公开(公告)号：US07261284B2

公开(公告)日：2007-08-28

申请号：US11328248

申请日：2006-01-10

Applicant: Filippi Ermanno

Inventor： Filippi Ermanno

IPC: B01F3/04

CPC classification number: B01D3/16 ,  B01J8/008 ,  B01J8/0415 ,  B01J8/0426 ,  B01J8/0496 ,  B01J19/305 ,  B01J19/325 ,  B01J2208/00106 ,  B01J2208/00212 ,  B01J2208/00884 ,  B01J2219/00024

Abstract: A process for effecting mass transfer between a liquid phase and a gaseous phase in a filled-type column comprising an external shell which accommodates at least one filler-containing basket wherethrough the phases are caused to flow in countercurrent relationship, advantageously comprises the step of feeding the gaseous phase to the at least one basket through a gas-permeable surface thereof which is larger than the basket cross-section, preferably in a prevailing radial flow direction.

Abstract translation: 一种用于在填充柱中进行液相和气相之间的质量传递的方法，其包括外壳，所述外壳容纳至少一个含有填料的篮，通过所述相以逆流方式流动，有利地包括进料步骤 气相通过其透气表面至至少一个篮子，其大于篮状横截面，优选地以主要的径向流动方向。

公开(公告)号：US07090807B1

公开(公告)日：2006-08-15

申请号：US09555899

申请日：1998-12-03

Applicant: Stefan Brauchle ,  Oliver Freitag ,  Barbara Strobel ,  Matthias Wolfsteiner

Inventor： Stefan Brauchle ,  Oliver Freitag ,  Barbara Strobel ,  Matthias Wolfsteiner

IPC: B01J8/04 ,  B01J8/02 ,  B01J4/00

CPC classification number: B01J8/0426 ,  B01D53/864 ,  B01D53/885 ,  B01J19/249 ,  B01J2208/00309 ,  B01J2208/022 ,  B01J2219/0002 ,  B01J2219/2453 ,  B01J2219/2462 ,  B01J2219/2465 ,  B01J2219/2479 ,  B01J2219/2481 ,  C01B3/583 ,  C01B2203/044 ,  C01B2203/047 ,  H01M8/0662

Abstract: An apparatus for the selective catalytic oxidation of carbon monoxide contained in a hydrogen-rich mixed gas flow, includes a reaction chamber filled with a catalyst and a cooling chamber through which a coolant flows formed between successive plates. The plates have openings that form inlet and outlet channels for the mixed gas flow and the coolant. An oxidizing gas is supplied directly into the inlet channel for the mixed gas flow. For two-stage apparatuses, a separating plate without an opening for the inlet channel for the mixed gas flow is arranged between the first and the second stage, and an apparatus for supplying the oxidizing gas to the second stage is passed into the outlet channel for the mixed gas flow from the first stage.

Abstract translation: 包含在富氢混合气流中的一氧化碳的选择性催化氧化装置包括填充有催化剂的反应室和冷却剂室，冷却剂在连续的板之间形成。 板具有形成用于混合气流和冷却剂的入口和出口通道的开口。 将氧化气体直接供给到用于混合气流的入口通道。 对于两级装置，在第一和第二阶段之间设置没有用于混合气流的入口通道的开口的分离板，并且用于将氧化气体供应到第二级的装置被传送到出口通道 来自第一阶段的混合气体流。

公开(公告)号：US06919048B2

公开(公告)日：2005-07-19

申请号：US10084493

申请日：2002-02-28

Applicant: Frédéric Hoffmann ,  Eric Lenglet ,  Philippe Mege

Inventor： Frédéric Hoffmann ,  Eric Lenglet ,  Philippe Mege

IPC: B01J8/06 ,  B01J8/00 ,  B01J8/04 ,  B01J8/12 ,  C07B61/00 ,  C07C5/333 ,  C07C11/02 ,  B01J8/08

CPC classification number: B01J8/085 ,  B01J8/003 ,  B01J8/004 ,  B01J8/0426 ,  B01J8/0496 ,  B01J8/125 ,  B01J2208/00168 ,  B01J2219/185 ,  B01J2219/1943

Abstract: An elongate reaction vessel and process includes at least two stages in the vertical direction in which an endothermic or exothermic catalytic reaction is carried out and comprises: a catalytic reaction zone (12a, 12b) per stage (6, 7); introducing (2) a reaction fluid to a stage adapted for transverse motion of the fluid across the whole vertical extent of the reaction zone; introducing and extracting the catalyst; a heat exchanger (5a) for reaction fluids located inside the vessel between two successive reaction zones; means (6) for transporting reaction fluids from one stage to another preferably connected to the exchanger of the stage under consideration and to the inlet for reaction fluids of the subsequent stage; and means for recovering reaction fluids downstream of the last stage. The temperature variation in each zone and the temperature level are respectively adjusted by the thickness of each zone and by heat exchange.

