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公开(公告)号：US6123833A
公开(公告)日：2000-09-26
申请号：US158160
申请日：1998-09-22
CPC分类号： C10G45/60 , C10G29/205 , C10G35/06
摘要： A method and apparatus are disclosed for removing water from a recycle gas stream in a catalyst regeneration process. A recycle gas stream contacts catalyst and the catalyst sorbs water from the recycle gas. Some of the now-dried recycle gas recirculates to the regeneration process, thereby decreasing the water content in the regeneration process. The catalyst containing sorbed water passes to a desorption zone, where water is desorbed from the catalyst and the desorbed water is rejected from the process. This method and apparatus are useful for extending the life of catalyst in catalytic hydrocarbon processes that employ continuous or semi-continuos catalyst regeneration zones.
摘要翻译： 公开了一种在催化剂再生过程中从循环气流中除去水的方法和装置。 循环气流与催化剂接触，催化剂从再循环气体中吸收水分。 一些现在干燥的再循环气体再循环到再生过程中，从而降低再生过程中的水分含量。 含有吸附水的催化剂通过解吸区，其中水从催化剂中解吸，脱附的水被从该方法中排出。 该方法和设备可用于延长催化剂在使用连续或半连续催化剂再生区的催化烃工艺中的寿命。
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公开(公告)号：US5600052A
公开(公告)日：1997-02-04
申请号：US365622
申请日：1994-12-28
申请人： Christine J. B. Girod , William W. Levy , Peter R. Pujado , Jacques J. L. Romatier , Dominique J. J. M. Sabin , Paul A. Sechrist
发明人： Christine J. B. Girod , William W. Levy , Peter R. Pujado , Jacques J. L. Romatier , Dominique J. J. M. Sabin , Paul A. Sechrist
CPC分类号： F28F13/14 , B01J8/0207 , B01J8/0285 , B01J8/0403 , B01J8/0496 , B01J8/087 , B01J8/125 , F28D9/0006 , F28F3/04 , F28F9/0268 , B01J2208/00106 , B01J2208/0053 , B01J2208/022 , B01J2219/2453 , B01J2219/2459 , B01J2219/2464 , B01J2219/247 , B01J2219/2471 , B01J2219/2474 , B01J2219/2481 , B01J2219/2498 , Y02P20/582 , Y10S585/91 , Y10S585/911
摘要： A reactor arrangement and process for indirectly contacting a reactant stream with a heat exchange stream uses an arrangement of heat exchange plates to control temperature conditions by varying the heat transfer factor in different portions of a continuous channel defined by the heat exchange plates. The reactor arrangement and process of this invention may be used to operate a reactor under isothermal or other controlled temperature conditions. The variation in the heat transfer factor within a single heat exchange section is highly useful in maintaining a desired temperature profile in an arrangement having a cross-flow of heat exchange medium relative to reactants. The corrugations arrangement eliminates or minimizes the typical step-wise approach to isothermal conditions.
摘要翻译： 用于间接地将反应物流与热交换流接触的反应器装置和方法使用热交换板的布置来通过改变由热交换板限定的连续通道的不同部分中的传热因子来控制温度条件。 本发明的反应器装置和方法可用于在等温或其它受控温度条件下操作反应器。 在单个热交换部分内的热传递因子的变化对于在具有相对于反应物的热交换介质的交叉流动的布置中维持期望的温度分布非常有用。 波纹布置消除或最小化了等温条件的典型逐步方法。
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公开(公告)号：US5104517A
公开(公告)日：1992-04-14
申请号：US524525
申请日：1990-05-17
申请人： David A. Lomas , Edward C. Haun , Paul A. Sechrist
发明人： David A. Lomas , Edward C. Haun , Paul A. Sechrist
IPC分类号： C10G11/18
CPC分类号： C10G11/18
摘要： An FCC process and apparatus is arranged to provide a low volume dilute disengagement zone in a reactor vessel. A vented riser that provides an open discharge of catalyst and gaseous products is directly discharged into a reactor vessel. The interior of the reactor vessel is arranged such that the outlet of the reactor riser is located close to and directed at the top of the reactor vessel. The reactor vessel operates with a dense bed of catalyst having an upper bed level that is only a short distance below the outlet of the reactor riser. The cyclone separators are located to the outside of the reactor riser and circulate catalyst back to the dense bed of the reactor section.
