专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明申请

US20070205139A1 FCC DUAL ELEVATION RISER FEED DISTRIBUTORS FOR GASOLINE AND LIGHT OLEFIN MODES OF OPERATION 审中-公开
标题翻译： FCC双重升压器供料分配器，用于汽油和轻油脂运行模式
公开(公告)号：US20070205139A1
公开(公告)日：2007-09-06
申请号：US11617894
申请日：2006-12-29
申请人： SATHIT KULPRATHIPANJA , Daniel N. Myers , Paolo Palmas , Mark W. Schnaith , Ismail B. Cetinkaya , Peter J. Van Opdorp , Charles L. Hemler
发明人： SATHIT KULPRATHIPANJA , Daniel N. Myers , Paolo Palmas , Mark W. Schnaith , Ismail B. Cetinkaya , Peter J. Van Opdorp , Charles L. Hemler
IPC分类号： C10G11/00
CPC分类号： C10G11/18 , B01J4/002
摘要： A fluid catalytic cracking process includes feeding hydrocarbon into a riser in the presence of a catalyst, cracking the hydrocarbon in the riser in the presence of the catalyst to form a cracked stream, and separating the catalyst from the cracked stream. When in a gasoline mode, the hydrocarbon is fed through a first distributor into the riser, and when in a light olefin mode, the hydrocarbon is fed through a second distributor into the riser. The second distributor is positioned at a higher elevation than the first distributor.
摘要翻译：流化催化裂解方法包括在催化剂存在下将烃进料到提升管中，在催化剂存在下裂解提升管中的烃，形成裂化物流，并将催化剂与裂化物流分离。当处于汽油模式时，烃通过第一分配器进料到提升管中，并且当处于轻烯烃模式时，烃通过第二分配器进料到提升管中。第二分配器位于比第一分配器更高的高度。

2. 发明授权

US4710357A FCC combustion zone catalyst cooling apparatus 失效
标题翻译： FCC燃烧区催化剂冷却装置
公开(公告)号：US4710357A
公开(公告)日：1987-12-01
申请号：US764360
申请日：1985-08-12
申请人： Ismail B. Cetinkaya , Daniel N. Myers
发明人： Ismail B. Cetinkaya , Daniel N. Myers
IPC分类号： B01J8/24 , C10G11/18 , B01J8/18
CPC分类号： B01J8/1809 , C10G11/182 , C10G11/187 , B01J2208/00203 , B01J2208/0053 , B01J2208/00548
摘要： An apparatus for the cooling of hot fluidized solid particles such as catalyst of an FCC petroleum refining process includes a conduit in which particles flow downward from a first dense phase fluidized bed into a cooling chamber and contact the shell side of a vertically oriented shell and tube heat exchanger where cooling occurs via indirect heat exchange with a cooling medium circulating in the tubes. The extent of cooling is controlled by the varying of the heat transfer coefficient between the tubes and particles in the heat exchanger. The coefficient is varied by changing the quantity of fluidizing gas fed to the fluidized bed in the heat exchanger. The heat exchanger is located within a lower portion of the cooling chamber totally below the particle inlet and outlet conduits. The heat exchanger can therefore be removed from service and protected by being buried under unfluidized relatively cool catalyst. The fluidizing gas supports combustion within a lower combustion zone.
摘要翻译：用于冷却FCC石油精炼方法的催化剂的热流化固体颗粒的装置包括一个导管，其中颗粒从第一密相流化床向下流到冷却室中，并接触垂直定向的壳和管的壳侧热交换器，其中通过与在管中循环的冷却介质的间接热交换进行冷却。冷却的程度由热交换器中的管和颗粒之间的传热系数的变化来控制。通过改变在热交换器中供给到流化床的流化气体的量来改变系数。热交换器位于冷却室的下部，完全在颗粒入口和出口管道下方。因此，热交换器可以从使用中除去并被埋在非流动的相对较冷的催化剂中而被保护。流化气体支持下燃烧区内的燃烧。

