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    HYDROGEN GENERATOR AND FUEL CELL POWER GENERATION SYSTEM
    83.
    发明申请
    HYDROGEN GENERATOR AND FUEL CELL POWER GENERATION SYSTEM 有权
    氢发电机和燃料电池发电系统

    公开(公告)号：US20120321971A1

    公开(公告)日：2012-12-20

    申请号：US13580310

    申请日：2011-03-02

    Applicant: Akira Maenishi ,  Yuji Mukai ,  Youji Kawaguchi ,  Masataka Ozeki

    Inventor： Akira Maenishi ,  Yuji Mukai ,  Youji Kawaguchi ,  Masataka Ozeki

    IPC: H01M8/06 ,  B01J19/00

    CPC classification number: H01M8/0612 ,  B01J8/0469 ,  B01J8/0492 ,  B01J8/0496 ,  B01J2208/00203 ,  B01J2208/00221 ,  B01J2208/00504 ,  B01J2208/0053 ,  C01B3/384 ,  C01B3/48 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/047 ,  C01B2203/0811 ,  C01B2203/1288 ,  H01M8/04089 ,  H01M8/0668 ,  Y02E60/50

    Abstract: A hydrogen generation apparatus 200 includes: an evaporating part 7; a reforming reaction part 9A connected to the downstream side of the evaporating part; a carbon monoxide reducing part 20 provided downstream from the reforming reaction part; and a gas guiding part 21 disposed between the reforming reaction part and the carbon monoxide reducing part and configured to guide a gas that has passed through the reforming reaction part to the carbon monoxide reducing part. The evaporating part and the carbon monoxide reducing part are arranged to be adjacent to each other such that, at least, a part of the evaporating part and a part of the carbon monoxide reducing part are heat exchangeable with each other. The evaporating part is configured such that a heat exchange amount at a portion of the evaporating part, the portion corresponding to the carbon monoxide reducing part, is less than a heat exchange amount at a portion of the evaporating part, the portion not corresponding to the carbon monoxide reducing part.

    Abstract translation: 氢产生装置200包括：蒸发部7; 与蒸发部的下游侧连接的重整反应部9A; 设置在重整反应部下游的一氧化碳还原部20; 以及设置在重整反应部和一氧化碳减少部之间并构成为将通过重整反应部的气体导向一氧化碳还原部的气体引导部21。 蒸发部分和一氧化碳减少部分被布置成彼此相邻，使得至少一部分蒸发部分和一氧化碳减少部分的一部分彼此可热交换。 蒸发部构成为，蒸发部的与一氧化碳减少部对应的部分的热交换量小于蒸发部的一部分的热交换量，该部分不对应于 一氧化碳减少部分。

    Flow reactors for chemical conversions with heterogeneous catalysts
    84.
    发明授权
    Flow reactors for chemical conversions with heterogeneous catalysts 失效
    用多相催化剂进行化学转化的流动反应器

    公开(公告)号：US08232415B2

    公开(公告)日：2012-07-31

    申请号：US12929624

    申请日：2011-02-04

    Applicant: Hassan Taheri ,  Curtis D. Dickinson ,  Paul A. Jacobson

    Inventor： Hassan Taheri ,  Curtis D. Dickinson ,  Paul A. Jacobson

    IPC: C07D307/60

    CPC classification number: F28F13/08 ,  B01J8/067 ,  B01J2208/00212 ,  B01J2208/00221 ,  B01J2208/00707 ,  C07C51/215 ,  C07C51/25 ,  C07C51/252 ,  C07C51/255 ,  F28D7/1646 ,  Y02P20/582 ,  C07C57/145 ,  C07C57/04

    Abstract: Improved apparatus for use in process systems which include exothermic chemical conversions of organic compounds to value added products is disclosed, more particularly, flow reactors for exothermic chemical conversions using a fixed heterogeneous catalyst with means for control of the exotherm. Flow reactors of the invention comprise a plurality of walled conduits each having an outer surface disposed for contact with a heat-transfer medium, an inlet distribution manifold adapted for flow communication with a downstream manifold through channels formed by heterogeneous catalytic material disposed within each conduit during operation in a sequence of zones for catalyst having the same or different length along the longitudinal coordinate of the conduit and within each zone essentially uniform cross-section of the conduit measured in a plane perpendicular to the longitudinal coordinate thereby defining volume of the zone, and the sequence of zones comprising of at least two zones such that each downstream zone has a larger or smaller cross-section than the contiguous upstream zone. Another aspect of the invention includes processes which use such flow reactors, for example the continuous manufacture of maleic anhydride.

