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1.发明授权Process for separating and/or introducing a flush material in an adsorption separation system 有权用于在吸附分离系统中分离和/或引入冲洗材料的方法公开(公告)号：US08404916B1
公开(公告)日：2013-03-26
申请号：US13310954
申请日：2011-12-05
IPC分类号： C07C7/12
摘要： Embodiments of the present invention provide, for an adsorption separation system for separating normal paraffins from a hydrocarbon feed stream, a process for switching the adsorption separation from a triple split desorbent system to a dual split desorbent system, and vice versa. Switching occurs by separating and/or introducing a second flush material in the adsorption separation system. This switching can occur during normal operations.
摘要翻译： 本发明的实施方案提供了用于从烃进料流中分离正链烷烃的吸附分离系统，用于将吸附分离从三分裂解吸系统切换到双分离解吸系统，反之亦然。 通过在吸附分离系统中分离和/或引入第二冲洗材料进行切换。 这种切换可能在正常操作期间发生。
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2.发明申请PROCESS FOR UPGRADING SWEETENED OR OXYGEN-CONTAMINATED KEROSENE OR JET FUEL, TO MINIMIZE OR ELIMINATE ITS TENDENCY TO POLYMERIZE OR FOUL WHEN HEATED 有权升级清洁或氧化污染的凯龙或喷射燃料的过程，以最小化或消除其在加热时聚合或加热的趋势公开(公告)号：US20110319698A1
公开(公告)日：2011-12-29
申请号：US13154572
申请日：2011-06-07
CPC分类号： C10G31/06 , C10G7/00 , C10G2300/1051 , C10G2300/202 , C10G2400/08
摘要： A process is presented for the removal of oxygen from a hydrocarbon stream. The oxygen can react and cause polymerization of the hydrocarbons when the hydrocarbon stream is heated. Controlling the removal of the oxygen from the hydrocarbon stream produces a hydrocarbon stream that is substantially free of oxygen and has a reduced activity for generating undesired compounds.
摘要翻译： 提出了从烃流中除去氧气的方法。 当烃流被加热时，氧可以反应并引起烃的聚合。 控制从烃流中除去氧气产生基本上不含氧气并且具有降低的活性以产生不需要的化合物的烃流。
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公开(公告)号：US20100292519A1
公开(公告)日：2010-11-18
申请号：US12467622
申请日：2009-05-18
IPC分类号： C07C2/00
CPC分类号： C07C6/126 , C07C7/1485 , C07C2521/04 , C07C2521/08 , C07C2529/08 , C07C2529/70 , C07C15/073 , C07C15/085 , C07C15/02
摘要： Byproduct formation in aromatic alkylation processes is reduced when different polyalkylated aromatic compounds are first fractionated into separate streams enriched in these respective polyalkylated aromatic compounds, and the separate streams are sent to different transalkylation reaction zones, which may or may not be in the same reactor. The different transalkylation reaction zones allow for greater control of the transalkylation of the respective polyalkylated aromatic compounds, such as diisopropylbenzene (DIPB) and triisopropylbenzene (TIPB) that accompany the alkylation of benzene with propylene in a process for cumene production.
摘要翻译： 当将不同的多烷基化芳族化合物首先分馏成富含这些各自的多烷基化芳族化合物的分离的流中时，芳族烷基化方法中的副产物形成降低，并且将分离的物流送入不同的烷基转移反应区，其可以是或不在同一个反应器中。 不同的烷基转移反应区可以更好地控制各种多烷基化芳族化合物如二异丙基苯（DIPB）和三异丙基苯（TIPB）在烷基化反应过程中伴随苯与丙烯烷基化反应的烷基转移。
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公开(公告)号：US07525003B2
公开(公告)日：2009-04-28
申请号：US11752508
申请日：2007-05-23
IPC分类号： C07C15/073 , C07C2/64
CPC分类号： C07C15/073 , C07C2/66 , C07C6/126
摘要： This ethylbenzene process involves contacting, in an alkylation zone, a first benzene recycle stream and an ethylene feed stream with an alkylation catalyst to form ethylbenzene. In a transalkylation zone, a polyethylbenzene recycle stream and a second benzene recycle stream are contacted with a transalkylation catalyst to form additional ethylbenzene. The effluents are passed into a dividing wall distillation column where a benzene overhead and a benzene side draw are removed and recycled. An ethylbenzene stream product stream is also removed. The remainder, largely polyethylbenzene and tar, is passed to a polyethylbenzene column for separation. The separated polyethylbenzene is recycled to the transalkylation reactor.
