公开(公告)号：US20060292059A1

公开(公告)日：2006-12-28

申请号：US11414936

申请日：2006-05-01

Applicant: Felice DiMascio

Inventor： Felice DiMascio

IPC: B01J29/00 ,  B01J29/18 ,  B01J29/08 ,  B01J21/16 ,  B01J21/18 ,  B01J27/128 ,  B01J31/00 ,  B01J27/24 ,  B01J27/138 ,  B01J27/06

CPC classification number: C01B11/024 ,  B01J8/009 ,  B01J8/0214 ,  B01J8/0221 ,  B01J8/025 ,  B01J8/0257 ,  B01J10/007 ,  B01J12/007 ,  B01J14/005 ,  B01J15/005 ,  B01J16/005 ,  B01J19/2475 ,  B01J19/249 ,  B01J19/2495 ,  B01J19/32 ,  B01J23/34 ,  B01J23/42 ,  B01J35/04 ,  B01J37/0232 ,  B01J2208/0069 ,  B01J2208/00814 ,  B01J2208/00884 ,  B01J2208/022 ,  B01J2208/025 ,  B01J2219/185 ,  B01J2219/1923 ,  B01J2219/2454 ,  B01J2219/2459 ,  B01J2219/2479 ,  B01J2219/2481 ,  B01J2219/249 ,  B01J2219/3221 ,  B01J2219/32227 ,  B01J2219/32466 ,  B01J2219/32483 ,  B01J2219/32491

Abstract: A catalyst element includes a porous housing; a filter core disposed within the housing; and a filler material comprising a catalyst particle, a redox particle, an oxidizing particle, or a combination comprising at least one of the foregoing particles, wherein the filler material is disposed within the housing; wherein the catalyst element comprises a plurality of tortuous flow paths, through which a reactive mixture may flow and contact at least a portion of each of the housing, filter core, and filler material. The catalyst element may be useful in a variety of chemical processes including hydrogenation, dehydrogenation, hydrogenolysis, oxidation, reduction, alkylation, dealkylation, carbonylation, decarbonylation, coupling, isomerization, amination, deamination, or hydrodehalogenation.

Abstract translation: 催化剂元件包括多孔壳体; 设置在所述壳体内的过滤芯; 以及填充材料，其包含催化剂颗粒，氧化还原颗粒，氧化颗粒或包含至少一种上述颗粒的组合，其中所述填充材料设置在所述壳体内; 其中所述催化剂元件包括多个曲折的流动路径，反应性混合物可以流过并接触所述壳体，过滤芯和填充材料中的每一个的至少一部分。 催化剂元件可用于各种化学方法，包括氢化，脱氢，氢解，氧化，还原，烷基化，脱烷基化，羰基化，脱羰基，偶联，异构化，胺化，脱氨基或加氢脱卤。

公开(公告)号：US20060269468A1

公开(公告)日：2006-11-30

申请号：US11202156

申请日：2005-08-11

Applicant: Sang-Moon Chung ,  Heon Ham

Inventor： Sang-Moon Chung ,  Heon Ham

IPC: D01F9/12 ,  B01J19/00

CPC classification number: B01J19/0013 ,  B01J15/005 ,  B01J2219/00038 ,  B82Y30/00 ,  B82Y40/00 ,  C01B32/162 ,  C01B2202/02 ,  C01B2202/04 ,  C01B2202/06 ,  D01F9/127 ,  D01F9/133

Abstract: The present invention relates to an apparatus and method for mass production of carbon nanotubes. More specifically, it relates to an apparatus and method for mass production of carbon nanotubes, which are capable of achieving mass synthesis of carbon nanotubes and simultaneous production of various structures of carbon nanotubes, by a manner that a plurality of independent reaction chambers are configured, and a heater supplying temperatures necessary for reaction in the corresponding reaction chambers is configured to have a plurality of reaction temperature sections, such that the heater moves according to reaction steps in the respective reaction chambers under different reaction steps and matches reaction temperature sections to thereby continuously provide proper reaction temperatures to the respective reaction chambers and at the same time, to stably supply and discharge reaction gases and stabilizing gases necessary for the respective reaction steps to and from respective reaction chambers, in order to continuously produce carbon nanotubes.

