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21.发明授权公开(公告)号：US08323476B2
公开(公告)日：2012-12-04
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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公开(公告)号：US20120277511A1
公开(公告)日：2012-11-01
申请号：US13440381
申请日：2012-04-05
CPC分类号： C10G45/68 , C10G35/04 , C10G59/02 , C10G61/04 , C10G2300/4006 , C10G2300/4018 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves increasing the processing temperatures in the reformers. 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. 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。 该方法涉及提高改性剂中的加工温度。 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。 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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公开(公告)号：US07622620B2
公开(公告)日：2009-11-24
申请号：US11615254
申请日：2006-12-22
IPC分类号： C10G65/02
CPC分类号： C10G29/205 , C10G11/10 , C10G11/16 , C10G35/12 , C10G49/002 , C10G49/14 , C10G51/026 , C10G59/02 , C10G65/02
摘要： One exemplary embodiment can include a hydrocarbon conversion process. Generally, the process includes passing a hydrocarbon stream through a hydrocarbon conversion zone comprising a series of reaction zones. Typically, the hydrocarbon conversion zone includes a staggered-bypass reaction system having a first, second, third, and fourth reaction zones, which are staggered-bypass reaction zones, and a fifth reaction zone, which can be a non-staggered-bypass reaction zone, subsequent to the staggered-bypass reaction system.
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24.发明申请公开(公告)号：US20090054712A1
公开(公告)日：2009-02-26
申请号：US12260312
申请日：2008-10-29
IPC分类号： C07C2/00
CPC分类号： C10G29/205 , C10G11/10 , C10G11/16 , C10G35/12 , C10G49/002 , C10G49/14 , C10G51/026 , C10G59/02 , C10G65/02
摘要： One exemplary embodiment can include a hydrocarbon conversion process. Generally, the process includes passing a hydrocarbon stream through a hydrocarbon conversion zone comprising a series of reaction zones. Typically, the hydrocarbon conversion zone includes a staggered-bypass reaction system having a first, second, third, and fourth reaction zones, which are staggered-bypass reaction zones, and a fifth reaction zone, which can be a non-staggered-bypass reaction zone, subsequent to the staggered-bypass reaction system.
摘要翻译： 一个示例性实施方案可以包括烃转化方法。 通常，该方法包括使烃流通过包含一系列反应区的烃转化区。 通常，烃转化区包括具有交错旁路反应区的第一，第二，第三和第四反应区的交错旁路反应系统，以及可以是非交错旁路反应的第五反应区 在交错旁路反应系统之后。
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25.发明申请公开(公告)号：US20080154076A1
公开(公告)日：2008-06-26
申请号：US11615254
申请日：2006-12-22
IPC分类号： C10G65/02
CPC分类号： C10G29/205 , C10G11/10 , C10G11/16 , C10G35/12 , C10G49/002 , C10G49/14 , C10G51/026 , C10G59/02 , C10G65/02
摘要： One exemplary embodiment can include a hydrocarbon conversion process. Generally, the process includes passing a hydrocarbon stream through a hydrocarbon conversion zone comprising a series of reaction zones. Typically, the hydrocarbon conversion zone includes a staggered-bypass reaction system having a first, second, third, and fourth reaction zones, which are staggered-bypass reaction zones, and a fifth reaction zone, which can be a non-staggered-bypass reaction zone, subsequent to the staggered-bypass reaction system.
摘要翻译： 一个示例性实施方案可以包括烃转化方法。 通常，该方法包括使烃流通过包含一系列反应区的烃转化区。 通常，烃转化区包括具有交错旁路反应区的第一，第二，第三和第四反应区的交错旁路反应系统，以及可以是非交错旁路反应的第五反应区 在交错旁路反应系统之后。
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