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    Integrated type reactor, method of making the same and method of conducting simultaneous exothermic and endothermic reactions
    2.
    发明专利
    Integrated type reactor, method of making the same and method of conducting simultaneous exothermic and endothermic reactions 有权
    一体化型反应器及其制备方法及其导致同时发生的和内毒素反应的方法

    公开(公告)号：JP2010012466A

    公开(公告)日：2010-01-21

    申请号：JP2009171869

    申请日：2009-07-23

    Applicant: Battelle Memorial Inst ,  バッテル メモリアル インスティテュートBattelle Memorial Institute

    Inventor： TONKOVICH ANNA LEE Y ,  PERRY STEVEN T ,  FITZGERALD SEAN P ,  ROBERTS GARY L

    IPC: B01J19/00 ,  B01J20060101 ,  C01B3/38

    Abstract: PROBLEM TO BE SOLVED: To provide a method and a reactor capable of reducing heat loss when supplying heat to an endothermic reaction conducted in a micro reactor. SOLUTION: Heat is supplied to an endothermic reaction chamber with small heat loss by circulating an endothermic reaction composition to an endothermic reaction chamber 15 which contains an endothermic reaction catalyst 17, supplying fuel and oxygen to an exothermic reaction chamber 12 which is arranged in vicinity of the endothermic reaction chamber 15 via a chamber wall with heat conductivity, burning fuel by the action of endothermic reaction catalysts 14, 16 which are included in the endothermic reaction chamber, and transporting generated heat to the endothermic reaction chamber through the chamber wall with heat conductivity. COPYRIGHT: (C)2010,JPO&INPIT

    Abstract translation: 要解决的问题：提供一种能够在向微反应器中进行的吸热反应供热时减少热损失的方法和反应器。 解决方案：通过将吸热反应组合物循环到含有吸热反应催化剂17的吸热反应室15，将吸热反应室供给到放热反应室12中，将热量供给到吸热反应室，该吸热反应室15配置在放热反应室12中，该放热反应催化剂17被布置 通过具有导热性的室壁在吸热反应室15附近，通过吸热反应室中包含的吸热反应催化剂14,16的作用燃烧燃料，并且通过室壁将产生的热量输送到吸热反应室 具有导热性。 版权所有（C）2010，JPO＆INPIT

    5.
    发明专利
    未知

    公开(公告)号：AT556769T

    公开(公告)日：2012-05-15

    申请号：AT05007860

    申请日：2000-08-17

    Applicant: BATTELLE MEMORIAL INSTITUTE

    Inventor： TONKOVICH ANNA LEE Y ,  WANG YONG ,  FITZGERALD SEAN P ,  MARCO JENNIFER L ,  ROBERTS GARY L ,  VANDERWIEL DAVID P ,  WEGENG ROBERT S

    IPC: B01D53/22 ,  B01J19/00 ,  B01D71/02 ,  B01J12/00 ,  B01J19/24 ,  B01J23/60 ,  B01J37/02 ,  B01J37/03 ,  C01B3/38 ,  C01B3/48 ,  C01B3/50 ,  C01B3/56 ,  C01B13/02 ,  H01M8/06

    Abstract: The present invention relates to methods for gas phase reactant catalytic reactions. In particular the present invention relates to a method of hydrocarbon steam reforming, comprising: passing a reactant stream comprising steam and hydrocarbon into at least one reaction chamber; wherein the reaction chamber has an internal volume having dimensions of chamber height, chamber width and chamber length; wherein the chamber has a length of greater than 1 cm; wherein the chamber height or chamber width is 2 mm or less; wherein the reaction chamber is in thermal contact through a reaction chamber wall with an exothermic reaction chamber; transferring heat from the exothermic reaction chamber to the reaction chamber through the reaction chamber wall at a rate such that heat flux between the reaction chamber and the exothermic reaction chamber is at least 0.6 W per cubic centimeter of the reaction chamber wall; wherein the method is controlled under conditions such that the hydrocarbon has a contact time of less than 300 ms; wherein the reactant stream is converted to a product stream; and wherein at least 70% of the equilibrium conversion of the hydrocarbon entering the reaction chamber is converted to hydrogen, carbon monoxide or carbon dioxide.

