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公开(公告)号:US20240042405A1
公开(公告)日:2024-02-08
申请号:US18490430
申请日:2023-10-19
发明人: Sreekanth Pannala , Vladimir Shtern , Lei Chen , David West
CPC分类号: B01J6/008 , B01J4/005 , B01J12/005 , B01J19/0053 , B01J19/02 , B01J19/2415 , C07C2/78 , B01J19/2405 , B01J19/246 , B01J2204/002 , B01J2219/00094 , B01J2219/1943 , C07C11/24
摘要: A reactor (12) and method for the conversion of hydrocarbons utilizes a reactor (12) having a unique feed assembly (56) that creates an inwardly spiraling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a conduit (46) with a constricted neck portion or nozzle (52). At least a portion of the swirling gas mixture forms a thin, annular mixed gas flow layer immediately adjacent to the conduit (46). A portion of the swirling gas mixture is combusted as the swirling gas mixture passes through the conduit (46) for conversion of hydrocarbons.
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公开(公告)号:US10059640B2
公开(公告)日:2018-08-28
申请号:US15129094
申请日:2015-03-25
申请人: BASF SE
发明人: Maximilian Vicari , Susanne Britzius , Lilian Kara-Hippen , Michael Russ , Matthias Kern , Christian Weichert
IPC分类号: C07C11/24 , C07C2/78 , B01D3/14 , C01B3/36 , C07D207/267 , C07C15/073 , C07C15/06 , C07C9/04 , C07C9/06 , C07C11/04 , C07C9/14 , C07C15/58 , C07C15/04 , C07C15/08
CPC分类号: C07C2/78 , B01D3/14 , B01J2219/00006 , C01B3/36 , C07C9/04 , C07C9/06 , C07C9/14 , C07C11/04 , C07C11/24 , C07C15/04 , C07C15/06 , C07C15/073 , C07C15/08 , C07C15/58 , C07D207/267
摘要: An apparatus (10) for the preparation of acetylene and synthesis gas by partial oxidation of hydrocarbons with oxygen is proposed. The apparatus (10) comprises a reactor (12), wherein the reactor (12) comprises a burner block (14) with a furnace chamber for the preparation of a composition C1 comprising at least acetylene and substituted acetylene, a first scrubber (22) which is constructed for adding a solvent to the composition C1 to obtain a composition C2, a second scrubber (26) which is constructed for adding the solvent to the composition C2 to obtain a composition C3, a first stripper (36) which is constructed for stripping the composition C3 to obtain a composition C4 comprising the substituted acetylene, acetylene and the solvent and for separating off the acetylene, a first column (46) which is constructed for partial degassing of the composition C4 under a pressure of from 1.0 bar to 1.5 bar to obtain a composition C5 and a first amount A1 of the solvent, a second stripper (56) to which the composition C5 can be fed for stripping a composition C9 to obtain a second amount A2 of the solvent and a composition C6, a third stripper (68) which is constructed for stripping the solvent from the first scrubber (22) to obtain a composition C9, wherein the third striper (68) is connected to the second stripper (56) for feeding the composition C9 to the second stripper (56), an apparatus (72) for adding a diluting gas to the composition C5, which is arranged between the first column (46) and the second stripper (56), a second column (76) which is constructed for adding water to the composition C6 to obtain a composition C7 comprising a third amount A3 of the solvent and water and to obtain a composition C8 comprising the substituted acetylene, and a mixing condenser (82) which is constructed for adding water to the composition C8 to obtain a composition C11 comprising the substituted acetylene.A process for the preparation of acetylene and synthesis gas by partial oxidation of hydrocarbons with oxygen is further proposed.
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3.
