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81. 发明申请

US20150129805A1 METHOD FOR PRODUCING CO AND/OR H2 IN AN ALTERNATING OPERATION BETWEEN TWO OPERATING MODES 审中-公开
标题翻译：在两种操作模式之间的替代操作中生产CO和/或H2的方法
公开(公告)号：US20150129805A1
公开(公告)日：2015-05-14
申请号：US14384460
申请日：2013-03-12
申请人： Bayer Intellectual Property GmbH
发明人： Alexander Karpenko , Kristian Voelskow , Emanuel Kockrick , Albert Tulke , Daniel Gordon Duff , Stefanie Eiden , Oliver Felix-Karl Schlüter , Vanessa Gepert , Ulrich Nieken , René Kelling
IPC分类号： C01B3/38
CPC分类号： C01B3/384 , B01J8/008 , B01J8/0453 , B01J8/0496 , B01J12/007 , B01J19/2485 , B01J23/002 , B01J23/36 , B01J23/63 , B01J23/892 , B01J35/04 , B01J2208/00398 , B01J2208/00415 , B01J2208/00522 , B01J2219/2416 , B01J2219/2428 , B01J2219/243 , C01B3/38 , C01B3/40 , C01B32/40 , C01B2203/0233 , C01B2203/0238 , C01B2203/0261 , C01B2203/085 , C01B2203/0866 , C01B2203/1005 , C01B2203/1041 , C01B2203/1058 , C01B2203/1064 , C01B2203/1088 , C01B2203/1235 , C01B2203/142 , C01B2203/1623 , C10K3/026 , Y02P20/133 , Y02P20/52
摘要： The invention relates to a method for producing syngas in an alternating operation between two operating modes. The method has the steps of providing a flow reactor; endothermically reacting carbon dioxide with hydrocarbons, water, and/or hydrogen in the flow reactor, at least carbon monoxide being formed as the product, under the effect of heat generated electrically by one or more heating elements (110, 111, 112, 113); and at the same time exothermically reacting hydrocarbons, carbon monoxide, and/or hydrogen as reactants in the flow reactor. The exothermic reaction releases a heat quantity Q1, the electric heating of the reactor releases a heat quantity Q2, and the exothermic reaction and the electric heating of the reactor are operated such that the sum of Q1 and Q2 is greater than or equal to the heat quantity Q3 which is required for an equilibrium yield Y of the endothermic reaction of ≧90%.
摘要翻译：本发明涉及在两种操作模式之间的交替操作中制造合成气的方法。该方法具有提供流动反应器的步骤; 在流动反应器中使二氧化碳与碳氢化合物，水和/或氢气吸热反应，至少一氧化碳作为产物形成，在由一个或多个加热元件（110,111,112,113）电产生的热的作用下， ; 同时在流动反应器中使烃，一氧化碳和/或氢气作为反应物放热反应。放热反应释放热量Q1，反应器的电加热释放热量Q2，并且操作反应器的放热反应和电加热，使得Q1和Q2的和大于或等于热量吸热反应的平衡产率Y所需的量Q3为≥90％。

82. 发明申请

US20150122128A1 HYDROGEN GENERATION ASSEMBLIES AND HYDROGEN PURIFICATION DEVICES 有权
标题翻译：氢发生装置和氢气净化装置
公开(公告)号：US20150122128A1
公开(公告)日：2015-05-07
申请号：US14594997
申请日：2015-01-12
申请人： ELEMENT 1 CORP.
发明人： David J. Edlund
IPC分类号： B01D71/02 , B01D63/00
CPC分类号： B01D71/022 , B01D53/22 , B01D63/00 , B01D63/088 , B01D2053/222 , B01D2313/086 , B01D2313/20 , B01D2325/20 , B01J8/0257 , B01J8/0278 , B01J8/0285 , B01J2208/00176 , B01J2208/00203 , B01J2208/00309 , B01J2208/00495 , B01J2208/00504 , B01J2208/00522 , B01J2208/0053 , B01J2219/00006 , B01J2219/0004 , C01B3/323 , C01B3/384 , C01B2203/0233 , C01B2203/0283 , C01B2203/0405 , C01B2203/043 , C01B2203/044 , C01B2203/0445 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/1217 , C01B2203/1223 , C01B2203/1229 , C01B2203/1241 , C01B2203/1247 , C01B2203/1288 , C01B2203/1294
摘要： Hydrogen generation assemblies, hydrogen purification devices, and their components, and methods of manufacturing those assemblies, devices, and components are disclosed. In some embodiments, the devices may include frames with membrane support structures and/or may include a microscreen structure configured to prevent intermetallic diffusion.
摘要翻译：公开了氢发生组件，氢气净化装置及其部件，以及制造这些组件，装置和部件的方法。在一些实施例中，装置可以包括具有膜支撑结构的框架和/或可以包括被配置为防止金属间扩散的微屏结构。

