公开(公告)号：US20110165483A1

公开(公告)日：2011-07-07

申请号：US13062905

申请日：2009-08-12

Applicant: Jun Yamamoto ,  Yukihiko Kiyohiro

Inventor： Jun Yamamoto ,  Yukihiko Kiyohiro

IPC: H01M8/06 ,  B01J19/00

CPC classification number: B01J8/0484 ,  B01J8/0085 ,  B01J8/009 ,  B01J8/0496 ,  B01J19/249 ,  B01J2208/00132 ,  B01J2208/00203 ,  B01J2208/00309 ,  B01J2208/00504 ,  B01J2208/0053 ,  B01J2219/1923 ,  B01J2219/2453 ,  B01J2219/2455 ,  B01J2219/2458 ,  B01J2219/2462 ,  B01J2219/2481 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/066 ,  C01B2203/0805 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/1276 ,  C01B2203/1288 ,  C01B2203/1294 ,  H01M8/0618 ,  H01M2008/1293

Abstract: A reformer includes a reforming chamber having a raw fuel passage through which a raw fuel flows, the reforming chamber being filled with or carrying a reforming catalyst, a supply chamber disposed upstream of the reforming chamber, for uniformly supplying the raw fuel to the raw fuel passage, and a discharge chamber disposed downstream of the reforming chamber, for uniformly discharging the raw fuel from the raw fuel passage. The raw fuel passage has first and second reversers for reversing the direction in which the raw fuel flows. The raw fuel passage has a cross-sectional area which is smaller in a downstream portion thereof than in an upstream portion thereof.

Abstract translation: 重整器包括：重整室，其具有原料燃料流过原料燃料通道，重整室填充或承载重整催化剂，供应室设置在重整室的上游，用于将原料燃料均匀地供应到原燃料 通道和设置在重整室下游的排放室，用于从原燃料通道均匀排出原燃料。 原燃料通道具有用于反转原燃料流动方向的第一和第二反向器。 原燃料通道的下游部分的横截面积比其上游部分的截面面积小。

公开(公告)号：US20080171241A1

公开(公告)日：2008-07-17

申请号：US11830669

申请日：2007-07-30

Applicant: Ian W. Kaye ,  Gerry Tucker

Inventor： Ian W. Kaye ,  Gerry Tucker

IPC: H01M8/04

CPC classification number: H01M8/04225 ,  B01J8/0214 ,  B01J8/0221 ,  B01J8/0242 ,  B01J8/0285 ,  B01J8/0438 ,  B01J8/0484 ,  B01J19/0093 ,  B01J19/249 ,  B01J2208/00061 ,  B01J2208/00309 ,  B01J2208/00398 ,  B01J2208/00407 ,  B01J2208/00415 ,  B01J2208/00504 ,  B01J2208/00646 ,  B01J2208/00716 ,  B01J2219/00783 ,  B01J2219/00835 ,  B01J2219/00873 ,  B01J2219/00907 ,  B01J2219/2453 ,  B01J2219/2458 ,  B01J2219/2459 ,  B01J2219/2462 ,  B01J2219/2465 ,  B01J2219/2467 ,  B01J2219/247 ,  B01J2219/2475 ,  B01J2219/2479 ,  B01J2219/2481 ,  B01J2219/2482 ,  C01B3/323 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/066 ,  C01B2203/0805 ,  C01B2203/0811 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0844 ,  C01B2203/0866 ,  C01B2203/1223 ,  C01B2203/1247 ,  C01B2203/142 ,  C01B2203/82 ,  H01M8/0228 ,  H01M8/0247 ,  H01M8/0258 ,  H01M8/0267 ,  H01M8/04007 ,  H01M8/04022 ,  H01M8/04037 ,  H01M8/04067 ,  H01M8/04223 ,  H01M8/04268 ,  H01M8/04298 ,  H01M8/0435 ,  H01M8/04365 ,  H01M8/04373 ,  H01M8/04388 ,  H01M8/04425 ,  H01M8/04559 ,  H01M8/04589 ,  H01M8/04604 ,  H01M8/04619 ,  H01M8/04626 ,  H01M8/04731 ,  H01M8/04738 ,  H01M8/04753 ,  H01M8/04768 ,  H01M8/04776 ,  H01M8/04955 ,  H01M8/0618 ,  H01M8/0631 ,  H01M8/0662 ,  H01M2008/1095 ,  Y02P20/128 ,  Y02P70/56

Abstract: Described herein are fuel cell systems and methods of using fuel cell systems. The systems include a fuel cell that generates electrical energy using hydrogen and a fuel processor that produces hydrogen from a fuel source. The fuel processor includes a reformer and a burner that heats the reformer.