3. 发明授权

US4578366A FCC combustion zone catalyst cooling process 失效
标题翻译： FCC燃烧区催化剂冷却过程
公开(公告)号：US4578366A
公开(公告)日：1986-03-25
申请号：US687352
申请日：1984-12-28
申请人： Ismail B. Cetinkaya , Daniel N. Myers
发明人： Ismail B. Cetinkaya , Daniel N. Myers
IPC分类号： B01J20060101 , B01J8/00 , B01J8/24 , B01J38/32 , C10G20060101 , C10G11/18 , B01J21/20
CPC分类号： B01J8/1809 , C10G11/182 , C10G11/187 , B01J2208/00203 , B01J2208/00256 , B01J2208/00292 , B01J2208/0053 , B01J2208/00548 , Y10S208/01
摘要： A process and apparatus for the cooling of hot fluidized solid particles such as catalyst of an FCC petroleum refining process. The particles flow downward from a first dense phase fluidized bed into a cooling chamber and contact the shell side of a vertically oriented shell and tube heat exchanger where cooling occurs via indirect heat exchange with a cooling medium circulating in the tubes. The extent of cooling is controlled by the varying of the heat transfer coefficient between the tubes and particles in the heat exchanger. The coefficient is varied by changing the quantity of fluidizing gas fed to the fluidized bed in the heat exchanger. The heat exchanger is located within a lower portion of the cooling chamber totally below the particle inlet and outlet conduits. The heat exchanger can therefore be removed from service and protected by being buried under unfluidized relatively cool catalyst. The fluidizing gas supports combustion within a lower combustion zone.
摘要翻译：用于冷却热液化固体颗粒如FCC石油精炼方法的催化剂的方法和设备。颗粒从第一密相流化床向下流入冷却室，并接触垂直取向的管壳式热交换器的壳侧，通过与在管中循环的冷却介质的间接热交换进行冷却。冷却的程度由热交换器中的管和颗粒之间的传热系数的变化来控制。通过改变在热交换器中供给到流化床的流化气体的量来改变系数。热交换器位于冷却室的下部，完全在颗粒入口和出口管道下方。因此，热交换器可以从使用中除去并被埋在非流动的相对较冷的催化剂中而被保护。流化气体支持下燃烧区内的燃烧。

4. 发明授权

US09422478B2 Char-handling processes in a pyrolysis system 有权
公开(公告)号：US09422478B2
公开(公告)日：2016-08-23
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 , Vincenza Myers
发明人： Paolo Palmas , Paul A. Sechrist , Sid Kulprathipanja , Stanley J. Frey , Barry Freel , Daniel N. Myers
IPC分类号： F23B90/00 , C10B23/00 , C10B49/22 , C10B53/02 , C10C5/00 , C10K1/02 , F23G5/027 , F23G5/30 , F23G5/46 , F23G5/50 , F23G7/10
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.

5. 发明授权

US08609566B2 Process for venting a catalyst cooler 有权
标题翻译：排气催化剂冷却器的方法
公开(公告)号：US08609566B2
公开(公告)日：2013-12-17
申请号：US13036603
申请日：2011-02-28
申请人： Paolo Palmas , Daniel N. Myers
发明人： Paolo Palmas , Daniel N. Myers
IPC分类号： B01J38/32
CPC分类号： C10G11/182 , B01J8/28 , B01J29/90 , B01J38/02 , B01J38/12 , B01J38/32 , B01J38/34 , B01J2208/00123 , B01J2208/00132
摘要： The process herein provide a catalyst cooler with a vent that communicates fluidizing gas to a lower chamber of a regenerator. Air that is used as fluidizing gas can then be consumed in the regenerator without promoting after burn in the upper chamber.
摘要翻译：本发明的方法提供一种催化剂冷却器，其具有将流化气体与再生器的下部室连通的排气口。用作流化气体的空气然后可以在再生器中消耗，而不会在上部室中燃烧之后被促进。