    Método para reformado con vapor de hidrocarburos
    9.
    发明专利
    Método para reformado con vapor de hidrocarburos 未知

    公开(公告)号：ES2386506T3

    公开(公告)日：2012-08-22

    申请号：ES05007860

    申请日：2000-08-17

    Applicant: BATTELLE MEMORIAL INSTITUTE

    Inventor： TONKOVICH ANNA LEE Y ,  WANG YONG ,  FITZGERALD SEAN P ,  MARCO JENNIFER L ,  ROBERTS GARY L ,  VANDERWIEL DAVID P ,  WEGENG ROBERT S

    IPC: B01D53/22 ,  B01J19/00 ,  B01D71/02 ,  B01J12/00 ,  B01J19/24 ,  B01J23/60 ,  B01J37/02 ,  B01J37/03 ,  C01B3/38 ,  C01B3/48 ,  C01B3/50 ,  C01B3/56 ,  C01B13/02 ,  H01M8/06

    Abstract: Método de reformado con vapor de hidrocarburo, comprendiendo:paso de una corriente de reactivos comprendiendo vapor e hidrocarburo en al menos una cámara de reacción;donde la cámara de reacción tiene un volumen interno con dimensiones de altura de cámara, anchura decámara y longitud de cámara;donde la cámara tiene una longitud mayor de 1 cm;donde la altura de cámara o anchura de cámara es de 2 mm o menos;donde la cámara de reacción tiene una entrada y una salida con una trayectoria de flujo en masa contiguodesde la entrada hasta la salida;donde la cámara de reacción está en contacto térmico a través de una pared de cámara de reacción con unacámara de reacción exotérmica;transferencia de calor desde la cámara de reacción exotérmica hasta la cámara de reacción a través de lapared de cámara de reacción;donde el método es controlado bajo condiciones de manera que el hidrocarburo tiene un tiempo de contactoinferior a 300 ms;donde la corriente de reactivos se convierte en un flujo de producto; ydonde al menos 70% de la conversión de equilibrio del hidrocarburo entrando en la cámara de reacción seconvierte a hidrógeno, monóxido de carbono o dióxido de carbono.

    10.
    发明专利
    未知

    公开(公告)号：NO330178B1

    公开(公告)日：2011-02-28

    申请号：NO20084211

    申请日：2008-10-08

    Applicant: BATTELLE MEMORIAL INSTITUTE

    Inventor： WEGENG ROBERT S ,  ROBERTS GARY L ,  WANG YONG ,  VANDERWIEL DAVID P ,  TONKOVICH ANNA LEE Y ,  FITZGERALD SEAN P ,  MARCO JENNIFER L

    IPC: B01D53/22 ,  B01J12/00 ,  B01D71/02 ,  B01J19/00 ,  B01J19/24 ,  B01J23/60 ,  B01J37/02 ,  B01J37/03 ,  C01B3/38 ,  C01B3/48 ,  C01B3/50 ,  C01B3/56 ,  C01B13/02 ,  H01M8/06

    Abstract: The present invention relates to methods for gas phase reactant catalytic reactions. In particular the present invention relates to a method of hydrocarbon steam reforming, comprising: passing a reactant stream comprising steam and hydrocarbon into at least one reaction chamber; wherein the reaction chamber has an internal volume having dimensions of chamber height, chamber width and chamber length; wherein the chamber has a length of greater than 1 cm; wherein the chamber height or chamber width is 2 mm or less; wherein the reaction chamber is in thermal contact through a reaction chamber wall with an exothermic reaction chamber; transferring heat from the exothermic reaction chamber to the reaction chamber through the reaction chamber wall at a rate such that heat flux between the reaction chamber and the exothermic reaction chamber is at least 0.6 W per cubic centimeter of the reaction chamber wall; wherein the method is controlled under conditions such that the hydrocarbon has a contact time of less than 300 ms; wherein the reactant stream is converted to a product stream; and wherein at least 70% of the equilibrium conversion of the hydrocarbon entering the reaction chamber is converted to hydrogen, carbon monoxide or carbon dioxide.

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