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41. 发明申请

US20140001096A1 PROCESS AND APPARATUS FOR DISTRIBUTING HYDROCARBON FEED TO A CATALYST STREAM 有权
标题翻译：将碳氢化合物分配给催化剂流的方法和装置
公开(公告)号：US20140001096A1
公开(公告)日：2014-01-02
申请号：US13534273
申请日：2012-06-27
申请人： Roger L. Throndson , Paolo Palmas , Lev Davydov , Mohammad-Reza Mostofi-Ashtiani
发明人： Roger L. Throndson , Paolo Palmas , Lev Davydov , Mohammad-Reza Mostofi-Ashtiani
IPC分类号： C10G11/00
CPC分类号： C10G11/18 , B01J8/1827 , B01J8/388 , B01J2208/00902
摘要： A process and apparatus described is for distributing hydrocarbon feed to catalyst in a riser. Hydrocarbon feed is delivered to a plenum in the riser. Nozzles from the plenum inject feed into the riser to contact the catalyst. Streams of regenerated catalyst and carbonized catalyst may be passed to the riser and mixed around an insert in a lower section of a riser. The plenum may be located in the riser.
摘要翻译：所描述的方法和装置是用于在提升管中将烃进料分配到催化剂。碳氢化合物进料被提供到提升管中的增压室。来自气室的喷嘴将进料注入到提升管中以接触催化剂。再生催化剂和碳化催化剂的流可以被传递到提升管并且在提升管的下部中的插入件周围混合。集气室可能位于提升管中。

42. 发明申请

US20130148463A1 PROCESS AND APPARATUS FOR MIXING TWO STREAMS OF CATALYST 有权
公开(公告)号：US20130148463A1
公开(公告)日：2013-06-13
申请号：US13323053
申请日：2011-12-12
申请人： Lev Davydov , Lisa M. Wolschlag , Paolo Palmas , Robert L. Mehlberg , Mohammad-Reza Mostofi-Ashtiani , Daniel R. Johnson , Chad R. Huovie , Michael S. Sandacz , Peter J. Van Opdorp , Thomas W. Lorsbach , Karthikeyan Paramanandam
发明人： Lev Davydov , Lisa M. Wolschlag , Paolo Palmas , Robert L. Mehlberg , Mohammad-Reza Mostofi-Ashtiani , Daniel R. Johnson , Chad R. Huovie , Michael S. Sandacz , Peter J. Van Opdorp , Thomas W. Lorsbach , Karthikeyan Paramanandam
IPC分类号： B01F15/02
CPC分类号： B01J8/0055 , B01J8/1863 , B01J8/1872 , B01J2208/0084 , B01J2208/00902 , B01J2208/00911 , C10G11/18
摘要： A process and apparatus for mixing streams of regenerated and carbonized catalyst involves passing a catalyst stream into and out of a chamber in a lower section of a riser. The chamber fosters mixing of the catalyst streams to reduce their temperature differential before contacting hydrocarbon feed.

43. 发明申请

US20120082591A1 APPARATUS FOR REGENERATING CATALYST 有权
标题翻译：用于再生催化剂的装置
公开(公告)号：US20120082591A1
公开(公告)日：2012-04-05
申请号：US12894925
申请日：2010-09-30
申请人： Paolo Palmas
发明人： Paolo Palmas
IPC分类号： B01J19/00
CPC分类号： B01J8/388 , B01J8/1827 , B01J8/1872 , B01J2208/0084 , C10G11/182
摘要： Disclosed is a catalyst distributor and process for mixing spent catalyst and recycled regenerated catalyst in a regenerator vessel. Mixing is conducted in a confined space to which catalyst is delivered from catalyst conduits protruding through the wall of the regenerator.
摘要翻译：公开了一种用于将废催化剂和循环再生的催化剂混合在再生器容器中的催化剂分配器和方法。在从再生器的壁突出的催化剂管道输送催化剂的密闭空间内进行混合。

