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公开(公告)号：US09528051B2
公开(公告)日：2016-12-27
申请号：US13327170
申请日：2011-12-15
CPC分类号： C10G59/04 , C10G69/08 , C10G2400/30
摘要： A process for reforming hydrocarbons is presented. The process involves applying process controls over the reaction temperatures to preferentially convert a portion of the hydrocarbon stream to generate an intermediate stream, which will further react with reduced endothermicity. The intermediate stream is then processed at a higher temperature, where a second reforming reactor is operated under substantially isothermal conditions.
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公开(公告)号：US09266091B2
公开(公告)日：2016-02-23
申请号：US13547335
申请日：2012-07-12
IPC分类号： B01J23/58 , C10G35/09 , B01J37/18 , B01J21/04 , B01J23/62 , B01J27/10 , B01J35/08 , B01J37/00 , B01J37/02 , B01J27/13 , B01J27/135 , B01J27/138
CPC分类号： B01J23/58 , B01J21/04 , B01J23/626 , B01J27/10 , B01J27/13 , B01J27/135 , B01J27/138 , B01J35/08 , B01J37/0072 , B01J37/0201 , B01J37/18 , C10G35/09
摘要： One exemplary embodiment can be a catalyst for catalytic reforming of naphtha. The catalyst can have a noble metal including one or more of platinum, palladium, rhodium, ruthenium, osmium, and iridium, at least two alkali metals or at least two alkaline earth metals, or mixtures of alkali metals and alkaline earth metals and a support.
摘要翻译： 一个示例性实施方案可以是用于石脑油的催化重整的催化剂。 催化剂可以具有包括铂，钯，铑，钌，锇和铱中的一种或多种的贵金属，至少两种碱金属或至少两种碱土金属，或碱金属和碱土金属的混合物和载体 。
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公开(公告)号：US08608952B2
公开(公告)日：2013-12-17
申请号：US12945786
申请日：2010-11-12
申请人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
发明人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
CPC分类号： C10G21/24 , C10G21/28 , C10G33/04 , C10G2300/1033 , C10G2300/203 , C10G2300/4081 , C10G2300/805
摘要： A process for de-acidifying a hydrocarbon feed includes contacting the hydrocarbon feed containing an organic acid with a feed-immiscible phosphonium ionic liquid to produce a hydrocarbon and feed-immiscible phosphonium ionic liquid mixture and separating the mixture to produce a hydrocarbon effluent having a reduced organic acid content relative to the hydrocarbon feed. Optionally, a de-emulsifier is added to at least one of the contacting and separating steps.
摘要翻译： 用于使烃进料脱酸的方法包括将含有机酸的烃进料与进料不混溶的鏻离子液体接触以产生烃和进料不混溶的鏻离子液体混合物，并分离混合物以产生具有还原的 有机酸含量相对于烃进料。 任选地，将去乳化剂加入到至少一个接触和分离步骤中。
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公开(公告)号：US20130256194A1
公开(公告)日：2013-10-03
申请号：US13547335
申请日：2012-07-12
CPC分类号： B01J23/58 , B01J21/04 , B01J23/626 , B01J27/10 , B01J27/13 , B01J27/135 , B01J27/138 , B01J35/08 , B01J37/0072 , B01J37/0201 , B01J37/18 , C10G35/09
摘要： One exemplary embodiment can be a catalyst for catalytic reforming of naphtha. The catalyst can have a noble metal including one or more of platinum, palladium, rhodium, ruthenium, osmium, and iridium, at least two alkali metals or at least two alkaline earth metals, or mixtures of alkali metals and alkaline earth metals and a support.
摘要翻译： 一个示例性实施方案可以是用于石脑油的催化重整的催化剂。 催化剂可以具有包括铂，钯，铑，钌，锇和铱中的一种或多种的贵金属，至少两种碱金属或至少两种碱土金属，或碱金属和碱土金属的混合物和载体 。
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5.发明申请INTEGRATED HYDROGENATION/DEHYDROGENATION REACTOR IN A CATALYTIC REFORMING PROCESS CONFIGURATION FOR IMPROVED AROMATICS PRODUCTION 有权用于改进芳族化合物生产的催化重整工艺配置中的集成氢化/脱氢反应器公开(公告)号：US20130158313A1
公开(公告)日：2013-06-20
申请号：US13327192
申请日：2011-12-15
IPC分类号： C07C5/42
CPC分类号： C07C5/41 , C07C15/04 , C07C15/06 , C10G35/04 , C10G35/085 , C10G35/095 , C10G35/24 , C10G59/00 , C10G59/02 , C10G69/08 , C10G2400/30
摘要： A process for reforming hydrocarbons is presented. The process involves applying process controls over the reaction temperatures to preferentially convert a portion of the hydrocarbon stream to generate an intermediate stream, which will further react with reduced endothermicity. The intermediate stream is then processed at a higher temperature, where a second reforming reactor is operated under substantially isothermal conditions.
