公开(公告)号：US20100094071A1

公开(公告)日：2010-04-15

申请号：US12525830

申请日：2008-01-31

Applicant: Gerhard Olbert ,  Franz Corr ,  Sven Crone

Inventor： Gerhard Olbert ,  Franz Corr ,  Sven Crone

IPC: C07C5/327

CPC classification number: F23C6/045 ,  B01J4/005 ,  C01B3/36 ,  C01B2203/0255 ,  C07C5/48 ,  F23C2900/06041 ,  F23L7/005 ,  Y02E20/344 ,  Y02P20/129 ,  C07C11/06 ,  C07C11/08

Abstract: A method is proposed for providing an oxygen-containing gas stream for the endothermic reaction of an initial stream comprising one or more hydrocarbons, having a predetermined oxygen concentration and a predetermined temperature, wherein a fluid fuel stream is combusted with a primary air stream at λ values of the primary air stream to the fluid fuel stream of from 0.6 to 1.2 to obtain a combustion gas stream, and a secondary air stream is admixed to the combustion gas stream to obtain the oxygen-containing gas stream for the endothermic reaction, with the predetermined oxygen concentration and the predetermined temperature of the oxygen-containing gas stream being adjusted via the flow rate and the temperature of the secondary air stream.

Abstract translation: 提出了一种方法，用于提供含有一种含氧气流，用于包含一种或多种具有预定氧浓度和预定温度的烃的初始流的吸热反应，其中流体燃料流与主空气流以λ 一次空气流到流体燃料流的值为0.6至1.2，以获得燃烧气体流，并且二次空气流与燃烧气体流混合以获得用于吸热反应的含氧气体流，其中 预定的氧浓度和含氧气流的预定温度通过二次气流的流量和温度进行调节。

公开(公告)号：US5785933A

公开(公告)日：1998-07-28

申请号：US779290

申请日：1997-01-21

Applicant: Brian A. Cunningham ,  Saverio G. Greco

Inventor： Brian A. Cunningham ,  Saverio G. Greco

IPC: B01F3/08 ,  B01F5/00

CPC classification number: B01J4/005 ,  B01J14/00 ,  B01J19/006 ,  B01J19/2465 ,  B01J4/004 ,  C10G29/205 ,  B01F5/0062 ,  B01J2219/00006 ,  B01J2219/00182 ,  B01J2219/00765

Abstract: A sulfuric acid-catalyzed alkylation reactor system is provided for alkylating isoparaffins with olefins to produce hydrocarbon alkylates. The reactor vessel has a vertical cylindrical wall, a top, an inverted conical bottom portion, internal perforated baffles and multiple emulsion injection inlet pipes, disposed tangentially to and communicating with the interior of the reactor vessel. The emulsion injection inlet pipes have static mixers incorporated therein and tangential injection of the emulsion imparts a circular motion to the contents of the reactor vessel, resulting in partial phase separation of the reacted products. The reactor vessel communicates with a settling vessel through a transfer pipe having a vertical portion suspended within the central portion of the reactor vessel and a horizontal portion sealably extending through the cylindrical wall of the reactor vessel. The transfer pipe has a first end near the conical bottom portion of the reactor vessel and a second end at a top portion of the settling vessel. The reactor system enables a sulfuric-acid catalyzed reaction of olefins with isoparaffins utilizing static mixing of the reactants, and minimizing leakage of the reactants to the environment.

Abstract translation: 提供硫酸催化的烷基化反应器系统用于使烯烃与异链烷烃烷基化以产生烃烷基化物。 反应器容器具有垂直的圆柱形壁，顶部，倒锥形底部部分，内部穿孔挡板和多个乳液注入入口管道，其与反应器容器的内部相切地设置并与其连通。 乳液注射入口管具有并入其中的静态混合器，并且乳液的切向注入向反应器容器的内容物施加圆周运动，导致反应产物的部分相分离。 反应器容器通过具有悬挂在反应器容器的中心部分中的垂直部分的输送管和与反应容器的圆筒壁密封地延伸的水平部分与沉降容器连通。 输送管具有在反应器容器的锥形底部附近的第一端和在沉降容器的顶部的第二端。 反应器系统使得烯烃与异链烷烃的硫酸催化反应利用反应物的静态混合，并且使反应物对环境的泄漏最小化。

公开(公告)号：EP4405091A1

公开(公告)日：2024-07-31

申请号：EP22786205.9

申请日：2022-09-16

Applicant: Dow Global Technologies LLC

Inventor： DHODAPKAR, Shrikant ,  LIU, Yu ,  KONSTANTINOV, Ivan A.

