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公开(公告)号：US08802019B2
公开(公告)日：2014-08-12
申请号：US13331362
申请日：2011-12-20
Applicant: Gerhard Olbert , Ulrike Wegerle , Grigorios Kolios , Albena Kostova , Jasmina Kessel , Alexander Weck , Alireza Rezai
Inventor： Gerhard Olbert , Ulrike Wegerle , Grigorios Kolios , Albena Kostova , Jasmina Kessel , Alexander Weck , Alireza Rezai
CPC classification number: B01J19/2485 , B01J8/0484 , B01J23/626 , B01J23/96 , B01J37/18 , B01J38/12 , B01J2219/00085 , B01J2219/182 , B01J2219/1925 , B01J2219/1943 , B01J2219/2414 , B01J2219/2416 , B01J2219/2419 , B01J2219/2422 , B01J2219/2443 , C07C5/48 , C07C2523/06 , C07C2523/42 , Y02P20/52 , Y02P20/584 , C07C11/06 , C07C11/08 , C07C11/09 , C07C11/167 , C07C15/46
Abstract: A reactor includes an essentially horizontal cylinder for carrying out an autothermal gas-phase dehydrogenation of a hydrocarbon-comprising gas stream using an oxygen-comprising gas stream to give a reaction gas mixture over a heterogeneous catalyst configured as monolith. The interior of the reactor is divided by a detachable, cylindrical or prismatic housing, which is arranged in the longitudinal direction of the reactor and is gastight in the circumferential direction, into an inner region having one or more catalytically active zones, each having a packing composed of monoliths stacked on top of one another, next to one another and behind one another and before each catalytically active zone in each case a mixing zone having solid internals are provided and into an outer region, which is supplied with an inert gas, arranged coaxially to the inner region. A heat exchanger is connected to the housing at one end of the reactor.
Abstract translation: 反应器包括基本上水平的气缸，用于使用含氧气流进行含烃气流的自热气相脱氢，以在构成为整料的多相催化剂上产生反应气体混合物。 反应器的内部由可拆卸的圆柱形或棱柱形壳体分隔，该壳体沿反应器的纵向方向布置并且在圆周方向上气密地进入具有一个或多个催化活性区域的内部区域，每个区域具有包装 由堆叠在彼此顶部，彼此相邻并且彼此相邻并且在每种情况下的每个催化活性区域之间的整体堆叠提供具有固体内部部分的混合区域并且设置在被供应有惰性气体的外部区域中，该外部区域被供应有惰性气体， 与内部区域同轴。 热交换器在反应器的一端连接到壳体。
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32.发明申请公开(公告)号：US20140087276A1
公开(公告)日：2014-03-27
申请号：US14008512
申请日：2012-10-23
Applicant: Hiromi Kita
Inventor： Hiromi Kita , Yutaka Yoshida , Kunihiro Ukai
CPC classification number: B01D53/0415 , B01D53/0438 , B01D53/0446 , B01D53/52 , B01D53/8603 , B01D2253/112 , B01D2253/1124 , B01D2255/20746 , B01D2255/20761 , B01D2255/20769 , B01D2255/20792 , B01D2256/24 , B01D2256/245 , B01D2257/304 , B01D2259/40096 , B01D2259/40098 , B01D2259/404 , B01D2259/41 , B01J8/008 , B01J8/0461 , B01J8/0484 , B01J8/0496 , B01J2208/00309 , B01J2208/00407 , B01J2208/00415 , B01J2208/00504 , B01J2208/0084 , B01J2208/00884 , B01J2208/00938 , B01J2219/00006 , C01B3/38 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/047 , C01B2203/066 , C01B2203/127 , C10G45/02 , H01M8/0618 , H01M8/0675
Abstract: A hydrodesulfurization device includes a hydro-desulfurizer configured to remove a sulfur component from a raw material; and a heater configured to heat the hydro-desulfurizer; wherein the hydro-desulfurizer includes a plurality of blocks formed by division in a circumferential direction and disposed annularly around an outer periphery of the heater; wherein the hydro-desulfurizer is configured such that the raw material having passed through inside of each of the blocks moves to its adjacent block; and wherein the hydro-desulfurizer is configured such that adjacent blocks are communicated with each other and the raw material flows in the adjacent blocks in opposite directions.
