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公开(公告)号：US11826721B2
公开(公告)日：2023-11-28
申请号：US17533838
申请日：2021-11-23
发明人： Bi-Zeng Zhan , Zunqing He , Hoon Taek Chung , Piotr Zelenay
CPC分类号： B01J20/20 , B01J20/0233 , B01J20/28007 , B01J20/3078 , B01J20/3204 , B01J20/3236 , B01J20/3295 , C10G25/003 , C10G2300/1025 , C10G2300/1051 , C10G2300/1055 , C10G2300/202 , C10G2300/207 , C10G2300/80
摘要： Metal nanoparticle-deposited, nitrogen-doped carbon adsorbents are disclosed, along with methods of removing sulfur compounds from a hydrocarbon feed stream using these adsorbents.
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2.发明授权公开(公告)号：US11660575B2
公开(公告)日：2023-05-30
申请号：US16717788
申请日：2019-12-17
发明人： Yao Ma , Melinda Jue , Ryan Lively , Dhaval Ajit Bhandari
IPC分类号： C01B32/336 , C01B32/306 , B01D71/02 , B01D67/00 , B01D69/02 , B01D53/02 , C07C7/13 , C10L3/10 , C10G25/05 , B01J20/20 , B01J20/28 , B01J20/30 , B01D53/22
CPC分类号： B01D71/021 , B01D53/02 , B01D53/228 , B01D67/0044 , B01D67/0067 , B01D69/02 , B01J20/20 , B01J20/2808 , B01J20/28033 , B01J20/28059 , B01J20/28061 , B01J20/28064 , B01J20/3078 , C01B32/306 , C01B32/336 , C07C7/13 , C10G25/05 , C10L3/103 , C10L3/104 , C10L3/105 , B01D2253/102 , B01D2253/306 , B01D2253/308 , B01D2256/245 , B01D2257/702 , B01D2325/02 , B01D2325/20 , C01P2002/72 , C01P2006/12 , C01P2006/16 , C10G2300/107 , C10G2300/1044 , C10G2300/1051 , C10G2300/1077 , C10G2300/205 , C10G2300/206 , C10G2300/208 , C10G2400/30 , C10L2290/542
摘要： Disclosed herein are carbon molecular sieves and methods of making the same through the pyrolysis of a polymer precursor in the presence of a reactive gas stream including a hydrogen source.
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公开(公告)号：US20190185767A1
公开(公告)日：2019-06-20
申请号：US16284077
申请日：2019-02-25
IPC分类号： C10G67/06 , C10G49/00 , H01M8/0612 , H01M8/0662 , C10G25/00 , C10G45/02
CPC分类号： C10G67/06 , C10G25/003 , C10G45/02 , C10G49/007 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/202 , C10G2300/207 , C10G2400/02 , C10G2400/04 , C10G2400/08 , H01M8/0618 , H01M8/0675
摘要： A fuel processing system and method for a sulfur bearing fuel include a hydrodesulfurization reactor followed by an adsorbent bed for removing sulfur or sulfur containing species from the fuel. In certain embodiments, the adsorbent bed is a ZnO bed. In another embodiment, a fuel processing system and method for a sulfur bearing fuel include a steam reformer, a hydrodesulfurization reactor, and an adsorbent bed.
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公开(公告)号：US20180142166A1
公开(公告)日：2018-05-24
申请号：US15817128
申请日：2017-11-17
CPC分类号： C10G55/06 , B01D3/14 , C10G7/00 , C10G47/02 , C10G2300/104 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2400/20
摘要： Process scheme configurations are disclosed that enable conversion of crude oil feeds with several processing units in an integrated manner into petrochemicals. The designs utilize minimum capital expenditures to prepare suitable feedstocks for the steam cracker complex. The integrated process for converting crude oil to petrochemical products including olefins and aromatics, and fuel products, includes mixed feed steam cracking and gas oil steam cracking. Feeds to the mixed feed steam cracker include light products and naphtha from hydroprocessing zones within the battery limits, recycle streams from the C3 and C4 olefins recovery steps, and raffinate from a pyrolysis gasoline aromatics extraction zone within the battery limits. Feeds to the gas oil steam cracker include unconverted oil intermediates from vacuum gas oil hydrotreating.
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公开(公告)号：US09850197B2
公开(公告)日：2017-12-26
申请号：US14563159
申请日：2014-12-08
发明人： Rafael Martinez Palou , Natalya Victorovna Likhanova , Eugenio Alejandro Flores Oropeza , Diego Javier Guzman Lucero
IPC分类号： C07C211/64 , C10G21/20 , C07C211/62 , C10G21/12 , C10G21/16 , C10G21/27 , C10G21/28 , B01D11/04 , C10G29/20
CPC分类号： C07C211/64 , B01D11/0492 , C07C211/62 , C10G21/12 , C10G21/16 , C10G21/20 , C10G21/27 , C10G21/28 , C10G29/20 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/202 , C10G2400/02 , C10G2400/04
摘要： Ionic liquids of the general formula C+A− where C+ represents an organic cation, specifically, but not limited to the imidazolium, pyridinium, isoquinolinium, ammonium types, which have aliphatic and aromatic substituents, while A− represents a carboxylate, aromatic and aliphatic anion. The ionic liquids are synthesized under conventional heating or microwave irradiation This invention is also related to the application of ionic liquids to remove sulfur compounds of naphthas through a liquid-liquid extraction and the recovery and reuse of ionic liquids by the application of heat, reduced pressure and washing with solvents.