Abstract translation: 本发明涉及一种大量生产碳纳米管的装置和方法。 更具体地说，本发明涉及碳纳米管的大规模生产的装置和方法，其能够通过构成多个独立的反应室的方式实现碳纳米管的大量合成和同时生产碳纳米管的各种结构， 并且在相应的反应室中提供反应所需温度的加热器被配置成具有多个反应温度部分，使得加热器根据在不同反应步骤下的反应室中的反应步骤移动，并使反应温度部分连续地匹配 为各反应室提供适当的反应温度，同时为了连续生产碳纳米管，稳定地向各反应室供给和排出各反应步骤所必需的反应气体和稳定气体。

公开(公告)号：US07101525B2

公开(公告)日：2006-09-05

申请号：US10343276

申请日：2001-07-27

Applicant: Joseph Steffen

Inventor： Joseph Steffen

IPC: C01C3/02 ,  B01J35/02 ,  B01J32/00 ,  C01B21/26

CPC classification number: B01J35/04 ,  B01J12/007 ,  B01J15/005 ,  B01J19/2485 ,  B01J19/249 ,  B01J23/42 ,  B01J35/06 ,  B01J2219/2459 ,  B01J2219/2462 ,  B01J2219/2481 ,  B01J2219/2498 ,  C01B21/265 ,  C01C3/0216

Abstract: The present invention relates to a catalytic device for the implementation of a reaction in a gaseous medium at high temperature, such as, for example, the synthesis of HCN or the oxidation of ammonia, comprising: at least one textured material (1) which is effective as catalyst for the said reaction, a support (2) comprising at least one ceramic part (3), the structure of which makes possible the passage of the gases, the said part (3) of the said support (2) having a corrugated face (6), so that the increase in surface area (β) produced by the corrugations with respect to a flat surface is at least equal to that (α) calculated for sawtooth corrugations and of between approximately 1.1 and approximately 3, the said textured material (1) being positioned so that it is held against the corrugated face (6) of the said part (3) of the said support (2) and follows the form thereof.

Abstract translation: 本发明涉及用于在高温下实施气态介质中的反应的催化装置，例如HCN的合成或氨的氧化，其包括：至少一种织构材料（1），其是 作为所述反应的催化剂有效的载体（2），包括至少一个陶瓷部分（3）的载体（2），其结构使气体通过成为可能，所述载体（2）的所述部分（3）具有 波纹面（6），使得波纹相对于平坦表面产生的表面积（β）的增加至少等于对于锯齿波纹计算的（α）和约1.1和约3之间的所述（α），所述 纹理材料（1）被定位成使得其被保持抵靠所述支撑件（2）的所述部分（3）的波纹面（6）并且遵循其形式。

公开(公告)号：US20060156627A1

公开(公告)日：2006-07-20

申请号：US11313252

申请日：2005-12-19

Applicant: Jennifer Brantley ,  Ian Kaye ,  Arpad Somogyvari ,  Gerry Tucker ,  Fan Chan

Inventor： Jennifer Brantley ,  Ian Kaye ,  Arpad Somogyvari ,  Gerry Tucker ,  Fan Chan

IPC: B01J7/00

CPC classification number: B01B1/005 ,  B01J8/0285 ,  B01J8/0496 ,  B01J12/007 ,  B01J15/005 ,  B01J19/2485 ,  B01J19/249 ,  B01J19/2495 ,  B01J2208/00203 ,  B01J2208/00309 ,  B01J2208/00504 ,  B01J2208/0053 ,  B01J2208/00672 ,  B01J2208/00716 ,  B01J2219/00157 ,  B01J2219/00159 ,  B01J2219/00783 ,  B01J2219/00788 ,  B01J2219/00804 ,  B01J2219/00822 ,  B01J2219/00824 ,  B01J2219/00828 ,  B01J2219/00835 ,  B01J2219/0086 ,  B01J2219/00862 ,  B01J2219/00869 ,  B01J2219/00871 ,  B01J2219/00873 ,  B01J2219/00997 ,  B01J2219/1923 ,  B01J2219/1943 ,  B01J2219/2453 ,  B01J2219/2458 ,  B01J2219/2459 ,  B01J2219/2462 ,  B01J2219/2465 ,  B01J2219/2479 ,  B01J2219/2481 ,  B01J2219/2485 ,  B01J2219/2493 ,  B01J2219/2497 ,  C01B3/323 ,  C01B3/38 ,  C01B3/382 ,  C01B3/384 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/0816 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0844 ,  C01B2203/085 ,  C01B2203/1223 ,  C01B2203/1229 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/1288 ,  C01B2203/142 ,  C01B2203/169 ,  C01B2203/82 ,  H01M8/04022 ,  H01M8/0618 ,  H01M8/0631 ,  H01M8/0662 ,  H01M2008/1095 ,  Y02P20/128

