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    HYDROGEN GENERATOR AND FUEL CELL POWER GENERATOR
    91.
    发明申请
    HYDROGEN GENERATOR AND FUEL CELL POWER GENERATOR 有权
    氢发电机和燃料电池发电机

    公开(公告)号：US20110065011A1

    公开(公告)日：2011-03-17

    申请号：US12992338

    申请日：2009-05-13

    Applicant: Akira Maenishi ,  Yuuji Mukai ,  Hiroki Fujioka

    Inventor： Akira Maenishi ,  Yuuji Mukai ,  Hiroki Fujioka

    IPC: H01M8/06 ,  B01J8/02

    CPC classification number: H01M8/0612 ,  B01J8/0469 ,  B01J8/0492 ,  B01J8/0496 ,  B01J2208/00203 ,  B01J2208/00221 ,  B01J2208/00504 ,  B01J2208/0053 ,  C01B3/384 ,  C01B3/48 ,  C01B3/583 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/1288 ,  C01B2203/1294 ,  C01B2203/169 ,  C01B2203/1695 ,  H01M8/0631

    Abstract: There is provided a hydrogen generator that prevents supply of droplets to a reforming catalyst layer and that exhibits stable performance.The hydrogen generator includes a water evaporation unit 7 to which a raw gas and water is supplied; a reforming catalyst layer 9 to which a gas mixture is supplied from the water evaporation unit 7; a burner 4 configured to mix and combust a fuel gas with air; a combustion exhaust gas flow channel 16 which is provided on an inner side of the water evaporation unit 7 and through which the combustion exhaust gas flows; and a conversion catalyst layer 10 which is disposed on an outer side of the water evaporation unit 7 and to which a reformed gas is supplied. The water evaporation unit 7 includes double cylinders 100 and 101 and a helical round bar 18 sandwiched between the cylinders 100 and 101, and a pitch of the helical round bar 18 in a downstream portion of the water evaporation unit 7 is made smaller than a pitch of the helical round bar 18 in a portion of the water evaporation unit 7 except the downstream portion thereof.

    Abstract translation: 提供了一种氢发生器，其防止液滴向重整催化剂层供应并且表现出稳定的性能。 氢发生器包括供水原料气体和水的水蒸发单元7; 从水蒸发单元7供给气体混合物的重整催化剂层9; 燃烧器4，其构造成将燃料气体与空气混合并燃烧; 燃烧废气流动通道16，其设置在水蒸发单元7的内侧并且燃烧废气流过该燃烧废气流动通道16; 以及设置在水蒸发单元7的外侧并且供给重整气体的转化催化剂层10。 水蒸发单元7包括双缸100和101以及夹在气缸100和101之间的螺旋形圆棒18，并且水蒸发单元7的下游部分中的螺旋形圆棒18的间距小于间距 在水蒸发单元7的除了其下游部分之外的部分中的螺旋形圆棒18。

    Maximum reaction rate converter for exothermic reactions
    92.
    发明授权
    Maximum reaction rate converter for exothermic reactions 有权
    用于放热反应的最大反应速率转化器

    公开(公告)号：US07842254B2

    公开(公告)日：2010-11-30

    申请号：US11932140

    申请日：2007-10-31

    Applicant: Shashi P. Singh ,  David P. Mann ,  Anant Pisut

    Inventor： Shashi P. Singh ,  David P. Mann ,  Anant Pisut

    IPC: B01J8/04

    CPC classification number: C01C1/0423 ,  B01J8/008 ,  B01J8/067 ,  B01J23/462 ,  B01J2208/00212 ,  B01J2208/00221 ,  B01J2208/00513 ,  B01J2208/00548 ,  B01J2219/00238 ,  C01C1/0441 ,  C01C1/0482 ,  Y02E60/364 ,  Y02P20/52

    Abstract: An ammonia converter is disclosed. The converter can alter the conversion of ammonia by controlling the reaction temperature of the exothermic reaction along the length of the reactor to parallel the equilibrium curve for the desired product. The converter can comprise a shell 101 and internal catalyst tubes 109. The feed gas stream enters the reactor, flows through the shell 101, and is heated by indirect heat exchange with the catalyst tubes 109. The catalyst tubes 109 comprise reactive zones 122 having catalyst and reaction limited zones 124 that can comprise inert devices that function to both separate the reactive zones, increase heat transfer area, and reduce the temperature of the reaction mixture as the effluent passes through the catalyst tube 109.

    Abstract translation: 公开了一种氨转化器。 转化器可以通过控制沿着反应器长度的放热反应的反应温度来平行所需产物的平衡曲线来改变氨的转化率。 转化器可以包括壳体101和内部催化剂管109.进料气体流进入反应器，流过壳体101，并通过与催化剂管109的间接热交换而加热。催化剂管109包含具有催化剂的反应区域122 和反应限制区124，其可以包括用于分离反应区的惰性装置，增加传热面积，并且当流出物通过催化剂管109时降低反应混合物的温度。

    Fixed-bed catalytic reactor
    94.
    发明授权
    Fixed-bed catalytic reactor 有权
    固定床催化反应器

    公开(公告)号：US07780925B2

    公开(公告)日：2010-08-24

    申请号：US11572403

    申请日：2005-07-22

    Applicant: Ermanno Filippi ,  Enrico Rizzi ,  Mirco Tarozzo

    Inventor： Ermanno Filippi ,  Enrico Rizzi ,  Mirco Tarozzo

    IPC: B01J8/04 ,  B01J10/00

    CPC classification number: B01J8/0415 ,  B01J8/0496 ,  B01J2208/0015 ,  B01J2208/00221 ,  B01J2208/00548 ,  B01J2208/00814 ,  B01J2208/00884 ,  F28D7/16 ,  F28D9/0006 ,  F28D9/0018

    Abstract: A radial chemical reactor (10, 110, 210, 310) for catalytic reactions comprising: a substantially cylindrical shell (12), a first catalytic bed (18) having a substantially ring shaped cross-section, coaxially supported in said shell (12) and having a reagent gases inlet side (20) and a reaction mixture outlet side (21); a plurality of heat exchangers (22) supported and distributed in a substantially ring-shaped respective portion of said first catalytic bed (18); at least one second catalytic bed (28) with a substantially ring-shaped cross-section, supported in said shell (12) coaxially to said first bed (18) and at a predetermined distance from said first bed, said second catalytic bed (28) having a reaction mixture inlet side (30) and a reaction gaseous products outlet side (31); a plurality of heat exchangers (32) supported and distributed in a substantially ring-shaped respective portion of said second catalytic bed (28).

    Abstract translation: 一种用于催化反应的径向化学反应器（10,110,210,310），包括：基本上圆柱形的壳体（12），具有基本环形横截面的第一催化床（18），同轴地支撑在所述壳体（12）中， 并具有试剂气体入口侧（20）和反应混合物出口侧（21）; 多个热交换器（22），其被支撑并分布在所述第一催化床（18）的基本上环形的相应部分中; 至少一个具有大致环形横截面的第二催化床（28），与所述第一床（18）同轴地支撑在所述外壳（12）中并且与所述第一床预定距离，所述第二催化床（28 ）具有反应混合物入口侧（30）和反应气体产物出口侧（31）; 多个热交换器（32），其被支撑并分布在所述第二催化床（28）的基本上环形的相应部分中。

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