摘要翻译： FCC方法和装置被布置成在反应器容器中提供低体积的稀释分离区。 提供催化剂和气体产物的开放排放的排气提升管直接排放到反应器容器中。 反应器容器的内部被布置成使得反应器提升管的出口靠近并且指向反应器容器的顶部。 反应器容器具有致密的催化剂床，其具有在反应器提升管的出口下方仅较短距离的上层水平。 旋风分离器位于反应器提升管的外部，并将催化剂循环回反应器部分的致密床。
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公开(公告)号：US4988430A
公开(公告)日：1991-01-29
申请号：US457463
申请日：1989-12-27
IPC分类号： C10G11/18
CPC分类号： C10G11/18 , C10G11/182
摘要： The use of lift gas for FCC risers is improved by the direct use of reactor vapors as the source of the lift gas. Reactor vapors recovered primarily from the stripping section of an FCC reactor/regenerator section provide an excellent source for lift gas material. These reactor vapors contain high concentrations of light paraffinic materials often with an equal weight percent amount of steam. The recovery of the stripping vapors independent from the product stream allows such gaseous mixtures to be readily processed for use as lift gas. The only processing requirements are the removal of particulate material and the compression of the gas to pressure conditions at the bottom of the riser. Compression of the gas requires a reduction in its temperature to suitable compressor inlet conditions. This invention is readily practiced in the most recent FCC reactor designs that separate the majority of product vapors from the catalyst in a closed riser cyclone arrangement. This invention is particularly suited for use in conjunction with hot catalyst stripping. Hot catalyst stripping produces a high concentration of very low molecular weight gas components in the effluent from the hot stripping zone which are highly suitable for use as lift gas material.
摘要翻译： 通过直接使用反应器蒸汽作为提升气体的来源，提高了用于FCC提升管的提升气体的使用。 主要从FCC反应器/再生器部分的汽提部分回收的反应器蒸气为提升气体材料提供了极好的来源。 这些反应器蒸气含有高浓度的轻石蜡材料，通常具有相等重量百分比的蒸汽量。 独立于产物流的汽提蒸气的回收允许这种气体混合物容易地加工以用作提升气体。 唯一的处理要求是去除颗粒物质并将气体压缩到提升管底部的压力条件。 压缩气体需要将其温度降低到合适的压缩机入口条件。 在最近的FCC反应器设计中容易实施本发明，其中大部分产物蒸气与封闭式立管旋风分离装置中的催化剂分离。 本发明特别适合与热催化剂汽提相结合使用。 热催化剂汽提在高温汽提区的流出物中产生非常低分子量气体组分的高浓度，这些气体组分非常适合用作提升气体材料。
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75.发明授权Production of diesel fuel from biorenewable feedstocks using non-flashing quench liquid 有权使用非闪蒸淬火液从生物可再生原料生产柴油公开(公告)号：US08921627B2
公开(公告)日：2014-12-30
申请号：US12333379
申请日：2008-12-12
CPC分类号： C10G3/60 , B01J8/0492 , B01J8/0496 , B01J2208/00283 , B01J2208/00362 , B01J2208/00539 , B01J2208/00548 , C10G3/46 , C10G3/50 , C10G45/02 , C10G65/12 , C10G2300/1014 , C10G2300/1018 , C10G2300/1022 , C10G2300/1037 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , Y02P30/20
摘要： A process has been developed for producing diesel boiling range fuel from renewable feedstocks such as plant oils and animal oils, fats, and greases. The process involves treating a renewable feedstock by hydrogenating and deoxygenating to provide a hydrocarbon fraction useful as a diesel or aviation boiling range fuel or fuel blending component. If desired, the hydrocarbon fraction can be isomerized to improve cold flow properties. A portion of the hydrogenated and deoxygenated feedstock is used as a non-flashing liquid quench stream to control the temperature of the hydrogenation and deoxygenation reactor.
摘要翻译： 已经开发了用于从可再生原料如植物油和动物油，脂肪和油脂生产柴油沸点燃料的方法。 该方法包括通过氢化和脱氧处理可再生原料以提供可用作柴油或航空沸程燃料或燃料混合组分的烃馏分。 如果需要，烃馏分可以被异构化以改善冷流动性能。 氢化和脱氧原料的一部分用作非闪蒸液体淬火流，以控制氢化和脱氧反应器的温度。
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公开(公告)号：US20130327629A1
公开(公告)日：2013-12-12
申请号：US13810405
申请日：2011-07-08
申请人： Paolo Palmas , Paul A. Sechrist , Sid Kulprathipanja , Stanley J. Frey , Barry Freel , Daniel N. Myers
发明人： Paolo Palmas , Paul A. Sechrist , Sid Kulprathipanja , Stanley J. Frey , Barry Freel , Daniel N. Myers
IPC分类号： C10B23/00
CPC分类号： C10B23/00 , C10B49/22 , C10B53/02 , C10C5/00 , C10K1/026 , F23G5/0273 , F23G5/30 , F23G5/46 , F23G5/50 , F23G7/10 , F23G2201/303 , F23G2201/304 , F23G2201/601 , F23G2206/10 , F23G2900/50205 , Y02E50/14 , Y02P20/133 , Y02P20/145 , Y02P30/20
摘要： Char-handling processes for controlling overall heat balance, ash accumulation, and afterburn in a reheater are provided. Carbonaceous biomass feedstock is pyrolyzed using a heat transfer medium forming pyrolysis products and a spent heat transfer medium. The spent heat transfer medium is separated into segregated char and char-depleted spent heat transfer medium. The char-depleted spent heat transfer medium is introduced into a dense bed of heat transfer medium fluidized by a stream of oxygen-containing regeneration gas. All or a portion of the segregated char is combusted in the dense bed using the stream of oxygen-containing regeneration gas. A portion of the segregated char may be exported out of the pyrolysis system to control the overall heat balance and ash accumulation.