IPC: B01J4/00 ,  B01J8/00 ,  B01J8/12 ,  B01J8/18

CPC classification number: B01J4/005 ,  B01J8/003 ,  B01J8/125 ,  B01J8/1881 ,  B01J2208/0092920130101 ,  B01J2219/0077420130101 ,  B01J8/0065

公开(公告)号：EP2900364B1

公开(公告)日：2018-06-13

申请号：EP13777193.7

申请日：2013-09-29

Applicant: Blue Cube IP LLC

Inventor： TIRTOWIDJOJO, Max M. ,  BAI, Hua ,  LUEBBE, Thomas Ulrich ,  MCMURRAY, Victor E.

IPC: B01J19/00 ,  B01J4/00 ,  C07C17/00 ,  F28C3/06 ,  B01J10/00

CPC classification number: B01J19/0013 ,  B01J4/002 ,  B01J4/005 ,  B01J10/00 ,  B01J2204/002 ,  B01J2219/00054 ,  B01J2219/00123 ,  B01J2219/00247 ,  B01J2219/00761 ,  F28C3/06

Abstract: The present invention provides a weir quench, an apparatus utilizing the weir quench and processes incorporating the same. The weir quench incorporates an inlet having an inner diameter (Di) and an upper chamber having an inner diameter (Duc), wherein the inlet inner diameter (Di) is at least 90% of the upper chamber inner diameter (Duc). The apparatus constitutes a reactor having an outlet with an inner diameter fluidly coupled with the weir quench inlet, wherein the ratio of the reactor oulet inner diameter (Dr) to the weir quench inlet diameter (Di) is greater than one. The weir quench, and apparatus are advantageously utilized in processes utilizing a limiting reagent.

公开(公告)号：EP3265222A1

公开(公告)日：2018-01-10

申请号：EP16707118.2

申请日：2016-03-01

Applicant: BASF SE

Inventor： BAYER, Robert ,  FREIBERG, Jürgen ,  SCHLIWA, Rudolf ,  KRÜGER, Marco

IPC: B01J8/08 ,  B01J8/12 ,  B01J8/18 ,  B01J8/40

CPC classification number: B01J8/40 ,  B01J4/001 ,  B01J4/005 ,  B01J8/087 ,  B01J8/12 ,  B01J8/125 ,  B01J8/1836 ,  B01J19/06 ,  B01J2208/00203 ,  B01J2208/00415 ,  B01J2219/00083 ,  B01J2219/00135 ,  B01J2219/00254 ,  B01J2219/185 ,  B01J2219/1943 ,  B01J2219/1946 ,  C08F2/01 ,  C08F120/06 ,  C08F220/06

Abstract: The invention relates to a device for producing poly(meth)acrylate in powder form, comprising a reactor (1) for droplet polymerisation that has a device (5), with holes through which a monomer solution is introduced, for dropletising said monomer solution so as to produce the poly(meth)acrylate, a gas supply point (13) above said dropletisation device (5), at least one gas extraction point (19) on the periphery of the reactor (1), and a fluidised bed (11), said reactor (1) having, above the gas extraction point (19), a region that has a constant hydraulic inner diameter and, below said gas extraction point (19), a hydraulic inner diameter that continually reduces. In the region with the continually-reducing hydraulic inner diameter, knockers (35) are mounted on the outer side of the reactor (1), each of said knockers (35) generating an impact energy of between 25J and 165J, and the number of knockers (35) being selected such that a surface-specific impact energy of between 1 and 7J/m² is applied.

公开(公告)号：EP2396089B1

公开(公告)日：2017-08-09

申请号：EP10740872.6

申请日：2010-02-11

Applicant: Natural Energy Systems Inc.

Inventor： HALLETT, Douglas, John ,  MCEWEN, Craig, Steven

IPC: A62D3/30

CPC classification number: B01J19/123 ,  B01J4/005 ,  B01J19/0066 ,  B01J19/0073 ,  B01J19/28 ,  B01J2219/00081 ,  B01J2219/00085 ,  B01J2219/00123 ,  B01J2219/00141 ,  B01J2219/0277 ,  B01J2219/0286 ,  B01J2219/0883 ,  B01J2219/182 ,  C01B3/503 ,  C01B3/586 ,  C01B2203/0405 ,  C01B2203/0445 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0495 ,  C10L3/10 ,  Y02P20/149 ,  Y02P30/10

公开(公告)号：EP3065858A2

公开(公告)日：2016-09-14

申请号：EP14806118.7

申请日：2014-11-05

Applicant: Watt Fuel Cell Corp.