Abstract: The invention relates to a fuel processor that produces hydrogen from a fuel. The fuel processor comprises a reformer and a heater. The reformer includes a catalyst that facilitates the production of hydrogen from the fuel; the heater provides heat to the reformer. Multipass reformer and heater chambers are described that reduce fuel processor size. Single layer fuel processors include reformer and heater chambers in a compact form factor that is well suited for portable applications. Some fuel processors described herein place an electrically resistive material in contact with a thermally conductive material to heat fuel entering the fuel processor. This is particularly useful during start-up of the fuel processor. Fuel processors described may also include features that facilitate assembly.

Abstract translation: 本发明涉及一种从燃料产生氢的燃料处理器。 燃料处理器包括重整器和加热器。 重整器包括有助于从燃料中产生氢气的催化剂; 加热器向重整器提供热量。 描述了多通道重整器和加热器室，其减少了燃料处理器的尺寸。 单层燃料处理器包括重整器和加热室，结构紧凑，非常适合便携式应用。 本文所述的一些燃料加工器将电阻材料与导热材料接触以加热进入燃料处理器的燃料。 这在燃料处理器启动时特别有用。 所描述的燃料处理器还可以包括便于组装的特征。

公开(公告)号：US20060110301A1

公开(公告)日：2006-05-25

申请号：US10992870

申请日：2004-11-19

Applicant: Larry Lewis ,  Jeff Diaz

Inventor： Larry Lewis ,  Jeff Diaz

IPC: B01J19/00

CPC classification number: B01J15/005 ,  B01D53/8653 ,  B01D2255/20723 ,  B01D2255/20776 ,  B01D2255/50 ,  B01J19/2425 ,  B01J19/2485 ,  B01J19/249 ,  B01J23/22 ,  B01J37/0225 ,  B01J37/0232 ,  B01J37/348 ,  B01J2219/00081 ,  B01J2219/00085 ,  B01J2219/32475 ,  F28D7/08 ,  F28D7/085 ,  F28F1/32 ,  Y02P20/129

Abstract: The invention provides a method and apparatus for integrating the heat transfer zones of plate fin and tube and finned tube exchangers and a catalytic mass transfer zone. The invention also provides a method for in situ regeneration of existing coated surface and augmentation of existing coated surface, or catalyst performance

Abstract translation: 本发明提供了一种用于整合板翅和管翅片翅片管交换器和催化传质区的传热区的方法和装置。 本发明还提供了用于现有涂覆表面的原位再生和现有涂覆表面的增加或催化剂性能的方法

公开(公告)号：US06969411B2

公开(公告)日：2005-11-29

申请号：US10946891

申请日：2004-09-22

Applicant: Roger R. Lesieur

Inventor： Roger R. Lesieur

IPC: B01J12/00 ,  B01J15/00 ,  B01J19/24 ,  B01J23/58 ,  B01J23/755 ,  B01J35/00 ,  B01J35/04 ,  C01B3/32 ,  C01B3/38 ,  C01B3/40 ,  H01M8/04 ,  H01M8/06 ,  B01J8/02

CPC classification number: H01M8/0631 ,  B01J12/007 ,  B01J15/005 ,  B01J19/2485 ,  B01J23/58 ,  B01J23/755 ,  B01J35/0006 ,  B01J35/04 ,  B01J2208/025 ,  B01J2219/00081 ,  B01J2219/00094 ,  C01B3/382 ,  C01B3/40 ,  C01B2203/0244 ,  C01B2203/0283 ,  C01B2203/066 ,  C01B2203/0844 ,  C01B2203/085 ,  C01B2203/0883 ,  C01B2203/1011 ,  C01B2203/1017 ,  C01B2203/1023 ,  C01B2203/1029 ,  C01B2203/1041 ,  C01B2203/1047 ,  C01B2203/1052 ,  C01B2203/1064 ,  C01B2203/1076 ,  C01B2203/1082 ,  C01B2203/1094 ,  C01B2203/1235 ,  C01B2203/1276 ,  C01B2203/142 ,  C01B2203/1604 ,  C01B2203/82 ,  Y02P20/52 ,  Y10S165/395 ,  Y10S165/396 ,  Y10S165/397

