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1.发明授权Process and system for the transfer of a metal catalyst component from one particle to another 有权金属催化剂组分从一个颗粒转移到另一个颗粒的方法和系统公开(公告)号：US07909988B2
公开(公告)日：2011-03-22
申请号：US12104482
申请日：2008-04-17
申请人： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Schreier , Simon R. Bare
发明人： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Schreier , Simon R. Bare
IPC分类号： C10G35/04
CPC分类号： C10G35/085 , C10G35/095 , C10G35/24
摘要： One exemplary embodiment can be a process for facilitating a transfer of a metal catalyst component from at least one donor particle to at least one recipient particle in a catalytic naphtha reforming unit. The process can include transferring an effective amount of the metal catalyst component from the at least one donor particle to the at least one recipient particle under conditions to effect such transfer to improve a conversion of a hydrocarbon feed.
摘要翻译： 一个示例性实施方案可以是促进金属催化剂组分从催化石脑油重整单元中的至少一个供体颗粒转移至至少一个受体颗粒的方法。 该方法可以包括在有效量的金属催化剂组分从至少一个供体颗粒转移到至少一个受体颗粒的条件下进行这种转移以提高烃进料的转化率。
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2.发明申请Process and System for the Transfer of a Metal Catalyst Component from One Particle to Another 有权将金属催化剂组分从一种颗粒转移到另一种颗粒的方法和系统公开(公告)号：US20110136655A1
公开(公告)日：2011-06-09
申请号：US13025631
申请日：2011-02-11
申请人： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Schreier , Simon R. Bare
发明人： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Schreier , Simon R. Bare
CPC分类号： C10G35/085 , C10G35/095 , C10G35/24
摘要： One exemplary embodiment can be a process for facilitating a transfer of a metal catalyst component from at least one donor particle to at least one recipient particle in a catalytic naphtha reforming unit. The process can include transferring an effective amount of the metal catalyst component from the at least one donor particle to the at least one recipient particle under conditions to effect such transfer to improve a conversion of a hydrocarbon feed.
摘要翻译： 一个示例性实施方案可以是促进金属催化剂组分从催化石脑油重整单元中的至少一个供体颗粒转移至至少一个受体颗粒的方法。 该方法可以包括在有效量的金属催化剂组分从至少一个供体颗粒转移到至少一个受体颗粒的条件下进行这种转移以提高烃进料的转化率。
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3.发明申请Process and System for the Addition of Promoter Metal In Situ in a Catalytic Reforming Unit 审中-公开在催化重整单元中原位添加助催化剂金属的方法和系统公开(公告)号：US20100116714A1
公开(公告)日：2010-05-13
申请号：US12269366
申请日：2008-11-12
IPC分类号： C10G35/06
CPC分类号： C10G35/06 , B01J23/08 , B01J27/13 , B01J27/32 , B01J38/02 , B01J38/10 , B01J38/44 , B01J38/48 , B01J38/60 , C10G35/085 , C10G2300/1044 , C10G2300/70
摘要： One exemplary embodiment can be a process for facilitating adding a promoter metal to at least one catalyst particle in situ in a catalytic naphtha reforming unit. The process can include introducing a compound comprising the promoter metal to the catalyst naphtha reforming unit and adding an effective amount of the promoter metal from the compound comprising the promoter metal to the catalyst particle under conditions to effect such addition and improve a conversion of a hydrocarbon feed.
摘要翻译： 一个示例性实施方案可以是促进助催化剂金属在催化石脑油重整单元中原位加入至少一种催化剂颗粒的方法。 该方法可以包括将催化剂石脑油重整单元引入包含助催化剂金属的化合物，并且在实施这种添加的条件下将有效量的助催化剂金属从包含促进剂金属的化合物加入催化剂颗粒中，并改善烃的转化率 饲料。
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4.发明申请PROCESS AND SYSTEM FOR THE TRANSFER OF A METAL CATALYST COMPONENT FROM ONE PARTICLE TO ANOTHER 有权金属催化剂组分从一种颗粒转移到另一种颗粒的方法和系统公开(公告)号：US20090261018A1
公开(公告)日：2009-10-22
申请号：US12104482
申请日：2008-04-17
申请人： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Schreier , Simon R. Bare
发明人： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Schreier , Simon R. Bare
CPC分类号： C10G35/085 , C10G35/095 , C10G35/24
摘要： One exemplary embodiment can be a process for facilitating a transfer of a metal catalyst component from at least one donor particle to at least one recipient particle in a catalytic naphtha reforming unit. The process can include transferring an effective amount of the metal catalyst component from the at least one donor particle to the at least one recipient particle under conditions to effect such transfer to improve a conversion of a hydrocarbon feed.
