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1.发明授权Hydrocarbon conversion apparatus including fluid bed reaction vessel and related processes 有权烃转化装置包括流化床反应容器及相关工艺公开(公告)号：US08691155B2
公开(公告)日：2014-04-08
申请号：US13051854
申请日：2011-03-18
CPC分类号： B01J8/24 , B01J8/1818 , C10G45/00 , C10G47/00 , C10G49/00
摘要： Embodiments of a hydrocarbon conversion apparatus are provided, as are embodiments of a hydroprocessing conversion process. In one embodiment, the hydrocarbon conversion apparatus includes a reaction vessel having a reaction chamber and a feed distribution chamber. A riser fluidly couples the feed distribution chamber to the reaction chamber, and a catalyst recirculation standpipe fluidly couples the reaction chamber to the feed distribution chamber. The catalyst recirculation standpipe forms a catalyst recirculation circuit with the reaction chamber, the feed distribution chamber, and the riser. A catalyst is circulated through the catalyst recirculation circuit during operation of the hydrocarbon conversion apparatus.
摘要翻译： 提供烃转化装置的实施方案，如加氢处理转化方法的实施方案。 在一个实施方案中，烃转化装置包括具有反应室和进料分配室的反应容器。 提升管将进料分配室流体地连接到反应室，并且催化剂再循环竖管将反应室流体地连接到进料分配室。 催化剂再循环立管与反应室，进料分配室和提升管形成催化剂再循环回路。 在烃转化装置的操作期间，催化剂循环通过催化剂再循环回路。
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2.发明申请HYDROCARBON CONVERSION APPARATUS INCLUDING FLUID BED REACTION VESSEL AND RELATED PROCESSES 有权包含流化床反应容器和相关工艺的油气转化装置公开(公告)号：US20120234725A1
公开(公告)日：2012-09-20
申请号：US13051854
申请日：2011-03-18
CPC分类号： B01J8/24 , B01J8/1818 , C10G45/00 , C10G47/00 , C10G49/00
摘要： Embodiments of a hydrocarbon conversion apparatus are provided, as are embodiments of a hydroprocessing conversion process. In one embodiment, the hydrocarbon conversion apparatus includes a reaction vessel having a reaction chamber and a feed distribution chamber. A riser fluidly couples the feed distribution chamber to the reaction chamber, and a catalyst recirculation standpipe fluidly couples the reaction chamber to the feed distribution chamber. The catalyst recirculation standpipe forms a catalyst recirculation circuit with the reaction chamber, the feed distribution chamber, and the riser. A catalyst is circulated through the catalyst recirculation circuit during operation of the hydrocarbon conversion apparatus.
摘要翻译： 提供烃转化装置的实施方案，如加氢处理转化方法的实施方案。 在一个实施方案中，烃转化装置包括具有反应室和进料分配室的反应容器。 提升管将进料分配室流体地连接到反应室，并且催化剂再循环竖管将反应室流体地连接到进料分配室。 催化剂再循环立管与反应室，进料分配室和提升管形成催化剂再循环回路。 在烃转化装置的操作期间，催化剂循环通过催化剂再循环回路。
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3.发明授权Process for converting a hydrocarbon stream, and optionally producing a hydrocracked distillate 有权用于转化烃流和任选地生产加氢裂化馏出物的方法公开(公告)号：US08691077B2
公开(公告)日：2014-04-08
申请号：US13418788
申请日：2012-03-13
CPC分类号： C10G45/58 , C10G47/26 , C10G65/10 , C10G65/12 , C10G69/04 , C10G2400/02 , C10G2400/30
摘要： One exemplary embodiment can be a process for converting a hydrocarbon stream. The process can include passing the hydrocarbon stream having one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream having one or more C9-C22 hydrocarbons, and passing the distillate hydrocarbon stream to a hydrocracking zone for selectively hydrocracking aromatic compounds including at least two rings obtaining a processed distillate product.
