , Yoshinari Sawama , Miki Niikawa , Kwihwan Park
CPC classification number: C07C1/02 , B01J10/00 , B01J19/0006 , B01J19/18 , B01J19/285 , C07C1/12 , C07C9/04 , B01J2219/00162 , B01J2219/00957 , B01J2219/0286 , B01J2219/30408 , C07C1/02 , C07C9/04
Abstract: A hydrocarbon is produced by applying mechanical energy to a metal body containing stainless steel by solid-solid contact so that a contact pressure per unit area is 30 kPa or more, in the presence of a gas containing carbon dioxide and a hydrogen source, thereby adding hydrogen to carbon dioxide. Further, a hydrocarbon is produced by providing a reaction vessel for applying mechanical energy to a metal body by solid-solid contact in the presence of a gas containing carbon dioxide and a hydrogen source, a gas introduction unit for introducing the gas containing carbon dioxide to the reaction vessel, a hydrogen source introduction unit for introducing the hydrogen source to the reaction vessel, and a gas discharge unit for discharging a gas containing the hydrocarbon produced in the reaction vessel, and adding hydrogen to the carbon dioxide in the reaction vessel.
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3.
公开(公告)号:US11806707B2
公开(公告)日:2023-11-07
申请号:US15734819
申请日:2019-04-24
Applicant: MAN Energy Solutions SE
Inventor: Christian Schuhbauer , Dieter Verbeek , Rolf Bank
CPC classification number: B01J8/067 , B01J8/0469 , B01J8/0496 , B01J8/065 , C07C1/041 , C07C1/042 , C07C1/048 , C07C1/12 , B01J2208/0053 , B01J2208/00539 , B01J2208/00548 , B01J2208/00663 , B01J2208/065
Abstract: A method for carrying out catalytic gas phase reactions including providing a tube bundle reactor which has a bundle of reaction tubes that are filled with a catalyst charge and are cooled by a heat transfer medium, conveying a reaction gas through the catalyst charge, the reaction gas flowing into each reaction tube divided into two part flows introduced in the axial direction of the reaction tube at different points in the catalyst charge the catalyst charge has at least two catalyst layers of different activity, wherein the activity of the first catalyst layer, in the flow direction of the reaction gas, is lower than the activity of the at least one other catalyst layer and in step a first part flow is introduced into the first catalyst layer and each further part flow is introduced past the first catalyst layer into the at least one further catalyst layer.
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4.
公开(公告)号:US20230348800A1
公开(公告)日:2023-11-02
申请号:US18136031
申请日:2023-04-18
Applicant: GTI Energy
Inventor: Terry MARKER , Martin B. LINCK , Jim WANGEROW , Pedro ORTIZ-TORAL
IPC: C10G50/00 , C10L3/08 , C07C1/12 , C07C1/04 , C07C5/13 , C07C9/04 , B01D3/14 , C10G47/32 , B01D3/06
CPC classification number: C10G50/00 , C10L3/08 , C07C1/12 , C07C1/04 , C07C5/13 , C07C9/04 , B01D3/143 , C10G47/32 , B01D3/06 , C10G2400/08 , C10G2300/1025 , C01B32/50
Abstract: Processes for converting methane and/or other hydrocarbons to synthesis gas (i.e., a gaseous mixture comprising H2 and CO) are disclosed, in which at least a portion of the hydrocarbon(s) is reacted with CO2. At least a second portion of the methane may be reacted with H2O (steam), thereby improving overall thermodynamics of the process, in terms of reducing endothermicity (ΔH) and the required energy input, compared to “pure” dry reforming in which no H2O is present. Such dry reforming (reaction with CO2 only) or CO2-steam reforming (reaction with both CO2 and steam) processes are advantageously integrated with Fischer-Tropsch synthesis to yield liquid hydrocarbon fuels. Further integration may involve the use of a downstream finishing stage involving hydroisomerization to remove FT wax. Yet other integration options involve the use of combined CO2-steam reforming and FT synthesis stages (optionally with finishing) for producing liquid fuels from gas streams generated in a number of possible processes, including the hydropyrolysis of biomass.
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公开(公告)号:US20230114967A1
公开(公告)日:2023-04-13
申请号:US17914128
申请日:2021-03-31
Applicant: Osaka Gas Co., Ltd.
Inventor: Mitsuaki Echigo , Hisao Ohnishi , Yuji Tsuda
IPC: C07C1/04 , C25B1/04 , C25B1/23 , C25B9/23 , C01B32/40 , C07C9/04 , B01J23/46 , B01J23/648 , B01J23/652 , B01J23/755 , B01J37/02 , B01J23/42 , B01J23/63 , B01J23/745 , B01J23/83 , C10G2/00
Abstract: As a hydrocarbon production system that synthesizes hydrocarbons using water and carbon dioxide as raw materials, a hydrocarbon production system capable of producing hydrocarbons by securing hydrogen and carbon monoxide required for hydrocarbon synthesis is provided. In a hydrocarbon production system that produces hydrocarbons from at least water and carbon dioxide, the hydrocarbon production system includes at least an electrolytic reaction unit, a reverse water-gas shift reaction unit, and a hydrocarbon synthesis reaction unit.
