公开(公告)号：US20180141807A1

公开(公告)日：2018-05-24

申请号：US15864550

申请日：2018-01-08

Applicant: Watt Fuel Cell Corp.

Inventor： Caine M. Finnerty ,  Paul DeWald

IPC: C01B3/36 ,  B01J4/00 ,  H01M8/22 ,  H01M8/0612 ,  C01B3/38 ,  C01B3/32 ,  B01J19/24 ,  B01J19/00 ,  B01J12/00

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 reformer includes a fuel vaporizer which utilizes heat from an upstream source of heat, specifically, an electric heater, operable in the start-up mode of the reformer, and therefore independent of the reforming reaction zone of the reformer, to vaporize fuel in a downstream vaporization zone.

公开(公告)号：US20180028999A1

公开(公告)日：2018-02-01

申请号：US15552838

申请日：2016-03-01

Applicant: BASF SE

Inventor： Robert Bayer ,  Jürgen Freiberg ,  Rudolf Schliwa ,  Marco Krüger

IPC: B01J8/40 ,  C08F220/06 ,  B01J4/00 ,  B01J19/06 ,  B01J8/18

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: An apparatus for producing pulverulent poly(meth)acrylate in a reactor for droplet polymerization having an apparatus for dropletization of a monomer solution for the production of the poly(meth)acrylate having holes through which the monomer solution is introduced, an addition point for a gas above the apparatus for dropletization, at least one gas withdrawal point on the circumference of the reactor and a fluidized bed, and above the gas withdrawal point the reactor has a region having a constant hydraulic internal diameter and below the gas withdrawal point the reactor has a hydraulic internal diameter that steadily decreases.

公开(公告)号：US09861946B1

公开(公告)日：2018-01-09

申请号：US15366481

申请日：2016-12-01

Applicant: PHILLIPS 66 COMPANY

Inventor： Brad P. Palmer

IPC: B01J8/02 ,  B01J4/00 ,  B01J8/06

CPC classification number: B01J8/0278 ,  B01J4/005 ,  B01J8/065 ,  B01J2208/00548 ,  B01J2208/00893 ,  B01J2208/0092 ,  B01J2208/00929 ,  B01J2208/00938

Abstract: The invention relates to distributing reactants more evenly across the interior space of a reactor vessel utilizing a distributor at the inlet end that initially directs the flow of reactants through a flange plate and a series of ring plates. The ring plates are physical spaced such that vapor along the wall of the inlet is mildly obstructed by the flange plate and the ring plates cause the vapor to alter course temper down any diverse velocities that may create hot spots within the catalyst bed.

公开(公告)号：US20170342594A1

公开(公告)日：2017-11-30

申请号：US15536245

申请日：2015-12-16

Applicant: Saint-Gobain Lumilog

Inventor： Bernard Beaumont ,  Manivannane Pourouchottamane

IPC: C30B25/14 ,  C30B29/40 ,  C23C16/44 ,  B01J4/00 ,  C23C16/30 ,  F15D1/08 ,  C23C16/455

CPC classification number: C30B25/14 ,  B01J4/002 ,  B01J4/005 ,  B01J2204/002 ,  B01J2204/005 ,  C23C16/303 ,  C23C16/4401 ,  C23C16/4404 ,  C23C16/45506 ,  C23C16/45565 ,  C23C16/45574 ,  C23C16/45587 ,  C30B29/406 ,  F15D1/08

Abstract: The invention concerns a reactor for chemical vapour deposition from first and second precursor gases, the reactor comprising: —a chamber including top and bottom walls and a side wall linking the top and bottom walls, —a support intended for receiving at least one substrate, mounted inside the chamber, and —at least one system for injecting precursor gases, the system comprising an injection head including at least one nozzle for supplying the first precursor gas (41) in a main direction of axis A-A′, the at least one nozzle including: a precursor gas supply conduit (321), and an outlet member (322) generating a substantially annular 43 vortex flow (44) around axis A-A′.

公开(公告)号：US20160272492A1

公开(公告)日：2016-09-22

申请号：US15033997

申请日：2014-11-06

Applicant: WATT FUEL CELL CORP.