83. 发明申请

US20130011301A1 HYDROGEN GENERATION ASSEMBLIES AND HYDROGEN PURIFICATION DEVICES 有权
标题翻译：氢发生装置和氢气净化装置
公开(公告)号：US20130011301A1
公开(公告)日：2013-01-10
申请号：US13178098
申请日：2011-07-07
申请人： David J. Edlund
发明人： David J. Edlund
IPC分类号： B01J19/00 , B23K31/02 , B01D53/22
CPC分类号： B01D71/022 , B01D53/22 , B01D63/00 , B01D63/088 , B01D2053/222 , B01D2313/086 , B01D2313/20 , B01D2325/20 , B01J8/0257 , B01J8/0278 , B01J8/0285 , B01J2208/00176 , B01J2208/00203 , B01J2208/00309 , B01J2208/00495 , B01J2208/00504 , B01J2208/00522 , B01J2208/0053 , B01J2219/00006 , B01J2219/0004 , C01B3/323 , C01B3/384 , C01B2203/0233 , C01B2203/0283 , C01B2203/0405 , C01B2203/043 , C01B2203/044 , C01B2203/0445 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/1217 , C01B2203/1223 , C01B2203/1229 , C01B2203/1241 , C01B2203/1247 , C01B2203/1288 , C01B2203/1294
摘要： Hydrogen generation assemblies, hydrogen purification devices, and their components, and methods of manufacturing those assemblies, devices, and components are disclosed. In some embodiments, the assemblies may include a vaporization region with packing material configured to transfer heat from a heated exhaust stream to a liquid-containing feed stream, and/or an insulation base adjacent a combustion region and configured to reduce external temperature of an enclosure. In some embodiments, the assemblies may include a cooling block configured to maintain an igniter assembly in thermal communication with a feed stream conduit, an igniter assembly including a catalytic coating, and/or a fuel stream distribution assembly. In some embodiments, the assemblies may include a heat conducting assembly configured to conduct heat from external heaters to an enclosure portion. In some embodiments, the devices may include frames with membrane support structures and/or may include a microscreen structure configured to prevent intermetallic diffusion.
摘要翻译：公开了氢发生组件，氢气净化装置及其部件，以及制造这些组件，装置和部件的方法。在一些实施例中，组件可以包括蒸发区域，其中填充材料配置成将热量从加热的排气流传递到含液体的进料流，和/或邻近燃烧区域的绝缘基底，并且被配置为降低外壳的外部温度。在一些实施例中，组件可以包括被配置为保持点火器组件与进料流管道，包括催化涂层和/或燃料流分配组件的点火器组件热连通的冷却块。在一些实施例中，组件可以包括被配置为将热量从外部加热器传导到外壳部分的导热组件。在一些实施例中，装置可以包括具有膜支撑结构的框架和/或可以包括被配置为防止金属间扩散的微屏结构。

84. 发明申请

US20120224997A1 Reformed Gas Production Method And Reformed Gas Production Apparatus 有权
标题翻译：改造天然气生产方式和改造天然气生产设备
公开(公告)号：US20120224997A1
公开(公告)日：2012-09-06
申请号：US13449521
申请日：2012-04-18
申请人： Osamu Okada , Kota Yokoyama , Naoki Inoue
发明人： Osamu Okada , Kota Yokoyama , Naoki Inoue
IPC分类号： B01J12/00 , G05D23/00
CPC分类号： C01B3/382 , B01J8/0492 , B01J8/0496 , B01J19/30 , B01J2208/00061 , B01J2208/00203 , B01J2208/00415 , B01J2208/00522 , B01J2208/00849 , B01J2208/00973 , B01J2208/025 , B01J2219/0004 , B01J2219/30215 , B01J2219/30223 , C01B2203/0244 , C01B2203/085 , C01B2203/1047 , C01B2203/1058 , C01B2203/1247 , C01B2203/142 , C01B2203/143 , C01B2203/1614 , C01B2203/1619 , C01B2203/169 , C10L3/08 , H01M8/0612 , Y02E60/50 , Y02P20/52 , Y02P70/56
摘要： The present invention relates to a reformed gas production apparatus that includes a reaction chamber containing a reforming catalyst, a supply route to the reaction chamber, a reformed gas conduction route from the reaction chamber, and a reaction chamber temperature control means that controls a temperature of the reaction chamber. The supply route supplies a fluid that includes a fuel containing a hydrocarbon having at least two carbon atoms, at least one of steam and a carbon dioxide-containing gas, and an oxygen-containing gas. The fuel can be a mixed fuel that includes a plurality of types of hydrocarbons that each have at least two carbon atoms. The reaction chamber temperature control means relates to the thermal decomposition index temperature of the fuel, which defines an upper limit temperature of the reforming reaction region.
摘要翻译：本发明涉及一种重整气体生产装置，其包括含有重整催化剂的反应室，到反应室的供给路径，来自反应室的重整气体传导路径，以及控制反应室温度控制装置，反应室。供应路线提供包含含有至少两个碳原子的烃，含蒸汽和含二氧化碳的气体中的至少一种和含氧气体的燃料的流体。燃料可以是混合燃料，其包括各自具有至少两个碳原子的多种类型的烃。反应室温度控制装置涉及限定重整反应区域的上限温度的燃料的热分解指数温度。