摘要翻译： 提供了用于控制再热器中总体热平衡，灰分积累和再燃烧的焦炭处理过程。 碳质生物质原料使用形成热解产物和废热转移介质的传热介质进行热解。 废弃的传热介质被分离成分离的炭和贫乏的传热介质。 将贫乏的废热转移介质引入通过含氧再生气体流流化的传热介质的致密层中。 所有或部分分离的炭在密实床中使用含氧再生气体气流燃烧。 分离的焦炭的一部分可以从热解系统输出以控制总体热平衡和灰分积累。
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77.发明授权Utilization of baffles in chlorination zone for continuous catalyst regeneration 有权挡板在氯化区的利用用于连续催化剂再生公开(公告)号：US08216522B2
公开(公告)日：2012-07-10
申请号：US13160141
申请日：2011-06-14
申请人： Bing Sun , Paul A. Sechrist
发明人： Bing Sun , Paul A. Sechrist
CPC分类号： B01J8/125
摘要： Catalyst regeneration vessels including a chlorination zone that includes an outer mixing chamber, an inner mixing chamber, and a catalyst bed. The outer mixing chamber can include a lower portion and an upper portion, the lower portion of the outer mixing chamber including at least one air nozzle that injects a drying air stream into the outer mixing chamber, at least one chlorine input nozzle that injects a chlorine input stream into the outer mixing chamber, and at least a first baffle. The chlorination zone can also contain a second baffle that directs the mixed drying air stream and chlorine input stream from the outer mixing chamber to the inner mixing chamber.
摘要翻译： 催化剂再生容器包括包括外混合室，内混合室和催化剂床的氯化区。 外部混合室可以包括下部和上部，外部混合室的下部包括至少一个空气喷嘴，其将干燥空气流注入到外部混合室中，至少一个氯输入喷嘴注入氯 输入流入外部混合室，以及至少第一挡板。 氯化区还可以包含将混合的干燥空气流和氯输入流从外部混合室引导到内部混合室的第二挡板。
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公开(公告)号：US08181942B2
公开(公告)日：2012-05-22
申请号：US12147040
申请日：2008-06-26
申请人： Paul A. Sechrist
发明人： Paul A. Sechrist
IPC分类号： B01F3/04
CPC分类号： B01J8/0453 , B01D15/14 , B01J8/0492
摘要： A liquid distribution device is presented for the collection and distribution of liquid between reactor or adsorbent beds. The device includes a liquid collection tray, a mixing chamber in fluid communication with the liquid collection tray, a rough distribution tray in fluid communication with the mixing chamber, a liquid distribution tray in fluid communication with the rough distribution tray, and a plurality of vapor pipes.
摘要翻译： 液体分配装置用于在反应器或吸附剂床之间收集和分配液体。 所述装置包括液体收集盘，与所述液体收集盘流体连通的混合室，与所述混合室流体连通的粗分配塔，与所述粗分配塔流体连通的液体分配塔，以及多个蒸气 管道。
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公开(公告)号：US20120082595A1
公开(公告)日：2012-04-05
申请号：US13218578
申请日：2011-08-26
申请人： Bing Sun , Paul A. Sechrist , Bryan K. Glover , Michael J. Vetter
发明人： Bing Sun , Paul A. Sechrist , Bryan K. Glover , Michael J. Vetter
IPC分类号： B01J8/02
CPC分类号： B01J8/12 , B01D53/0423 , B01J8/085 , B01J2208/00849 , B01J2208/00929 , B01J2219/00024
摘要： An apparatus for contacting a bed of particulate material with a cross flowing fluid, which maintains the bed of particulate material within a retention volume. The apparatus includes partitions for retaining particles, with apertures disposed within the partitions. The apertures are covered by louvers that extend above the edges of the apertures to prevent solid particles from spilling through inlet apertures.
摘要翻译： 用于使颗粒材料床与交叉流动流体接触的装置，其将颗粒材料床保持在保持体积内。 该装置包括用于保持颗粒的分隔物，孔中设置在隔板内。 这些孔由在孔的边缘上方延伸的百叶窗覆盖以防止固体颗粒溢出入口孔。
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公开(公告)号：US20110301393A1
公开(公告)日：2011-12-08
申请号：US12793290
申请日：2010-06-03
IPC分类号： C07C1/00
CPC分类号： C07C1/20 , B01J8/26 , B01J2208/00212 , B01J2219/0004 , C07C2529/85 , C07C11/02
摘要： A process and apparatus is presented for the improved selectivity of oxygenate conversion to olefins. The process includes passing a process stream through a two stage reactor, wherein the process stream is separated from the catalyst in the first stage before passing the process stream to the second stage. The catalyst is continuously passed through the two stages, and cycles through a regeneration unit to control the carbon content on the catalyst.
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