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1.
公开(公告)号:US20220340419A1
公开(公告)日:2022-10-27
申请号:US17725296
申请日:2022-04-20
IPC分类号: C01B3/12 , B01J6/00 , C01C1/04 , C01B32/50 , C07C273/04 , C07C273/02 , C07C29/151 , C07C1/04 , C10G2/00 , C25B1/04 , C25B15/08 , C25B9/17 , B01D53/18 , B01D53/14
摘要: Ammonia, methanol, Fischer Tropsch products, and derivatives thereof are made by using hydrogen and oxygen supplied from an electrolyzer that is at least partially powered by renewable power, resulting in green process and systems that produce green products disclosed herein. A process using biomass and renewable energy includes producing an unshifted syngas from biomass and oxygen in a gasification unit, introducing water into an electrolyzer to produce an oxygen product and a hydrogen product, and introducing the oxygen product to the gasification unit. The electrolyzer is powered by renewable energy, and the oxygen product supplies at least a portion of the oxygen to the gasification unit.
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公开(公告)号:US20220081289A1
公开(公告)日:2022-03-17
申请号:US17420501
申请日:2020-04-07
申请人: HALDOR TOPSØE A/S
摘要: A plant, such as a hydrocarbon plant, is provided, which consists of a syngas stage for syngas generation and a synthesis stage where said syngas is synthesized to produce syngas derived product, such as hydrocarbon product. The plant makes effective use of various streams; in particular CO2 and H2. The plant does not comprise an external feed of hydrocarbons. A method for producing a product stream, such as a hydrocarbon product stream is also provided.
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公开(公告)号:US20200325021A1
公开(公告)日:2020-10-15
申请号:US16834720
申请日:2020-03-30
IPC分类号: C01B32/05 , C07C277/02 , C07D251/58 , C01B3/12
摘要: A process to extract carbon from hydrophobic waste comprises: combining the hydrophobic waste with an oxide of an active metal to form a storable, moisture-resistant feedstock for high-temperature processing; heating the feedstock in a furnace to yield an effluent gas entraining a carbide of the active metal; cooling the effluent gas entraining the carbide of the active metal; introducing nitrogen into the cooled effluent gas entraining the carbide of the active metal, to yield a cyanamide of the active metal and elemental carbon; and acidically hydrolyzing the cyanamide of the active metal to yield a cyanamide compound and a salt of the active metal.
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4.
公开(公告)号:US20190225489A1
公开(公告)日:2019-07-25
申请号:US16334220
申请日:2017-09-10
发明人: Mordechay Herskowitz , Tomy Hos
摘要: The invention provides a process for preparing liquid fuels and chemicals, which process comprises feeding carbon monoxide and hydrogen to a hydrogenation reactor, wherein the molar ratio CO:H2 is in the range of 1:0.5 to 1:0.9, catalytically hydrogenating said carbon monoxide in said hydrogenation reactor, condensing the effluent of said hydrogenation reactor to recover one or more organic liquid(s) and an aqueous solution, feeding a non-condensable component of said effluent into an oligomerization reactor; condensing an effluent discharged from the oligomerization reactor to obtain an additional organic liquid and an additional gaseous stream, separating said additional organic liquid, and either combusting said additional gaseous stream to produce heat and electricity, or processing same to obtain recyclable gaseous streams utilizable in said process.
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公开(公告)号:US10329495B2
公开(公告)日:2019-06-25
申请号:US15675360
申请日:2017-08-11
申请人: UOP LLC
摘要: A process is presented for the removal of contaminants like oxygenates from hydrocarbons. The contaminant oxygenates are removed from hydrocarbons that may be feed to cracking units. A crude feed stream is fed to a water wash column along with water to remove oxygenates and is subsequently treated with an adsorbent to effectively remove all the oxygenates from the crude hydrocarbon. A regenerant medium from a naphtha hydrotreating unit is used to regenerate the adsorbent.