摘要翻译： 一个示例性实施方案可以是促进金属催化剂组分从催化石脑油重整单元中的至少一个供体颗粒转移至至少一个受体颗粒的方法。 该方法可以包括在有效量的金属催化剂组分从至少一个供体颗粒转移到至少一个受体颗粒的条件下进行这种转移以提高烃进料的转化率。
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公开(公告)号：US20100018906A1
公开(公告)日：2010-01-28
申请号：US12177851
申请日：2008-07-22
申请人： Mark P. Lapinski , Richard R. Rosin
发明人： Mark P. Lapinski , Richard R. Rosin
CPC分类号： B01D53/864 , B01D53/02 , B01D2251/202 , B01D2253/108 , B01D2255/1026 , B01D2255/20746 , B01D2255/20753 , B01D2256/16 , B01D2256/24 , B01D2257/502 , B01J23/96 , B01J38/10 , C10G35/06
摘要： One exemplary embodiment can be a process for lowering an amount of carbon monoxide in a stream rich in hydrogen. The process can include passing the stream rich in hydrogen through a carbon monoxide removal zone to produce a product stream having no more than about 10 vppm carbon monoxide and communicating the product stream to a reduction zone receiving a catalyst comprising unreduced metal species.
摘要翻译： 一个示例性实施方案可以是用于降低富含氢气的一氧化碳的量的方法。 该方法可以包括使富含氢的物流通过一氧化碳去除区，以产生具有不超过约10vppm一氧化碳的产物流，并将产物流连通至含有未还原金属物质的催化剂的还原区。
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6.发明授权Process and system for the transfer of a metal catalyst component from one particle to another 有权金属催化剂组分从一个颗粒转移到另一个颗粒的方法和系统公开(公告)号：US08404105B2
公开(公告)日：2013-03-26
申请号：US13025631
申请日：2011-02-11
申请人： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Scheier , Simon R. Bare
发明人： Mark P. Lapinski , Gregory J. Gajda , Jeffry T. Donner , Richard R. Rosin , Marc R. Scheier , Simon R. Bare
IPC分类号： C10G35/04
CPC分类号： C10G35/085 , C10G35/095 , C10G35/24
摘要： One exemplary embodiment can be a process for facilitating a transfer of a metal catalyst component from at least one donor particle to at least one recipient particle in a catalytic naphtha reforming unit. The process can include transferring an effective amount of the metal catalyst component from the at least one donor particle to the at least one recipient particle under conditions to effect such transfer to improve a conversion of a hydrocarbon feed.
摘要翻译： 一个示例性实施方案可以是促进金属催化剂组分从催化石脑油重整单元中的至少一个供体颗粒转移至至少一个受体颗粒的方法。 该方法可以包括在有效量的金属催化剂组分从至少一个供体颗粒转移到至少一个受体颗粒的条件下进行这种转移以提高烃进料的转化率。
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公开(公告)号：US07687049B2
公开(公告)日：2010-03-30
申请号：US12177851
申请日：2008-07-22
申请人： Mark P. Lapinski , Richard R. Rosin
发明人： Mark P. Lapinski , Richard R. Rosin
CPC分类号： B01D53/864 , B01D53/02 , B01D2251/202 , B01D2253/108 , B01D2255/1026 , B01D2255/20746 , B01D2255/20753 , B01D2256/16 , B01D2256/24 , B01D2257/502 , B01J23/96 , B01J38/10 , C10G35/06
摘要： One exemplary embodiment can be a process for lowering an amount of carbon monoxide in a stream rich in hydrogen. The process can include passing the stream rich in hydrogen through a carbon monoxide removal zone to produce a product stream having no more than about 10 vppm carbon monoxide and communicating the product stream to a reduction zone receiving a catalyst comprising unreduced metal species.
摘要翻译： 一个示例性实施方案可以是用于降低富含氢气的一氧化碳的量的方法。 该方法可以包括使富含氢的物流通过一氧化碳去除区，以产生具有不超过约10vppm一氧化碳的产物流，并将产物流连通至含有未还原金属物质的催化剂的还原区。
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公开(公告)号：US20100166622A1
公开(公告)日：2010-07-01
申请号：US12722035
申请日：2010-03-11
申请人： Mark P. Lapinski , Richard R. Rosin
发明人： Mark P. Lapinski , Richard R. Rosin
IPC分类号： B01J19/00
CPC分类号： B01D53/864 , B01D53/02 , B01D2251/202 , B01D2253/108 , B01D2255/1026 , B01D2255/20746 , B01D2255/20753 , B01D2256/16 , B01D2256/24 , B01D2257/502 , B01J23/96 , B01J38/10 , C10G35/06
摘要： One exemplary embodiment can be a process for lowering an amount of carbon monoxide in a stream rich in hydrogen. The process can include passing the stream rich in hydrogen through a carbon monoxide removal zone to produce a product stream having no more than about 10 vppm carbon monoxide and communicating the product stream to a reduction zone receiving a catalyst comprising unreduced metal species.
摘要翻译： 一个示例性实施方案可以是用于降低富含氢气的一氧化碳的量的方法。 该方法可以包括使富含氢的物流通过一氧化碳去除区，以产生具有不超过约10vppm一氧化碳的产物流，并将产物流连通至含有未还原金属物质的催化剂的还原区。
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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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