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公开(公告)号:US20240359154A1
公开(公告)日:2024-10-31
申请号:US18763904
申请日:2024-07-03
Applicant: SABIC Global Technologies B.V.
Inventor: Joseph William SCHROER , Scott STEVENSON , Andrew Mark WARD , Tim ABBOTT , Kenneth Francis LAWSON , Michael Edward HUCKMAN , Zhun ZHAO , Arno OPRINS
IPC: B01J19/00 , B01D53/047 , B01D53/26 , B01J4/00 , B01J6/00 , B01J19/24 , C01B3/12 , C01B3/34 , C01B3/48 , C01B3/56 , C01C1/02 , C01C1/04 , C07C4/02 , C07C4/04 , C07C29/132 , C07C29/152 , F25J3/02 , H01M8/04082 , H01M8/0606 , H01M8/0612 , H01M8/1007 , H02J15/00
CPC classification number: B01J19/0053 , B01D53/047 , B01D53/265 , B01J4/008 , B01J6/008 , B01J19/0033 , B01J19/2465 , C01B3/12 , C01B3/342 , C01B3/48 , C01B3/56 , C01C1/02 , C01C1/0417 , C01C1/0488 , C07C4/02 , C07C4/04 , C07C29/132 , C07C29/152 , F25J3/0233 , H01M8/04201 , H01M8/0606 , H01M8/0618 , H02J15/006 , H02J15/008 , B01D2256/16 , B01D2256/245 , B01J2219/00051 , B01J2219/00132 , B01J2219/00761 , B01J2219/0871 , C01B2203/0216 , C01B2203/0233 , C01B2203/0238 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/0294 , C01B2203/04 , C01B2203/061 , C01B2203/066 , C01B2203/068 , C01B2203/085 , C01B2203/148 , H01M8/1007
Abstract: A methanol synthesis plant comprising: a feed pretreating section operable to pretreat a feed stream; a synthesis gas (syngas) generation section comprising one or more reactors operable to produce a syngas synthesis product stream comprising synthesis gas from the feed stream; a methanol synthesis section comprising one or more methanol synthesis reactors operable to produce a synthesis product comprising methanol; and/or a methanol purification section operable to remove at least one component from the synthesis product to provide a purified methanol product; wherein the methanol synthesis plant is configured such that, relative to a conventional methanol synthesis plant, more of the net energy required by the methanol synthesis plant, the feed pretreating section, the syngas generation section, the methanol synthesis section, the methanol purification section, or a combination thereof, is provided by a non-carbon based energy source, a renewable energy source, and/or electricity.
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公开(公告)号:US20240336478A1
公开(公告)日:2024-10-10
申请号:US18413978
申请日:2024-01-16
Applicant: Iogen Corporation
Inventor: Brian Foody
CPC classification number: C01B3/382 , C01B3/48 , C01B2203/0244 , C01B2203/0283 , C01B2203/085 , C01B2203/1241 , C01B2203/86
Abstract: Provided herein is process of obtaining hydrogen from a blue hydrogen production facility that meets a target carbon intensity (CIT), the process comprising: generating hydrogen from non-renewable feedstock; capturing and sequestering fossil CO2 derived from the non-renewable feedstock; and at least partially powering hydrogen production with renewable electricity, the renewable electricity being derived from biomass in which biogenic carbon produced therefrom (e.g., carbon dioxide, char and the like) is captured and sequestered; and wherein the use of the renewable electricity in the hydrogen production allows the carbon intensity of the hydrogen produced therefrom to be reduced sufficiently so that the target carbon intensity (CIT) is achieved.
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公开(公告)号:US12103897B2
公开(公告)日:2024-10-01
申请号:US17803830
申请日:2022-12-13
Applicant: INFINIUM TECHNOLOGY, LLC
Inventor: Robert Schuetzle , Dennis Schuetzle , Harold Wright , Orion Hanbury , Matthew Caldwell , Ramer Rodriguez
CPC classification number: C07C1/0485 , C01B3/40 , C01B32/40 , C25B1/04 , C25B15/081 , C01B2203/0233 , C01B2203/0244 , C01B2203/1241
Abstract: The present invention describes a processes, systems, and catalysts for the conversion of carbon dioxide and water and electricity into low carbon or zero carbon high quality fuels and chemicals. In one aspect, the present invention provides an integrated process for the conversion of a feed stream comprising carbon dioxide to a product stream comprising hydrocarbons between 5 and 24 carbon atoms in length.
