公开(公告)号：US08293195B2

公开(公告)日：2012-10-23

申请号：US13483248

申请日：2012-05-30

Applicant: Kenneth L. Blanchard ,  David P. Mann

Inventor： Kenneth L. Blanchard ,  David P. Mann

IPC: B01J8/00 ,  B01J8/02 ,  C01B31/20

CPC classification number: B01J20/28052 ,  B01J8/0085 ,  B01J8/0411 ,  B01J8/0415 ,  B01J8/0453 ,  B01J8/0492 ,  B01J2208/00539 ,  B01J2208/00557 ,  B01J2208/00849 ,  B01J2208/00884 ,  B01J2208/00938 ,  B01J2208/025 ,  B01J2219/00024 ,  B01J2220/56 ,  C01B32/50 ,  Y10T29/49352 ,  Y10T29/49716

Abstract: Systems and methods for contacting a liquid, gas, and/or a multi-phase mixture with particulate solids. The system can include a body having a first head and a second head disposed thereon. Two or more discrete fixed beds can be disposed across a cross-section of the body. One or more unobstructed fluid flow paths can bypass each fixed bed, and one or more baffles can be disposed between the fixed beds.

Abstract translation: 用于使液体，气体和/或多相混合物与颗粒状固体接触的系统和方法。 该系统可以包括具有设置在其上的第一头部和第二头部的主体。 两个或更多个离散的固定床可以跨越身体的横截面布置。 一个或多个无障碍流体流动路径可以绕过每个固定床，并且一个或多个挡板可以设置在固定床之间。

公开(公告)号：US20120245365A1

公开(公告)日：2012-09-27

申请号：US13496967

申请日：2010-09-08

Applicant: Hans-Jörg Wölk ,  Gerhard Mestl

Inventor： Hans-Jörg Wölk ,  Gerhard Mestl

IPC: B01J27/198 ,  B01J19/00 ,  B01J21/06 ,  C07D307/89 ,  B01J37/02

CPC classification number: B01J8/04 ,  B01J21/063 ,  B01J23/22 ,  B01J35/1014 ,  B01J37/08 ,  B01J2208/025 ,  C07C51/265 ,  C07C63/16

Abstract: A method for producing phthalic anhydride by catalytic gas-phase oxidation of o-xylene and/or naphthalene, carried out by means of a catalyst arrangement which has a first catalyst layer at the gas inlet side and at least one second catalyst layer after the first catalyst layer in the gas flow direction with different catalytic activity, wherein when the gas-phase oxidation is being carried out a lower maximum temperature is formed in the first catalyst layer than in the second catalyst layer. Furthermore, a method for producing the catalyst arrangement, as well as the catalyst arrangement itself.

Abstract translation: 一种通过邻二甲苯和/或萘的催化气相氧化生产邻苯二甲酸酐的方法，其通过催化剂装置进行，催化剂装置在气体入口侧具有第一催化剂层，在第一催化剂层之后具有至少一个第二催化剂层 催化剂层在气体流动方向上具有不同的催化活性，其中当进行气相氧化时，在第一催化剂层中形成比在第二催化剂层中更低的最高温度。 此外，催化剂装置的制造方法以及催化剂装置本身。

公开(公告)号：US08133445B2

公开(公告)日：2012-03-13

申请号：US12573376

申请日：2009-10-05

Applicant: Christophe Boyer ,  Fabrice Giroudiere

Inventor： Christophe Boyer ,  Fabrice Giroudiere

IPC: B01J8/02 ,  B01J35/02 ,  B01J19/00 ,  F28D7/00 ,  C01B3/02

CPC classification number: B01J8/0257 ,  B01J8/0278 ,  B01J8/0285 ,  B01J8/0292 ,  B01J8/067 ,  B01J2208/00203 ,  B01J2208/00495 ,  B01J2208/00504 ,  B01J2208/0053 ,  B01J2208/00769 ,  B01J2208/00849 ,  B01J2208/025 ,  C01B3/323 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/0822 ,  C01B2203/1229 ,  F28F13/08 ,  Y02P20/128 ,  Y02P20/52

