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21. 发明公开

EP2393595A4 UTILIZATION OF BAFFLES IN CHLORINATION ZONE FOR CONTINUOUS CATALYST REGENERATION 有权
标题翻译： EERER CHLORINIUNUNGSZONE中的VERWENDUNG VON DEAMPERERFÜRKONTINUIERLICHE KATALYSATORREGENERATION
公开(公告)号：EP2393595A4
公开(公告)日：2013-10-30
申请号：EP10738900
申请日：2010-01-14
申请人： UOP LLC
发明人： SUN BING , SECHRIST PAUL A
IPC分类号： B01J38/42 , B01F3/06 , B01J8/18
CPC分类号： B01J8/125

22. 发明公开

EP2864278A4 APPARATUS FOR RETAINING SOLID MATERIAL IN A RADIAL FLOW REACTOR AND METHOD OF MAKING 审中-公开
标题翻译：装置，用于保持固体材料在径向流反应器及其制造方法
公开(公告)号：EP2864278A4
公开(公告)日：2016-07-13
申请号：EP13806152
申请日：2013-06-17
申请人： UOP LLC
发明人： VETTER MICHAEL J , YUAN QUAN , SECHRIST PAUL A
IPC分类号： C07C7/12 , B01D15/22 , B01D35/16 , B01D35/28
CPC分类号： B01J8/0214 , B01D53/0431 , B01J8/008 , B01J8/0257 , B01J2208/00884

23. 发明公开

EP2341995A4 IMPROVED HEAT PUMP FOR HIGH PURITY BOTTOM PRODUCT 有权
标题翻译： VERBESSERTEWÄRMEPUMPEFÜREIN HOCHREINES SUMPFPRODUKT
公开(公告)号：EP2341995A4
公开(公告)日：2014-01-22
申请号：EP09829525
申请日：2009-09-29
申请人： UOP LLC
发明人： SECHRIST PAUL A , WEGERER DAVID A
IPC分类号： B01D1/00 , B01D1/28 , B01D3/00 , B01D3/32 , B01D3/42
CPC分类号： B01D3/322 , B01D3/4266
摘要： An apparatus for reducing the energy consumption of a distillation column is disclosed. The apparatus draws off an intermediate vapor stream from the rectification section of the distillation column, where the vapor stream is compressed and used to reboil a portion of the bottoms stream. The compressed vapor stream transfers energy to the bottoms stream, thereby condensing a portion of the vapor stream while vaporizing the bottoms stream.
摘要翻译：公开了一种用于降低蒸馏塔的能量消耗的装置。该装置从蒸馏塔的精馏段中抽出中间蒸汽流，蒸馏塔被压缩并用于再沸腾一部分底部物流。压缩的蒸汽流将能量转移到塔底物流，从而在蒸发塔底物流的同时冷凝蒸汽流的一部分。

24. 发明公开

EP2448653A4 VESSEL, SYSTEM, AND PROCESS FOR MINIMIZING UNEQUAL FLOW DISTRIBUTION 审中-公开
标题翻译：容器，用于最小化不正确的河流分布的系统和方法
公开(公告)号：EP2448653A4
公开(公告)日：2012-11-28
申请号：EP10800197
申请日：2010-05-20
申请人： UOP LLC
发明人： SECHRIST PAUL A
IPC分类号： C07C7/13 , B01D53/04 , B01D53/047 , C01B3/56 , C07C7/11
CPC分类号： B01D53/047 , B01D53/0446 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2253/116 , B01D2256/16 , B01D2259/402 , B01J8/008 , B01J8/025 , B01J8/0278 , B01J2208/00938 , C01B3/56 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/0495

