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1.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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2.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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3.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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4.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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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：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：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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公开(公告)号：US08912110B2
公开(公告)日：2014-12-16
申请号：US13547351
申请日：2012-07-12
申请人： Manuela Serban , Mark P. Lapinski
发明人： Manuela Serban , Mark P. Lapinski
IPC分类号： B01J31/00 , B01J37/00 , B01J27/138 , B01J27/132 , B01J27/13 , B01J27/125 , B01J23/02 , B01J23/06 , B01J23/10 , B01J23/58 , B01J23/56 , B01J23/42 , B01J23/44 , B01J23/70 , B01J23/72 , B01J23/90 , B01J23/96 , C10G35/04 , C10G35/06 , C08F4/02 , C08F4/60
CPC分类号： B01J37/18 , B01J23/63 , B01J27/10 , B01J27/13 , B01J27/135 , B01J27/138 , B01J35/008 , B01J35/08 , B01J37/0072 , B01J37/0201 , C10G35/06 , C10G69/10 , C10G2300/1044 , C10G2400/02 , C10G2400/04
摘要： One embodiment is 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, an alkali or alkaline-earth metal, a lanthanide-series metal, and a support. Generally, an average bulk density of the catalyst is about 0.300 to about 1.00 gram per cubic centimeter. The catalyst has a platinum content of less than about 0.375 wt %, a tin content of about 0.1 to about 2 wt %, a potassium content of about 100 to about 600 wppm, and a cerium content of about 0.1 to about 1 wt %. The lanthanide-series metal can be distributed at a concentration of the lanthanide-series metal in a 100 micron surface layer of the catalyst less than two times a concentration of the lanthanide-series metal at a central core of the catalyst.
摘要翻译： 一个实施方案是用于石脑油催化重整的催化剂。 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，碱金属或碱土金属，镧系金属和载体。 通常，催化剂的平均体积密度为约0.300至约1.00克/立方厘米。 催化剂的铂含量小于约0.375重量％，锡含量为约0.1至约2重量％，钾含量为约100至约600wppm，铈含量为约0.1至约1重量％。 镧系元素金属可以在催化剂的100微米表面层中以镧系元素金属的浓度分布，其量小于催化剂中心核心处的镧系金属浓度的两倍。
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10.发明授权Counter-current catalyst flow with split feed and two reactor train processing 有权逆流催化剂流动与分流进料和两个反应堆列车加工公开(公告)号：US08882994B2
公开(公告)日：2014-11-11
申请号：US13327164
申请日：2011-12-15
申请人： Mark D. Moser , David A. Wegerer , Kurt M. VandenBussche , Manuela Serban , Mark P. Lapinski , Mary Jo Wier , Gregory J. Gajda
发明人： Mark D. Moser , David A. Wegerer , Kurt M. VandenBussche , Manuela Serban , Mark P. Lapinski , Mary Jo Wier , Gregory J. Gajda
IPC分类号： C10G35/04
CPC分类号： C10G59/02 , C10G59/06 , C10G2400/30
摘要： A process is presented for the increasing the yields of aromatics from reforming a hydrocarbon feedstream. The process includes splitting a naphtha feedstream into a light hydrocarbon stream, and a heavier stream having a relatively rich concentration of naphthenes. The heavy stream is reformed to convert the naphthenes to aromatics and the resulting product stream is further reformed with the light hydrocarbon stream to increase the aromatics yields. The process includes passing a catalyst stream in a counter-current flow relative to the hydrocarbon process stream.
摘要翻译： 提出了一种从碳氢化合物原料流重整提高芳族化合物产率的方法。 该方法包括将石脑油进料流分解成轻质烃物流，以及将较稠油的浓度较高的环烷烃。 将重质流重整以将环烷烃转化为芳族化合物，并且所得产物流用轻质烃流进一步重整以提高芳烃产率。 该方法包括使相对于烃工艺物流的逆流流动催化剂流。
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