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公开(公告)号:US12091319B2
公开(公告)日:2024-09-17
申请号:US18212294
申请日:2023-06-21
Applicant: Air Products and Chemicals, Inc.
Inventor: Xiang-Dong Peng , Yu Zhang , Tori Dawn Courtney
CPC classification number: C01B3/382 , C01B3/48 , C01B3/52 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/0811 , C01B2203/0833 , C01B2203/0894 , C01B2203/1241 , C01B2203/1276 , C01B2203/142 , C01B2203/146 , C01B2203/148
Abstract: A process for producing syngas that uses the syngas product from an oxygen-fired reformer to provide all necessary heating duties, which eliminates the need for a fired heater. Without the flue gas stream leaving a fired heater, all of the carbon dioxide produced by the reforming process is concentrated in the high-pressure syngas stream, allowing essentially complete carbon dioxide capture.
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公开(公告)号:US20240228896A1
公开(公告)日:2024-07-11
申请号:US18559375
申请日:2022-05-05
Applicant: ENERKEM INC.
Inventor: Jean-Pierre CRETE , Louis DENOMME , Frédéric ST-ONGE , Xeniya SAVELYEVA
CPC classification number: C10K3/026 , C01B3/12 , C10J3/46 , C10K1/005 , C10K1/08 , C10K1/20 , C10K3/06 , C01B2203/0222 , C01B2203/0244 , C01B2203/0475 , C01B2203/062 , C10J2300/0913 , C10J2300/0969 , C10J2300/1618 , C10J2300/1659 , C10J2300/1815
Abstract: It is provided a process for increasing production of carbon monoxide (CO) and recycling carbon dioxide when treating synthesis gas using a carbon dioxide-to-carbon monoxide conversion unit, such as a Reverse Water Gas Shift (RWGS) reactor, converting excess CO2 from the produced syngas to additional CO, using an external source of green, renewable or low carbon intensity hydrogen.
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公开(公告)号:US12024485B2
公开(公告)日:2024-07-02
申请号:US17773306
申请日:2020-10-23
Inventor: Veronika Gronemann , Stephan Haase , Lutz Janko , Hans Kopetsch , Chin Han Lim
IPC: C07C29/151 , C01B3/38 , C07C29/152
CPC classification number: C07C29/1518 , C01B3/382 , C07C29/152 , C01B2203/0244 , C01B2203/061
Abstract: A process for producing methanol, wherein a make-up gas stream from a reformer unit is admixed with a hydrogen-containing stream from a hydrogen recovery stage to obtain a hydrogen-rich synthesis gas, which is combined with a residual gas stream and the combined stream is passed through a bed of a methanol synthesis catalyst at elevated pressure and elevated temperature to obtain a product stream comprising methanol and the residual gas stream and wherein the product stream is cooled to remove methanol from the residual gas stream. Wherein a portion of the residual gas stream is removed as a purge gas stream and a portion of the hydrogen-rich synthesis gas stream is removed and combined with the purge gas stream to obtain a mixed synthesis gas stream and the mixed synthesis gas stream is sent to the hydrogen recovery stage to produce the hydrogen-containing stream.
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公开(公告)号:US12006214B2
公开(公告)日:2024-06-11
申请号:US17211148
申请日:2021-03-24
Applicant: Minish Mahendra Shah , Lawrence Bool
Inventor: Minish Mahendra Shah , Lawrence Bool
CPC classification number: C01B3/363 , C01B3/382 , C01B2203/0211 , C01B2203/0216 , C01B2203/0244 , C01B2203/0811 , C01B2203/0827 , C01B2203/1241
Abstract: The present invention relates to integrating a hot oxygen burner with an auto thermal reformer of reducing in a system for generating synthesis gas.
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公开(公告)号:US20240150170A1
公开(公告)日:2024-05-09
申请号:US18503036
申请日:2023-11-06
Applicant: Charm Industrial, Inc.
