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1. 发明申请

US20170361291A1 Steam-Hydrocarbon Reforming Reactor 有权
公开(公告)号：US20170361291A1
公开(公告)日：2017-12-21
申请号：US15186911
申请日：2016-06-20
申请人： Air Products and Chemicals, Inc.
发明人： Bo Jin , Wenyuan Li , Xianming Jimmy Li , William Robert Licht
IPC分类号： B01J7/02 , B01J23/755 , B01J21/04 , B01J35/04 , C01B3/40 , B01J23/745 , B01J35/00
CPC分类号： B01J7/02 , B01J8/062 , B01J19/30 , B01J21/04 , B01J23/745 , B01J23/755 , B01J35/0006 , B01J35/04 , B01J2208/00513 , B01J2208/00716 , B01J2208/025 , B01J2219/30207 , B01J2219/30223 , B01J2219/30408 , B01J2219/30475 , B01J2219/30491 , C01B3/40 , C01B2203/0233 , C01B2203/1017 , C01B2203/1029 , C01B2203/1058 , C01B2203/1082 , C01B2203/1235 , Y02P20/52
摘要： Steam-hydrocarbon reforming reactor with a reformer tube containing ceramic-supported catalyst pellets and metal foam particles. The ceramic-supported catalyst pellets have a porous support comprising one or more of alumina, calcium aluminate, and magnesium aluminate. The metal foam particles comprise Fe and/or Ni. The ceramic-supported catalyst pellets and metal foam particles may be layered or interspersed.

2. 发明申请

US20170282149A1 REACTOR AND TEMPERATURE CONTROL METHOD THEREOF 审中-公开
公开(公告)号：US20170282149A1
公开(公告)日：2017-10-05
申请号：US15345175
申请日：2016-11-07
申请人： National Tsing Hua University
发明人： Fan-Gang Tseng , Chun Liu
IPC分类号： B01J19/24 , C01B17/00 , B01J19/00 , C01B3/40 , B01J7/02 , B01J7/00
CPC分类号： B01J19/245 , B01J7/00 , B01J7/02 , B01J19/0013 , B01J19/249 , B01J2219/00063 , B01J2219/00159 , B01J2219/24 , C01B3/326 , C01B3/40 , C01B17/00 , C01B2203/0233 , C01B2203/0261 , C01B2203/0883 , C01B2203/1011 , C01B2203/1029 , C01B2203/1076 , C01B2203/1223 , C01B2203/1247 , C01B2203/143 , C01B2203/1614
摘要： A reactor suitable for a reaction containing an exothermic reaction is provided. The reactor includes the following components. A reaction channel has an inlet and an outlet, and has a front-end reaction zone, middle-end reaction zones, and a back-end reaction zone from the inlet to the outlet. A front-end catalyst support and a front-end catalyst are located in the front-end reaction zone, a middle-end catalyst support and a middle-end catalyst are respectively located in the middle-end reaction zones, and a back-end catalyst support and a back-end catalyst are located in the back-end reaction zone. The concentration of the front-end catalyst is less than the concentration of the back-end catalyst, and the concentration of the middle-end catalyst is decided via a computer simulation of reaction parameters. The reaction parameters include size and geometric shape of the reaction channel.

3. 发明授权

US08747769B2 Catalytic reactor including a cell-like structure and elements optimizing the contact thereof with the inner wall of the reactor 有权
标题翻译：催化反应器包括细胞状结构和优化其与反应器内壁的接触的元件
公开(公告)号：US08747769B2
公开(公告)日：2014-06-10
申请号：US13513346
申请日：2010-11-24
申请人： Pascal Del-Gallo , Daniel Gary , Aude Cuni , Mathieu Cornillac
发明人： Pascal Del-Gallo , Daniel Gary , Aude Cuni , Mathieu Cornillac
IPC分类号： B01J7/00 , C01B3/40
CPC分类号： B01J19/2485 , B01J12/007 , B01J15/005 , B01J19/2495 , B01J35/04 , C01B3/16 , C01B3/40 , C01B2203/0233 , C01B2203/0238 , C01B2203/0244 , C01B2203/0261 , C01B2203/1011 , C01B2203/1029 , C01B2203/1058 , C01B2203/1241 , Y02P20/142 , Y02P20/52
摘要： The invention relates to a catalytic reactor including: a reaction chamber; at least one catalytic structure made up of at least one catalytic cell-like architecture having outer dimensions at most 10% smaller than the inner dimensions of the reaction chamber; an annular space between the inner wall of the reaction chamber and the cell-like architectures; and at least one second structure positioned in the annular space, selected from among: a) a fibrous structure, or b) a structure including at least one metal collar clasping at least one portion of the cell-like architectures and supporting metal fins.
摘要翻译：本发明涉及一种催化反应器，包括：反应室; 至少一个由至少一个催化细胞样结构组成的催化结构，外部尺寸至少比反应室的内部尺寸小10％; 在反应室的内壁和电池状结构之间的环形空间; 以及定位在所述环形空间中的至少一个第二结构，其选自以下部分：a）纤维结构，或b）包括至少一个金属套环的结构，所述至少一个金属套环夹住所述电池状结构的至少一部分和支撑金属翅片。