Abstract: A fuel gas-steam reformer assembly, preferably an autothermal reformer assembly, for use in a fuel cell power plant, includes a catalyst bed which is formed from a cylindrical monolithic open cell foam body. The foam body is preferably formed from a high temperature material such as stainless steel, nickel alloys and iron-aluminum alloys, or from a ceramic material. The foam body includes open cells or pores which are contained within the metal or ceramic lattice. The lattice is coated with a porous wash coat which serves as a high surface area substrate onto which catalysts used in the reformer are applied. The foam body has an inlet end into which a mixture of fuel, steam and air is fed to begin the reforming process. An inlet portion of the foam body may be provided with an iron oxide and/or noble metal catalyst and the remainder of the foam body may be provided with a nickel and/or noble metal catalyst. An advantage of including an autothermal reformer in a fuel processing system is the compactness of the autothermal reformer. The inclusion of the foam catalyst bed rather than the traditional catalyzed pellet bed allows the reformer to be made even more compact and light weight.

Abstract translation: 用于燃料电池发电厂的燃料气体 - 蒸汽重整器组件，优选自热重整器组件包括由圆柱形整体开放泡沫体形成的催化剂床。 泡沫体优选由诸如不锈钢，镍合金和铁 - 铝合金的高温材料或陶瓷材料形成。 泡沫体包括容纳在金属或陶瓷晶格内的开孔或孔。 该格子涂覆有多孔洗涤涂层，其用作高表面积底物，在其上施加用于重整器中的催化剂。 泡沫体具有入口端，燃料，蒸汽和空气的混合物供入入口端，以开始重整过程。 泡沫体的入口部分可以设置有氧化铁和/或贵金属催化剂，泡沫体的其余部分可以设置有镍和/或贵金属催化剂。 在燃料处理系统中包括自热重整器的优点是自热重整器的紧凑性。 包含泡沫催化剂床而不是传统的催化颗粒床允许重整器更加紧凑和重量轻。

公开(公告)号：US20040141910A1

公开(公告)日：2004-07-22

申请号：US10736212

申请日：2003-12-15

Inventor： Ricardo Blach Vizoso

IPC: C01B017/02

CPC classification number: B01D71/04 ,  B01D53/8612 ,  B01D53/885 ,  B01D71/025 ,  B01J15/005 ,  B01J19/2415 ,  B01J19/2425 ,  B01J19/244 ,  B01J19/2475 ,  B01J35/065 ,  B01J2219/182 ,  C01B3/04 ,  C01B3/501 ,  C01B17/0495 ,  C01B2203/041 ,  C01B2203/0485 ,  Y02E60/364

Abstract: The reactor is comprised of a body, a tubular ceramic porous membrane element placed coaxially inside it to remove the hydrogen, and a catalyst for the thermal breakdown of the hydrogen sulfide into sulfur and hydrogen, wherein said catalyst has been deposited directly on the tubular ceramic porous membrane element in the form of a layer. The reactor is applicable for treating gases containing hydrogen sulfide.

Abstract translation: 该反应器包括一个主体，同轴地放置在其中以去除氢的管状陶瓷多孔膜元件，以及用于将硫化氢热分解成硫和氢的催化剂，其中所述催化剂直接沉积在管状陶瓷上 一层多孔膜元件。 该反应器适用于处理含硫化氢的气体。

公开(公告)号：US06660685B1

公开(公告)日：2003-12-09

申请号：US09509949

申请日：2000-06-06

Applicant: Martin Schüssler ,  Tomas Stefanovski ,  Detlef zur Megede

Inventor： Martin Schüssler ,  Tomas Stefanovski ,  Detlef zur Megede

IPC: B01J2372

CPC classification number: F23C13/08 ,  B01B1/005 ,  B01J12/007 ,  B01J15/005 ,  B01J19/249 ,  B01J35/02 ,  B01J2219/2453 ,  B01J2219/2482 ,  B01J2219/2497 ,  C01B3/16 ,  C01B3/326 ,  C01B3/583 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/107 ,  C01B2203/1082 ,  H01M8/0631 ,  H01M8/0662 ,  Y02P20/52 ,  Y02P70/56

Abstract: To carry out a heterogeneously catalysed reaction, a reaction mixture comprising hydrocarbon and water is fed onto a catalyst that is produced by compressing at least one catalyst powder into a highly compressed layer which forms a shaped body. The reaction mixture is pressed through the catalyst layer with a pressure drop.