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公开(公告)号:US10259718B2
公开(公告)日:2019-04-16
申请号:US15527657
申请日:2015-12-02
申请人: Haldor Topsøe A/S
发明人: Per Juul Dahl
摘要: In a process for co-production of ammonia and methanol, the outlet stream from the reformer is split into two parts, one of which is subjected to shift, carbon dioxide removal, methanation, compression and ammonia synthesis, while the other part is compressed and fed to a once-through methanol synthesis section. Methanol is withdrawn from the methanol synthesis section, and the remaining effluent from said section is divided into two streams comprising hydrogen, of which one is fed to the shift section, while the other is recycled to the desulfurization unit. This way a favourable co-production method is obtained because recycle hydrogen for the desulfurization is provided, and furthermore a compression step is avoided.
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公开(公告)号:US10087330B2
公开(公告)日:2018-10-02
申请号:US12378260
申请日:2009-02-12
IPC分类号: B32B5/16 , C09C1/56 , B82Y30/00 , C01B3/12 , C09D11/324 , C10J3/54 , H01G9/00 , H01G11/34 , H01M4/92 , H01G11/24 , C08K3/04 , C09D11/02 , H01G9/022 , H01M4/86
摘要: The invention is directed to processes for increasing the surface area of a carbon black starting material and for forming mesoporous carbon black. The process includes the step of contacting a carbon black starting material having a first BET nitrogen surface area with an oxidant in a fluidized bed under conditions effective to form a carbon black product having a second BET nitrogen surface area greater than the first BET nitrogen surface area. The invention is also directed to carbon black product formed by this process.
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公开(公告)号:US20180207599A1
公开(公告)日:2018-07-26
申请号:US15741998
申请日:2016-07-07
发明人: Ian Metcalfe
摘要: This invention relates to a method of chemical looping using non-stoichiometric materials with a variable degree of non-stoichiometry. One application of these methods is in the water gas shift reaction for H2 production. The methods of the invention can overcome limitations, e.g. those associated with chemical equilibria, which prevent chemical processes from proceeding with complete conversion of starting materials to products.
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公开(公告)号:US20180127660A1
公开(公告)日:2018-05-10
申请号:US15638385
申请日:2017-06-30
发明人: Paul E. King , Jennifer Wilcox
IPC分类号: C10G2/00 , C01B32/50 , C01B21/02 , C01C1/04 , C01B3/12 , C01B3/38 , B01D53/22 , B01D71/02 , C25B1/04
CPC分类号: C10G2/35 , B01D53/228 , B01D71/022 , C01B3/12 , C01B3/384 , C01B21/02 , C01B32/50 , C01B2203/0238 , C01B2203/0283 , C01B2203/062 , C01B2203/0855 , C01B2203/1241 , C01B2210/0012 , C01B2210/0046 , C01B2210/0051 , C01C1/04 , C10G2/341 , C10G2300/1022 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/703 , C25B1/04
摘要: An input stream of gaseous nitrogen and carbon dioxide is introduced into a first interior volume of a separation vessel that is divided into first and second interior volumes by a separation membrane that includes a metal layer. The metal layer selectively permits movement of nitrogen through the metal layer. An output stream of gaseous nitrogen and carbon dioxide is conveyed out of the first interior volume and into a reaction vessel. The volume fraction of carbon dioxide is greater in the output stream than in the input stream; the volume fraction of nitrogen is reduced in the output stream relative to the input stream. Nitrogen is removed from the second interior volume to maintain a gradient of nitrogen partial pressure across the separation membrane that causes net transport of nitrogen from the first interior volume through the separation membrane into the second interior volume.
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公开(公告)号:US20170267524A1
公开(公告)日:2017-09-21
申请号:US15338073
申请日:2016-10-28
申请人: GTLpetrol, LLC
发明人: Rodney J. Allam
IPC分类号: C01B3/50 , C01B3/56 , B01D53/047 , C01B3/12
CPC分类号: C01B3/506 , B01D53/002 , B01D53/047 , B01D53/75 , B01D53/864 , B01D2256/16 , B01D2257/502 , B01D2257/504 , B01D2257/80 , B01D2259/416 , C01B3/12 , C01B3/50 , C01B3/56 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/042 , C01B2203/043 , C01B2203/046 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , C01B2203/0827 , C01B2203/147 , Y02C10/08
摘要: The GTLpetrol Process for Maximum H2 Production. The GTLpetrol process uses a proprietary combination of two stage pressure swing adsorption hydrogen purification plus a C02 condensation removal step to give H2 recoveries in the range of 95% to 98% based on H2+CO from synthesis gas generation.
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