4. 发明授权

US08349289B2 Reactive flash volatilization of fluid fuels 有权
标题翻译：流体燃料的反应性闪蒸挥发
公开(公告)号：US08349289B2
公开(公告)日：2013-01-08
申请号：US12043030
申请日：2008-03-05
申请人： Lanny D. Schmidt , Paul J. Dauenhauer , Bradon J. Dreyer , James R. Salge
发明人： Lanny D. Schmidt , Paul J. Dauenhauer , Bradon J. Dreyer , James R. Salge
IPC分类号： C01B3/24
CPC分类号： C01B3/342 , B01J23/42 , B01J23/63 , B01J35/04 , B01J37/0201 , B01J37/0242 , C01B3/26 , C01B3/326 , C01B3/382 , C01B3/386 , C01B3/40 , C01B2203/0244 , C01B2203/0261 , C01B2203/0277 , C01B2203/06 , C01B2203/061 , C01B2203/062 , C01B2203/0861 , C01B2203/1005 , C01B2203/1023 , C01B2203/1029 , C01B2203/1041 , C01B2203/1047 , C01B2203/1058 , C01B2203/1064 , C01B2203/107 , C01B2203/1076 , C01B2203/1082 , C01B2203/1217 , C01B2203/1235 , C01B2203/1288 , C01B2203/1619 , Y02P20/52
摘要： The invention provides methods for the production of synthesis gas. More particularly, various embodiments of the invention relate to systems and methods for volatilizing fluid fuel to produce synthesis gas by using a metal catalyst on a solid support matrix.
摘要翻译：本发明提供了生产合成气的方法。更具体地，本发明的各种实施方案涉及通过在固体载体基质上使用金属催化剂来挥发流体燃料以产生合成气的系统和方法。

5. 发明申请

US20120235096A1 Catalytic Reactor Including a Cell-Like Structure and Elements Optimizing the Contact Thereof with the Inner Wall of the Reactor 有权
标题翻译：催化反应器包括细胞样结构和元件优化与反应器内壁的接触
公开(公告)号：US20120235096A1
公开(公告)日：2012-09-20
申请号：US13513346
申请日：2010-11-24
申请人： Pascal Del-Gallo , Daniel Gary , Aude Cuni , Mathieu Cornillac
发明人： Pascal Del-Gallo , Daniel Gary , Aude Cuni , Mathieu Cornillac
IPC分类号： B01J7/00 , C01B3/40
CPC分类号： B01J19/2485 , B01J12/007 , B01J15/005 , B01J19/2495 , B01J35/04 , C01B3/16 , C01B3/40 , C01B2203/0233 , C01B2203/0238 , C01B2203/0244 , C01B2203/0261 , C01B2203/1011 , C01B2203/1029 , C01B2203/1058 , C01B2203/1241 , Y02P20/142 , Y02P20/52
摘要： The invention relates to a catalytic reactor including: a reaction chamber; at least one catalytic structure made up of at least one catalytic cell-like architecture having outer dimensions at most 10% smaller than the inner dimensions of the reaction chamber; an annular space between the inner wall of the reaction chamber and the cell-like architectures; and at least one second structure positioned in the annular space, selected from among: a) a fibrous structure, or b) a structure including at least one metal collar clasping at least one portion of the cell-like architectures and supporting metal fins.
摘要翻译：本发明涉及一种催化反应器，包括：反应室; 至少一个由至少一个催化细胞样结构组成的催化结构，外部尺寸至少比反应室的内部尺寸小10％; 在反应室的内壁和电池状结构之间的环形空间; 以及定位在所述环形空间中的至少一个第二结构，其选自以下部分：a）纤维结构，或b）包括至少一个金属套环的结构，所述至少一个金属套环夹住所述电池状结构的至少一部分和支撑金属翅片。