Abstract translation: 为了进行非均相催化的反应，将包含烃和水的反应混合物加入到通过将至少一种催化剂粉末压缩成形成成形体的高度压缩层而产生的催化剂上。 将反应混合物通过压力下降通过催化剂层。

公开(公告)号：US06585940B2

公开(公告)日：2003-07-01

申请号：US09339288

申请日：1999-06-24

Applicant: Fumio Abe ,  Naomi Noda ,  Junichi Suzuki

Inventor： Fumio Abe ,  Naomi Noda ,  Junichi Suzuki

IPC: B01J802

CPC classification number: H01M8/0631 ,  B01J15/005 ,  B01J19/2485 ,  B01J2219/00135 ,  B01J2219/182 ,  C01B3/16 ,  C01B3/26 ,  C01B3/323 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/0261 ,  C01B2203/0277 ,  C01B2203/0283 ,  C01B2203/0288 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/085 ,  C01B2203/1023 ,  C01B2203/1041 ,  C01B2203/1047 ,  C01B2203/1082 ,  C01B2203/1094 ,  C01B2203/1205 ,  C01B2203/1223 ,  C01B2203/142 ,  C01B2203/143 ,  C01B2203/146 ,  C01B2203/1604 ,  C01B2203/1661 ,  C01B2203/82 ,  Y02P20/52

Abstract: A reformer is disposed in the flow path of a reactant fluid. The reformer includes an electrically heatable heater unit of honeycomb structure, in the upstream of the flow path of a reactant fluid, and a catalyst unit of honeycomb structure capable of generating hydrogen from a reactant fluid containing an organic compound or carbon monoxide, by catalysis, in the downstream of the above heater unit. The heater unit and catalyst unit satisfy the following relationship: Cell density of the heater unit≦Cell density of the catalyst unit. The reformer improve efficiency for production of hydrogen and reduce CO as the by-product.

Abstract translation: 重整器设置在反应物流体的流路中。 改性器包括在反应物流体的流动路径的上游的蜂窝结构的电加热加热器单元，以及能够通过催化从含有机化合物或一氧化碳的反应物流产生氢的蜂窝结构的催化剂单元， 在上述加热器单元的下游。 加热器单元和催化剂单元满足以下关系：加热器单元的电池密度<=催化剂单元的电池密度。 改造者提高氢的生产效率，并减少作为副产品的CO。

公开(公告)号：US20030077202A1

公开(公告)日：2003-04-24

申请号：US10262512

申请日：2002-09-30

Inventor： Dimitri Furkasov ,  Alexander Kalinnikov ,  Garri Boronov ,  Ricardo Blach Bizoso

IPC: B01J008/00

CPC classification number: B01D53/8671 ,  B01D2257/108 ,  B01J8/0242 ,  B01J15/005 ,  B01J19/0006 ,  B01J19/24 ,  B01J19/2485 ,  B01J35/04 ,  B01J2219/0002 ,  B01J2219/00063 ,  B01J2219/00094 ,  B01J2219/00135 ,  B01J2219/00155 ,  B01J2219/00186 ,  B01J2219/00263 ,  B01J2219/00768 ,  B01J2219/185 ,  B01J2219/32466 ,  G21C9/06 ,  G21C19/317 ,  Y02E30/40

Abstract: The system provides for the monitoring and elimination of hydrogen and combustible gases in the air, with the help of catalysers, being implemented in an apparatus consisting of a passive hydrogen recombiner and a monitoring detector, in which use is made of the free convective feed of a recorded and eliminated gaseous mixture of components, the components having a construction of the same type, it being possible to locate the detector both inside and outside the recombiner.

Abstract translation: 该系统提供了在催化剂的帮助下监测和消除空气中的氢气和可燃气体，该装置在由被动氢气重组器和监测探测器组成的装置中实现，其中使用自由对流进料 记录和消除的组分的气体混合物，组分具有相同类型的结构，可以将检测器定位在重组器内部和外部。