Abstract: This invention relates to a chamber in which a chemical reaction is carried out in the presence of catalyst and reagents, comprising at least one catalytic tube (10) into which is placed an internal tube (12) for evacuating the gas that is produced, means for introducing reagents (15) and means for introducing the catalyst (16) that are located in the upper portion of the chamber (1), means for heating the catalytic tube (10) that are arranged in the lower portion of the chamber (1), and in which the catalytic tube (10) comprises, in its upper portion above the catalyst (13), means that promote heat exchange between the reagents and the gas that is produced. The invention also relates to the process that uses this chamber.

Abstract translation: 本发明涉及一种在催化剂和试剂的存在下进行化学反应的室，包括至少一个催化管（10），其中放置有用于抽空所产生气体的内管（12） 用于引入试剂（15）和用于引入位于室（1）上部的催化剂（16）的装置，用于加热设置在室（1）的下部的催化剂管（10）的装置 ），并且其中催化管（10）在其上部在催化剂（13）上方包括促进试剂和所产生气体之间的热交换的装置。 本发明还涉及使用该室的方法。

公开(公告)号：US20120040261A1

公开(公告)日：2012-02-16

申请号：US13255381

申请日：2010-03-11

Applicant: Haruyuki Nakanishi ,  Hidekazu Arikawa ,  Susumu Hikazudani ,  Chikashi Inazumi ,  Sadao Araki ,  Takuma Mori

Inventor： Haruyuki Nakanishi ,  Hidekazu Arikawa ,  Susumu Hikazudani ,  Chikashi Inazumi ,  Sadao Araki ,  Takuma Mori

IPC: H01M8/06 ,  B01J7/00 ,  C01B3/04 ,  F02B43/10

CPC classification number: C01B3/047 ,  B01J8/0221 ,  B01J8/0438 ,  B01J21/04 ,  B01J23/42 ,  B01J23/44 ,  B01J23/462 ,  B01J23/745 ,  B01J23/755 ,  B01J35/023 ,  B01J2208/00061 ,  B01J2208/00274 ,  B01J2208/025 ,  C01B2203/06 ,  C01B2203/066 ,  C01B2203/1041 ,  C01B2203/1047 ,  C01B2203/1052 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/107 ,  Y02E60/364

Abstract: A hydrogen generating apparatus for effectively generating hydrogen from ammonia and relates to the hydrogen generating apparatus for generating hydrogen from ammonia. The apparatus comprises an ammonia oxidation part having ammonia oxidation catalysts which oxidizes ammonia, and an ammonia decomposition part having an ammonia decomposition catalyst which decomposes ammonia to generate nitrogen and hydrogen. The decomposition part is located downstream of the oxidation part in a direction of feed gas flow. The oxidation catalyst contains both a noble metal catalyst and a base metal catalyst, and a loading concentration of the noble metal catalyst in an upstream portion of the oxidation part is higher than a loading concentration of the noble metal catalyst in a downstream portion of the oxidation part, and/or the decomposition catalyst contains both a noble metal catalyst and a base metal catalyst, and a loading concentration of the noble metal catalyst in a downstream portion of the decomposition part is higher than a loading concentration of the noble metal catalyst in an upstream portion of the decomposition part.

Abstract translation: 一种用于从氨有效地产生氢的氢产生装置，涉及用于从氨产生氢的氢生成装置。 该装置包括具有氧化氨的氨氧化催化剂的氨氧化部分和具有分解氨以产生氮和氢的氨分解催化剂的氨分解部分。 分解部分沿着进料气流的方向位于氧化部分的下游。 氧化催化剂含有贵金属催化剂和贱金属催化剂，氧化部分上游部分的贵金属催化剂的负载浓度高于贵金属催化剂在氧化部分的下游部分的负载浓度 部分和/或分解催化剂含有贵金属催化剂和贱金属催化剂，并且贵金属催化剂在分解部分的下游部分的负载浓度高于贵金属催化剂在负载浓度 分解部分的上游部分。