25. 发明公开

EP1812132A4 FLUID DISTRIBUTION APPARATUS 有权
标题翻译：液体分配装置
公开(公告)号：EP1812132A4
公开(公告)日：2009-03-18
申请号：EP05814894
申请日：2005-10-28
申请人： UOP LLC
发明人： FREY STANLEY J , SECHRIST PAUL A , KAUFF DANIEL A
IPC分类号： B01D15/00 , B01D24/08 , B01D24/48
CPC分类号： B01D15/1821 , B01D15/14 , B01D24/008 , B01D24/14 , B01D2201/44
摘要： Disclosed is a mixer-distributor-collector apparatus for use between beds of solid particles in a fluid-solid contacting vessel. The apparatus includes a solids retaining screen, fluid deflector, passageway, fluid distributor, and flow manipulator. The flow manipulator is a device such as a honeycomb, porous solid, perforated plate, screen, or grid having an open area greater than the open area of the fluid distributor and is located below and spaced apart from the fluid distributor. The apparatus improves the fluid flow characteristics by minimizing or eliminating fluid velocity jets and/or other turbulence which can disturb the downstream particle bed. In an exemplary application, the invention finds use in simulated moving bed (SMB) adsorptive separation processes.

26. 发明专利

BR112013024615A2 processo para a regeneração de partículas de catalisador, e, regenerador de catalisador contínuo 未知
公开(公告)号：BR112013024615A2
公开(公告)日：2016-12-13
申请号：BR112013024615
申请日：2012-06-07
申请人： UOP LLC
发明人： GLOVER BRYAN K , MOORE MICHAEL A , SECHRIST PAUL A
IPC分类号： B01J4/00 , B01J37/08 , C01G55/00
摘要： processo para a regeneração de partículas de catalisador, e, regenerador de catalisador contínuo processos e aparelhos para regenerar partículas de catalisador são fornecidos. os processos incluem a introdução de partículas de catalisador usado para uma zona de queima de um regenerador de catalisador contínuo. quando introduzido, as partículas de catalisador, que contêm um metal do grupo da platina, portam depósito de coque. no processo, um gás de combustão a uma temperatura de pelo menos 490ºc com um teor de oxigênio de pelo menos 0,5% em mol é alimentado para a zona de queima. ali, os depósito de coque sobre as partículas do catalisador são queimados com o gás de combustão. as partículas de catalisador passam da zona de queima para uma z9ona de halogenação no regenerador de catalisador contínuo e as partículas do catalisador são oxi-halogenadas para redispersar o metal do grupo da platina, para formar partículas de catalisador regenerado.

27. 发明专利

ZA201000632B HYDROCARBON CONVERSION UNIT INCLUDING A REACTION ZONE RECEIVING TRANSFERRED CATALYST 未知
公开(公告)号：ZA201000632B
公开(公告)日：2011-10-26
申请号：ZA201000632
申请日：2010-01-27
申请人： UOP LLC
发明人： FECTEAU DAVID J , SECHRIST PAUL A , NAUNHEIMER CHRISTOPHER
IPC分类号： C10G20060101
摘要： One exemplary embodiment can include an apparatus for transferring catalyst from a regeneration zone to a reaction zone in a hydrocarbon conversion unit. The hydrocarbon conversion unit can include a transfer vessel, and first, second, and third lines. The transfer vessel can transfer regenerated catalyst from the regeneration zone at a first pressure to the reaction zone at a second pressure where the second pressure is greater than the first pressure. Generally, the first line communicates the catalyst to the transfer vessel and is coupled to a first valve to allow catalyst into the transfer vessel and the second line communicates the catalyst from the transfer vessel and is coupled to a second valve to allow catalyst out of the transfer vessel. The third line for allowing the passage of gas therethrough may be at a pressure higher than the first pressure having a first portion communicating with the transfer vessel and having a second portion coupled to third and fourth valves. Each of the third and fourth valves can have a first position that is open and a second position that is closed, which may correspond, respectively, to the opening and closing of the first and second valves to allow gas to pass therethrough.