Abstract translation: 这里描述的是燃料电池系统和使用燃料电池系统的方法。 该系统包括使用氢气产生电能的燃料电池和从燃料源产生氢气的燃料处理器。 燃料处理器包括重整器和加热重整器的燃烧器。

公开(公告)号：US20040184976A1

公开(公告)日：2004-09-23

申请号：US10804896

申请日：2004-03-19

Applicant: Methanol Casale S.A.

Inventor： Giorgio Pagani ,  Enrico Rizzi ,  Umberto Zardi

IPC: B01J008/00

CPC classification number: F28D7/12 ,  B01J8/0085 ,  B01J8/0484 ,  B01J8/0496 ,  B01J2208/00203 ,  B01J2208/0053 ,  B01J2208/00814 ,  B01J2208/00884 ,  B01J2219/182 ,  C07C29/152 ,  F28D7/06 ,  F28F2280/02 ,  Y02P20/52 ,  C07C31/04

Abstract: A horizontal chemical reactor comprises at least one catalytic bed (5a-5d) arranged horizontally in the reactor and comprising a lower gas-permeable wall (6) for gas outlet, and a holding element (2) of the at least one catalytic bed.

Abstract translation: 水平化学反应器包括在反应器中水平布置的至少一个催化床（5a-5d），并包括用于气体出口的下部气体可渗透壁（6）和至少一个催化床的保持元件（2）。

公开(公告)号：US20030161768A1

公开(公告)日：2003-08-28

申请号：US10391581

申请日：2003-03-20

Inventor： Koichi Kawamoto ,  Masatoshi Tanaka ,  Michizo Miyoshi

IPC: B01J008/02 ,  B01J008/04 ,  H01M008/06

CPC classification number: B01J8/0496 ,  B01B1/005 ,  B01J8/0465 ,  B01J8/0484 ,  B01J8/0492 ,  B01J2208/00141 ,  B01J2208/00203 ,  B01J2208/00495 ,  B01J2208/00504 ,  C01B3/48 ,  C01B3/583 ,  C01B2203/0205 ,  C01B2203/0227 ,  C01B2203/0288 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/0816 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0844 ,  C01B2203/0866 ,  C01B2203/0883 ,  C01B2203/1241 ,  C01B2203/1288 ,  C01B2203/146 ,  C01B2203/82 ,  H01M8/0631 ,  H01M8/0668 ,  Y02P20/128

Abstract: A fuel reforming apparatus for a polymer electrolyte membrane fuel cell, characterized in that each of a reformer, a carbon monoxide converter, a carbon monoxide selective oxidizing reactor, a cooling device for cooling the inlet port of the carbon monoxide converter, and a cooling device for cooling the inlet gas of the carbon monoxide selective oxidizing reactor is formed cylindrical, the reformer is arranged in the center, the carbon monoxide converter is arranged on the outer circumferential portion of the reformer, and the carbon monoxide selective oxidizing reactor is arranged on the outer circumferential portion of the carbon monoxide converter so as to make reformer, transformer and reactor integral.

Abstract translation: 一种用于聚合物电解质膜燃料电池的燃料重整装置，其特征在于，重整器，一氧化碳转化器，一氧化碳选择氧化反应器，用于冷却一氧化碳转化器的入口的冷却装置和冷却装置 为了冷却一氧化碳选择性氧化反应器的入口气体是圆柱形的，重整器布置在中心，一氧化碳转化器设置在重整器的外圆周部分上，一氧化碳选择氧化反应器设置在 一氧化碳转化器的外圆周部分，以使重整器，变压器和反应器成为一体。

公开(公告)号：US5948211A

公开(公告)日：1999-09-07

申请号：US545559

申请日：1995-10-19

Applicant: Neil Yeoman ,  Ronald Pinaire ,  Michael A. Ulowetz

Inventor： Neil Yeoman ,  Ronald Pinaire ,  Michael A. Ulowetz

IPC: B01D3/00 ,  B01D3/16 ,  B01D3/20 ,  B01J8/00 ,  B01J8/04 ,  B01J8/06 ,  B01J10/00 ,  B01J19/00 ,  B01D3/32

CPC classification number: B01J19/006 ,  B01D3/009 ,  B01D3/16 ,  B01D3/20 ,  B01J8/003 ,  B01J8/0415 ,  B01J8/0453 ,  B01J8/048 ,  B01J8/0484 ,  B01J8/06 ,  B01J2208/00548 ,  B01J2208/021 ,  B01J2219/00049 ,  B01J2219/00164 ,  B01J2219/00774