44. 发明授权

US08137631B2 Unit, system and process for catalytic cracking 有权
标题翻译：单元，系统和催化裂化过程
公开(公告)号：US08137631B2
公开(公告)日：2012-03-20
申请号：US12333262
申请日：2008-12-11
申请人： Paolo Palmas , Robert L. Mehlberg
发明人： Paolo Palmas , Robert L. Mehlberg
IPC分类号： F27B15/08 , C10G51/00
CPC分类号： C10G11/18 , C10G11/182 , C10G51/06 , C10G2300/1059 , C10G2300/107 , C10G2300/1088 , C10G2300/301 , C10G2300/4081 , C10G2400/02 , C10G2400/20
摘要： One exemplary embodiment can be a fluid catalytic cracking unit. The fluid catalytic cracking unit can include a first riser, a second riser, and a disengagement zone. The first riser can be adapted to receive a first feed terminating at a first reaction vessel having a first volume. The second riser may be adapted to receive a second feed terminating at a second reaction vessel having a second volume. Generally, the first volume is greater than the second volume. What is more, the disengagement zone can be for receiving a first mixture including at least one catalyst and one or more products from the first reaction vessel, and a second mixture including at least one catalyst and one or more products from the second reaction vessel. Typically, the first mixture is isolated from the second mixture.
摘要翻译：一个示例性实施方案可以是流化催化裂化装置。流化催化裂化装置可以包括第一提升管，第二提升管和分离区。第一提升管可适于接收终止于具有第一容积的第一反应容器的第一进料。第二提升管可以适于接收在具有第二容积的第二反应容器处终止的第二进料。通常，第一体积大于第二体积。此外，分离区可以用于接收包含至少一种催化剂和来自第一反应容器的一种或多种产物的第一混合物，以及包含至少一种催化剂和来自第二反应容器的一种或多种产物的第二混合物。通常，第一混合物与第二混合物分离。

45. 发明授权

US07744744B1 Converted FCC bubbling bed regenerator 有权
标题翻译：转换FCC鼓泡床再生器
公开(公告)号：US07744744B1
公开(公告)日：2010-06-29
申请号：US11322755
申请日：2005-12-30
申请人： Paolo Palmas , Frank S. Rosser, Jr. , Patrick D. Walker
发明人： Paolo Palmas , Frank S. Rosser, Jr. , Patrick D. Walker
IPC分类号： C10G11/18 , F27B15/08 , F27B15/09 , B01J38/36
CPC分类号： C10G11/182 , B01J29/06 , B01J35/0006 , B01J37/04 , B01J38/36
摘要： An apparatus and process for regenerating cracking catalyst may include a regenerator, a distributor penetrating the bottom of the regenerator, a spent catalyst conduit, a return standpipe, and a recirculating standpipe, wherein the return standpipe and the recirculating standpipe are connected to the upper half of the regenerator. An apparatus for regenerating cracking catalyst may include a spent catalyst standpipe and a recirculation standpipe positioned on an inner side of the regenerator vessel.
摘要翻译：用于再生裂化催化剂的装置和方法可以包括再生器，穿过再生器底部的分配器，废催化剂管道，回流立管和再循环立管，其中回流立管和再循环竖管连接到上半部的再生器。用于再生裂化催化剂的装置可以包括废催化剂立管和位于再生器容器内侧的再循环立管。