6. 发明申请

US20100294994A1 PROCESS FOR THE PRODUCTION OF SYNTHESIS GAS AND HYDROGEN STARTING FROM LIQUID OR GASEOUS HYDROCARBONS 审中-公开
标题翻译：生产合成气和从液体或气体烃开始氢化的方法
公开(公告)号：US20100294994A1
公开(公告)日：2010-11-25
申请号：US12743482
申请日：2008-11-17
申请人： Luca Basini , Alessandra Guarinoni , Andrea Lainati
发明人： Luca Basini , Alessandra Guarinoni , Andrea Lainati
IPC分类号： C01B3/38 , B01J19/00
CPC分类号： C01B3/386 , B01J4/002 , B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J2208/00495 , B01J2219/185 , B01J2219/1946 , C01B3/48 , C01B2203/0233 , C01B2203/0238 , C01B2203/0261 , C01B2203/0283 , C01B2203/085 , C01B2203/0872 , C01B2203/1023 , C01B2203/1029 , C01B2203/1035 , C01B2203/1047 , C01B2203/1052 , C01B2203/1058 , C01B2203/1064 , C01B2203/107 , C01B2203/1247 , C01B2203/1252 , C01B2203/1276 , C01B2203/1288 , C01B2203/143 , C01B2203/82 , Y02P20/142
摘要： A process is described for producing synthesis gas and hydrogen starting from liquid hydrocarbon feedstocks, possibly also mixed with gaseous hydrocarbon streams, comprising at least the following operations: 1) nebulizing/vaporizing a stream of a liquid hydrocarbon feedstock consisting of one or more of the following hydrocarbons: naphthas, various kinds of gas oils, such as LCO, HCO and VGO, other products of refining cycles and oil up-grading, such as DAO, other heavy residues, at a N temperature ranging from 50 to 500° C. and a pressure of 2 to 50 atm, the nebulization also being effected with the help of a gaseous propellant, possibly with the addition of CO2, selected from vapour and/or a gaseous hydrocarbon and resulting in the formation of a nebulized/vaporized liquid hydrocarbon stream; 2) mixing the nebulized/vaporized liquid hydrocarbon stream coming from phase 1) with: a) an oxidizing stream, possibly mixed with vapour, b) possibly a gaseous hydrocarbon stream at a temperature ranging from 50 to 500° C. and a pressure of 2 to 50 atm, with the formation of a possibly biphasic liquid-gas reaction mixture; 3) passing the reaction mixture coming from phase 2) through at least a first structured catalytic bed with the formation of a mixture of reaction products comprising H2 and CO, said structured catalytic bed comprising a catalytic partial oxidation catalyst, arranged on one or more layers, the reaction mixture flowing through each of the layers with a contact time varying from 0.01 to 100 ms, preferably from 0.1 to 10 ms; 4) cooling the mixture of reaction products coming from phase 3). The relative equipment for effecting said process is also described.
摘要翻译：描述了从液态烃原料开始生产合成气和氢气的方法，其可能还与气态烃流混合，所述方法至少包括以下操作：1）将由一种或多种以下碳氢化合物：石脑油，各种瓦斯油，如LCO，HCO和VGO，其他产品的精炼循环和油上调，如DAO，其他重残渣，N温度范围为50-500℃。并且压力为2至50大气压，雾化还通过气体推进剂的帮助进行，可能加入选自蒸气和/或气态烃的CO 2，并导致形成雾化/蒸发的液体烃流; 2）将来自相1）的雾化/蒸发的液体烃流与以下物质混合：a）氧化物流，可能与蒸气混合，b）可能的气态烃物流，温度范围为50-500℃， 2至50个大气压，形成可能的双相液气反应混合物; 3）使来自相2）的反应混合物通过至少第一结构化催化床，形成包含H 2和CO的反应产物的混合物，所述结构化催化床包含催化部分氧化催化剂，其被布置在一层或多层上反应混合物以0.01至100ms，优选0.1至10ms的接触时间流过各层; 4）冷却来自相3）的反应产物的混合物。还描述了用于实现所述过程的相关设备。