公开(公告)号：US20110278201A1

公开(公告)日：2011-11-17

申请号：US13116481

申请日：2011-05-26

Applicant: Kevin Kelly ,  James R. Butler

Inventor： Kevin Kelly ,  James R. Butler

IPC: C10G45/04 ,  B01J19/00

CPC classification number: B01J8/025 ,  B01J35/0006 ,  B01J2208/00884 ,  B01J2208/025 ,  C10G45/04 ,  C10G2300/1055 ,  C10G2300/202 ,  C10G2400/04 ,  C10L1/08

Abstract: Methods and systems for diesel formation are described herein. The diesel hydrotreating systems generally include a hydrodesulfurization unit having a catalyst system disposed therein and adapted to contact an input stream with the catalyst system therein to form diesel. The catalyst system generally includes a plurality of catalysts including a first catalyst including a hydrodesulfurization catalyst having a first pore diameter and a second catalyst having a second pore diameter, wherein the second pore diameter is larger than the first pore diameter.

Abstract translation: 本文描述了柴油机形成的方法和系统。 柴油加氢处理系统通常包括加氢脱硫单元，其具有设置在其中的催化剂体系，并且适于将输入流与其中的催化剂体系接触以形成柴油。 催化剂体系通常包括多种催化剂，其包括第一催化剂，其包括具有第一孔径的加氢脱硫催化剂和具有第二孔径的第二催化剂，其中第二孔径大于第一孔径。

公开(公告)号：US20110272123A1

公开(公告)日：2011-11-10

申请号：US13138225

申请日：2009-06-29

Applicant: Thomas Bruce Avis ,  Gregory C. Yust

Inventor： Thomas Bruce Avis ,  Gregory C. Yust

IPC: F28D7/02

CPC classification number: F28D7/106 ,  B01J8/0465 ,  B01J2208/00141 ,  B01J2208/00203 ,  B01J2208/0053 ,  B01J2208/00849 ,  B01J2208/00884 ,  B01J2208/025 ,  C01B3/16 ,  C01B2203/0205 ,  C01B2203/0883 ,  C01B2203/0894 ,  C01B2203/1258 ,  C01B2203/127 ,  C01B2203/82 ,  F28D1/06 ,  F28D7/024 ,  F28F1/36 ,  Y10T29/49826

Abstract: A cylindrical shift converter (4) is disposed within an annular heat exchanger (28, 24) which has an outer wall (5). A plurality of spiral rods (90) create a plurality of spiral gas passages (26a) between the outer wall and a thin shell (92). The outer diameter of the thin shell is at least about 3/16 inch (about 4 mm) less than the inner diameter of an inner wall (20) of an annular hydrodesulfurizer (10), to facilitate inserting the shift converter and heat exchanger into the hydrodesulfurizer to form a unitized assembly (2). The spiral passages open into the hydrodesulfurizer.

Abstract translation: 圆柱形换档转换器（4）设置在具有外壁（5）的环形热交换器（28,24）内。 多个螺旋杆（90）在外壁和薄壳（92）之间产生多个螺旋形气体通道（26a）。 薄壳的外径比环形加氢脱硫剂（10）的内壁（20）的内径小至少约3/16英寸（约4mm），以便于将换档转换器和热交换器插入 该加氢脱硫剂形成一个组合式组件（2）。 螺旋通道通向加氢脱硫剂。

公开(公告)号：US08025846B2

公开(公告)日：2011-09-27

申请号：US12138862

申请日：2008-06-13

Applicant: Ulrich Cremer ,  Hagen Wilmer ,  Andreas Raichle ,  Hermann Petersen ,  Holger Borchert ,  Horst Strahberger ,  Klaus Joachim Mueller-Engel

Inventor： Ulrich Cremer ,  Hagen Wilmer ,  Andreas Raichle ,  Hermann Petersen ,  Holger Borchert ,  Horst Strahberger ,  Klaus Joachim Mueller-Engel