公开(公告)号:US20180155258A1
公开(公告)日:2018-06-07
申请号:US15829067
申请日:2017-12-01
申请人: L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude , Kyoto University
IPC分类号: C07C7/12 , B01J20/22 , B01D53/047 , B01D53/04
CPC分类号: C07C7/12 , B01D53/02 , B01D53/0454 , B01D53/047 , B01D2253/204 , B01D2256/24 , B01D2256/245 , B01D2257/7022 , B01D2257/7025 , B01D2259/40007 , B01J20/223 , C07C9/04 , C07C9/06 , C07C11/04 , C07C11/24
摘要: The present invention provides a gas separation system and a gas separation method capable of separating various types of hydrocarbon gas with high selectivity, and a gas separation system is for separating one type or more of hydrocarbon gases from mixed gas consisting of two types or more of hydrocarbon gases; having a porous metal-organic complex having pores determined by metal ion-containing planar ligands facing each other and pillar ligands coordinating between the planar ligands, and a controller for controlling at least a pressure of the mixed gas; and in which the pressure is controlled to control adsorption of the hydrocarbon gas to the porous metal-organic complex or desorption thereof from the porous metal-organic complex.
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公开(公告)号:US09815919B2
公开(公告)日:2017-11-14
申请号:US15099844
申请日:2016-04-15
IPC分类号: C07C51/14 , C08F110/06 , C07C29/16 , C07C1/20 , C07C1/24 , C07C2/76 , C07C5/09 , C07C2/40 , C07C2/48 , C07C2/84 , C07C11/04 , C07C11/12 , C07C11/21 , C07C15/04 , C07C15/06 , C07C29/48 , C07C31/10 , C07C45/50 , C07C47/02 , C07C1/207 , C08F110/02 , C10B57/16
CPC分类号: C08F110/06 , C07C1/20 , C07C1/2076 , C07C1/24 , C07C2/403 , C07C2/48 , C07C2/76 , C07C2/84 , C07C5/09 , C07C11/04 , C07C11/12 , C07C11/21 , C07C15/04 , C07C15/06 , C07C29/16 , C07C29/48 , C07C31/10 , C07C45/505 , C07C47/02 , C07C51/14 , C08F110/02 , C10B57/16 , Y02P30/42 , C07C11/06 , C07C11/24
摘要: The invention relates to a process for converting hydrocarbons into products containing aldehydes and/or alcohols. The invention also relates to producing olefins from the aldehyde and alcohol, to polymerizing the olefins, and to equipment useful for these processes.
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公开(公告)号:US09809506B2
公开(公告)日:2017-11-07
申请号:US15294898
申请日:2016-10-17
IPC分类号: G05B17/00 , C07C2/00 , C07C4/02 , C07C4/04 , B01J19/24 , C07C5/327 , B01J8/04 , C07C11/04 , C10G9/26 , C07C5/32
CPC分类号: C07C4/04 , B01J8/04 , B01J8/0438 , B01J8/0496 , B01J19/24 , B01J19/2415 , B01J19/2485 , B01J2208/00513 , B01J2208/00548 , B01J2219/00076 , B01J2219/00087 , B01J2219/00164 , B01J2219/24 , C07C5/32 , C07C5/327 , C07C11/04 , C10G9/26 , C07C11/24
摘要: The invention relates to a hydrocarbon conversion process and a reactor configured to carry out the hydrocarbon conversion process. The hydrocarbon conversion process is directed to increasing the overall equilibrium production of ethylene from typical pyrolysis reactions. The hydrocarbon conversion process can be carried out by exposing a hydrocarbon feed to a peak pyrolysis gas temperature in a reaction zone in the range of from 850° C. to 1200° C.
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公开(公告)号:US20170291861A1
公开(公告)日:2017-10-12
申请号:US15630146
申请日:2017-06-22
申请人: UOP LLC
发明人: Robert L. Bedard , Christopher Naunheimer , Gavin P. Towler , Laura E. Leonard , Gregory O. Woodcock , Donald L. Mittendorf , Aziz Sattar , Christopher D. Gatto , Robert S. Murray
CPC分类号: C07C2/78 , B01J6/008 , B01J19/02 , B01J19/2415 , B01J19/26 , B01J2219/00094 , B01J2219/00123 , B01J2219/00157 , B01J2219/0204 , B01J2219/0236 , B01J2219/0263 , B01J2219/0281 , B01J2219/0286 , B01J2219/029 , C10G50/00 , C10G2300/1025 , C10G2400/24 , C07C11/24
摘要: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.