85. 发明授权

US07807860B2 Autothermal cracking process and reactor 有权
标题翻译：自热裂解过程和反应器
公开(公告)号：US07807860B2
公开(公告)日：2010-10-05
申请号：US10543696
申请日：2004-02-06
申请人： Derek Alan Colman , Michael John Alexander Matthewman , Ian Allan Beattie Reid , Vaughan Clifford Williams , William Terence Woodfin
发明人： Derek Alan Colman , Michael John Alexander Matthewman , Ian Allan Beattie Reid , Vaughan Clifford Williams , William Terence Woodfin
IPC分类号： C07C5/333
CPC分类号： B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J2208/00522 , B01J2219/00094 , B01J2219/00265 , C07C5/48
摘要： The present invention provides a reactor design that enables an auto-thermal cracking process to be conducted at any suitable pressure wherein the gaseous reactants are preheated separately before mixing and then presented to the reaction zone in a uniformly distributed manner. In particular, the present invention-relates to apparatus for reacting a first and second gaseous reactant to form a gaseous product wherein the apparatus comprises at least one first supply means for the first gaseous reactant, at least one second supply means for the second gaseous reactant, a resistance zone and a reaction zone, preferably comprising a catalyst, wherein the first supply means comprises a plurality of first outlets for delivery of the first gaseous reactant, and the second supply means comprises a plurality of second outlets for delivery of the second gaseous reactant, the resistance zone is porous, the reaction zone is positioned downstream of the resistance zone with respect to the flow of the first and second gaseous reactants and wherein the first supply means and the second supply means are arranged such that the first gas and the second gas are contacted in an essentially parallel manner and mixed prior to contacting the resistance zone. The present invention also provides a process for the production of a mono-olefin utilizing said apparatus.
摘要翻译：本发明提供一种反应器设计，使得能够在任何合适的压力下进行自热裂解过程，其中气态反应物在混合之前分别预热，然后以均匀分布的方式呈现给反应区。特别地，本发明涉及用于使第一和第二气体反应物反应以形成气态产物的装置，其中所述装置包括用于第一气态反应物的至少一个第一供应装置，用于第二气态反应物的至少一个第二供应装置，电阻区和反应区，优选包括催化剂，其中第一供应装置包括多个用于输送第一气态反应物的第一出口，第二供应装置包括多个第二出口，用于输送第二气态反应物，电阻区是多孔的，反应区相对于第一和第二气态反应物的流动位于阻力区的下游，并且其中第一供应装置和第二供应装置被布置成使得第一气体和第二气体以基本上平行的方式接触并在接触阻力区之前混合。本发明还提供了利用所述装置生产单烯烃的方法。