7. 发明授权

US07527661B2 Compact devices for generating pure hydrogen 有权
标题翻译：用于产生纯氢的紧凑型装置
公开(公告)号：US07527661B2
公开(公告)日：2009-05-05
申请号：US11109186
申请日：2005-04-18
申请人： Anand Chellappa , Thomas R. Vencill , Michael Roy Powell , Ned A. Godshall
发明人： Anand Chellappa , Thomas R. Vencill , Michael Roy Powell , Ned A. Godshall
IPC分类号： C01B3/36 , C01B3/24 , C10J3/46 , C10J3/54 , B01J7/00 , B01J19/00 , H01M8/06 , B28D7/00
CPC分类号： C01B3/505 , B01J19/0093 , B01J19/249 , B01J35/04 , B01J37/0225 , B01J2219/00783 , B01J2219/00822 , B01J2219/00824 , B01J2219/00835 , B01J2219/00873 , B01J2219/00907 , B01J2219/2453 , B01J2219/2458 , B01J2219/246 , B01J2219/2462 , B01J2219/2466 , B01J2219/2467 , B01J2219/2475 , B01J2219/2479 , B01J2219/2486 , B01J2219/2497 , C01B3/047 , C01B3/323 , C01B3/384 , C01B2203/0233 , C01B2203/041 , C01B2203/0445 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/1029 , C01B2203/1082 , C01B2203/1217 , C01B2203/1247 , C01B2203/1288 , Y02E60/364 , Y02P20/128 , Y02P20/52 , Y10T428/31678
摘要： A hydrogen generator comprising a hydrogen membrane reactor, a fuel supply, a reaction fuel supply line, an air supply, an air supply line, a combustion fuel supply line, a tail gas supply line, a combustion by-product line for transporting combustion by-products from the combustion chamber, and a reaction product line. A membrane assembly to be joined to a reactor chamber of a hydrogen generator, which comprises a membrane; and a membrane support comprising a sintered porous metal. A reactor assembly comprising a reaction chamber containing a porous metal substrate, two membrane assemblies, a fuel supply, a reaction fuel supply line, and a tail gas supply line and a reaction product line. Methods associated with the hydrogen generator, membrane assembly and reactor assembly.
摘要翻译：一种氢发生器，包括氢膜反应器，燃料供应，反应燃料供应管线，空气供应源，供气管线，燃烧燃料供应管线，尾气供应管线，用于运输燃烧的燃烧副产物线 - 来自燃烧室的产物和反应产物线。一种膜组件，其连接到氢生成器的反应室，该氢气发生器包括膜; 以及包含烧结多孔金属的膜支撑体。一种反应器组件，包括含有多孔金属基底的反应室，两个膜组件，燃料供应管线，反应燃料供应管线和尾气供应管线以及反应产物线。与氢发生器，膜组件和反应器组件相关的方法。

8. 发明申请

US20090035192A1 Catalytic EGR oxidizer for IC engines and gas turbines 有权
标题翻译：用于IC发动机和燃气轮机的催化EGR氧化器
公开(公告)号：US20090035192A1
公开(公告)日：2009-02-05
申请号：US12217058
申请日：2008-07-01
申请人： Herng Shinn Hwang
发明人： Herng Shinn Hwang
IPC分类号： B01D53/46 , B01D53/86 , C01B3/26 , C01B31/18 , B01D53/62
CPC分类号： B01D53/90 , B01D53/9409 , B01D53/944 , B01D2251/202 , B01D2251/204 , B01D2255/1021 , B01D2258/012 , C01B3/326 , C01B3/382 , C01B3/386 , C01B3/40 , C01B3/48 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/06 , C01B2203/085 , C01B2203/0861 , C01B2203/1005 , C01B2203/1011 , C01B2203/1023 , C01B2203/1029 , C01B2203/1041 , C01B2203/1047 , C01B2203/1052 , C01B2203/1058 , C01B2203/1064 , C01B2203/107 , C01B2203/1076 , C01B2203/1082 , C01B2203/1211 , C01B2203/1217 , C01B2203/1235 , C01B2203/1241 , C01B2203/1247 , C01B2203/84 , F01N3/0253 , F01N3/0814 , F01N3/0842 , F01N2240/30 , F02M26/36 , Y02P20/128 , Y02P20/52
摘要： By using catalytic partial oxidation or autothermal reforming process, a catalytic oxidizer installed in the engine's Exhaust Gas Recycle (EGR) line can be used to produce from fossil fuels or bio-fuels a reformate gas containing H2 and CO for an IC engine or a gas turbine. Thus, a system consisting of an EGR Oxidizer and an IC engine/gas turbine can be used by itself as a driving device, or can be combined with an electric generator and a battery bank to produce, store and transmit electricity to be used in stationary or mobile power generation, transportation and utility etc.The Oxidizer can also be used to provide reducing gases to regenerate the NOx or diesel particulate traps, so that the traps can continuously be used for reducing emissions from IC engine, diesel truck, gas turbine, power plant etc.
摘要翻译：通过使用催化部分氧化或自热重整方法，安装在发动机废气回收（EGR）管线中的催化氧化剂可用于从化石燃料或生物燃料生产含有用于IC发动机或气体的H 2和CO的重整气体涡轮。因此，由EGR氧化器和IC发动机/燃气轮机组成的系统本身可以被用作驱动装置，或者可以与发电机和电池组组合以产生，存储和传输待使用的电力或移动发电，运输和公用事业等。氧化剂还可用于提供还原气体以再生NOx或柴油颗粒捕集器，使得捕集阱可以连续地用于减少IC发动机，柴油卡车，燃气轮机，发电厂等