摘要翻译： 该乙苯方法包括在烷基化区中与烷基化催化剂接触第一苯再循环流和乙烯进料流以形成乙苯。 在烷基转移区中，将聚乙苯再循环流和第二苯再循环流与烷基转移催化剂接触以形成另外的乙苯。 流出物被送入分离塔蒸馏塔，其中苯塔顶馏出物和苯侧馏分被除去并再循环。 还除去乙苯料流产物流。 其余的，主要是聚乙苯和焦油，被送到聚乙苯塔进行分离。 将分离的聚乙苯再循环至烷基转移反应器。
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公开(公告)号：US20080289946A1
公开(公告)日：2008-11-27
申请号：US11752532
申请日：2007-05-23
IPC分类号： B01D3/14
摘要： The apparatus includes an alkylation unit connected to a first benzene recycle conduit, a feed conduit and an alkylation effluent conduit; a transalkylation unit connected to an polyalkylbenzene recycle conduit, a second benzene recycle conduit, and a transalkylation effluent conduit. A dividing wall distillation column is in fluid communication with the transalkylation effluent conduit, the alkylation effluent conduit, a product stream, a bottoms stream conduit and first and second benzene recycle conduits. A polyalkylbenzene fractionation column is connected to the bottoms stream conduit, the polyalkylbenzene recycle conduit and a heavy component conduit.
摘要翻译： 该装置包括连接到第一苯循环导管，进料管和烷基化流出物导管的烷基化单元; 连接到多烷基苯再循环导管，第二苯循环导管和烷基转移流出物导管的烷基转移单元。 分隔壁蒸馏塔与烷基转移流出物导管，烷基化流出物导管，产物流，塔底流导管和第一和第二苯循环导管流体连通。 多烷基苯分馏塔连接到底部料流管道，聚烷基苯再循环管道和重组分管道。
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6.发明授权
公开(公告)号：US5013424A
公开(公告)日：1991-05-07
申请号：US559820
申请日：1990-07-30
IPC分类号： A62D3/00 , A62D3/37 , A62D101/22 , A62D101/24 , B01J23/44 , B01J23/88 , C10G1/00 , C10G45/02 , C10G65/04 , C10G65/12 , C10M175/00 , C10N40/08 , C10N40/22
CPC分类号： A62D3/37 , C10G45/02 , A62D2101/22 , A62D2101/24 , A62D2203/02
摘要： A process for the production of hydrogenated, distillable hydrocarbonaceous product from a feed comprising hydrocarbonaceous compounds and having a non-distillable component, and a feed comprising halogenated organic compounds by means of contacting the feed comprising hydrocarbonaceous compounds and having a non-distillable component with a hot hydrogen-rich gaseous stream to increase the temperature of this feed stream to vaporize at least a portion of the distillable hydrocarbonaceous compounds thereby producing a distillable hydrocarbonaceous product which is immediately hydrogenated in an integrated hydrogenation zone. The feed comprising halogenated organic compounds is contacted in a second hydrogenated hydrocarbonaceous product and at least one water-soluble inorganic halide compound.
摘要翻译： 一种从包含烃类化合物并具有不可蒸馏组分的原料生产氢化，可蒸馏的含烃产物的方法，以及包含卤化有机化合物的进料，其通过使包含烃类化合物的进料与含有不可蒸馏组分的物质接触， 热的富氢气流以增加该进料流的温度以蒸发至少一部分可蒸馏烃类化合物，从而产生可在一体化氢化区中立即氢化的可蒸馏烃类产物。 包含卤代有机化合物的进料在第二氢化烃产物和至少一种水溶性无机卤化物化合物中接触。
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公开(公告)号：US09150469B2
公开(公告)日：2015-10-06
申请号：US12467622
申请日：2009-05-18
CPC分类号： C07C6/126 , C07C7/1485 , C07C2521/04 , C07C2521/08 , C07C2529/08 , C07C2529/70 , C07C15/073 , C07C15/085 , C07C15/02
摘要： Byproduct formation in aromatic alkylation processes is reduced when different polyalkylated aromatic compounds are first fractionated into separate streams enriched in these respective polyalkylated aromatic compounds, and the separate streams are sent to different transalkylation reaction zones, which may or may not be in the same reactor. The different transalkylation reaction zones allow for greater control of the transalkylation of the respective polyalkylated aromatic compounds, such as diisopropylbenzene (DIPB) and triisopropylbenzene (TIPB) that accompany the alkylation of benzene with propylene in a process for cumene production.
