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公开(公告)号：US5688473A
公开(公告)日：1997-11-18
申请号：US596902
申请日：1996-03-13
CPC分类号： C10G35/10 , B01J8/003 , Y10T137/3127 , Y10T137/7838
摘要： An apparatus for replacing particles in a process that transfers particles is disclosed. The apparatus employs a seal zone which is in communication with two zones of the process and in which particles that are being added to the process are purged. The apparatus allows particles to be replaced without reducing the normal rate of particle transfer through the process, which results in a savings in downtime costs. This invention is adaptable to a multitude of processes for the catalytic conversion of hydrocarbons in which deactivated catalyst particles are regenerated.
摘要翻译： 公开了一种在转移颗粒的工艺中替换颗粒的装置。 该设备采用密封区域，其与该过程的两个区域连通，并且其中被添加到该过程中的颗粒被清除。 该设备允许更换颗粒，而不会降低通过该过程的正常的颗粒转移速率，从而节省停机成本。 本发明适用于催化转化烃的多种方法，其中失活的催化剂颗粒被再生。
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公开(公告)号：US08499702B2
公开(公告)日：2013-08-06
申请号：US12837376
申请日：2010-07-15
申请人： Paolo Palmas , Paul Alvin Sechrist , Daniel N. Myers , Sid Kulprathipanja , Stanley Joseph Frey , Barry Freel
发明人： Paolo Palmas , Paul Alvin Sechrist , Daniel N. Myers , Sid Kulprathipanja , Stanley Joseph Frey , Barry Freel
IPC分类号： F23B90/00
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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3.发明申请ADSORPTION VESSELS HAVING REDUCED VOID VOLUME AND UNIFORM FLOW DISTRIBUTION 审中-公开具有减少无效体积和均匀流量分布的吸附船公开(公告)号：US20130152795A1
公开(公告)日：2013-06-20
申请号：US13330448
申请日：2011-12-19
申请人： Kirit M. Patel , Bradley P. Russell , Paul Alvin Sechrist , Michael Jerome Vetter , Hua Chen , Pengfei Chen
发明人： Kirit M. Patel , Bradley P. Russell , Paul Alvin Sechrist , Michael Jerome Vetter , Hua Chen , Pengfei Chen
IPC分类号： B01D53/02
CPC分类号： B01D53/0407 , B01D53/0423 , B01D53/0446 , B01D53/047
摘要： Adsorption vessels and systems utilizing adsorption vessels are provided herein. In one embodiment, an adsorption vessel for receiving a fluid mixture and for separating a component from therein includes a vessel wall extending from a bottom end to a top end and defining a vessel chamber. A bottom inlet is formed in the bottom end of the adsorption vessel for introducing the fluid mixture to the vessel chamber. Further, a support plate is positioned in the vessel chamber above the bottom end, and defines a bottom void volume between the support plate and the bottom end. A filler material having a total porosity of less than about 25% is positioned in the bottom void volume and defines a channel for flow of the fluid mixture from the bottom inlet to the support plate.
摘要翻译： 本文提供了使用吸附容器的吸附容器和系统。 在一个实施例中，用于接收流体混合物并用于从其中分离组分的吸附容器包括从底端延伸到顶端并限定容器室的容器壁。 在吸附容器的底端形成底部入口，用于将流体混合物引入容器室。 此外，支撑板位于容器室中的底端上方，并且在支撑板和底端之间限定底部空隙体积。 具有小于约25％的总孔隙率的填充材料位于底部空隙体积中并且限定用于从底部入口到支撑板的流体混合物的流动的通道。
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公开(公告)号：US20120272822A1
公开(公告)日：2012-11-01
申请号：US13098290
申请日：2011-04-29
申请人： Paul Alvin Sechrist
发明人： Paul Alvin Sechrist
IPC分类号： B01D53/047
CPC分类号： B01D53/047 , B01D53/0438 , B01D53/261 , B01D2253/108 , B01D2259/40086 , B01D2259/65 , F28D7/16 , F28D9/00
摘要： One exemplary embodiment can include a process for pressure swing adsorption. Generally, the process includes passing a fluid through a first channel for adsorbing at least one component while simultaneously passing a stream desorbing a component through a second channel. The first and second channels may be in thermal communication for transferring heat from the first channel undergoing adsorption to the second channel undergoing desorption.