摘要翻译： 介绍了烃类重整方法。 该方法包括对反应温度进行过程控制以优先转化一部分烃流以产生中间流，其将进一步与降低的吸热性反应。 然后在较高温度下处理中间物流，其中第二重整反应器在基本等温条件下操作。
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公开(公告)号：US20120277507A1
公开(公告)日：2012-11-01
申请号：US13416604
申请日：2012-03-09
CPC分类号： C10G35/06 , C10G35/04 , C10G35/065 , C10G35/085 , C10G59/06 , C10G2300/1044 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
摘要翻译： 提出了一种重整烃流的方法。 该方法包括将石脑油进料流分成至少两个进料流并将每个进料流通过分离重整器。 改性剂在不同条件下运行，以利用不同烃组分的反应性质的差异。 该方法利用普通的催化剂和用于回收生成的所需芳族化合物的常见的下游方法。
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7.发明申请Adsorbing Polynuclear Aromatics From a Reforming Process Using Adsorbents Containing Iron 有权使用含有铁的吸附剂从重整过程吸附多核芳烃公开(公告)号：US20110152589A1
公开(公告)日：2011-06-23
申请号：US12701187
申请日：2010-02-05
申请人： Manuela Serban , Mark P. Lapinski , Mark D. Moser
发明人： Manuela Serban , Mark P. Lapinski , Mark D. Moser
CPC分类号： C10G25/003 , C10G61/06 , C10G2300/1044 , C10G2300/1096 , C10G2300/301 , C10G2300/305 , C10G2300/4018 , C10G2400/02
摘要： An exemplary embodiment can be a process for removing one or more polynuclear aromatics from at least one reformate stream from a reforming zone. The PNAs may be removed using an adsorption zone. The adsorption zone can include first and second vessels each vessel containing an activated carbon adsorbent. Generally, the process includes passing the at least a portion of an effluent of the reforming zone through the first vessel containing a first activated carbon adsorbent wherein the first activated carbon adsorbent comprises iron.
摘要翻译： 示例性实施方案可以是从重整区从至少一种重整产物流中除去一种或多种多核芳烃的方法。 可以使用吸附区去除PNA。 吸附区可以包括第一和第二容器，每个容器含有活性炭吸附剂。 通常，该方法包括使重整区的流出物的至少一部分通过包含第一活性炭吸附剂的第一容器，其中第一活性炭吸附剂包含铁。
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8.发明授权Integrated hydrogenation/dehydrogenation reactor in a catalytic reforming process configuration for improved aromatics production 有权在催化重整过程配置中用于改进芳族化合物生产的集成氢化/脱氢反应器公开(公告)号：US09024097B2
公开(公告)日：2015-05-05
申请号：US13327192
申请日：2011-12-15
IPC分类号： C10G35/04 , C07C5/02 , C07C5/41 , C07C15/04 , C07C15/06 , C10G35/085 , C10G35/095 , C10G35/24 , C10G59/02
CPC分类号： C07C5/41 , C07C15/04 , C07C15/06 , C10G35/04 , C10G35/085 , C10G35/095 , C10G35/24 , C10G59/00 , C10G59/02 , C10G69/08 , C10G2400/30
摘要： A process for reforming hydrocarbons is presented. The process involves applying process controls over the reaction temperatures to preferentially convert a portion of the hydrocarbon stream to generate an intermediate stream, which will further react with reduced endothermicity. The intermediate stream is then processed at a higher temperature, where a second reforming reactor is operated under substantially isothermal conditions.
摘要翻译： 介绍了烃类重整方法。 该方法包括对反应温度进行过程控制以优先转化一部分烃流以产生中间流，其将进一步与降低的吸热性反应。 然后在较高温度下处理中间物流，其中第二重整反应器在基本等温条件下操作。
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公开(公告)号：US08608949B2
公开(公告)日：2013-12-17
申请号：US12945752
申请日：2010-11-12
申请人： Alakananda Bhattacharyya , Manuela Serban , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Joseph A. Kocal , Warren K. Bennion
发明人： Alakananda Bhattacharyya , Manuela Serban , Beckay J. Mezza , Kurt M. Vanden Bussche , Christopher P. Nicholas , Joseph A. Kocal , Warren K. Bennion
CPC分类号： C10G21/08 , B01D11/043 , B01D11/0492 , C10G21/28 , C10G2300/1074 , C10G2300/206 , C10G2300/4081 , C10G2300/805 , C10G2400/06
摘要： A process for removing a metal from a vacuum gas oil feed includes contacting the vacuum gas oil feed comprising the metal with a VGO-immiscible ionic liquid to produce a vacuum gas oil and VGO-immiscible ionic liquid mixture, and separating the mixture to produce a vacuum gas oil effluent having a reduced metal content relative to the vacuum gas oil feed.
摘要翻译： 从真空瓦斯油进料中除去金属的方法包括使包含金属的真空瓦斯油进料与VGO不混溶的离子液体接触以产生真空瓦斯油和VGO不混溶的离子液体混合物，并分离混合物以产生 减压瓦斯油流出物相对于真空瓦斯油进料具有降低的金属含量。
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公开(公告)号：US20130158317A1
公开(公告)日：2013-06-20
申请号：US13327220
申请日：2011-12-15
IPC分类号： C07C15/00
CPC分类号： C07C15/00 , C10G35/00 , C10G59/00 , C10G2400/30
摘要： A process for the production of aromatics through the reforming of a hydrocarbon stream is presented. The process utilizes the differences in properties of components within the hydrocarbon stream to increase the energy efficiency. The differences in the reactions of different hydrocarbon components in the conversion to aromatics allows for different treatments of the different components to reduce the energy used in reforming process.
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