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41. 发明申请

US20140363343A1 Apparatuses and Methods for Controlling Heat for Rapid Thermal Processing of Carbonaceous Material 审中-公开
标题翻译：用于控制碳质材料快速热处理的热量的装置和方法
公开(公告)号：US20140363343A1
公开(公告)日：2014-12-11
申请号：US14346517
申请日：2012-09-14
申请人： Sathit Kulprathipanja , Paolo Palmas
发明人： Sathit Kulprathipanja , Paolo Palmas
IPC分类号： C10B53/02
CPC分类号： C10B53/02 , B01J8/0055 , B01J8/1836 , B01J8/26 , B01J8/32 , B01J2208/00176 , B01J2208/00194 , B01J2208/00292 , B01J2208/00513 , C10B49/22 , C10C5/00 , F23C10/04 , F23C2206/103 , F23G2201/304 , F23G2203/502 , F23G2209/26 , F28D7/1615 , F28F1/14 , Y02E50/14
摘要： Embodiments of apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material are provided herein. The apparatus comprises a reheater for containing a fluidized bubbling bed comprising an oxygen-containing gas, inorganic heat carrier particles, and char and for burning the char into ash to form heated inorganic particles. An inorganic particle cooler is in fluid communication with the reheater to receive a first portion of the heated inorganic particles. The inorganic particle cooler is configured to receive a cooling medium for indirect heat exchange with the first portion of the heated inorganic particles to form first partially-cooled heated inorganic particles that are fluidly communicated to the reheater and combined with a second portion of the heated inorganic particles to form second partially-cooled heated inorganic particles. A reactor is in fluid communication with the reheater to receive the second partially-cooled heated inorganic particles.
摘要翻译：本文提供了用于控制用于碳质材料的快速热处理的热量的装置和方法的实施例。该装置包括一个再热器，用于容纳包含含氧气体，无机热载体颗粒和炭的流化鼓泡床，并用于将炭烧成灰分以形成加热的无机颗粒。无机颗粒冷却器与再热器流体连通以接收第一部分加热的无机颗粒。无机颗粒冷却器构造成接收用于与加热的无机颗粒的第一部分进行间接热交换的冷却介质，以形成第一部分冷却的加热的无机颗粒，其流体连通到再热器并与第二部分加热的无机颗粒颗粒形成第二部分冷却的加热无机颗粒。反应器与再热器流体连通以接收第二部分冷却的加热的无机颗粒。

42. 发明授权

US08864979B2 Process and apparatus for fluid catalytic cracking 有权
标题翻译：流化床催化裂化的工艺和装置
公开(公告)号：US08864979B2
公开(公告)日：2014-10-21
申请号：US13425657
申请日：2012-03-21
申请人： Paolo Palmas
发明人： Paolo Palmas
IPC分类号： B01J8/18 , B01J8/24 , B01J8/26 , C10G51/06 , C10G11/18 , C10G11/05
CPC分类号： C10G11/182 , B01J8/0055 , B01J8/08 , B01J8/26 , B01J21/20 , B01J29/90 , B01J38/06 , C10G11/00
摘要： One exemplary embodiment can be a process for fluid catalytic cracking. The process can include sending a first catalyst from a first riser reactor and a second catalyst from a second riser reactor to a regeneration vessel having a first stage and a second stage. The first catalyst may be sent to the first stage and the second catalyst may be sent to the second stage of the regeneration vessel. Generally, the first stage is positioned above the second stage.
摘要翻译：一个示例性实施方案可以是流化催化裂化的方法。该方法可以包括将第一催化剂从第一提升管反应器和第二催化剂从第二提升管反应器送到具有第一阶段和第二阶段的再生容器。可将第一催化剂送至第一阶段，第二催化剂可送至再生容器的第二阶段。通常，第一阶段位于第二阶段之上。

43. 发明申请

US20140034552A1 METHODS AND FUEL PROCESSING APPARATUSES FOR UPGRADING A PYROLYSIS OIL STREAM AND A HYDROCARBON STREAM 有权
标题翻译：用于升级溶解油流和油气流的方法和燃料加工装置
公开(公告)号：US20140034552A1
公开(公告)日：2014-02-06
申请号：US13563011
申请日：2012-07-31
申请人： Lance Awender Baird , Paolo Palmas
发明人： Lance Awender Baird , Paolo Palmas
IPC分类号： C10G11/02 , B01J8/00
CPC分类号： C10G11/18 , B01J4/002 , B01J2204/002 , B01J2204/007 , C10G11/187 , C10G51/04 , C10G2300/1011 , C10G2300/1074 , C10G2300/4006 , Y02P30/20
摘要： Methods and fuel processing apparatuses for upgrading a pyrolysis oil stream and a hydrocarbon stream are provided herein. In an embodiment, a method for upgrading a pyrolysis oil stream and a hydrocarbon stream includes providing a pyrolysis oil stream and providing a hydrocarbon stream separate from the pyrolysis oil stream. The pyrolysis oil stream and the hydrocarbon stream are mixed in a mixing zone and in the absence of a particulate cracking catalyst. The pyrolysis oil stream and the hydrocarbon stream are introduced in a substantially common direction into the mixing zone to form a mixture of the pyrolysis oil stream and the hydrocarbon stream. The mixture of the pyrolysis oil stream and the hydrocarbon stream are catalytically cracked in the presence of the particulate cracking catalyst.
摘要翻译：本文提供了用于升级热解油流和烃流的方法和燃料处理装置。在一个实施方案中，用于升级热解油流和烃流的方法包括提供热解油流并提供与热解油流分离的烃流。将热解油流和烃流在混合区和不存在颗粒裂化催化剂的情况下混合。将热解油流和烃流以基本上共同的方向引入混合区以形成热解油流和烃流的混合物。热解油流和烃流的混合物在颗粒裂化催化剂存在下被催化裂化。

44. 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。

45. 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。

46. 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。

47. 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。

48. 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。

49. 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。

50. 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。

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