摘要翻译： 一个示例性实施例可以包括用于变压吸附的过程。 通常，该方法包括使流体通过用于吸附至少一种组分的第一通道，同时使通过第二通道解吸组分的流通过。 第一和第二通道可以是热连通的，以将来自经历吸附的第一通道的热量传递到经历解吸的第二通道。
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公开(公告)号：US5672798A
公开(公告)日：1997-09-30
申请号：US597048
申请日：1996-02-05
IPC分类号： B01J8/28 , B01J38/10 , B01J38/58 , C07C2/58 , C07C2/66 , C07C2/86 , C10G50/00 , C07C2/68 , C07C2/56
摘要： Hydrocarbons are alkylated in a fluidized riser-reactor using a solid catalyst which is regenerated within the process by contact with hydrogen. The alkylation and regeneration steps are separated to prevent the admixture of hydrogen and any olefins present in the process. Two separate modes of regeneration are performed simultaneously: a mild liquid-phase washing and a vapor-phase hot hydrogen stripping operation.
摘要翻译： 碳氢化合物在使用固体催化剂的流化提升管 - 反应器中烷基化，所述固体催化剂在该方法中通过与氢接触而再生。 分离烷基化和再生步骤以防止氢气与该方法中存在的任何烯烃的混合物。 同时进行两种分离的再生模式：温和的液相洗涤和气相热氢提取操作。
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公开(公告)号：US20120330076A1
公开(公告)日：2012-12-27
申请号：US13170143
申请日：2011-06-27
CPC分类号： C07C2/66 , C07C15/085
摘要： One exemplary embodiment can be a process for alkylating. The process can include providing a first effluent from a first alkylation zone, and providing a second effluent from a second alkylation zone. Generally, the first and second effluents are provided to an exchanger for reboiling a fractionation zone.
摘要翻译： 一个示例性实施方案可以是烷基化的方法。 该方法可以包括提供来自第一烷基化区的第一流出物，以及提供来自第二烷基化区的第二流出物。 通常，将第一和第二流出物提供给用于再沸腾分馏区的交换器。
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7.发明申请公开(公告)号：US20110243807A1
公开(公告)日：2011-10-06
申请号：US13160141
申请日：2011-06-14
申请人： Bing Sun , Paul Alvin Sechrist
发明人： Bing Sun , Paul Alvin Sechrist
IPC分类号： B01J15/00
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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8.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：US07985381B2
公开(公告)日：2011-07-26
申请号：US12366729
申请日：2009-02-06
申请人： Bing Sun , Paul Alvin Sechrist
发明人： Bing Sun , Paul Alvin 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：US5675048A
公开(公告)日：1997-10-07
申请号：US597047
申请日：1996-02-05
摘要： Hydrocarbons are alkylated in a fluidized riser-reactor using a solid catalyst which is regenerated within the process by contact with hydrogen. The alkylation and regeneration steps are separated to prevent the admixture of hydrogen and any olefins present in the process. Two separate modes of regeneration are performed simultaneously on different portions of the catalyst: a partial liquid-phase hydrogenative regeneration at reaction conditions and a high temperature (complete) liquid-phase hydrogenative regeneration.
摘要翻译： 碳氢化合物在使用固体催化剂的流化提升管 - 反应器中烷基化，所述固体催化剂在该方法中通过与氢接触而再生。 分离烷基化和再生步骤以防止氢气与该方法中存在的任何烯烃的混合物。 在催化剂的不同部分上同时进行两种分离的再生模式：在反应条件和高温（完全）液相氢化再生下的部分液相氢化再生。
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公开(公告)号：US20120012039A1
公开(公告)日：2012-01-19
申请号：US12837376
申请日：2010-07-15
申请人： Paolo Palmas , Paul Alvin Sechrist , Daniel N. Myers , Sid Kulprathipanja , Stanley Joseph Frey , Barry Freel
发明人： Paolo Palmas , Paul Alvin Sechrist , Daniel N. Myers , Sid Kulprathipanja , Stanley Joseph Frey , Barry Freel
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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