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公开(公告)号:US20170291860A1
公开(公告)日:2017-10-12
申请号:US15629447
申请日:2017-06-21
申请人: UOP LLC
发明人: Robert L. Bedard , Christopher Naunheimer , Gavin P. Towler , Laura E. Leonard , Rodolphe Dudebout , Gregory O. Woodcock , Donald L. Mittendorf , Aziz Sattar , Christopher D. Gatto , Robert S. Murray
CPC分类号: C07C2/78 , B01J6/008 , B01J19/02 , B01J19/10 , B01J19/2415 , B01J19/26 , B01J2219/00094 , B01J2219/00123 , B01J2219/00157 , B01J2219/0204 , B01J2219/0236 , B01J2219/0263 , B01J2219/0281 , B01J2219/0286 , B01J2219/029 , C10G50/00 , C10G2300/1025 , C10G2400/24 , C07C11/24
摘要: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.
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公开(公告)号:US20170216809A1
公开(公告)日:2017-08-03
申请号:US15491280
申请日:2017-04-19
申请人: UOP LLC
发明人: Robert L. Bedard , Christopher Naunheimer , Gavin P. Towler , Laura E. Leonard , Rodolphe Dudebout , Gregory O. Woodcock , Donald L. Mittendorf
CPC分类号: B01J19/10 , B01J3/008 , B01J6/008 , B01J19/02 , B01J19/2415 , B01J19/26 , B01J2219/00094 , B01J2219/00123 , B01J2219/00157 , B01J2219/0204 , B01J2219/0236 , B01J2219/0263 , B01J2219/0281 , B01J2219/0286 , B01J2219/029 , C07C2/78 , C10G50/00 , C10G2300/1025 , C10G2400/24 , C07C11/24
摘要: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.
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公开(公告)号:US20170036971A1
公开(公告)日:2017-02-09
申请号:US15294898
申请日:2016-10-17
CPC分类号: C07C4/04 , B01J8/04 , B01J8/0438 , B01J8/0496 , B01J19/24 , B01J19/2415 , B01J19/2485 , B01J2208/00513 , B01J2208/00548 , B01J2219/00076 , B01J2219/00087 , B01J2219/00164 , B01J2219/24 , C07C5/32 , C07C5/327 , C07C11/04 , C10G9/26 , C07C11/24
摘要: The invention relates to a hydrocarbon conversion process and a reactor configured to carry out the hydrocarbon conversion process. The hydrocarbon conversion process is directed to increasing the overall equilibrium production of ethylene from typical pyrolysis reactions. The hydrocarbon conversion process can be carried out by exposing a hydrocarbon feed to a peak pyrolysis gas temperature in a reaction zone in the range of from 850° C. to 1200° C.
摘要翻译: 本发明涉及一种碳氢化合物转化方法和一种配置成进行烃转化方法的反应器。 烃转化过程旨在从典型的热解反应中增加乙烯的总体平衡产生。 烃转化方法可以通过将烃进料暴露于850℃至1200℃范围内的反应区中的峰值热解气体温度来进行。
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公开(公告)号:US09499457B2
公开(公告)日:2016-11-22
申请号:US14942287
申请日:2015-11-16
IPC分类号: C07C2/00 , C07C4/02 , G05B17/00 , C07C4/04 , B01J19/24 , C07C5/327 , B01J8/04 , C07C11/04 , C10G9/26
CPC分类号: C07C4/04 , B01J8/04 , B01J8/0438 , B01J8/0496 , B01J19/24 , B01J19/2415 , B01J19/2485 , B01J2208/00513 , B01J2208/00548 , B01J2219/00076 , B01J2219/00087 , B01J2219/00164 , B01J2219/24 , C07C5/32 , C07C5/327 , C07C11/04 , C10G9/26 , C07C11/24
摘要: The invention relates to a hydrocarbon conversion process and a reactor configured to carry out the hydrocarbon conversion process. The hydrocarbon conversion process is directed to increasing the overall equilibrium production of ethylene from typical pyrolysis reactions. The hydrocarbon conversion process can be carried out by exposing a hydrocarbon feed to a peak pyrolysis gas temperature in a reaction zone in the range of from 850° C. to 1200° C.
摘要翻译: 本发明涉及一种碳氢化合物转化方法和一种配置成进行烃转化方法的反应器。 烃转化过程旨在从典型的热解反应中增加乙烯的总体平衡产生。 烃转化方法可以通过将烃进料暴露于850℃至1200℃范围内的反应区中的峰值热解气体温度来进行。
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