86. 发明申请

US20090216051A1 APPARATUS AND METHOD FOR THE REMOVAL OF WATER FROM ETHANOL 审中-公开
标题翻译：从乙醇中去除水的装置和方法
公开(公告)号：US20090216051A1
公开(公告)日：2009-08-27
申请号：US12365017
申请日：2009-02-03
申请人： Christopher J. Brown , Vladimir Hlavacek , Marian Simo
发明人： Christopher J. Brown , Vladimir Hlavacek , Marian Simo
IPC分类号： C07C29/88 , C07C29/76 , B01J19/00
CPC分类号： C07C29/76 , B01D15/00 , B01J8/0055 , B01J8/0453 , B01J8/0496 , B01J8/067 , B01J8/388 , B01J20/3483 , B01J2208/003 , B01J2208/00309 , B01J2208/00513 , B01J2208/00522 , B01J2208/0053 , C01B3/323 , C01B2203/0244 , C01B2203/0283 , C01B2203/0425 , C01B2203/0495 , C01B2203/107 , C01B2203/1076 , C01B2203/1229 , C07C31/08 , C07C31/12
摘要： An apparatus and method for drying ethanol includes a first reaction chamber for carrying out the removal of water from wet ethanol, a feed inlet for introducing the wet ethanol into the reaction chamber, a product outlet for removing dry ethanol from the reaction chamber, an optional fuel inlet for introducing a fuel into the reaction chamber, and a particulate bed, including sorbent particles, that is disposed within the reaction chamber. In a preferred embodiment, the bed is divided into first and second zones each provided with different size sorbent particles. In another preferred embodiment, the bed contains a mixture of sorbent particles and catalyst particles. The sorbent particles operate to remove water from the wet ethanol and form hydrated-sorbent particles. The catalyst particles operate to promote chemical reaction of the fuel, generating heat that causes removal of water from the hydrated-sorbent particles and regenerating the sorbent particles.
摘要翻译：用于乙醇干燥的装置和方法包括用于从湿乙醇中除去水的第一反应室，用于将湿乙醇引入反应室的进料入口，用于从反应室除去干乙醇的产物出口，任选的用于将燃料引入反应室的燃料入口和设置在反应室内的包括吸附剂颗粒的颗粒床。在一个优选的实施方案中，床分成第一和第二区，每个区具有不同尺寸的吸附剂颗粒。在另一个优选的实施方案中，该床含有吸附剂颗粒和催化剂颗粒的混合物。吸附剂颗粒用于从湿乙醇中除去水并形成水合吸附剂颗粒。催化剂颗粒用于促进燃料的化学反应，产生导致从水合吸附剂颗粒中除去水并再生吸附剂颗粒的热量。

87. 发明授权

US07566429B2 Catalytic reactive separation system for energy-efficient production of cumene 失效
标题翻译：催化反应分离系统，用于能量生产异丙苯
公开(公告)号：US07566429B2
公开(公告)日：2009-07-28
申请号：US11152997
申请日：2005-06-14
申请人： Genoveva Buelna , Tina M. Nenoff
发明人： Genoveva Buelna , Tina M. Nenoff
IPC分类号： B01J8/02 , C07C2/66
CPC分类号： B01D3/009 , B01J8/025 , B01J2208/00256 , B01J2208/00274 , B01J2208/00522 , B01J2219/30207 , B01J2219/30433 , C07C2/66 , Y02P20/127 , Y02P20/52 , Y02P20/57 , Y10S203/06 , C07C15/085
摘要： The present invention relates to an atmospheric pressure, reactive separation column packed with a solid acid zeolite catalyst for producing cumene from the reaction of benzene with propylene. Use of this un-pressurized column, where simultaneous reaction and partial separation occur during cumene production, allow separation of un-reacted, excess benzene from other products as they form. This high-yielding, energy-efficient system allows for one-step processing of cumene, with reduced need for product purification. Reacting propylene and benzene in the presence of beta zeolite catalysts generated a selectivity greater than 85% for catalytic separation reactions at a reaction temperature of 115 degrees C and at ambient pressure. Simultaneously, up to 76% of un-reacted benzene was separated from the product; which could be recycled back to the reactor for re-use.
摘要翻译：本发明涉及一种装有固体酸沸石催化剂的大气压反应性分离塔，用于从苯与丙烯反应制备异丙基苯。使用这种未加压的柱，其中在异丙基苯生产期间发生同时的反应和部分分离，允许在其形成时将未反应的过量苯与其它产物分离。这种高产能，高能效的系统可以对枯烯进行一步加工，减少对产品净化的需求。在β沸石催化剂存在下反应丙烯和苯，在115℃的反应温度和环境压力下，催化分离反应的选择性大于85％。同时，高达76％的未反应的苯与产物分离; 其可以被再循环回到反应器中以供重复使用。