Inventor： Caine M. Finnerty ,  Paul DeWald

IPC: C01B3/38 ,  B01J19/00 ,  B01J7/00

CPC classification number: C01B3/386 ,  B01J4/001 ,  B01J4/002 ,  B01J4/005 ,  B01J7/00 ,  B01J8/0285 ,  B01J8/065 ,  B01J8/067 ,  B01J8/1836 ,  B01J8/24 ,  B01J12/005 ,  B01J12/007 ,  B01J19/0013 ,  B01J19/0093 ,  B01J19/2415 ,  B01J19/2445 ,  B01J2208/00389 ,  B01J2208/00902 ,  B01J2208/00911 ,  B01J2219/00006 ,  B01J2219/00058 ,  B01J2219/00063 ,  B01J2219/00069 ,  B01J2219/00117 ,  B01J2219/00132 ,  B01J2219/00135 ,  B01J2219/00155 ,  B01J2219/00157 ,  B01J2219/00159 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00234 ,  B01J2219/00585 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/0844 ,  C01B2203/085 ,  C01B2203/1223 ,  C01B2203/1229 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/141

Abstract: A multi-tubular chemical reactor (400) includes an igniter (435) for the initiation of gas phase exothermic reaction within the gas phase reaction zones (409) of the tubular reactor units (408). A method of carrying out a gas phase exothermic reaction within the multi-tubular chemical reactor comprising: introducing gaseous reactants into a tubular reactor unit (408); initiating with radiant heat an exothermic reaction of the gaseous reactants within the reactor unit; and transferring heat produced by the exothermic reaction occurring within the gas phase reaction zone of the reactor unit to the gas phase reaction zone of one or more adjacent reactor units (408), thereby initiating an exothermic reaction within at least one adjacent reactor unit (408) until in such manner an exothermic reaction has been initiated in each of the plurality of spaced-apart reactor units (408).

Abstract translation: 多管式化学反应器（400）包括用于在管状反应器单元（408）的气相反应区（409）内引发气相放热反应的点火器（435）。 一种在多管式化学反应器内进行气相放热反应的方法，包括：将气态反应物引入管式反应器单元（408）中; 用辐射热引发气体反应物在反应器单元内的放热反应; 以及将由反应器单元的气相反应区内发生的放热反应产生的热量转移到一个或多个相邻的反应器单元（408）的气相反应区，从而在至少一个相邻的反应器单元（408）内引发放热反应 ），直到以这种方式在多个间隔开的反应器单元（408）中的每一个中已经开始放热反应。

公开(公告)号：US20150153746A1

公开(公告)日：2015-06-04

申请号：US14403183

申请日：2012-11-21

Applicant: AMTPacific Co., Ltd.

Inventor： Byeong Kyeom Lee ,  Kwang Hyun Kim

IPC: G05D11/00

CPC classification number: B01D3/141 ,  B01D3/008 ,  B01D53/185 ,  B01J4/005 ,  B01J4/008 ,  B01J4/02 ,  B67D7/78 ,  G05D11/003 ,  Y10T137/479 ,  Y10T137/4857 ,  Y10T137/85938 ,  Y10T137/86212 ,  Y10T137/87539 ,  Y10T137/87547 ,  Y10T137/87877

Abstract: The present invention is capable of precisely controlling a supply ratio of liquid and continuously supplying liquid at a constant rate by using partition plates for controlling the amount of liquid distribution.

Abstract translation: 本发明能够通过使用用于控制液体分配量的隔板来精确地控制液体的供给比率并以恒定速率连续供给液体。

公开(公告)号：US08969644B2

公开(公告)日：2015-03-03

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: C07C5/48 ,  F23C6/04 ,  B01J4/00 ,  C01B3/36 ,  F23L7/00

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：US20140246522A1

公开(公告)日：2014-09-04

申请号：US14278078

申请日：2014-05-15

Applicant: SOLVAY SA

Inventor： Thierry CARTAGE ,  Olivier Jacques F.J.G. BODSON ,  Marc THIJSSEN

IPC: B05B1/20

CPC classification number: B05B1/20 ,  B01D53/79 ,  B01D53/83 ,  B01D2251/2062 ,  B01D2251/606 ,  B01D2257/302 ,  B01D2257/404 ,  B01J4/004 ,  B01J4/005 ,  B01J8/004 ,  B05B1/02 ,  B05B7/1486 ,  F23J7/00 ,  F23J15/003 ,  F23J2219/60 ,  Y10T83/0481 ,  Y10T83/0596 ,  Y10T137/0318 ,  Y10T137/0391 ,  Y10T137/8593

Abstract: A device for distributing a fluid in a controlled manner, in particular for distributing a gas loaded with particles, the device comprising a pipe (1) provided with at least one inlet orifice (2) and with a series of outlet orifices (3) spread along the pipe (1) and cut in a side wall of this pipe, wherein at least one section (4) of the side wall, located downstream of at least one outlet orifice and limited by a section (5) of the edge of the outlet orifice (3), has a concave shape such that this section (5) of the edge of such outlet orifice (3) is positioned inside the pipe so that, when the device is in service, the flow direction of a fluid exiting such outlet orifice (3) and travelling along such deformed concave wall section (4) of the edge of this outlet orifice (3) is controlled by the shape of such section (5) of the edge.