IPC: B01J35/02

CPC classification number: B01J8/0015 ,  B01J8/06 ,  B01J23/002 ,  B01J23/22 ,  B01J35/008 ,  B01J35/026 ,  B01J37/009 ,  B01J37/0221 ,  B01J2208/00752 ,  B01J2208/00769 ,  B01J2208/025 ,  B01J2219/30215 ,  B01J2219/30475 ,  B01J2523/00 ,  B07B1/4618 ,  C07C51/235 ,  C07C51/265 ,  C07C51/313 ,  Y10T29/49345 ,  C07C57/04 ,  C07C63/16 ,  B01J2523/17 ,  B01J2523/55 ,  B01J2523/68 ,  B01J2523/69 ,  B01J2523/15 ,  B01J2523/47 ,  B01J2523/51 ,  B01J2523/53

Abstract: A process for introducing annular coated catalysts K into a reaction tube of a tube bundle reactor, in which adhering pairs of annular coated catalysts K formed in the preparation of the annular coated catalysts K, before the introduction thereof into the reaction tube, are removed at least partly from the annular coated catalysts K.

Abstract translation: 将环状涂覆的催化剂K引入管束反应器的反应管中的过程，其中在将环状涂覆的催化剂K的制备中形成的环状涂覆的催化剂K在其引入反应管之前形成的粘附成对的环状涂覆的催化剂K被除去 最少部分地来自环形涂层催化剂K.

公开(公告)号：US20110217230A1

公开(公告)日：2011-09-08

申请号：US13042762

申请日：2011-03-08

Applicant: Frank Kleine Jäger ,  Julian Prölß

Inventor： Frank Kleine Jäger ,  Julian Prölß

IPC: C01G49/06 ,  B82Y40/00

CPC classification number: B01J8/0438 ,  B01J4/002 ,  B01J8/0449 ,  B01J8/0492 ,  B01J19/2485 ,  B01J2208/00504 ,  B01J2208/0053 ,  B01J2208/00716 ,  B01J2208/025 ,  B01J2219/00006 ,  B01J2219/00265 ,  B82Y30/00 ,  C01G1/02 ,  C01G49/06 ,  C01P2004/64 ,  F23C13/00 ,  F23C99/006 ,  F23C2900/03001 ,  F23D91/02 ,  F23D2900/21007

Abstract: The invention relates to a process for producing nanoparticulate solids by means of a Péclet number-stabilized gas-phase reaction.

Abstract translation: 本发明涉及通过Péclet数稳定气相反应生产纳米颗粒固体的方法。

公开(公告)号：US08002856B2

公开(公告)日：2011-08-23

申请号：US12087922

申请日：2006-12-20

Applicant: Vaughan Clifford Williams

Inventor： Vaughan Clifford Williams

IPC: C01B3/38 ,  C07C4/02 ,  C07C4/06

CPC classification number: B01J19/2485 ,  B01J8/0085 ,  B01J8/009 ,  B01J19/24 ,  B01J19/30 ,  B01J23/825 ,  B01J23/835 ,  B01J23/8926 ,  B01J35/04 ,  B01J2208/00362 ,  B01J2208/00557 ,  B01J2208/00814 ,  B01J2208/00849 ,  B01J2208/00884 ,  B01J2208/021 ,  B01J2208/025 ,  B01J2219/00123 ,  B01J2219/00166 ,  B01J2219/192 ,  B01J2219/1928 ,  B01J2219/3023 ,  B01J2219/30234 ,  B01J2219/30246 ,  B01J2219/30249 ,  B01J2219/30416 ,  B01J2219/30475 ,  B01J2219/3085

Abstract: The present invention relates to a process for contacting a hydrocarbon and an oxygen-containing gas with a catalyst bed in a reactor at a space velocity of at least 10,000 h−1, said process being characterised in that a) the reactor has a polygonal internal cross-section at least in the section where the catalyst bed is held, b) the catalyst bed is made up of 2 or more layers of catalyst in the form of tiles of polygonal shape, said tiles have at least 4 sides, c) each layer of catalyst comprises at least 4 tiles which tessellate together to form said layer, and d) the edges where 2 tiles meet in one layer do not align with the edges where 2 tiles meet in an adjacent layer.