88. 发明申请

US20080166674A1 Temperature control method 审中-公开
标题翻译：温度控制方法
公开(公告)号：US20080166674A1
公开(公告)日：2008-07-10
申请号：US11652201
申请日：2007-01-10
申请人： William C. Pfefferle
发明人： William C. Pfefferle
IPC分类号： B01J8/00
CPC分类号： B01J10/007 , B01J12/007 , B01J14/005 , B01J15/005 , B01J16/005 , B01J19/249 , B01J35/04 , B01J2208/0015 , B01J2208/00212 , B01J2208/00513 , B01J2208/00522 , B01J2219/00085 , B01J2219/2453 , B01J2219/2454 , B01J2219/2458 , B01J2219/2461 , B01J2219/2462 , B01J2219/2482 , F28D9/00
摘要： The invention provides a method for limiting the temperature of the catalyst in exothermic mass-transfer-limited reactions by placing a flow-through catalyst in thermal contact with a downstream non-catalytic flow-through structure placed in the flow stream whereby a portion of the heat-of-reaction is transferred to the downstream non-catalytic structure.
摘要翻译：本发明提供了一种通过将流过催化剂与放置在流动流中的下游非催化流通结构热接触来限制在放热质量传递限制反应中的催化剂的温度的方法，反应热转移到下游非催化结构。

89. 发明申请

US20080071100A1 EXOTHERMIC REACTION SYSTEM 有权
标题翻译：超热反应系统
公开(公告)号：US20080071100A1
公开(公告)日：2008-03-20
申请号：US11865905
申请日：2007-10-02
申请人： Barry Billig , Bhupendra Baria
发明人： Barry Billig , Bhupendra Baria
IPC分类号： C07D303/00
CPC分类号： F28D7/16 , B01J8/048 , B01J8/0496 , B01J8/067 , B01J2208/00212 , B01J2208/00522 , B01J2208/0053 , C07D301/10 , F28D7/0066 , F28D7/0091
摘要： A reactor and heat exchanger assembly is provided with the heat exchanger integrally affixed to the reactor exit head and adapted to immediately cool reactor gases from the reactor.
摘要翻译：反应器和热交换器组件设置有热交换器，其一体地固定到反应器出口头并且适于立即冷却来自反应器的反应器气体。

90. 发明申请

US20080039665A1 Apparatus and Method for the Removal of Water from Ethanol 有权
标题翻译：从乙醇中去除水的装置和方法
公开(公告)号：US20080039665A1
公开(公告)日：2008-02-14
申请号：US11771553
申请日：2007-06-29
申请人： Christopher Brown , Vladimir Hlavacek , Marian Simo
发明人： Christopher Brown , Vladimir Hlavacek , Marian Simo
IPC分类号： B01J8/02 , B01J19/00 , C07C29/00
CPC分类号： C07C29/76 , B01D15/00 , B01J8/0055 , B01J8/0453 , B01J8/0496 , B01J8/067 , B01J8/388 , B01J20/3483 , B01J2208/003 , B01J2208/00309 , B01J2208/00513 , B01J2208/00522 , B01J2208/0053 , C01B3/323 , C01B2203/0244 , C01B2203/0283 , C01B2203/0425 , C01B2203/0495 , C01B2203/107 , C01B2203/1076 , C01B2203/1229 , C07C31/08 , C07C31/12
摘要： An apparatus and method for drying ethanol includes a first reaction chamber for carrying out the removal of water from wet ethanol, a feed inlet for introducing the wet ethanol into the reaction chamber, a product outlet for removing dry ethanol from the reaction chamber, an optional fuel inlet for introducing a fuel into the reaction chamber, and a particulate bed, including sorbent particles, that is disposed within the reaction chamber. In a preferred embodiment, the bed is divided into first and second zones each provided with different size sorbent particles. In another preferred embodiment, the bed contains a mixture of sorbent particles and catalyst particles. The sorbent particles operate to remove water from the wet ethanol and form hydrated-sorbent particles. The catalyst particles operate to promote chemical reaction of the fuel, generating heat that causes removal of water from the hydrated-sorbent particles and regenerating the sorbent particles.
摘要翻译：用于乙醇干燥的装置和方法包括用于从湿乙醇中除去水的第一反应室，用于将湿乙醇引入反应室的进料入口，用于从反应室除去干乙醇的产物出口，用于将燃料引入反应室的燃料入口和设置在反应室内的包括吸附剂颗粒的颗粒床。在一个优选的实施方案中，床分成第一和第二区，每个区具有不同尺寸的吸附剂颗粒。在另一个优选的实施方案中，该床含有吸附剂颗粒和催化剂颗粒的混合物。吸附剂颗粒用于从湿乙醇中除去水并形成水合吸附剂颗粒。催化剂颗粒用于促进燃料的化学反应，产生导致从水合吸附剂颗粒中除去水并再生吸附剂颗粒的热量。

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