摘要翻译： 当将不同的多烷基化芳族化合物首先分馏成富含这些各自的多烷基化芳族化合物的分离的流中时，芳族烷基化方法中的副产物形成降低，并且将分离的物流送入不同的烷基转移反应区，其可以是或不在同一个反应器中。 不同的烷基转移反应区可以更好地控制各种多烷基化芳族化合物如二异丙基苯（DIPB）和三异丙基苯（TIPB）在烷基化反应过程中伴随苯与丙烯烷基化反应的烷基转移。
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公开(公告)号：US20120103194A1
公开(公告)日：2012-05-03
申请号：US12913243
申请日：2010-10-27
IPC分类号： B01D19/00
CPC分类号： B01D19/0005
摘要： A process is presented for the removal of dissolved oxygen from hydrocarbon streams. The hydrocarbons streams include kerosene and jet fuels. The process includes mixing the hydrocarbons streams with an oxygen free gas to form a gas-liquid mixture. The mixture is allowed to disengage into a gas stream and a liquid stream, thereby removing dissolved oxygen from the hydrocarbon stream.
摘要翻译： 介绍了从烃流中去除溶解氧的过程。 烃流包括煤油和喷气燃料。 该方法包括将烃流与无氧气体混合以形成气液混合物。 使混合物脱离成气流和液体流，从而从烃流中除去溶解的氧。
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公开(公告)号：US07713386B2
公开(公告)日：2010-05-11
申请号：US11752532
申请日：2007-05-23
摘要： The apparatus includes an alkylation unit connected to a first benzene recycle conduit, a feed conduit and an alkylation effluent conduit; a transalkylation unit connected to an polyalkylbenzene recycle conduit, a second benzene recycle conduit, and a transalkylation effluent conduit. A dividing wall distillation column is in fluid communication with the transalkylation effluent conduit, the alkylation effluent conduit, a product stream, a bottoms stream conduit and first and second benzene recycle conduits. A polyalkylbenzene fractionation column is connected to the bottoms stream conduit, the polyalkylbenzene recycle conduit and a heavy component conduit.
摘要翻译： 该装置包括连接到第一苯循环导管，进料管和烷基化流出物导管的烷基化单元; 连接到多烷基苯再循环导管，第二苯循环导管和烷基转移流出物导管的烷基转移单元。 分隔壁蒸馏塔与烷基转移流出物导管，烷基化流出物导管，产物流，塔底流导管和第一和第二苯循环导管流体连通。 多烷基苯分馏塔连接到底部料流管道，聚烷基苯再循环管道和重组分管道。
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公开(公告)号：US07525004B2
公开(公告)日：2009-04-28
申请号：US11752516
申请日：2007-05-23
IPC分类号： C07C15/073 , C07C2/64
CPC分类号： C07C2/66 , C07C6/126 , C07C15/073
摘要： This ethylbenzene process involves contacting, in an alkylation zone, a first benzene recycle stream and an ethylene feed stream with an alkylation catalyst to form ethylbenzene. In a transalkylation zone, a polyethylbenzene recycle stream and a second benzene recycle stream are contacted with a transalkylation catalyst to form additional ethylbenzene. The effluents are passed into a benzene distillation column. From the benzene distillation column, a first benzene recycle stream is removed as overhead; a second benzene recycle stream is removed as a side draw; and a bottoms stream comprising polyethylbenzene, ethylbenzene, and flux oil is removed from an end. The bottoms stream is passed to a dividing wall distillation column where the polyethylbenzene recycle stream is removed from an intermediate point; an ethylbenzene product stream is removed from a first end, and a heavy oil stream is removed from a second end.
摘要翻译： 该乙苯方法包括在烷基化区中与烷基化催化剂接触第一苯再循环流和乙烯进料流以形成乙苯。 在烷基转移区中，将聚乙苯再循环流和第二苯再循环流与烷基转移催化剂接触以形成另外的乙苯。 将废水送入苯蒸馏塔。 从苯蒸馏塔中取出第一个苯循环物流作为塔顶馏出物; 第二个苯循环流作为侧面吸附除去; 从末端除去包含聚乙基苯，乙苯和助熔剂油的底部料流。 将塔底物流送入分隔壁蒸馏塔，其中从中间点除去多乙基苯循环物流; 从第一端去除乙苯产物流，并从第二端除去重油流。
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