Abstract translation: 细长的反应容器和方法包括沿垂直方向的至少两个阶段，其中进行吸热或放热的催化反应，并包括：每个阶段（6,7）的催化反应区（12a，12b）; 将反应流体引入（2）适于在反应区的整个垂直范围内流体横向运动的阶段; 引入和提取催化剂; 位于两个连续反应区之间的反应流体的热交换器（5a）; 用于将反应流体从一个阶段转移到另一个阶段的装置（6），优选地连接到所考虑的阶段的交换器和后续阶段的反应流体的入口; 以及用于在最后阶段下游回收反应流体的装置。 每个区域的温度变化和温度水平分别通过每个区域的厚度和通过热交换来调整。

公开(公告)号：US20040106813A1

公开(公告)日：2004-06-03

申请号：US10706449

申请日：2003-11-12

Inventor： Peter Moritz ,  Peter Faessler ,  Claudia von Scala ,  Oliver Bailer

IPC: C07C051/43

CPC classification number: C07C67/08 ,  B01D3/009 ,  B01D3/343 ,  B01J8/0426 ,  B01J19/249 ,  B01J19/32 ,  B01J2208/00274 ,  B01J2208/00283 ,  B01J2219/2453 ,  B01J2219/2458 ,  B01J2219/246 ,  B01J2219/2481 ,  B01J2219/32206 ,  B01J2219/32213 ,  B01J2219/32227 ,  B01J2219/32237 ,  B01J2219/32272 ,  B01J2219/32466 ,  B01J2219/32475 ,  B01J2219/3325 ,  Y02P20/127 ,  C07C69/24 ,  C07C69/52

Abstract: The method for the esterification of a fatty acid F is carried out in a column with a packing. In addition to functioning as a catalytic reactor, the packing functions as a stripping section. A heteregenous catalysis of a fatty acid is carried out with an alcohol used in the same molar ratio or in excess. A gaseous alcohol-rich counter-flow is produced in a sump of the column by vaporisation. Water is removed from the reaction zone by means of the counter-flow acting as a stripping gas. The loaded stripping gas is at least partially liquefied at the head of the column. The head product is separated into a water-rich fraction as well as an alcohol-rich fraction. The alcohol-rich fraction is returned to the process as a starting material for the esterification and for the production of the stripping gas.

Abstract translation: 脂肪酸F的酯化方法在具有包装的柱中进行。 除了作为催化反应器的功能之外，包装起剥离部分的作用。 使用相同摩尔比或过量的醇进行脂肪酸的纯化催化。 通过蒸发在柱的集水槽中产生富含气态的醇的逆流。 通过作为汽提气体的逆流将水从反应区域除去。 负载的汽提气体在柱的头部处至少部分液化。 将头部产物分离成富含水的级分以及富含醇的级分。 富含醇的馏分作为用于酯化和汽提气体的生产的原料返回到该方法中。

公开(公告)号：US20030039601A1

公开(公告)日：2003-02-27

申请号：US09925366

申请日：2001-08-10

Inventor： Thomas Gilbert Halvorson ,  Victor Emmanuel Bergsten ,  Prasad S. Apte ,  Nitin Ramesh Keskar ,  Christo Steyn ,  Richard Andrew Vanslooten

IPC: C01B003/26 ,  B01L007/00 ,  B01J008/00

CPC classification number: C01B3/384 ,  B01J8/009 ,  B01J8/0426 ,  B01J8/0453 ,  B01J8/0496 ,  B01J2208/00132 ,  B01J2208/00185 ,  B01J2208/00194 ,  B01J2208/00495 ,  B01J2208/0053 ,  B01J2219/00006 ,  B01J2219/00777 ,  C01B13/0251 ,  C01B13/0255 ,  C01B2203/0227 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/0811 ,  C01B2203/1241 ,  C01B2203/84 ,  C01B2210/0046

Abstract: A reaction vessel for the production of synthesis gas that contains four subassemblies: (1) a first heat exchanger that transfers heat between two low pressure streams (an oxygen containing stream and an oxygen depleted stream); (2) a second heat exchanger that transfers heat between two high pressure fluid streams (a hydrocarbon-containing reactant stream and a synthesis gas product stream); (3) mixed conductor ceramic membranes; and (4) a catalyst bed. Each of these subassemblies are configured so that they freely expand or contract independently from each other, and to thus avoid inducing high mechanical loads and damaging material stresses.