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公开(公告)号：US09815047B2
公开(公告)日：2017-11-14
申请号：US13976655
申请日：2011-12-28
IPC分类号： C07C4/06 , B01J29/70 , C10G11/18 , C10G47/16 , C10G11/05 , B01J29/85 , B01J37/00 , C01B39/48 , C01B39/10
CPC分类号： B01J29/70 , B01J29/85 , B01J37/0009 , B01J37/0036 , B01J2229/186 , C01B39/10 , C01B39/48 , C07C4/06 , C07C2529/06 , C07C2529/40 , C10G11/05 , C10G11/18 , C10G47/16 , C10G2300/1033 , C10G2300/1048 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/301 , C10G2400/30
摘要： The catalyst for producing aromatic hydrocarbon is for producing monocyclic aromatic hydrocarbon having 6 to 8 carbon number from oil feedstock having a 10 volume % distillation temperature of 140° C. or higher and a 90 volume % distillation temperature of 380° C. or lower and contains crystalline aluminosilicate and phosphorus. A molar ratio (P/Al ratio) between phosphorus contained in the crystalline aluminosilicate and aluminum of the crystalline aluminosilicate is from 0.1 to 1.0. The production method of monocyclic aromatic hydrocarbon is a method of bringing oil feedstock having a 10 volume % distillation temperature of 140° C. or higher and a 90 volume % distillation temperature of 380° C. or lower into contact with the catalyst for producing monocyclic aromatic hydrocarbon.
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7.发明授权公开(公告)号：US09725973B2
公开(公告)日：2017-08-08
申请号：US14685968
申请日：2015-04-14
IPC分类号： C10G31/06 , C10G33/00 , C10G33/06 , E21B43/34 , E21B21/06 , B01D3/02 , B01D45/16 , C10G7/00 , C10G31/10 , B01D3/00 , B01D3/08 , B01D17/04 , C02F1/04 , C02F103/10
CPC分类号： E21B21/065 , B01D3/007 , B01D3/02 , B01D3/08 , B01D17/042 , B01D45/16 , C02F1/04 , C02F2103/10 , C10G7/006 , C10G31/06 , C10G31/10 , C10G2300/1007 , C10G2300/1033 , C10G2300/1051 , C10G2300/1055 , C10G2300/1081 , C10G2300/1088 , C10G2300/1096 , C10G2300/208 , E21B21/062 , E21B21/063 , E21B43/34
摘要： Methods and processes for recycling base oils from spent invert emulsion drilling fluids may include frictionally heating a spent drilling fluid that comprises an invert emulsion and solids, wherein the solids are at about 50% or less by volume of the spent drilling fluid; and simultaneously evaporating oil and water from the invert emulsion at a temperature lower than an atmospheric boiling point for the oil.
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公开(公告)号：US20170044444A1
公开(公告)日：2017-02-16
申请号：US15118588
申请日：2015-02-11
申请人： ECOLAB USA INC.
IPC分类号： C10G21/20 , B01D53/78 , C07D403/14 , B01D53/52
CPC分类号： C10G21/20 , B01D53/52 , B01D53/77 , B01D53/78 , B01D2256/24 , B01D2257/306 , C07D251/04 , C07D401/12 , C07D403/14 , C07D409/12 , C10G29/20 , C10G2300/1051 , C10G2300/207
摘要： A process for scavenging hydrogen sulfide present in a fluid stream is provided. The process includes treating the fluid stream with a polytriazine, wherein the polytriazine converts the hydrogen sulfide to a corresponding thiol or thioether derivative, thereby reducing the amount of hydrogen sulfide present in the fluid stream.
摘要翻译： 提供了清除存在于流体流中的硫化氢的方法。 该方法包括用多三嗪处理流体物流，其中聚三嗪将硫化氢转化成相应的硫醇或硫醚衍生物，从而减少流体物流中存在的硫化氢的量。
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公开(公告)号：US09505993B2
公开(公告)日：2016-11-29
申请号：US14572946
申请日：2014-12-17
CPC分类号： C10G67/02 , C10G45/04 , C10G45/08 , C10G65/04 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/202 , C10G2400/02 , C10G2400/04 , C10G2400/06
摘要： A process for the concomitant production of at least two hydrocarbon cuts with low sulphur contents from a mixture of hydrocarbons having a total sulphur content in the range 30 to 10000 ppm by weight, by a) hydrodesulphurization in the presence of hydrogen and a hydrodesulphurization catalyst; b) separating hydrogen sulphide from the partially desulphurized effluent obtained from a); c) hydrodesulphurization of the partially desulphurized mixture obtained from b) in the presence of hydrogen and a hydrodesulphurization catalyst, the temperature of the second hydrodesulphurization being higher than that of the first hydrodesulphurization; d) fractionating the desulphurized mixture obtained in c) into at least two desulphurized hydrocarbon cuts.
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10.发明申请公开(公告)号：US20160273285A1
公开(公告)日：2016-09-22
申请号：US14435535
申请日：2014-05-27
CPC分类号： E21B21/065 , B01D3/007 , B01D3/02 , B01D3/08 , B01D17/042 , B01D45/16 , C02F1/04 , C02F2103/10 , C10G7/006 , C10G31/06 , C10G31/10 , C10G2300/1007 , C10G2300/1033 , C10G2300/1051 , C10G2300/1055 , C10G2300/1081 , C10G2300/1088 , C10G2300/1096 , C10G2300/208 , E21B21/062 , E21B21/063 , E21B43/34
摘要： Methods and processes for recycling base oils from spent invert emulsion drilling fluids may include frictionally heating a spent drilling fluid that comprises an invert emulsion and solids, wherein the solids are at about 50% or less by volume of the spent drilling fluid; and simultaneously evaporating oil and water from the invert emulsion at a temperature lower than an atmospheric boiling point for the oil.
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