6. 发明授权

US08603406B2 For drying regenerated catalyst in route to a propane dehydrogenation reactor 有权
标题翻译：用于干燥经丙烷脱氢反应器的再生催化剂
公开(公告)号：US08603406B2
公开(公告)日：2013-12-10
申请号：US12871296
申请日：2010-08-30
申请人： David N. Myers , Daniel N. Myers , Paolo Palmas , Laura E. Leonard , Wolfgang A. Spieker
发明人： David N. Myers , Daniel N. Myers , Paolo Palmas , Laura E. Leonard , Wolfgang A. Spieker
IPC分类号： B01J23/90 , B01J19/00 , B01J8/00 , B01J8/02 , B01J8/18 , B01J35/02 , B01J29/70 , F27B15/00 , F27B15/08 , F27B15/14 , F27B15/16
CPC分类号： B01J38/30 , B01J8/28 , B01J8/34 , C07C5/3335 , Y02P20/52 , Y02P20/584 , C07C11/06
摘要： An apparatus and process are presented for drying a catalyst in a reactor-regenerator system. The process includes a continuous operating system with catalyst circulating between a reactor and regenerator, and the catalyst is dried before returning the catalyst to the reactor. The process uses air that is split between the drying stage and the combustion stage without adding equipment outside of the regenerator, minimizing energy, capital cost, and space requirements.
摘要翻译：提出了用于干燥反应器 - 再生器系统中的催化剂的装置和方法。该方法包括具有在反应器和再生器之间循环的催化剂的连续操作系统，并且在将催化剂返回到反应器之前将催化剂干燥。该过程使用在干燥阶段和燃烧阶段之间分配的空气，而不需要在再生器外部添加设备，从而最小化能源，资本成本和空间要求。

7. 发明申请

US20120230882A1 SLURRY COLUMN GASOLINE ALKYLATION USING GAS PHASE OLEFIN INJECTION 审中-公开
标题翻译：使用气相烯烃注射的浆液柱汽油烷基化
公开(公告)号：US20120230882A1
公开(公告)日：2012-09-13
申请号：US13480626
申请日：2012-05-25
申请人： Douglas A. Nafis , Lev Davydov , David N. Myers , Carl J. Stevens , Daniel N. Myers
发明人： Douglas A. Nafis , Lev Davydov , David N. Myers , Carl J. Stevens , Daniel N. Myers
IPC分类号： B01J8/22 , B01J8/00
CPC分类号： B01J29/90 , B01J29/084 , B01J38/10 , B01J38/56 , B01J38/58 , C07C2/58 , C07C2529/08 , Y02P20/584 , C07C9/16
摘要： Alkylation systems and processes are provided herein that include a slurry reactor. The slurry reactor receives a reactor feed slurry including catalyst and liquid isobutane, a olefin feed, and a circulating reactor vapor stream, where the slurry reactor produces a reactor liquid effluent stream, the reactor liquid effluent stream including catalyst, isobutane, and a liquid alkylate product. The catalyst in the reactor feed slurry can be regenerated catalyst from a catalyst regenerator. The catalyst can be regenerated after being removed from the liquid alkylate product and isobutane in the reactor liquid effluent stream.
摘要翻译：本文提供了包括淤浆反应器的烷基化系统和方法。浆料反应器接收包括催化剂和液体异丁烷，烯烃进料和循环反应器蒸气流的反应器进料浆料，其中浆料反应器产生反应器液体流出物流，反应器液体流出物流包括催化剂，异丁烷和液体烷基化物产品。反应器进料浆料中的催化剂可以由催化剂再生器再生催化剂。催化剂可以在反应器液体流出物流中从液体烷基化物产物和异丁烷中除去后再生。

8. 发明授权

US07368090B2 FCC spent catalyst distributor 失效
标题翻译： FCC废催化剂分配器
公开(公告)号：US07368090B2
公开(公告)日：2008-05-06
申请号：US10925481
申请日：2004-08-25
申请人： Daniel N. Myers , Mikhail Tretyak , Rusty M. Pittman , Steven Niewiedzial
发明人： Daniel N. Myers , Mikhail Tretyak , Rusty M. Pittman , Steven Niewiedzial
IPC分类号： B01J8/18 , B01J23/90 , B32B5/02 , C10G11/00 , C10G11/02
CPC分类号： C10G11/182 , B01J38/30
摘要： An distributor arrangement introduces spent FCC catalyst more uniformly across the dense bed of the regenerator to provide more even contact with regeneration gas in order to avoid hot spots and zones of incomplete combustion. The invention forms a fluidized hopper to collect spent catalyst and a horizontally extended header with multiple horizontally extended outlet arms to place catalyst into the regenerator. The invention may use an aeration means to fluidize the header to further assist catalyst flow. Furthermore, the spent catalyst delivered to the top of the regenerator dense reduces NOx emissions in the flue gas.
摘要翻译：分销商安排将废FCC催化剂更均匀地引入再生器的致密床，以提供与再生气体更均匀的接触，以避免热点和不完全燃烧的区域。本发明形成流化料斗以收集废催化剂和具有多个水平延伸的出口臂的水平延伸的集管，以将催化剂置于再生器中。本发明可以使用曝气装置来使集管流化以进一步辅助催化剂流动。此外，输送到再生器顶部的废催化剂致密地减少烟道气中的NO x排放。