Inventor： FINNERTY, Caine, M. ,  DEWALD, Paul

IPC: B01J12/00 ,  B01J19/24 ,  B01J4/00 ,  C01B3/38 ,  H01M8/24 ,  C01B3/32 ,  H01M8/06

CPC classification number: C01B3/36 ,  B01J4/001 ,  B01J4/002 ,  B01J4/005 ,  B01J12/007 ,  B01J19/0013 ,  B01J19/24 ,  B01J19/2425 ,  B01J2219/00006 ,  B01J2219/00058 ,  B01J2219/0006 ,  B01J2219/00069 ,  B01J2219/00074 ,  B01J2219/00103 ,  B01J2219/00132 ,  B01J2219/00135 ,  B01J2219/00159 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00234 ,  B01J2219/00238 ,  B01J2219/24 ,  C01B3/326 ,  C01B3/386 ,  C01B2203/0205 ,  C01B2203/0261 ,  C01B2203/041 ,  C01B2203/066 ,  C01B2203/0833 ,  C01B2203/0838 ,  C01B2203/085 ,  C01B2203/1005 ,  C01B2203/1276 ,  C01B2203/1282 ,  C01B2203/1288 ,  H01M8/0618 ,  H01M8/0631 ,  H01M8/22

Abstract: A liquid fuel catalytic partial oxidation (CPOX) reformer can include a plurality or an array of spaced-apart CPOX reactor units, each reactor unit including an elongate tube having a gas-permeable wall with internal and external surfaces, the wall enclosing an open gaseous flow passageway with at least a portion of the wall having CPOX catalyst disposed therein and/or comprising its structure. The catalyst-containing wall structure and open gaseous flow passageway enclosed thereby define a gaseous phase CPOX reaction zone, the catalyst-containing wall section being gas-permeable to allow gaseous CPOX reaction mixture to diffuse therein and hydrogen rich product reformate to diffuse therefrom. At least the exterior surface of the CPOX reaction zone can include a hydrogen barrier. The liquid fuel CPOX reformer can include a vaporizer, one or more igniters, and a source of liquid reformable fuel.

Abstract translation: 液体燃料催化部分氧化（CPOX）重整器可以包括多个或一组间隔开的CPOX反应器单元，每个反应器单元包括具有内部和外部表面的气体可渗透壁的细长管，该壁包围开放气体 流动通道，其中具有CPOX催化剂的壁的至少一部分设置在其中和/或包括其结构。 含有催化剂的壁结构和封闭的气态流动通道限定了气相CPOX反应区，含催化剂的壁段是透气的，以允许气态CPOX反应混合物在其中扩散，富氢产物重整产物从其扩散。 至少CPOX反应区的外表面可以包括氢屏障。 液体燃料CPOX重整器可包括蒸发器，一个或多个点火器和液体可重整燃料源。

公开(公告)号：EP3065857A2

公开(公告)日：2016-09-14

申请号：EP14803012.5

申请日：2014-11-06

Applicant: Watt Fuel Cell Corp.

Inventor： FINNERTY, Caine, M. ,  DEWALD, Paul

IPC: B01J12/00 ,  B01J19/24 ,  C01B3/38 ,  H01M8/24 ,  B01J4/00 ,  H01M8/06 ,  H01M8/10 ,  H01M8/12

CPC classification number: H01M8/0631 ,  B01J4/001 ,  B01J4/002 ,  B01J4/005 ,  B01J12/007 ,  B01J19/2425 ,  B01J2219/00006 ,  B01J2219/00058 ,  B01J2219/0006 ,  B01J2219/00069 ,  B01J2219/00135 ,  B01J2219/00159 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00234 ,  B01J2219/00238 ,  C01B3/323 ,  C01B3/386 ,  C01B3/48 ,  C01B2203/0261 ,  C01B2203/066 ,  C01B2203/1223 ,  C01B2203/1229 ,  C01B2203/1241 ,  C01B2203/1247 ,  H01M8/04201 ,  H01M8/04223 ,  H01M8/04776 ,  H01M8/243 ,  H01M2008/1293

Abstract: Integrated gaseous fuel catalytic partial oxidation (CPOX) reformer and fuel cell systems can include a plurality or an array of spaced-apart CPOX reactor units, each reactor unit including an elongate tube having a gas-permeable wall with internal and external surfaces, the wall enclosing an open gaseous flow passageway with at least a portion of the wall having CPOX catalyst disposed therein and/or comprising its structure. The catalyst-containing wall structure and open gaseous flow passageway enclosed thereby define a gaseous phase CPOX reaction zone, the catalyst-containing wall section being gas-permeable to allow gaseous CPOX reaction mixture to diffuse therein and hydrogen rich product reformate to diffuse therefrom. The gaseous fuel CPOX reformer also can include one or more igniters, and a source of gaseous reformable fuel. The hydrogen-rich reformate can be converted to electricity within a fuel cell unit integrated with the gaseous fuel CPOX reformer.