9. 发明申请

US20080289180A1 FUEL PROCESSOR FOR USE IN A FUEL CELL SYSTEM 审中-公开
标题翻译：用于燃料电池系统的燃料处理器
公开(公告)号：US20080289180A1
公开(公告)日：2008-11-27
申请号：US12186433
申请日：2008-08-05
申请人： Jennifer BRANTLEY , Kenneth NEWELL , David SOPCHAK , Ian W. KAYE , Jesse THOMPSON , Arpad SOMOGYVARI
发明人： Jennifer BRANTLEY , Kenneth NEWELL , David SOPCHAK , Ian W. KAYE , Jesse THOMPSON , Arpad SOMOGYVARI
IPC分类号： B21D51/16 , H01M8/00
CPC分类号： H01M8/04022 , B01J8/0449 , B01J8/0484 , B01J8/0492 , B01J8/0496 , B01J8/06 , B01J8/065 , B01J8/067 , B01J19/0093 , B01J19/2495 , B01J2208/00309 , B01J2208/00504 , B01J2208/0053 , B01J2208/00672 , B01J2219/00788 , B01J2219/00835 , B01J2219/00846 , B01J2219/0086 , B01J2219/00869 , B01J2219/00873 , B01J2219/00891 , C01B3/323 , C01B2203/0233 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/1017 , C01B2203/1023 , C01B2203/1029 , C01B2203/1064 , C01B2203/1076 , C01B2203/1223 , C01B2203/1288 , C01B2203/1614 , H01M8/0631 , Y02P20/128 , Y02P70/56 , Y10T29/49345
摘要： A method for manufacturing a fuel processor may comprise coupling a plurality of micro-tubes in parallel to form a flow field tube array, each of the plurality of micro-tubes designed to receive a fluid flow, depositing a catalyst layer inside each of the plurality of micro-tubes, and attaching at least one burner to a first end of the flow field tube array.
摘要翻译：一种用于制造燃料处理器的方法可以包括并联耦合多个微管以形成流场管阵列，多个微管中的每一个被设计成接收流体流，在多个微管之内沉积催化剂层的微管，并且将至少一个燃烧器附接到流场管阵列的第一端。

10. 发明申请

US20080010993A1 REFORMED ALCOHOL POWER SYSTEMS 有权
标题翻译：改造酒精电力系统
公开(公告)号：US20080010993A1
公开(公告)日：2008-01-17
申请号：US11762623
申请日：2007-06-13
申请人： David Morgenstern
发明人： David Morgenstern
IPC分类号： F02M35/10
CPC分类号： F02M27/02 , C01B3/323 , C01B3/326 , C01B3/384 , C01B3/48 , C01B2203/0227 , C01B2203/1029 , C01B2203/1217 , C01B2203/1229 , C01B2203/1235 , F02M25/12 , Y02P20/52 , Y02T10/121
摘要： Improved alcohol reforming processes and reformed alcohol power systems utilizing those processes are disclosed. In preferred embodiments, the alcohol reforming processes utilize a thermally conductive reforming catalyst that allows efficient, low-temperature reforming of an alcohol fuel to produce a reformate gas mixture comprising hydrogen. The present invention makes possible the efficient utilization of alcohol fuels in an internal combustion engine to generate electrical or mechanical power such as in vehicular applications.
摘要翻译：公开了改进的酒精重整方法和利用这些方法改造的酒精功率系统。在优选的实施方案中，醇重整方法利用导热重整催化剂，其允许醇燃料的有效的低温重整以产生包含氢的重整气体混合物。本发明使得内燃机中的醇燃料的有效利用成为可能，例如在车辆应用中产生电力或机械动力。

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