46. 发明申请

US20060094917A1 External second stage cyclones in olefin production process 有权
标题翻译：烯烃生产过程中外部二级旋风分离器
公开(公告)号：US20060094917A1
公开(公告)日：2006-05-04
申请号：US11236477
申请日：2005-09-27
申请人： Paolo Palmas , Daniel Myers , Richard Johnson
发明人： Paolo Palmas , Daniel Myers , Richard Johnson
IPC分类号： C07C1/00
CPC分类号： B01J38/12 , B01J8/0055 , B01J8/1818 , B01J8/24 , B01J8/26 , B01J29/85 , B01J29/90 , B01J2208/00292 , B01J2219/00006 , C07C1/20 , Y02P20/584 , Y02P30/42 , C07C11/02
摘要： The present invention comprises a process and apparatus for producing olefins from oxygenates in a reactor. This process comprises these oxygenates with a catalyst to produce a gaseous mixture comprising light olefins and by-products, sending the mixture to a single stage cyclone within said reactor to separate said catalyst from said gaseous mixture and then sending said the to a second stage cyclone. The second stage cyclone is located outside of said reactor and it functions to remove the catalyst from the mixture. Then the catalyst can be returned to the reactor after having been treated in a regeneration zone to remove carbonaceous deposits from the catalyst.
摘要翻译：本发明包括在反应器中由含氧化合物生产烯烃的方法和装置。该方法包括这些含氧化物与催化剂以产生包含轻质烯烃和副产物的气体混合物，将混合物送入所述反应器内的单级旋风分离器，以将所述催化剂与所述气体混合物分离，然后将所述催化剂送至第二级旋风分离器。第二级旋风分离器位于所述反应器的外部，其功能是从混合物中除去催化剂。然后可以在再生区中处理催化剂之后将催化剂返回到反应器中以从催化剂除去含碳沉积物。

47. 发明授权

US06491875B1 Fluidized particle contacting process with elongated combustor 失效
标题翻译：流化颗粒接触过程与细长燃烧器
公开(公告)号：US06491875B1
公开(公告)日：2002-12-10
申请号：US09429409
申请日：1999-10-28
申请人： Paolo Palmas
发明人： Paolo Palmas
IPC分类号： B32B2704
CPC分类号： C10G11/182
摘要： A particulate catalyst is regenerated by upward transport in a combustor having an extended length and separated from combustion gases with a single stage of cyclones. The extended length combustor ends with a termination device arranged to tangentially discharge particulate catalyst and gases into an open disengaging vessel and to achieve a high separation efficiency. Initial high separation efficiency provided by the termination device permits a single downstream stage of cyclones to reduce particulate emissions to acceptable levels. The combination of the separation device and the extended combustor can accommodate changes in particulate densities in the extended combustor without inducing cyclone overload.
摘要翻译：颗粒催化剂通过在具有延长长度的燃烧器中向上输送再生，并与具有单级旋风分离器的燃烧气体分离。延长长度的燃烧器末端具有端接装置，该端接装置设置成切向地将颗粒催化剂和气体排放到开放式分离容器中并实现高分离效率。由终端设备提供的初始高分离效率允许旋风分离器的单个下游阶段将颗粒物排放减少到可接受的水平。分离装置和延长的燃烧器的组合可以适应扩展燃烧器中的颗粒密度的变化，而不会引起旋风分离器过载。

48. 发明授权

US6063263A Process for feed contacting with immediate catalyst separation 有权
标题翻译：即时催化分离的进料接触方法
公开(公告)号：US6063263A
公开(公告)日：2000-05-16
申请号：US270585
申请日：1999-03-16
申请人： Paolo Palmas
发明人： Paolo Palmas
IPC分类号： B01J8/00 , C10G11/18 , C10G11/00
CPC分类号： B01J8/006 , C10G11/18
摘要： A particular arrangement of an FCC unit creates an immediate and sustained gravity separation of catalyst and hydrocarbon vapors in short contact time cracking operation. A transverse feed contactor ejects the mixture of catalyst and hydrocarbon vapors transversely into a central portion of a separation vessel for vertical disengagement of catalyst from vapors. The vapors travel upwardly in the vessel into an inertial separator that quickly segregates entrained catalyst from the hydrocarbon vapors and collects separated catalyst at a higher elevation for stripping of adsorbed hydrocarbons from the catalyst.
摘要翻译： FCC单元的特定布置在短时间接触时间开裂操作中产生催化剂和烃蒸气的立即和持续的重力分离。横向进料接触器将催化剂和烃蒸汽的混合物横向喷射到分离容器的中心部分，以使催化剂与蒸汽垂直分离。蒸汽在容器中向上行进惯性分离器，其快速地将夹带的催化剂从烃蒸气中分离出来，并在更高的高度收集分离的催化剂，以从催化剂中汽提吸附的烃。