Abstract translation: 加氢脱硫装置包括：配置成从原料中除去硫成分的加氢脱硫装置; 以及加热器，其被配置为加热所述加氢脱硫器; 其特征在于，所述加氢脱硫装置具有沿圆周方向分割而形成的多个块，并且围绕所述加热器的外周环状设置; 其中所述加氢脱硫器被配置为使得已经穿过每个块的内部的原料移动到其相邻的块; 并且其中所述加氢脱硫器被构造成使得相邻的块彼此连通并且所述原料在相反的方向上在相邻的块中流动。
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公开(公告)号：US08105564B2
公开(公告)日：2012-01-31
申请号：US12088286
申请日：2006-06-19
Applicant: Raymund Sonnenschein , Peter Adler , Yuriy Kasatkin , Adolf Petrik , Leonid Schwarzmann
Inventor： Raymund Sonnenschein , Peter Adler , Yuriy Kasatkin , Adolf Petrik , Leonid Schwarzmann
CPC classification number: C01B33/043 , B01D3/009 , B01J8/0085 , B01J8/009 , B01J8/025 , B01J8/0285 , B01J8/0426 , B01J8/0438 , B01J8/0453 , B01J8/048 , B01J8/0484 , B01J8/0492 , B01J8/0496 , B01J8/065 , B01J8/067 , B01J19/30 , B01J19/32 , B01J2208/00176 , B01J2208/00212 , B01J2208/00221 , B01J2208/00247 , B01J2208/00274 , B01J2208/00283 , B01J2208/0053 , B01J2208/00884 , B01J2208/021 , B01J2219/30475 , B01J2219/32466 , B01J2219/3325 , C01B33/10773 , Y02P20/127 , Y10S203/06
Abstract: Provided is a plant for the continuous production of monosilane and tetrachlorosilane by catalytic dismutation of trichlorosilane, wherein the plant contains: a countercurrent reactor having a double wall, a catalyst bed containing a catalyst which is located in the countercurrent reactor, a condenser at the top of the countercurrent reactor, a vaporizer unit at the bottom of the countercurrent reactor, a trichlorosilane feed line for the introduction of trichlorosilane into the countercurrent reactor, a heat exchanger, with the trichlorosilane conveyed by line via the heat exchanger and preheated there by a bottom product from the vaporizer unit and, for this purpose, the bottom product is fed by line via the heat exchanger into the double wall at a level in the lower part of the countercurrent reactor and discharged from the double wall at a level in the upper part of the countercurrent reactor, a condensation unit downstream of the condenser, and a distillation column having an outlet for monosilane.
Abstract translation: 提供了通过三氯硅烷的催化歧化连续生产甲硅烷和四氯硅烷的设备，其中该装置包含：具有双壁的逆流反应器，含有位于逆流反应器中的催化剂的催化剂床，位于顶部的冷凝器 逆流反应器底部的蒸发器单元，用于将三氯硅烷引入逆流反应器的三氯硅烷进料管线，热交换器，三氯硅烷通过热交换器通过管线输送并通过底部预热 来自蒸发器单元的产品，并且为此目的，底部产物通过热交换器通过管线被供给到逆流反应堆的下部中的水平面处的双壁中，并且在双层壁的上部排出 的逆流反应器，在冷凝器下游的冷凝单元和具有外部反应器的蒸馏塔 甲硅烷。
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公开(公告)号：US20110291051A1
公开(公告)日：2011-12-01
申请号：US13102641
申请日：2011-05-06
Applicant: Frank Hershkowitz , Richard John Basile , Jeffrey William Frederick , John William Fulton , Paul F. Keusenkothen , Bryan A. Patel , Andrew Richard Szafran
Inventor： Frank Hershkowitz , Richard John Basile , Jeffrey William Frederick , John William Fulton , Paul F. Keusenkothen , Bryan A. Patel , Andrew Richard Szafran
CPC classification number: G06F19/709 , B01J8/0453 , B01J8/048 , B01J8/0484 , B01J8/0492 , C01B3/46 , C01B2203/0216 , C01B2203/0233 , C01B2203/0238 , C01B2203/0266 , C10G9/26
Abstract: A reactor with minimal dead volume especially suited to reverse-flow applications comprises: a) a reactor body; b) a first head engaged with said reactor body; c) a first conduit extending from outside said head to at least partially through said head; and d) a first valve in flow communication with said first conduit controlling fluid flow along a flow path extending from the first valve and through the reactor body. The reactor is especially suited for use in a process for rapid stream-switching of at least two streams in a reverse-flow reactor.
