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1.发明申请公开(公告)号：US20100018900A1
公开(公告)日：2010-01-28
申请号：US12179542
申请日：2008-07-24
IPC分类号： C10G35/02
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 n-butane and a stream having an effective amount of naphtha for reforming. Generally, the naphtha has 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. The process can include introducing the combined stream to a reforming reaction zone. Typically, the combined stream has an n-butane:naphtha mass ratio of about 0.10:1.00—about 1.00:1.00.
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正丁烷的流和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，根据ASTM D86-07测定，石脑油具有不小于约95重量％的一种或多种沸点为约38-约260℃的化合物。 该方法可以包括将组合的流引入重整反应区。 通常，组合物流的正丁烷：石脑油质量比为约0.10:1.00-约1.00:1.00。
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2.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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3.发明授权公开(公告)号：US08753503B2
公开(公告)日：2014-06-17
申请号：US12179524
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 isopentane and a stream having an effective amount of naphtha for reforming. Generally, the naphtha has 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. The process may include introducing the combined stream to a reforming reaction zone. The combined stream can have an isopentane:naphtha mass ratio of about 0.10:1.00-about 1.00:1.00.
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异戊烷的物流和具有有效量的石脑油的物流混合以重整来生产重整产品的方法。 通常，根据ASTM D86-07测定，石脑油具有不小于约95重量％的一种或多种沸点为约38-约260℃的化合物。 该方法可以包括将组合的流引入重整反应区。 合并的流可以具有约0.10:1.00-约1.00:1.00的异戊烷：石脑油质量比。
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4.发明申请公开(公告)号：US20100018899A1
公开(公告)日：2010-01-28
申请号：US12179524
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 isopentane and a stream having an effective amount of naphtha for reforming. Generally, the naphtha has 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. The process may include introducing the combined stream to a reforming reaction zone. The combined stream can have an isopentane:naphtha mass ratio of about 0.10:1.00—about 1.00:1.00.
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异戊烷的物流和具有有效量的石脑油的物流混合以重整来生产重整产品的方法。 通常，根据ASTM D86-07测定，石脑油具有不小于约95重量％的一种或多种沸点为约38-约260℃的化合物。 该方法可以包括将组合的流引入重整反应区。 合并的流可以具有约0.10:1.00-约1.00:1.00的异戊烷：石脑油质量比。
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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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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：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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公开(公告)号：US20120277500A1
公开(公告)日：2012-11-01
申请号：US13440487
申请日：2012-04-05
IPC分类号： C07C2/00
CPC分类号： C10G35/04 , C07C4/06 , C10G35/06 , C10G61/04 , C10G2300/1044 , C10G2300/4018 , C10G2400/30 , Y02P20/584 , C07C15/02 , C07C15/067
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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9.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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10.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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