9. 发明授权

US6010620A Distribution apparatus and method for short time contact of hydrocarbon compounds with particles 失效
标题翻译：碳氢化合物与颗粒短时间接触的分配装置和方法
公开(公告)号：US6010620A
公开(公告)日：2000-01-04
申请号：US967525
申请日：1997-11-11
申请人： Daniel N. Myers , Aziz A. Sattar
发明人： Daniel N. Myers , Aziz A. Sattar
IPC分类号： B01J8/00 , B01J8/12 , B01J8/24 , B01J19/26 , C10G11/18
CPC分类号： C10G11/18 , B01J19/26 , B01J8/005 , B01J8/0055 , B01J8/12 , B01J8/1827 , B01J2208/00495 , B01J2208/00539 , B01J2208/00548
摘要： An arrangement for the controlled production of an essentially linear array of hydrocarbon feed injection jets maintains stable and reliable jets by passing individual piping for each jet through a support shroud that is located in a contacting vessel. Controlled atomization is provided by independently injecting a uniform quantity of gas medium into each of the plurality of uniformly created feed injection streams upstream of a discharge nozzle that separately discharges each mixed stream of hydrocarbons and gas medium into a stream of catalyst particles at or about the inner end of the support shroud. The feed injection jets are suitable for positioning in an inner location of large contacting vessel. Uniformity of distribution is obtained by dividing the hydrocarbons streams from an oil header into an individual oil conduit for each spray injection nozzle. The individual oil conduits each pass the feed perpendicularly into a separate mixing conduit that discharges a mixture of gas medium and oil into each spray nozzle. Another header supplies individual gas conduits that pass the gas medium longitudinally into the mixture conduits at a right angle to the catalyst stream. The ends of the mixture conduits dispose the spray injection nozzles in positions to produce an array of feed injection jets.
摘要翻译：用于控制生产基本上线性的烃类进料喷射射流阵列的装置通过使每个射流的各个管道通过位于接触容器中的支撑罩而保持稳定和可靠的喷射。通过在排放喷嘴上游的多个均匀产生的进料注入流中的每一个中独立地注入均匀量的气体介质来提供可控制的雾化，其将烃和气体介质的每个混合流分别排放到催化剂颗粒流中或附近支撑罩的内端。进料喷射射流适合于定位在大型接触容器的内部位置。通过将来自油头的碳氢化合物流分成用于每个喷射喷嘴的单个油导管来获得分布的均匀性。各个油管道各自将进料垂直地送入单独的混合管道，将气体介质和油的混合物排放到每个喷嘴中。另一个头部供应单独的气体导管，其将气体介质沿着与催化剂流成直角的方向纵向通入混合物管道。混合物管道的端部将喷射喷嘴设置在产生一系列进料喷射射流的位置。

10. 发明授权

US10041667B2 Apparatuses for controlling heat for rapid thermal processing of carbonaceous material and methods for the same 有权
公开(公告)号：US10041667B2
公开(公告)日：2018-08-07
申请号：US13240513
申请日：2011-09-22
申请人： Sathit Kulprathipanja , Daniel N. Myers , Vincenza Myers , Paolo Palmas
发明人： Sathit Kulprathipanja , Daniel N. Myers , Paolo Palmas
IPC分类号： F23C10/18 , C10B49/22 , C10B53/02 , F23C10/26
CPC分类号： F23C10/18 , C10B49/22 , C10B53/02 , F23C2206/103 , Y02E50/14
摘要： A rapid thermal processing system includes an inorganic heat carrier particles reheater coupled to an inorganic particle cooler. For example. inorganic heat carrier particles may be cooled in a shell and tube inorganic particle cooler by indirect heat exchange with a cooling medium. The cooled inorganic heat carrier particles may then be supplied to a reactor to transfer heat to carbonaceous material.

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式