Abstract translation: 具有最小死体积特别适合逆流应用的反应器包括：a）反应器体; b）与所述反应器主体接合的第一头部; c）从所述头部外部至少部分地穿过所述头部延伸的第一导管; 以及d）与所述第一管道流动连通的第一阀门，其沿着沿着从所述第一阀门延伸并通过所述反应器主体的流动路径控制流体流动。 该反应器尤其适用于在逆流反应器中快速流切换至少两股物流的方法。
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公开(公告)号：US08043757B2
公开(公告)日：2011-10-25
申请号：US12344077
申请日：2008-12-24
Applicant: Ian W. Kaye , Gerry Tucker
Inventor： Ian W. Kaye , Gerry Tucker
IPC: H01M8/04
CPC classification number: H01M8/04225 , B01J8/0214 , B01J8/0221 , B01J8/0242 , B01J8/0285 , B01J8/0438 , B01J8/0484 , B01J19/0093 , B01J19/249 , B01J2208/00061 , B01J2208/00309 , B01J2208/00398 , B01J2208/00407 , B01J2208/00415 , B01J2208/00504 , B01J2208/00646 , B01J2208/00716 , B01J2219/00783 , B01J2219/00835 , B01J2219/00873 , B01J2219/00907 , B01J2219/2453 , B01J2219/2458 , B01J2219/2459 , B01J2219/2462 , B01J2219/2465 , B01J2219/2467 , B01J2219/247 , B01J2219/2475 , B01J2219/2479 , B01J2219/2481 , B01J2219/2482 , C01B3/323 , C01B3/38 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/066 , C01B2203/0805 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0844 , C01B2203/0866 , C01B2203/1223 , C01B2203/1247 , C01B2203/142 , C01B2203/82 , H01M8/0228 , H01M8/0247 , H01M8/0258 , H01M8/0267 , H01M8/04007 , H01M8/04022 , H01M8/04037 , H01M8/04067 , H01M8/04223 , H01M8/04268 , H01M8/04298 , H01M8/0435 , H01M8/04365 , H01M8/04373 , H01M8/04388 , H01M8/04425 , H01M8/04559 , H01M8/04589 , H01M8/04604 , H01M8/04619 , H01M8/04626 , H01M8/04731 , H01M8/04738 , H01M8/04753 , H01M8/04768 , H01M8/04776 , H01M8/04955 , H01M8/0618 , H01M8/0631 , H01M8/0662 , H01M2008/1095 , Y02P20/128 , Y02P70/56
Abstract: Fuel cell systems and methods are described. A method for generating electrical energy in a fuel cell receives hydrogen from a fuel processor configured to process a fuel source to produce the hydrogen, includes transporting a heating medium from the fuel processor to the fuel cell when electrical energy output by the fuel cell includes less than an electrical threshold or when temperature of a component in the fuel cell is less than a temperature threshold, heating a portion of the fuel cell, transporting hydrogen from the fuel processor to the fuel cell, detecting temperature of the component or electrical output of the fuel cell, and generating electrical energy in the fuel cell when the temperature of the component is about equal to or greater than the threshold temperature or when electrical energy output by the fuel cell is about equal to or greater than an electrical threshold.