    Abstract translation: 公开了一种改进的用于工艺系统的装置，其包括有机化合物对增值产物的放热化学转化，更具体地，涉及使用具有用于控制放热的装置的固定多相催化剂的放热化学转化的流动反应器。 本发明的流动反应器包括多个壁管道，每个管道具有被设置用于与传热介质接触的外表面，适于通过设置在每个管道内的非均相催化材料形成的通道与下游歧管流动连通的入口分配歧管 沿着导管的纵向坐标具有相同或不同长度的催化剂区域序列的操作，并且在每个区域内，在垂直于纵向坐标的平面中测量的管道基本上均匀的横截面，从而限定区域的体积，以及 所述区域序列包括至少两个区域，使得每个下游区域具有比所述连续上游区域更大或更小的横截面。 本发明的另一方面包括使用这种流动反应器的方法，例如连续制造马来酸酐。

    Baffle structure improving heat transfer efficiency of reactor or heat exchanger
    87.
    发明授权
    Baffle structure improving heat transfer efficiency of reactor or heat exchanger 有权
    挡板结构提高了反应堆或热交换器的传热效率

    公开(公告)号：US08043583B2

    公开(公告)日：2011-10-25

    申请号：US11700056

    申请日：2007-01-31

    Applicant: Sang Baek Shin ,  Sang Phil Han ,  Ye Hoon Im ,  Young Bae Kim ,  Jung Hoon Chang ,  Sang Oeb Na ,  Won Am Lee

    Inventor： Sang Baek Shin ,  Sang Phil Han ,  Ye Hoon Im ,  Young Bae Kim ,  Jung Hoon Chang ,  Sang Oeb Na ,  Won Am Lee

    IPC: B01J8/06 ,  F28F9/00 ,  C07C51/16

    CPC classification number: F28F9/22 ,  B01J8/008 ,  B01J8/067 ,  B01J2208/00221 ,  F28D7/0091

    Abstract: Disclosed is a shell-and-tube reactor or heat exchanger, which alternately comprises a doughnut-type baffle plate and a first disc-type baffle plate in order to increase heat transfer efficiency. In the reactor or heat exchanger, a second disc-type baffle plate is placed in an empty space inside of the doughnut-type baffle plate, and some tubes, through the inside of which a first object for heat transfer with a heat transfer medium, are present in a region inside of the doughnut-type baffle plate and outside of the second disc-type baffle plate. Also disclosed is a method for producing an oxide, comprising: using said reactor or heat exchanger, and causing a catalytic vapor-phase oxidation reaction in the tubes, through the inside of which the first object for heat transfer with the heat transfer medium is passed.

    Abstract translation: 公开了一种管壳式反应器或热交换器，其交替地包括环形挡板和第一盘式挡板，以提高传热效率。 在反应器或热交换器中，第二盘式挡板放置在环形挡板的内部的空的空间中，并且一些管通过其内部具有传热介质传热的第一物体， 存在于环形挡板的内侧的区域和第二盘状挡板的外侧。 还公开了一种生产氧化物的方法，包括：使用所述反应器或热交换器，并在管中引起催化气相氧化反应，通过其内部，传热介质的第一物体通过 。

    FLUID COOLED REFORMER AND METHOD FOR COOLING A REFORMER
    88.
    发明申请
    FLUID COOLED REFORMER AND METHOD FOR COOLING A REFORMER 有权
    流体冷却改性剂和冷却改性剂的方法

    公开(公告)号：US20110243805A1

    公开(公告)日：2011-10-06

    申请号：US12749985

    申请日：2010-03-30

    Applicant: Jonathan Dwight Berry ,  Hasan Karim ,  Abdul Rafey Khan

    Inventor： Jonathan Dwight Berry ,  Hasan Karim ,  Abdul Rafey Khan

    IPC: F25B29/00 ,  F28D21/00

    CPC classification number: C01B3/386 ,  B01J8/0278 ,  B01J2208/00176 ,  B01J2208/00221 ,  B01J2208/00371 ,  B01J2208/0053 ,  B01J2208/00849 ,  C01B2203/0261 ,  C01B2203/0877 ,  C01B2203/0883 ,  C01B2203/84 ,  C10J3/466 ,  C10J2200/09 ,  C10J2300/0959 ,  C10J2300/0989 ,  C10J2300/1861 ,  C10J2300/1884 ,  F23C2900/03002

    Abstract: The present subject matter discloses a fluid cooled reformer for gas turbine systems and a method for cooling both a fuel reformer and a heated reformate stream produced by such fuel reformer. The fluid cooled reformer may include a pressure vessel and a reactor assembly disposed within the pressure vessel. The reactor assembly may include a reactor and may be configured to receive and reform an oxygen/fuel mixture to produce a heated reformate stream. Additionally, the fluid cooled reformer may include an inlet configured to direct a fluid stream into the pressure vessel. At least a portion of the fluid stream may be used to cool the reactor assembly. A reformate cooling section may be disposed downstream of the reactor of the reactor assembly and may be configured to cool the heated reformate stream.

    Abstract translation: 本发明公开了一种用于燃气轮机系统的流体冷却重整器和用于冷却由这种燃料重整器产生的燃料重整器和加热的重整产品流的方法。 流体冷却的重整器可以包括压力容器和设置在压力容器内的反应器组件。 反应器组件可以包括反应器，并且可以被配置为接收和改造氧/燃料混合物以产生加热的重整产物流。 此外，流体冷却的重整器可以包括构造成将流体流引导到压力容器中的入口。 流体流的至少一部分可用于冷却反应器组件。 重整物冷却段可以设置在反应器组件的反应器的下游，并且可以被配置为冷却加热的重整产物流。

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