Abstract translation: 一种用于生产合成气的反应容器，其包含四个子组件：（1）在两个低压流（含氧流和贫氧流）之间传递热的第一热交换器; （2）在两个高压流体流（含烃反应物流和合成气产物流）之间传递热量的第二热交换器; （3）混合导体陶瓷膜; 和（4）催化剂床。 这些子组件中的每一个被构造成使得它们彼此独立地自由地膨胀或收缩，并且因此避免引起高机械载荷并损坏材料应力。

公开(公告)号：US20020071790A1

公开(公告)日：2002-06-13

申请号：US09732230

申请日：2000-12-07

Inventor： Richard Woods ,  Kandaswamy Duraiswamy ,  Shawn Barge

IPC: F23D011/44 ,  C10G001/00

CPC classification number: F23G7/07 ,  B01J8/0426 ,  B01J8/0453 ,  B01J8/0469 ,  B01J8/048 ,  B01J8/0496 ,  B01J2208/00176 ,  B01J2208/00185 ,  B01J2208/00194 ,  B01J2208/00203 ,  B01J2208/00212 ,  B01J2208/00221 ,  B01J2208/00495 ,  B01J2208/00504 ,  B01J2208/0053 ,  B01J2208/00849 ,  C01B3/382 ,  C01B2203/0244 ,  C01B2203/0283 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0844 ,  C01B2203/0866 ,  C01B2203/1241 ,  C01B2203/142 ,  C01B2203/82 ,  F23G2206/20 ,  Y02P20/128 ,  Y02P20/129

Abstract: An integrated reactor for producing fuel gas for a fuel cell, the integrated reactor comprises an waste gas oxidizer (WGO) assembly having an associated WGO chamber, an inlet, an outlet and a flow path for exothermic gases produced in the WGO chamber. The integrated reactor has an autothermal reactor (ATR) assembly located within the WGO chamber. The ATR assembly has an inlet means and an outlet means for process gases flowing therethrough and a catalyst bed which is intermediate the inlet and outlet means. At least a part of the inlet means of the ATR assembly is located in the flow path of the WGO chamber to facilitate the transfer of thermal energy.

Abstract translation: 一种用于生产用于燃料电池的燃料气体的集成反应器，该集成反应器包括废气氧化器（WGO）组件，其具有与WGO室中产生的放热气体相关联的WGO室，入口，出口和流路。 集成反应器具有位于WGO室内的自热反应器（ATR）组件。 ATR组件具有用于工艺气体流过的入口装置和出口装置以及位于入口和出口装置之间的催化剂床。 ATR组件的入口装置的至少一部分位于WGO室的流动路径中以便于热能传递。

公开(公告)号：US3948775A

公开(公告)日：1976-04-06

申请号：US482023

申请日：1974-06-24

Applicant: Seiya Otani ,  Takeshi Umemoto ,  Masazumi Kanaoka ,  Shoichi Akita ,  Koji Ogawa ,  Yoshio Noguchi ,  Hiroshi Fujita

Inventor： Seiya Otani ,  Takeshi Umemoto ,  Masazumi Kanaoka ,  Shoichi Akita ,  Koji Ogawa ,  Yoshio Noguchi ,  Hiroshi Fujita

IPC: B01D15/00 ,  B01D53/04 ,  B01J8/02 ,  B01J8/04 ,  B01D29/08

CPC classification number: B01D53/0423 ,  B01D15/00 ,  B01D53/0446 ,  B01J8/0207 ,  B01J8/0214 ,  B01J8/0292 ,  B01J8/0426 ,  B01J8/0438 ,  B01D2253/102 ,  B01D2253/106 ,  B01D2253/108 ,  B01D2253/116 ,  B01D2259/41

Abstract: A horizontal multiple-chamber, packed column structure for adsorptive separation process wherein loading and unloading of packing material is facilitated, and efficient, effective contact between the packing material and a fluid passing therethrough is provided by the configuration and placement of a fluid inlet and distributor at one end thereof and fluid collector and fluid outlet at the horizontally opposite end, each chamber also including a plurality of axially extending rods to maintain a relatively uniform packing density of packing material in the chamber.

Abstract translation: 用于吸附分离过程的水平多室填充柱结构，其中促进包装材料的装载和卸载，并且通过流体入口和分配器的配置和放置来提供包装材料和通过其的流体之间的有效，有效的接触 在其一端处，在水平相对端处的流体收集器和流体出口，每个室还包括多个轴向延伸的杆，以保持在腔室中的包装材料的相对均匀的填充密度。