Abstract translation: 描述燃料电池系统和方法。 用于在燃料电池中产生电能的方法从配置成处理燃料源以产生氢气的燃料处理器接收氢，包括当由燃料电池输出的电能包括较少的电力时将加热介质从燃料处理器传送到燃料电池 比电气阈值或当燃料电池中的部件的温度低于温度阈值时，加热燃料电池的一部分，将氢从燃料处理器输送到燃料电池，检测部件的温度或电气输出的温度 并且当所述部件的温度大约等于或大于所述阈值温度时或当所述燃料电池输出的电能大约等于或大于电阈值时，在所述燃料电池中产生电能。
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Patent Agency Ranking
公开(公告)号：US20090155156A1
公开(公告)日：2009-06-18
申请号：US12088286
申请日：2006-06-19
Applicant: Raymund Sonnenschein , Peter Adler , Yuriy Kasatkin , Adolf Petrik , Leonid Schwarzmann
Inventor： Raymund Sonnenschein , Peter Adler , Yuriy Kasatkin , Adolf Petrik , Leonid Schwarzmann
CPC classification number: C01B33/043 , B01D3/009 , B01J8/0085 , B01J8/009 , B01J8/025 , B01J8/0285 , B01J8/0426 , B01J8/0438 , B01J8/0453 , B01J8/048 , B01J8/0484 , B01J8/0492 , B01J8/0496 , B01J8/065 , B01J8/067 , B01J19/30 , B01J19/32 , B01J2208/00176 , B01J2208/00212 , B01J2208/00221 , B01J2208/00247 , B01J2208/00274 , B01J2208/00283 , B01J2208/0053 , B01J2208/00884 , B01J2208/021 , B01J2219/30475 , B01J2219/32466 , B01J2219/3325 , C01B33/10773 , Y02P20/127 , Y10S203/06
Abstract: The present invention relates to a plant and a process for the continuous production of monosilane and tetrachlorosilane by catalytic dismutation of trichlorosilane at an operating temperature and a pressure of from 1 to 50 bar abs. in a plant according to claim 1, in which—trichlorosilane (A) is preheated in a heat exchanger (7), and fed to the 10 countercurrent reactor (1) which is provided with catalyst (3),—product mixture formed in the countercurrent reactor (1) is at least partly condensed by means of the condenser (5) at a temperature in the range from −25 to 50° C. with the condensate flowing back into the countercurrent reactor (1),—the product phase which is not condensed in the condenser (5) is passed to the 15 condensation unit (8) which is operated at a temperature in the range from −40 to −110° C.,—the volatile product phase from the condensation unit (8) is fed to the distillation column (9) which is operated at a temperature in the range from −60 to −170° C. and monosilane (C) is discharged at the top of the distillation column (9), 20—the SiCl4-containing bottoms from the countercurrent reactor (1) are brought to a temperature in the range from 60 to 110° C. in the vaporizer unit (6) and—bottom product from the vaporizer (6) is conveyed via a heat exchanger (7) into the double wall (2) of the countercurrent reactor (1) and the SiCl4-containing product stream (B) is discharged at a level in the upper region of the reactor (1).
Abstract translation: 本发明涉及一种在操作温度和1至50巴绝对压力下通过三氯硅烷的催化分解连续生产甲硅烷和四氯硅烷的设备和方法。 在根据权利要求1的设备中，其中在热交换器（7）中预热三氯硅烷（A），并送入设有催化剂（3）的10逆流反应器（1）， - 形成在 逆流反应器（1）通过冷凝器（5）至少部分地在-25至50℃的温度范围内冷凝，冷凝物流回到逆流反应器（1）中，产物相位 在冷凝器（5）中未冷凝的冷凝单元（8）在-40至-110℃的温度范围内运行， - 来自冷凝单元（8）的挥发性产物相 进料到在-60至-70℃范围内操作的蒸馏塔（9）中，并且甲硅烷（C）在蒸馏塔（9）的顶部排出，20- SiCl 4 - 来自逆流反应器（1）的含底部物质在蒸发器单元（6）中的温度范围为60至110℃，-toto 来自蒸发器（6）的产物经由热交换器（7）输送到逆流反应器（1）的双壁（2）中，并且含SiCl4的产物流（B）在上部区域中被排出 的反应器（1）。
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公开(公告)号：US20080206117A1
公开(公告)日：2008-08-28
申请号：US12038667
申请日：2008-02-27
Applicant: Hideaki Komaki , Katsumi Takahashi
Inventor： Hideaki Komaki , Katsumi Takahashi
CPC classification number: H01M8/0612 , B01J8/0438 , B01J8/048 , B01J8/0484 , B01J8/0492 , B01J8/0496 , B01J8/065 , B01J8/067 , B01J2208/00212 , B01J2208/00309 , B01J2208/00398 , B01J2208/0053 , B01J2208/00548 , B01J2208/00716 , B01J2219/00117 , B01J2219/00159 , B01J2219/1923 , C01B3/323 , C01B3/382 , C01B3/384 , C01B3/583 , C01B2203/00 , C01B2203/0244 , C01B2203/0283 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0816 , C01B2203/0833 , C01B2203/0844 , C01B2203/0866 , C01B2203/0883 , C01B2203/1023 , C01B2203/1076 , C01B2203/1223 , C01B2203/1276 , C01B2203/1288 , C01B2203/141 , C01B2203/142 , C01B2203/143 , C01B2203/146 , C01B2203/1604 , C01B2203/169 , C01B2203/82 , H01M8/0631 , H01M8/0662
Abstract: A gas mixture containing a fuel, water and air is supplied to one end of a reforming room, and a reformed gas containing hydrogen is discharged from the other end thereof. Two or more such reforming units are connected in series, and the upstream part of each reforming room is filled with a first catalyst which catalyzes a partial oxidation reaction in an oxygen-rich environment, and the downstream part is filled with a second catalyst which performs the reforming reaction. The gas mixture which has been heated in a heating unit passes through a distribution tube and is distributed evenly to the reforming units. The reforming room is composed of a reforming tube in which a reforming catalyst is charged, or two or more such reforming tubes, parallel to each other. After being reformed the high-temperature reformed gas is passed around the reforming tubes, and fed back to a manifold.