Abstract: A downcomer having a screened or otherwise liquid permeable wall is provided for use in a mass transfer or distillation column. The liquid permeable wall provides another avenue for liquid to be removed from the downcomer to increase the liquid handling capacity of the downcomer. When wetted, the liquid permeable wall provides a barrier against vapor entry into the downcomer through the wall.

Abstract translation: 提供具有屏蔽或其它液体可渗透壁的降液管用于传质或蒸馏塔。 液体可渗透壁为液体从降液管中除去提供另一条通道，以增加降液管的液体处理能力。 当润湿时，液体可渗透壁提供阻挡蒸汽通过壁进入降液管的屏障。

公开(公告)号：US5855741A

公开(公告)日：1999-01-05

申请号：US376046

申请日：1995-01-19

Applicant: David H. Koch ,  Neil Yeoman

Inventor： David H. Koch ,  Neil Yeoman

IPC: B01D3/00 ,  B01D3/16 ,  B01D3/20 ,  B01J8/00 ,  B01J8/04 ,  B01J8/06 ,  B01J10/00 ,  B01D3/14

CPC classification number: B01J8/06 ,  B01D3/009 ,  B01D3/16 ,  B01D3/20 ,  B01J8/003 ,  B01J8/0415 ,  B01J8/0453 ,  B01J8/048 ,  B01J8/0484 ,  B01J2208/00548 ,  B01J2208/021 ,  Y10S203/06 ,  Y10S203/09

Abstract: A column having a region for reaction with distillation of fluid streams is provided with structures including catalyst-filled containers having liquid permeable upper surfaces which allow for the accumulation and flow of liquid from a liquid stream. The containers include catalyst beds positioned beneath the upper surface of the containers. A portion of the liquid on the containers is driven through the catalyst bed by the liquid head created by the accumulated liquid and is catalytically reacted. Another portion of the liquid may be directed through a downcomer which allows the accumulated liquid to leave the container without passing through the catalyst bed so that higher volumetric flow rates can be achieved.

Abstract translation: 具有用于与流体流的蒸馏反应的区域的塔被提供有包括具有液体可渗透上表面的催化剂填充容器的结构，其允许来自液体流的液体的积聚和流动。 容器包括位于容器上表面下方的催化剂床。 容器中的液体的一部分通过催化剂床被积聚的液体产生的液体头驱动并被催化反应。 液体的另一部分可以被引导通过降液管，其允许积聚的液体离开容器而不通过催化剂床，使得可以实现更高的体积流速。

公开(公告)号：US5447609A

公开(公告)日：1995-09-05

申请号：US962498

申请日：1992-10-16

Applicant: Neil Yeoman ,  Ronald Pinaire ,  Michael A. Ulowetz ,  O. Jeffrey Berven ,  Timothy P. Nace ,  David A. Furse

Inventor： Neil Yeoman ,  Ronald Pinaire ,  Michael A. Ulowetz ,  O. Jeffrey Berven ,  Timothy P. Nace ,  David A. Furse

IPC: B01D3/00 ,  B01D3/16 ,  B01D3/20 ,  B01J8/00 ,  B01J8/04 ,  B01J8/06 ,  B01J10/00 ,  B01J19/00

CPC classification number: B01J8/003 ,  B01D3/009 ,  B01D3/16 ,  B01D3/20 ,  B01J19/006 ,  B01J19/0073 ,  B01J8/04 ,  B01J8/0415 ,  B01J8/0453 ,  B01J8/048 ,  B01J8/0484 ,  B01J8/06 ,  B01J2208/00548 ,  B01J2208/021 ,  B01J2219/00049 ,  B01J2219/00164 ,  B01J2219/00774 ,  Y10S203/06 ,  Y10S203/17

Abstract: A reaction with distillation column is provided with a plurality of discrete catalytic reaction containers. The containers contain a plurality of solid catalyst particles which form a catalytic reaction zone. The containers also comprise a liquid collection tray cover which defines a liquid accumulation zone immediately overlying the catalytic reaction zone. Overflow weirs are provided on the tray cover to allow for overflow of liquid on the tray cover. A member may be provided within the containers to create an open area within the catalytic reaction zone to facilitate entry of the liquid into the catalytic reaction zone. The containers can be individually positioned within the reactor to suit particular process requirements.