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公开(公告)号:US11519079B2
公开(公告)日:2022-12-06
申请号:US17177760
申请日:2021-02-17
Applicant: HONEYWELL INTERNATIONAL INC.
Inventor: Rebecca Kamire , Stephen Yates
Abstract: A carbon dioxide conversion system for an environment includes a first gas-liquid contactor-separator downstream of the environment; an electrochemical conversion cell downstream of the first gas-liquid contactor-separator; and a cleaned ionic liquid storage intermediate the first gas-liquid contactor-separator and the electrochemical conversion cell.
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公开(公告)号:US11242603B2
公开(公告)日:2022-02-08
申请号:US16484314
申请日:2018-02-01
Applicant: Siemens Aktiengesellschaft
Inventor: Maximilian Fleischer , Kerstin Wiesner-Fleischer , Andreas Engelbrecht , Martin Hämmerle , Ralf Moos
IPC: C25B3/25 , C25B15/02 , C25B9/65 , C07C9/04 , C07C9/06 , C07C9/08 , C07C31/02 , C07C47/02 , C07C53/00
Abstract: Various embodiments include an electrolysis method comprising: applying a pulsed voltage or a pulsed current between an anode and a cathode; repeatedly measuring a respective current OCP at the cathode in a zero-current state relative to a reference system; and controlling the pulsed voltage or the pulsed current so a working potential of the cathode in the current-carrying state with respect to the reference system has a defined progression relative to the respective current OCP. The defined progression includes a first phase at a cathodic level and a second phase at an anodic level.
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公开(公告)号:US20210300840A1
公开(公告)日:2021-09-30
申请号:US17218394
申请日:2021-03-31
Applicant: UOP LLC
Inventor: Nathan Siedler , Charles Luebke , David Wegerer , Parag Jain
IPC: C07C1/12 , C07C11/04 , C07C11/24 , B01D53/047 , C07C9/04
Abstract: A process for producing acetylene, ethylene, or both is disclosed. The process includes combusting a fuel stream to produce a combustion gas effluent stream and pyrolyzing a feed stream in a pyrolysis zone in the presence of the combustion gas effluent stream to produce a pyrolysis zone effluent stream which is further quenched and compressed. The compressed quenched stream is separated in a solvent separation column to produce a net gas stream comprising hydrogen, methane, and at least one carbon oxide and a product stream. A portion of the carbon oxide of the net gas stream is converted into methane in a methanation reactor and a reactor effluent stream is sent to an amine scrubber where carbon dioxide is removed and a methane containing stream is generated as an effluent. The methane containing stream is then recycled to the pyrolysis zone of the supersonic reactor.
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公开(公告)号:US10793487B2
公开(公告)日:2020-10-06
申请号:US16341750
申请日:2017-10-13
Applicant: Terje Ernst Mikalsen
Inventor: Terje Ernst Mikalsen
Abstract: It is disclosed a system for producing methanol/methane, said system comprising an electrolysis section (1) producing hydrogen and oxygen from the cleaving of water molecules, and said system further comprising a closed cultivation/breeding container/pond (5) for aquatic organisms creating CO2 through their metabolism to be liberated into the water surrounding said organisms forming CO2-rich water, said CO2-rich water being transported to a CO2-liberating section forming gaseous CO2 and CO2-poor water, said liberated gaseous CO2 being transported to a reactor (6,6′) and being combined with said hydrogen from said electrolysis plant (1) for creating methanol and/or methane as an end product, said methanol/methane being isolated and exited from said system.
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10.
公开(公告)号:US10766770B2
公开(公告)日:2020-09-08
申请号:US16302559
申请日:2017-05-18
Applicant: GRANNUS, LLC
Inventor: James Kelly Merritt , Matthew Cox
IPC: C01B3/02 , C01B3/38 , C01B3/50 , H01M8/0612 , H01M8/0668 , H01M8/0606 , C25B5/00 , H01M8/04082 , C01B3/36 , C07C273/04 , H01M8/04119 , C07C1/12 , C07C9/04
Abstract: Disclosed herein are methods and systems for the production of hydrogen-containing compounds, such as ammonia and urea from a product stream of a fuel cell unit. The production of ammonia and optionally urea can also include a net power production. Alternatively, the hydrogen stream from the fuel cell unit can be directed to the production of synthetic hydrocarbons liquids.
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