Inventor: Peter Reinhardt , Shaun Kinetic , Kelly Kinetic , Jacob Wilkins , Brian Jamieson
CPC classification number: C01B3/382 , B01J4/002 , C01B3/50 , C21B13/0073 , C01B2203/0233 , C01B2203/0244 , C01B2203/04 , C01B2203/1235 , C01B2203/147 , C01B2203/1628 , C01B2203/169
Abstract: Disclosed herein are systems and methods for producing synthesis gas (syngas) using bio-oil. In some embodiments, syngas is produced by steam reforming bio-oil. In some embodiments, the bio-oil is provided in liquid form. In some embodiments at least some of the liquid bio-oil is transitioned into droplet form when entering a reformer for steam-reforming. In some embodiments, the reformer produces a gas stream comprising syngas, which may be fed to a furnace (e.g., direct reducing furnace, shaft furnace) for reducing iron ore to iron. In some embodiments, the amount of oxygen provided to the reformer is regulated based on an equivalence ratio (ER) corresponding to moles of oxygen fed to the reformer divided by moles of oxygen necessary to achieve stoichiometric combustion of the bio-oil, wherein an exemplary ER value is from about 0.1 to about 0.6.
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公开(公告)号:US20240140795A1
公开(公告)日:2024-05-02
申请号:US18373533
申请日:2023-09-27
Applicant: SK Innovation Co, Ltd.
Inventor: Hee Jung Jeon , Ok Youn Kim , Dong Min Yun
IPC: C01B3/44 , B01J8/00 , B01J8/18 , B01J8/26 , C01B3/52 , C01B3/56 , C01B32/40 , C07C1/04 , C10J1/26
CPC classification number: C01B3/44 , B01J8/0055 , B01J8/1818 , B01J8/26 , C01B3/52 , C01B3/56 , C01B32/40 , C07C1/043 , C10J1/26 , C01B2203/0244 , C01B2203/0415 , C01B2203/042 , C01B2203/0475 , C01B2203/1058 , C01B2203/1082 , C01B2203/1241 , C10J2300/0946
Abstract: Provided is a method of manufacturing syngas including (S1) heat-treating organic wastes under a catalyst in a first reactor to produce a first mixed gas; (S2) separating the catalyst and carbon dioxide (CO2) from the first mixed gas, and recovering a mixed gas from which the catalyst and the carbon dioxide (CO2) have been removed; (S3) converting the carbon dioxide (CO2) separated in (S2) into carbon monoxide (CO) by a reverse Boudouard reaction in a second reactor; and (S4) mixing the mixed gas recovered in (S2) and the carbon monoxide (CO) converted in (S3) to produce syngas.
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公开(公告)号:US20240125270A1
公开(公告)日:2024-04-18
申请号:US18393133
申请日:2023-12-21
Applicant: 8 Rivers Capital, LLC
Inventor: Rodney John Allam , Navid Rafati
IPC: F02C6/18 , B01D53/047 , B01J7/00 , B01J7/02 , C01B3/36 , C01B3/38 , C01B3/48 , C01B3/56 , C07C29/00 , C10K3/04 , F01K13/00 , F01K23/10 , F02C3/22 , F02C3/28 , F02C3/34
CPC classification number: F02C6/18 , B01D53/047 , B01J7/00 , B01J7/02 , C01B3/36 , C01B3/382 , C01B3/48 , C01B3/56 , C07C29/00 , C10K3/04 , F01K13/00 , F01K23/10 , F02C3/22 , F02C3/28 , F02C3/34 , B01D2256/16 , B01D2257/502 , B01D2257/504 , B01D2259/402 , C01B2203/0233 , C01B2203/0244 , C01B2203/0255 , C01B2203/0261 , C01B2203/0283 , C01B2203/0288 , C01B2203/042 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , C01B2203/0833 , C01B2203/0838 , C01B2203/0883 , C01B2203/0894 , C01B2203/1235 , C01B2203/1241 , C01B2203/141 , C01B2203/142 , C01B2203/146 , C01B2203/84 , C10J2300/1846 , F05D2220/32 , F05D2260/61 , Y02E20/14 , Y02E20/16 , Y02E20/32
Abstract: The present disclosure relates to systems and methods useful for power production. In particular, a power production cycle utilizing CO2 as a working fluid may be configured for simultaneous hydrogen production. Beneficially, substantially all carbon arising from combustion in power production and hydrogen production is captured in the form of carbon dioxide. Further, produced hydrogen (optionally mixed with nitrogen received from an air separation unit) can be input as fuel in a gas turbine combined cycle unit for additional power production therein without any atmospheric CO2 discharge.
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