Abstract translation: 与蒸馏塔的反应提供有多个离散的催化反应容器。 这些容器含有形成催化反应区的多个固体催化剂颗粒。 容器还包括限定刚好覆盖催化反应区的液体积聚区的液体收集盘盖。 溢流堰被提供在托盘盖上以允许托盘盖上的液体溢出。 可以在容器内提供构件以在催化反应区内形成开放区域，以便于液体进入催化反应区。 容器可以单独定位在反应器内以适应特定的工艺要求。

公开(公告)号：US3567404A

公开(公告)日：1971-03-02

申请号：US3567404D

申请日：1967-08-18

Applicant: PULLMAN INC

Inventor： AXELROD LEONARD C ,  EAGLE RAYMOND S ,  FLEMING JAMES B ,  KAHN GERHARD M ,  QUARTULLI ORLANDO J

IPC: B01J8/00 ,  B01J8/04 ,  C01C1/04 ,  B01J9/04

CPC classification number: C01C1/0423 ,  B01J8/0005 ,  B01J8/0484 ,  B01J2219/182 ,  Y02P20/52

Abstract: A REACTOR VESSEL HAVING AN OUTER SHELL, A HEAT EXCHANGER AND AN INNER SHELL, THE INNER SHELL CONTAINING A SERIES OF CATALYTIC REACTION BEDS HAVING THEIR ENTRANCE AREAS DISPOSED PARALLEL TO THE LONGITUDINAL AXIS OF THE OUTER AND INNER SHELLS.

公开(公告)号：US3086852A

公开(公告)日：1963-04-23

申请号：US72442758

申请日：1958-03-27

Applicant: EXXON RESEARCH ENGINEERING CO

Inventor： FENSKE MERRELL R ,  JONES JENNINGS H

IPC: B01J8/04 ,  B01J8/08 ,  B01J8/28 ,  C07B39/00 ,  C07C5/367 ,  C07C5/387 ,  C07C17/10 ,  C07C45/38 ,  C07C51/265 ,  C07D301/10

CPC classification number: C07D301/10 ,  B01J8/0469 ,  B01J8/048 ,  B01J8/0484 ,  B01J8/087 ,  B01J8/28 ,  B01J2208/00044 ,  B01J2208/00274 ,  B01J2208/0038 ,  C07B39/00 ,  C07C5/367 ,  C07C5/387 ,  C07C17/10 ,  C07C45/38 ,  C07C51/265 ,  Y10S585/921 ,  C07C19/01 ,  C07C47/04 ,  C07C63/16

公开(公告)号：US20190201861A1

公开(公告)日：2019-07-04

申请号：US15862273

申请日：2018-01-04

Applicant: Chevron Phillips Chemical Company LP

Inventor： Vincent D. McGahee ,  Daniel M. Hasenberg

IPC: B01J8/06 ,  B01J8/08 ,  B01J8/00 ,  B01J19/24 ,  C10G35/04

CPC classification number: B01J8/062 ,  B01J8/0085 ,  B01J8/0214 ,  B01J8/0438 ,  B01J8/0442 ,  B01J8/0484 ,  B01J8/0488 ,  B01J8/065 ,  B01J8/087 ,  B01J19/2445 ,  B01J2208/00504 ,  B01J2208/025 ,  B01J2219/00038 ,  B01J2219/2419 ,  C10G35/04 ,  C10G59/02 ,  C10G2300/1044

Abstract: A naphtha reforming reactor system comprising a first reactor comprising a first inlet and a first outlet, wherein the first reactor is configured to operate as an adiabatic reactor, and wherein the first reactor comprises a first naphtha reforming catalyst; and a second reactor comprising a second inlet and a second outlet, wherein the second inlet is in fluid communication with the first outlet of the first reactor, wherein the second reactor is configured to operate as an isothermal reactor, and wherein the second reactor comprises a plurality of tubes disposed within a reactor furnace, a heat source configured to heat the interior of the reactor furnace; and a second naphtha reforming catalyst disposed within the plurality of tubes, wherein the first naphtha reforming catalyst and the second naphtha reforming catalyst are the same or different.