Abstract translation: 集成的气体燃料的催化部分氧化（CPOX）重整器和燃料电池系统可以包括多个或以间隔开的CPOX反应器单元，每个反应器单元，其包括具有带内，外表面的透气性壁伸长管，所述壁的阵列 封闭开放的气流通道与所述壁的至少一部分具有CPOX催化剂设置于其中和/或包含其结构。 含催化剂的壁结构，从而封闭开放气流通道限定气相CPOX反应区中，该含催化剂的壁部分是透气的，以允许气态CPOX反应混合物，以在其中扩散和富氢气产物重整从扩散那里。 因此，该气体燃料重整CPOX可包括一个或多个点火器和气体重整燃料的来源。 的富氢重整可与气体燃料重整CPOX集成在燃料电池单元内转换为电能。

公开(公告)号：EP2415706A1

公开(公告)日：2012-02-08

申请号：EP10758180.3

申请日：2010-03-11

Applicant: JGC Corporation ,  Osaka Gas Co., Ltd.

Inventor： OGURO, Shuichi ,  YAMADA, Nobuhiro

IPC: C01B3/36 ,  C01B3/38 ,  F23D14/62

CPC classification number: C01B3/386 ,  B01F5/0493 ,  B01J4/005 ,  B01J8/0278 ,  B01J2208/00548 ,  B01J2208/00849 ,  C01B2203/0261 ,  C01B2203/1276 ,  F23D14/62

Abstract: [Problem] To provide a gas mixing device capable of promptly mixing a combustible gas with a combustion supporting gas with its simple configuration, and a synthetic gas manufacturing apparatus using the device.
[Means for Resolution] In a gas mixing device which supplies a combustible gas and a combustion supporting gas from flow channels of a double pipe including an inner pipe 21 and an outer pipe 22 and mixes the gases, a first guide member 23 guides the gas, flowing out from a gas outflow port on one end side of the inner pipe 21, outward, and a second guide member 24 is formed in an annular shape along an inner peripheral wall of the outer pipe 22 of the second guide member 24 so that the inner peripheral portion is located closer to the upstream side than the outer peripheral portion and the inner peripheral portion is located closer to the center than the outer peripheral portion of the first guide member 23. In addition, a third guide member 25 is provided so as to face a region surrounded by the second guide member 24.

Abstract translation: [问题]提供一种能够迅速地混合可燃气体与助燃气体以其简单的结构，以及使用该装置的合成气体制造设备的气体混合装置。 [用于解决在一个气体混合装置，该装置从双管包括内管21和外管22的流动通道供给的可燃气体和助燃气体和混合气体，第一引导构件23个引导气体 ，从内管21的一端侧的气体流出口流出，向外和第二引导构件24设置在环状的设计形状沿着形成于在第二引导构件24，从而做的外管22的内周壁 内周部位于更靠近上游侧的外周部和内周部位于更靠近中心比所述第一导向构件的外周部23.此外，第三引导部件25被设置成 为面对由第二引导构件24日所包围的区域

公开(公告)号：EP2170766A1

公开(公告)日：2010-04-07

申请号：EP08750811.5

申请日：2008-04-22

Applicant: Helbio S.A. Hydrogen and Energy Production Systems

Inventor： VERYKIOS, Xenophon ,  LYGOURAS, Dimitrios, K.

IPC: C01B3/38 ,  B01J8/02

CPC classification number: C01B3/384 ,  B01J4/002 ,  B01J4/005 ,  B01J12/007 ,  B01J19/006 ,  B01J19/2415 ,  B01J19/2425 ,  B01J2219/00081 ,  B01J2219/00117 ,  B01J2219/00777 ,  C01B2203/0233 ,  C01B2203/0811 ,  C01B2203/0822 ,  C01B2203/1035 ,  Y02P20/128 ,  Y02P20/129

Abstract: Described herein is a highly heat integrated steam reformer/combustor assembly that can be used in a fuel processor for hydrogen production from a fuel source. The assembly comprises a reforming section and a combustion section separated by a wall. Catalyst able to induce the reforming reactions is coated on the wall facing the reforming section. Catalyst able to induce the combustion reactions is coated on the wall facing the combustion section. A setam and fuel mixture is supplied to the reforming section where it is reformed to product hydrogen. A fuel and air mixture is supplied to the combustion section where it is combusted to supply the heat for the reformer. Catalytic combustion takes place on the combustion catalyst coated on one side of the wall while catalytic reforming takes place on the reforming catalyst coated on the other side of the wall. Heat transfer is very facile and efficient across the wall. Multiple such assemblies can be bundled to form reactors of any size.