摘要翻译： 一个示例性实施方案可以是用于转化烃流的方法。 该方法可以包括使具有一个或多个C 40 +烃的烃流通过浆料加氢裂化区获得具有一个或多个C 9 -C 22烃的馏出物烃流，并将馏出物烃流送入加氢裂化区，以选择性加氢裂化芳族化合物，包括 至少两个环获得经处理的馏出物。
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4.发明申请公开(公告)号：US20130240406A1
公开(公告)日：2013-09-19
申请号：US13418788
申请日：2012-03-13
IPC分类号： C10G65/10
CPC分类号： C10G45/58 , C10G47/26 , C10G65/10 , C10G65/12 , C10G69/04 , C10G2400/02 , C10G2400/30
摘要： One exemplary embodiment can be a process for converting a hydrocarbon stream. The process can include passing the hydrocarbon stream having one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream having one or more C9-C22 hydrocarbons, and passing the distillate hydrocarbon stream to a hydrocracking zone for selectively hydrocracking aromatic compounds including at least two rings obtaining a processed distillate product.
摘要翻译： 一个示例性实施方案可以是用于转化烃流的方法。 该方法可以包括使具有一个或多个C 40 +烃的烃流通过浆料加氢裂化区获得具有一个或多个C 9 -C 22烃的馏出物烃流，并将馏出物烃流送入加氢裂化区，以选择性加氢裂化芳族化合物，包括 至少两个环获得经处理的馏出物。
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5.发明申请SOLID CATALYST HYDROCARBON CONVERSION PROCESS USING STACKED MOVING BED REACTORS 失效使用堆叠移动床反应器的固体催化剂碳氢化合物转化工艺公开(公告)号：US20110152591A1
公开(公告)日：2011-06-23
申请号：US12958818
申请日：2010-12-02
IPC分类号： C07C2/00
摘要： Systems and processes for hydrocarbon conversion are provided that utilize a plurality of moving bed reactors. The reactors may be moving bed radial flow reactors. Optional mixers that mix a portion of a second hydrocarbon feed with the effluent stream from an upstream reactor, to produce reactor feed streams may be employed, and the reactor feed streams may be introduced at injection points prior to each reactor. Catalyst can be provided from the reaction zone of one reactor to the reaction zone of a downstream reactor through catalyst transfer pipes, and can be regenerated after passing through the reaction zones of the reactors. The moving bed reactors can be stacked in one or more reactor stacks.
摘要翻译： 提供了利用多个移动床反应器的烃转化的系统和方法。 反应器可以是移动床径流反应器。 可以使用将一部分第二烃进料与来自上游反应器的流出物流混合以产生反应器进料流的任选混合器，并且反应器进料流可以在每个反应器之前的注入点引入。 催化剂可以通过催化剂转移管从一个反应器的反应区提供到下游反应器的反应区，并且可以在通过反应器的反应区之后再生。 移动床反应器可以堆叠在一个或多个反应器堆叠中。
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公开(公告)号：US20120275974A1
公开(公告)日：2012-11-01
申请号：US13440527
申请日：2012-04-05
IPC分类号： B01J19/00
CPC分类号： C01B3/26 , B01J8/008 , B01J8/0415 , B01J8/0492 , B01J8/0496 , B01J2208/00194 , B01J2208/0053 , B01J2219/024 , C01B2203/0277
摘要： An apparatus for reforming a hydrocarbon stream is presented. The apparatus involves changing the design of reformers and associated equipment to allow for increasing the processing temperatures in the reformers and heaters. The reformers are operated under different conditions to utilize advantages in the equilibriums, but require modifications to prevent increasing thermal cracking and to prevent increases in coking.
摘要翻译： 提出了一种用于重整烃流的装置。 该设备包括改变重整器和相关设备的设计，以允许提高重整器和加热器中的加工温度。 改造者在不同条件下运行，以利用平衡中的优点，但需要进行修改以防止增加热裂解并防止焦化增加。
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7.发明申请SOLID CATALYST HYDROCARBON ALKYLATION USING STACKED MOVING BED RADIAL FLOW REACTORS 有权固体催化剂碳氢化合物采用堆叠移动床径向流动反应器公开(公告)号：US20110152590A1
公开(公告)日：2011-06-23
申请号：US12958737
申请日：2010-12-02
IPC分类号： C07C2/00
摘要： Systems and processes for the alkylation of a hydrocarbon are provided that utilize a plurality of moving bed radial flow reactors. An olefin injection point can be provided prior to each reactor by providing a mixer that mixes olefin with a hydrocarbon feed, or with the effluent stream from an upstream reactor, to produce a reactor feed stream. Catalyst can be provided from the reaction zone of one reactor to the reaction zone of a downstream reactor through catalyst transfer pipes, and can be regenerated after passing through the reaction zones of the reactors. The moving bed radial flow reactors can be stacked in one or more reactor stacks.