Abstract translation: 将包含燃料，水和空气的气体混合物供给到重整室的一端，并且从其另一端排出含有氢的重整气体。 两个以上的这样的重整单元串联连接，并且每个重整室的上游部分填充有在富氧环境中催化部分氧化反应的第一催化剂，并且下游部分填充有执行的第二催化剂 改性反应。 在加热单元中加热的气体混合物通过分配管并均匀地分配到重整单元。 重整室由其中装有重整催化剂的重整管或彼此平行的两个或更多个这样的重整管组成。 改性后，将高温重整气体绕过重整管，并送回歧管。
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公开(公告)号：US20080118796A1
公开(公告)日：2008-05-22
申请号：US11835747
申请日：2007-08-08
Applicant: Jennifer Brantley , Kenneth Newell , David Sopchak , Ian W. Kaye , Jesse Thompson , Arpad Somogyvari
Inventor： Jennifer Brantley , Kenneth Newell , David Sopchak , Ian W. Kaye , Jesse Thompson , Arpad Somogyvari
IPC: H01M8/18
CPC classification number: H01M8/04022 , B01J8/0449 , B01J8/0484 , B01J8/0492 , B01J8/0496 , B01J8/06 , B01J8/065 , B01J8/067 , B01J19/0093 , B01J19/2495 , B01J2208/00309 , B01J2208/00504 , B01J2208/0053 , B01J2208/00672 , B01J2219/00788 , B01J2219/00835 , B01J2219/00846 , B01J2219/0086 , B01J2219/00869 , B01J2219/00873 , B01J2219/00891 , C01B3/323 , C01B2203/0233 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/1017 , C01B2203/1023 , C01B2203/1029 , C01B2203/1064 , C01B2203/1076 , C01B2203/1223 , C01B2203/1288 , C01B2203/1614 , H01M8/0631 , Y02P20/128 , Y02P70/56 , Y10T29/49345
Abstract: In one embodiment, a fuel processor for use in a fuel cell system, may have a bottom plate, having a regenerator having a first inlet to receive an air flow, a burner flow chamber within the regenerator, the burner flow chamber having a second inlet to receive the air flow from the regenerator, and a reformer flow chamber positioned between the regenerator and the burner flow chamber, the reformer flow chamber having a third inlet to receive the air flow from the burner chamber, wherein the burner flow chamber and the reformer flow chamber is formed of a monolithic structure having an elongated, rounded baffle in the center of the monolithic structure. The fuel processor may also have a top plate coupled to the bottom plate to enclose the fuel processor, the top plate having a top surface and a bottom surface.