28. 发明专利

ES2363022T3 APARATO DE DISTRIBUCION DE FLUIDO. 未知
公开(公告)号：ES2363022T3
公开(公告)日：2011-07-19
申请号：ES05814894
申请日：2005-10-28
申请人： UOP LLC
发明人： FREY STANLEY J , SECHRIST PAUL A , KAUFF DANIEL A
IPC分类号： B01D15/00 , B01D24/08 , B01D24/48
摘要： Un aparato mezclador-distribuidor-colector (3) situado entre un lecho superior y un lecho inferior de partículas sólidas (2) en una vasija (1) que tiene un eje geométrico vertical (13), cuyo aparato comprende: un límite superior (5) para retener el lecho superior de partículas sólidas y permitir el flujo hacia abajo de un fluido con un perfil de velocidades del fluido a través del aparato mezclador-distribuidor-colector (3); un distribuidor (6) de fluido situado debajo del límite superior (5) y separado de él, mejorando el distribuidor (6) de fluido la uniformidad del perfil de velocidades del fluido; una placa (8) de desviación de fluido que se extiende horizontalmente a través del área de la sección transversal de la vasija y que está situada entre el límite superior (5) y el distribuidor (6) de fluido y separada de ellos, al menos un paso (9) a través de la placa (8) de desviación de fluido que proporciona comunicación de fluido entre el límite superior (5) y el distribuidor (6) de fluido; y un manipulador de flujo (7) seleccionado del grupo que consiste en placas perforadas, tamices, rejillas, sólidos porosos, nidos de abeja y combinaciones de los mismos; en el que el límite superior (5), el distribuidor (6) de fluido y el manipulador de flujo (7) están orientados sustancialmente paralelos entre sí y sustancialmente perpendiculares al eje geométrico (13) de la vasija vertical, y el manipulador de flujo (7) está situado debajo del distribuidor (6) de fluido y separado de él en una distancia (X), y tiene un área abierta, OAM, tal que la relación OAM/OAD sea mayor que 1, siendo OAD el área abierta del distribuidor (6) de fluido.

29. 发明专利

TR201000831T1 未知
公开(公告)号：TR201000831T1
公开(公告)日：2010-04-21
申请号：TR201000831
申请日：2008-07-16
申请人： UOP LLC
发明人： FECTEAU DAVID J , NAUNHEIMER CHRISTOPHER , SECHRIST PAUL A
IPC分类号： C10G35/12 , C10G9/32
摘要： One exemplary embodiment can include an apparatus for transferring catalyst from a regeneration zone to a reaction zone in a hydrocarbon conversion unit. The hydrocarbon conversion unit can include a transfer vessel, and first, second, and third lines. The transfer vessel can transfer regenerated catalyst from the regeneration zone at a first pressure to the reaction zone at a second pressure where the second pressure is greater than the first pressure. Generally, the first line communicates the catalyst to the transfer vessel and is coupled to a first valve to allow catalyst into the transfer vessel and the second line communicates the catalyst from the transfer vessel and is coupled to a second valve to allow catalyst out of the transfer vessel. The third line for allowing the passage of gas therethrough may be at a pressure higher than the first pressure having a first portion communicating with the transfer vessel and having a second portion coupled to third and fourth valves. Each of the third and fourth valves can have a first position that is open and a second position that is closed, which may correspond, respectively, to the opening and closing of the first and second valves to allow gas to pass therethrough.

30. 发明专利

CA2695168A1 HYDROCARBON CONVERSION UNIT INCLUDING A REACTION ZONE RECEIVING TRANSFERRED CATALYST 未知
公开(公告)号：CA2695168A1
公开(公告)日：2009-02-05
申请号：CA2695168
申请日：2008-07-16
申请人： UOP LLC
发明人： FECTEAU DAVID J , SECHRIST PAUL A , NAUNHEIMER CHRISTOPHER
IPC分类号： C10G35/12 , C10G9/32
摘要： One embodiment includes an apparatus for transferring catalyst from a regeneration zone to a reaction zone in a hydrocarbon conversion unit which includes a transfer vessel, and first, second, and third lines. The transfer vessel can transfer regenerated catalyst from the regeneration zone at a first pressure to the reaction zone at a second pressure where the second pressure is greater than the first pressure. Generally, the first line communicates the catalyst to the transfer vessel and the second line communicates the catalyst from the transfer vessel. The third line for allowing the passage of gas therethrough may be at a pressure higher than the first pressure having a first portion communicating with the transfer vessel and having a second portion coupled to third and fourth valves.

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