摘要翻译： 提供用于烷基化烃的系统和方法，其利用多个移动床径流反应器。 可以在每个反应器之前提供烯烃注入点，通过提供将烯烃与烃进料或与上游反应器的流出物流混合以产生反应器进料流的混合器。 催化剂可以通过催化剂转移管从一个反应器的反应区提供到下游反应器的反应区，并且可以在通过反应器的反应区之后再生。 移动床径向流动反应器可以堆叠在一个或多个反应器堆叠中。
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公开(公告)号：US20110147264A1
公开(公告)日：2011-06-23
申请号：US12958765
申请日：2010-12-02
CPC分类号： C10G47/28 , B01J8/085 , B01J8/125 , B01J8/22 , B01J2208/00548 , B01J2219/0004 , C10G65/10 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2400/02 , C10G2400/04 , C10G2400/06
摘要： Systems and processes for the hydroprocessing of a hydrocarbonaceous feed are provided that utilize a plurality of moving bed reactors. The reactors may be moving bed radial flow reactors. A hydrogen injection point can be provided prior to each reactor by providing a mixer that mixes hydrogen with a hydrocarbonaceous feed, or with the effluent stream from an upstream reactor, to produce a reactor feed stream. Catalyst can be provided from the reaction zone of one reactor to the reaction zone of a downstream reactor through catalyst transfer pipes, and can be regenerated after passing through the reaction zones of the reactors. The moving bed reactors can be stacked in one or more reactor stacks.
摘要翻译： 提供了用于烃类进料的加氢处理的系统和方法，其利用多个移动床反应器。 反应器可以是移动床径流反应器。 可以在每个反应器之前提供氢注入点，通过提供将氢气与烃类进料混合的混合器，或与来自上游反应器的流出物料流一起产生反应器进料流。 催化剂可以通过催化剂转移管从一个反应器的反应区提供到下游反应器的反应区，并且可以在通过反应器的反应区之后再生。 移动床反应器可以堆叠在一个或多个反应器堆叠中。
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9.发明申请公开(公告)号：US20100018901A1
公开(公告)日：2010-01-28
申请号：US12179552
申请日：2008-07-24
IPC分类号： C10G35/00
CPC分类号： C10G35/04
摘要： One exemplary embodiment can be a process for producing a reformate by combining a stream having an effective amount of methane and a stream having an effective amount of naphtha for reforming. Generally, the naphtha includes not less than about 95%, by weight, of one or more compounds having a boiling point of about 38-about 260° C. as determined by ASTM D86-07. Moreover, the process can include introducing the combined stream to a reforming reaction zone. Generally, the combined stream has a methane:naphtha mass ratio of about 0.03:1.00-about 0.10:1.00.
摘要翻译： 一个示例性实施方案可以是通过将具有有效量的甲烷的流与具有有效量的石脑油的流组合用于重整来生产重整产品的方法。 通常，石脑油包括按ASTM D86-07测定的一种或多种沸点为约38-约260℃的化合物的重量百分比不小于约95％。 此外，该方法可以包括将组合的流引入重整反应区。 一般来说，组合物流的甲烷：石脑油质量比为约0.03:1.00-约0.10:1.00。
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公开(公告)号：US09023298B2
公开(公告)日：2015-05-05
申请号：US13440527
申请日：2012-04-05
IPC分类号： B01J8/00 , B01J8/04 , B01J19/00 , B01J19/24 , C01B3/00 , C01B3/02 , C01B3/22 , C01B3/24 , C01B3/26 , C01B3/32 , C01B3/34 , C01B3/38
CPC分类号： C01B3/26 , B01J8/008 , B01J8/0415 , B01J8/0492 , B01J8/0496 , B01J2208/00194 , B01J2208/0053 , B01J2219/024 , C01B2203/0277
摘要： An apparatus for reforming a hydrocarbon stream is presented. The apparatus involves changing the design of reformers and associated equipment to allow for increasing the processing temperatures in the reformers and heaters. The reformers are operated under different conditions to utilize advantages in the equilibriums, but require modifications to prevent increasing thermal cracking and to prevent increases in coking.
摘要翻译： 提出了一种用于重整烃流的装置。 该设备包括改变重整器和相关设备的设计，以允许提高重整器和加热器中的加工温度。 改造者在不同条件下运行，以利用平衡中的优点，但需要进行修改以防止增加热裂解并防止焦化增加。
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