49. 发明授权

US09266083B2 Apparatuses for stripping gaseous hydrocarbons from particulate material and processes for the same 有权
标题翻译：用于从颗粒物质中汽提气态烃的装置及其工艺
公开(公告)号：US09266083B2
公开(公告)日：2016-02-23
申请号：US13338997
申请日：2011-12-28
申请人： Mitchell John Kowalczyk , Paolo Palmas
发明人： Mitchell John Kowalczyk , Paolo Palmas
IPC分类号： B01J8/34 , B01J8/26 , B01J19/32 , B01J38/02 , B01J38/12 , C10G11/18 , B01J8/00 , B01J8/18 , B01J8/24 , B01J19/00 , B01J38/00 , C10G11/14
CPC分类号： B01J8/26 , B01J8/34 , B01J19/32 , B01J38/02 , B01J38/12 , B01J2219/3221 , B01J2219/32241 , C10G11/18
摘要： Apparatuses and processes are provided for stripping gaseous hydrocarbons from particulate material. One process comprises the step of contacting particles that contain hydrocarbons with a stripping vapor in countercurrent flow to remove at least a portion of the hydrocarbons with the stripping vapor to form stripped particles. Contacting the particles includes advancing the particles down a sloping element of a structured packing toward a reinforcing rod that is disposed adjacent to a lower section of the sloping element. The particles are advanced down through an opening formed in the sloping element proximate the reinforcing rod. The particles are contacted with the stripping vapor that is rising up through the opening.
摘要翻译：提供了用于从颗粒材料中汽提气态烃的装置和方法。一个方法包括以逆流方式将含有烃的颗粒与汽提蒸汽接触的步骤，以用汽提蒸汽除去至少一部分烃，以形成剥离的颗粒。与颗粒接触包括将颗粒沿着规定填料的倾斜元件向着靠近倾斜元件的下部设置的加强杆推进。颗粒通过形成在靠近加强杆的倾斜元件中的开口向下推进。颗粒与通过开口上升的汽提蒸汽接触。

50. 发明授权

US09227167B2 Process for cracking a hydrocarbon feed 有权
标题翻译：裂解烃进料的方法
公开(公告)号：US09227167B2
公开(公告)日：2016-01-05
申请号：US13189624
申请日：2011-07-25
申请人： Paolo Palmas , Robert L. Mehlberg , Keith A. Couch , Paul S. Nishimura
发明人： Paolo Palmas , Robert L. Mehlberg , Keith A. Couch , Paul S. Nishimura
IPC分类号： C10G11/00 , B01J8/18 , B01J8/00 , B01J8/26 , C07C4/06 , C10G11/18
CPC分类号： B01J8/1827 , B01J8/0065 , B01J8/26 , C07C4/06 , C07C2529/08 , C07C2529/40 , C10G11/18 , C10G2300/1088 , C10G2400/20 , Y02P20/584 , C07C11/06
摘要： An embodiment can be a process for catalytically cracking a hydrocarbon feed. The process can include providing the hydrocarbon feed including an effective amount of one or more C4-C6 olefins for producing at least one light olefin to a riser. Typically, at least about 99%, by mole, of the hydrocarbon feed is a gas.
摘要翻译：一个实施方案可以是用于催化裂化烃进料的方法。该方法可以包括提供烃进料，包括有效量的一种或多种用于将至少一种轻质烯烃生产至提升管的C 4 -C 6烯烃。通常，烃进料的至少约99％摩尔是气体。

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