Abstract translation: 一种用于以受控的方式分配流体的装置，特别是用于分配装载有颗粒的气体的装置，该装置包括设置有至少一个入口孔（2）和与一系列出口孔（3）扩散的管道（1） 沿着所述管（1）并在所述管的侧壁上切割，其中所述侧壁的至少一个部分（4）位于至少一个出口孔的下游并且被所述侧壁的边缘的部分（5）限定 出口孔（3）具有凹形形状，使得该出口孔（3）的边缘部分（5）位于管内，使得当设备使用时，流出的流体的流动方向 出口孔（3）并且沿着该出口孔（3）的边缘的这种变形的凹壁部分（4）移动，由边缘的这种部分（5）的形状来控制。

公开(公告)号：US20130037751A1

公开(公告)日：2013-02-14

申请号：US13386062

申请日：2009-07-23

Applicant: Anders Karlsson

Inventor： Anders Karlsson

IPC: B01F5/06 ,  C01B3/02 ,  B01J7/00

CPC classification number: C01B3/38 ,  B01J4/002 ,  B01J4/005 ,  B01J19/248 ,  B01J19/2485 ,  B01J19/2495 ,  B01J2219/00103 ,  B01J2219/00117 ,  B01J2219/1923 ,  B01J2219/1941 ,  B01J2219/1947 ,  B01J2219/2419 ,  B01J2219/2422 ,  C01B3/363 ,  C01B3/382 ,  C01B2203/0244 ,  C01B2203/1023 ,  C01B2203/1235 ,  C01B2203/1276 ,  F01N2240/30 ,  H01M8/0631 ,  Y02E60/50

Abstract: A mixing device for a fuel reformer for mixing at least two fluids is provided. The mixing device includes at least a first plurality of holes which is arranged along a first row, and a second plurality of holes which is arranged along a second row. The mixing device can be used in a fuel reformer for converting hydrocarbon fuel into hydrogen rich gas by auto-thermal reaction process having a, preferably cylindrically shaped and double walled, housing with two side walls forming a reaction chamber of the fuel reformer, wherein hydrocarbon fuel and an oxidizing agent are mixed by the mixing device.

Abstract translation: 提供一种用于混合至少两种流体的燃料重整器的混合装置。 混合装置包括至少沿着第一排布置的第一多个孔和沿第二排布置的第二多个孔。 该混合装置可用于燃料重整器中，用于通过具有形成燃料重整器的反应室的两个侧壁的优选圆柱形和双壁壳体的自动热反应方法将烃燃料转化为富氢气体，其中烃 燃料和氧化剂通过混合装置混合。

公开(公告)号：US20120119150A1

公开(公告)日：2012-05-17

申请号：US13292777

申请日：2011-11-09

Applicant: Dirk GROßSCHMIDT ,  Michael Russ ,  Peter Renze ,  Maximilian Vicari ,  Christian Weichert ,  Kai Rainer Ehrhardt ,  Horst Neuhauser ,  Hans Zapf ,  Michael L. Hayes

Inventor： Dirk GROßSCHMIDT ,  Michael Russ ,  Peter Renze ,  Maximilian Vicari ,  Christian Weichert ,  Kai Rainer Ehrhardt ,  Horst Neuhauser ,  Hans Zapf ,  Michael L. Hayes

IPC: C09K3/00 ,  B01J19/00

CPC classification number: B01J4/004 ,  B01J4/005 ,  B01J19/2415 ,  B01J2204/002 ,  B01J2219/00123 ,  B01J2219/00157 ,  B01J2219/00159 ,  B01J2219/00247 ,  B01J2219/1923 ,  B01J2219/1928 ,  B01J2219/1943 ,  C01B3/363 ,  C01B2203/0255 ,  C07C2/78 ,  Y02P20/129 ,  C07C11/24

Abstract: A process for preparing acetylene and synthesis gas by partial oxidation of hydrocarbons with oxygen, by first separately preheating the hydrocarbon gas and oxygen gas, and then reacting the gases and cooling the products rapidly. The reactor wall is blanketed with a purge gas stream, introduced through a plurality of feed lines. These feed lines deliver purge gas in a vector direction within a 10° angle of the main flow direction of the reactive gas stream. The purge gas is delivered at multiple stages relative to the main flow direction of the reactive gas stream, and the free cross section of the firing space available to the reactive gas stream, at the height of the feed lines of the purge gas stream, is approximately constant.

Abstract translation: 通过首先分别预热烃气体和氧气，然后使气体反应并迅速冷却产物，通过用氧气对烃进行部分氧化来制备乙炔和合成气的方法。 反应器壁用吹扫气流覆盖，通过多条进料管线引入。 这些进料管线在反应气流的主流动方向的10°角内沿向量方向传送吹扫气体。 净化气体相对于反应性气体流的主流动方向以多个阶段递送，并且在吹扫气体流的进料管线的高度处可用于反应气体流的可燃空间的自由横截面为 大致恒定。