Abstract translation: 本发明涉及使烃和含氧气体与催化剂床在反应器中以至少10,000h -1的空间速度接触的方法，所述方法的特征在于：a）反应器具有多边形内部 至少在催化剂床保持部分的截面，b）催化剂床由多层形状的瓷砖形式的2层或更多层催化剂组成，所述砖具有至少4个侧面，c）每个 催化剂层包括至少4块镶嵌在一起以形成所述层的瓦片，以及d）2瓦片在一层中相遇的边缘不与2瓦片在相邻层中相遇的边缘对准。

公开(公告)号：US20110200515A1

公开(公告)日：2011-08-18

申请号：US13124968

申请日：2009-09-17

Applicant: Stephen Philip Roe

Inventor： Stephen Philip Roe

IPC: C01B21/22 ,  B01J8/02 ,  B01J8/00 ,  B23P23/00

CPC classification number: B01J19/2495 ,  B01D53/8631 ,  B01D53/8634 ,  B01D2251/11 ,  B01D2251/208 ,  B01D2255/1021 ,  B01D2255/1023 ,  B01D2255/1025 ,  B01D2255/1026 ,  B01D2255/1028 ,  B01D2255/104 ,  B01D2255/106 ,  B01D2255/2025 ,  B01D2255/2045 ,  B01D2255/2047 ,  B01D2255/206 ,  B01D2255/2073 ,  B01D2255/20738 ,  B01D2255/20746 ,  B01D2255/20753 ,  B01D2255/20761 ,  B01D2255/2092 ,  B01D2255/30 ,  B01D2255/402 ,  B01D2255/405 ,  B01D2255/904 ,  B01D2255/9202 ,  B01D2257/402 ,  B01D2257/406 ,  B01J8/0214 ,  B01J23/40 ,  B01J23/464 ,  B01J23/74 ,  B01J35/0006 ,  B01J35/04 ,  B01J2208/00849 ,  B01J2208/00884 ,  B01J2208/025 ,  B01J2219/00024 ,  C01B21/265 ,  C01B21/28 ,  C01C3/0216 ,  C01C3/022 ,  Y02C20/10 ,  Y02P20/153 ,  Y10T29/49716

Abstract: A catalyst containment unit includes two concentric perforate members defining an annular space in which a particulate catalyst may be placed, and process fluid-impermeable end members mounted on the ends of the perforate members, wherein one end member extends across the unit to provide a closed end and the other end member closes the annular space thereby providing an open end through which gases may enter or exit the unit, and suspending means attached to one or both end members for securing the unit within an ammonia oxidation vessel. The unit may be suspended, for example, below a precious metal ammonia oxidation gauze pack and may contain a particulate ammonia oxidation catalyst or nitrous oxide abatement catalyst. A catalyst combination includes a precious metal ammonia oxidation catalyst gauze on a supporting framework and a particulate catalyst disposed in a catalyst containment unit.

Abstract translation: 催化剂容纳单元包括两个同心的穿孔构件，其限定可以放置颗粒催化剂的环形空间，以及安装在穿孔构件的端部上的处理流体不可渗透的端部构件，其中一个端构件延伸穿过该单元以提供闭合 并且另一端构件封闭环形空间，从而提供气体可以进入或离开单元的开口端，以及附接到一个或两个端部构件的悬挂装置，用于将单元固定在氨氧化容器内。 该单元可以例如悬浮在贵金属氨氧化纱布包下方，并且可以含有颗粒状氨氧化催化剂或一氧化二氮消除催化剂。 催化剂组合包括在支撑骨架上的贵金属氨氧化催化剂纱布和设置在催化剂容纳单元中的颗粒催化剂。