Abstract translation: 在一个实施例中，用于燃料电池系统的燃料处理器可以具有底板，具有一个再生器，该再生器具有用于接收气流的第一入口，再生器内的燃烧器流动室，燃烧器流动室具有第二入口 为了接收来自再生器的空气流，以及位于再生器和燃烧器流动室之间的重整器流动室，重整器流动室具有第三入口以接收来自燃烧器室的空气流，其中燃烧器流动室和重整器 流动室由在整体结构的中心具有细长的圆形挡板的整体结构形成。 燃料处理器还可以具有联接到底板以封闭燃料处理器的顶板，顶板具有顶表面和底表面。
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公开(公告)号：US07014822B1
公开(公告)日：2006-03-21
申请号：US09868222
申请日：1999-12-10
Applicant: Norihisa Shinke , Kazuhiro Hirai , Seisaku Higashiguchi
Inventor： Norihisa Shinke , Kazuhiro Hirai , Seisaku Higashiguchi
IPC: B01J10/00
CPC classification number: H01M8/0631 , B01J8/0484 , B01J8/0492 , B01J8/0496 , B01J19/2485 , B01J19/249 , B01J2208/00309 , B01J2208/00495 , B01J2208/0053 , B01J2208/022 , B01J2219/00006 , B01J2219/0002 , B01J2219/00117 , B01J2219/00155 , B01J2219/00159 , B01J2219/00777 , B01J2219/2453 , B01J2219/2462 , B01J2219/2474 , B01J2219/2477 , B01J2219/2481 , B01J2219/2493 , B01J2219/2496 , C01B3/384 , C01B3/48 , C01B3/583 , C01B2203/0233 , C01B2203/0294 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0844 , C01B2203/0866 , C01B2203/0883 , C01B2203/1011 , C01B2203/1047 , C01B2203/1052 , C01B2203/1064 , C01B2203/1076 , C01B2203/1082 , C01B2203/1229 , C01B2203/1241 , C01B2203/127 , C01B2203/1276 , C01B2203/1288 , C01B2203/82 , C10K3/02 , C10K3/04
Abstract: A fluid processing apparatus having a plurality of processing spaces (S) includes a plurality of containers (B) juxtaposed in a direction to each other forming processing spaces (S) respectively therein. Pressing means (H) is provided for pressing the containers (B) as juxtaposed from opposed sides thereof in the juxtaposing direction of the containers. Each container (B) includes a pair of container-forming members (41a) disposed in the juxtaposing direction and having peripheral portions thereofjoined and welded to each other. At least one of the pair of container-forming members (41a) is in the form of a dish-like member having a peripheral portion used as a joining margin and a bulging central portion.
Abstract translation: 具有多个处理空间（S）的流体处理装置包括分别在彼此形成处理空间（S）的方向上并列的多个容器（B）。 提供压制装置（H），用于将容器（B）从容器的并列方向上的相对侧并排地挤压。 每个容器（B）包括一对以并置方向设置的容器形成构件（41a），并且其周边部分彼此结合并焊接。 一对容器形成构件（41a）中的至少一个是具有用作接合边缘的周边部分和凸起中心部分的盘状构件的形式。
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公开(公告)号：US20060000141A1
公开(公告)日：2006-01-05
申请号：US10531715
申请日：2003-10-17
Applicant: Takeshi Kuwabara , Yoshio Tomizawa , Yasushi Yoshino , Jun Ono , Shigeki Kobayashi , Saburo Maruko
Inventor： Takeshi Kuwabara , Yoshio Tomizawa , Yasushi Yoshino , Jun Ono , Shigeki Kobayashi , Saburo Maruko
IPC: B01J8/00
CPC classification number: B01J4/002 , B01J8/0484 , B01J19/26 , B01J2208/00504 , B01J2219/00006 , C01B3/38 , C01B3/382 , C01B2203/0244 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0844 , C01B2203/0894 , C01B2203/1276 , C01B2203/142 , C01B2203/82 , C01B2203/84 , H01M8/0612 , Y02P20/129
Abstract: The system is a self-oxidation internal heating steam reforming system for conducting self-oxidation of a raw material gas under the presence of oxygen and conducting steam reforming to generate a hydrogen-rich reformed gas. The system includes a steam generator including a combustion section for combusting an air-fuel mixture obtained by mixing a combustion air with a fuel, thereby heating water using a combustion gas generated in the combustion section to generate hydrogen; a first sucking-mixer for sucking the raw material gas into a steam stream coming from the steam generator to obtain a raw material-steam mixture; and a reformer for oxidizing the raw material gas in the raw material-steam mixture by an oxygen-containing gas supplied from outside, thereby conducting steam reforming of the raw material gas using the reaction heat of the oxidation to generate a hydrogen-rich reformed gas.
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