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61. 发明申请

WO2004022214A2 MULTI-PORT AUTOTHERMAL REFORMER 审中-公开
标题翻译：多端口自动转换器
公开(公告)号：WO2004022214A2
公开(公告)日：2004-03-18
申请号：PCT/US2003/027578
申请日：2003-09-03
申请人： GENERAL MOTORS CORPORATION
发明人： PETTIT, William, H. , SENNOUN, Mohammed, E., H. , VOECKS, Gerald, E.
IPC分类号： B01J
CPC分类号： B01J8/001 , B01J8/025 , B01J8/0278 , B01J2208/0053 , B01J2208/00716 , C01B3/382 , C01B2203/00 , C01B2203/0244 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0844 , C01B2203/0883 , C01B2203/0894 , C01B2203/1276 , C01B2203/1288 , C01B2203/1604 , C01B2203/1619 , C01B2203/169 , C01B2203/82 , Y02P20/128
摘要： An autothermal reformer is provided for a fuel cell system utilizing one volume and a plurality of inlets for both start-up and normal operation. In startup mode, thermal combustion is employed for heating the catalyst reformation section of the reformer. Two inlets are used to feed air and fuel into the system, which are mixed and ignited in the common volume. Once the catalyst has reached light-off temperature, a second set of inlets provide air, steam and fuel into the common volume. The mixture then passes into the catalytic reformation system.
摘要翻译：为燃料电池系统提供一种自热重整器，该燃料电池系统利用一个体积和多个用于启动和正常运行的入口。在启动模式下，采用热燃烧来加热重整器的催化剂重整段。两个入口用于将空气和燃料进入系统，这些入口在共同体积中混合和点燃。一旦催化剂达到关闭温度，第二组入口将空气，蒸汽和燃料提供到共用体积中。然后混合物进入催化重整体系。

62. 发明申请

WO2003092879A1 STAGED AIR AUTOTHERMAL REFORMER FOR IMPROVED STARTUP AND OPERATION 审中-公开
标题翻译：用于改进启动和操作的标准空气自动翻新机
公开(公告)号：WO2003092879A1
公开(公告)日：2003-11-13
申请号：PCT/US2003/011550
申请日：2003-04-16
申请人： GENERAL MOTORS CORPORATION , ROBB, Gary, M.
发明人： ROBB, Gary, M.
IPC分类号： B01J8/02
CPC分类号： C01B3/382 , B01J8/0438 , B01J8/0492 , B01J2208/00061 , B01J2208/00548 , B01J2208/00628 , B01J2208/00707 , B01J2208/00716 , C01B2203/0244 , C01B2203/0844 , C01B2203/1241 , C01B2203/143 , C01B2203/1604 , C01B2203/1619 , C01B2203/169 , C01B2203/82
摘要： An autothermal reformer (48) comprises a first stage (50) that selectively receives a fuel flow (24), a first oxidant flow (28), and a steam flow (26). The first stage has (50) a first portion (72) of a catalyst bed (70). The fluids within the first stage are routed through the first portion (72) of the catalyst bed (70) and react. There is a second stage (62) downstream from and communicating with the first stage (50). The second stage (62) receives the fluids (74) from the first stage (50) and also selectively receives a second oxidant flow (64). The second oxidant flow (64) and the fluids received from the first stage (50) flow through a second portion (76) of a catalyst bed (70) and further react.
摘要翻译：自热重整器（48）包括选择性地接收燃料流（24），第一氧化剂流（28）和蒸汽流（26）的第一级（50）。第一阶段具有（50）催化剂床（70）的第一部分（72）。第一阶段内的流体通过催化剂床（70）的第一部分（72）并进行反应。在第一阶段（50）下游和与第一阶段（50）进行通信的是第二阶段（62）。第二级（62）从第一级（50）接收流体（74）并且还选择性地接收第二氧化剂流（64）。第二氧化剂流（64）和从第一级（50）接收的流体流过催化剂床（70）的第二部分（76）并进一步反应。

63. 发明申请

WO2003059857A1 多管式反応器、多管式反応器を用いる気相接触酸化方法、及び多管式反応器に適用されるスタートアップ方法审中-公开
标题翻译：多层反应器，使用多层反应器的蒸气相催化氧化方法和应用于多反应器的启动方法
公开(公告)号：WO2003059857A1
公开(公告)日：2003-07-24
申请号：PCT/JP2003/000160
申请日：2003-01-10
申请人：三菱化学株式会社 , 矢田修平 , 保坂浩親 , 強力正康 , 神野公克 , 小川寧之 , 鈴木芳郎
发明人：矢田修平 , 保坂浩親 , 強力正康 , 神野公克 , 小川寧之 , 鈴木芳郎
IPC分类号： C07C45/35
CPC分类号： B01J35/026 , B01J8/06 , B01J8/067 , B01J23/002 , B01J23/8876 , B01J2208/00221 , B01J2208/0053 , B01J2208/00716 , B01J2523/00 , C07C45/33 , C07C45/35 , C07C51/215 , C07C51/252 , F28D7/1607 , F28D2021/0022 , F28F9/026 , F28F9/028 , F28F9/22 , F28F2265/10 , C07C47/22 , C07C57/04 , B01J2523/12 , B01J2523/13 , B01J2523/22 , B01J2523/305 , B01J2523/41 , B01J2523/54 , B01J2523/68 , B01J2523/842 , B01J2523/845 , B01J2523/847
摘要： A multipipe reactor, wherein pipes having smaller tolerances between a nominal size and actual sizes are used as reaction pipes to stably perform a high yield reaction for a long period, a catalyst is filled into the reaction pipes so that the catalyst layer peak temperature portions of the reaction pipes are not overlapped with the connection portions thereof with baffle boards to effectively prevent hot spots from occurring and stably perform a reaction for a long period without the clogging of the reaction pipes, a heat medium and material gas are allowed to flow in the direction of a counter flow and a specified type of catalyst is filled into the reaction pipes so that activity is increased starting at the inlet of the material gas toward the outlet thereof to prevent the automatic oxidation reaction of products so as to prevent equipment from being damaged due to the reaction, and, at the time of starting, gas with a temperature of 100 to 400 C ° is led to the outside of the reaction pipes to increase the temperature of the reaction pipes and, at the room temperature, a solid heat medium is heated to circulate the medium to the outside of the reaction pipes to efficiently start up the reactor without affecting the activity of the catalyst.
摘要翻译：使用具有公称尺寸和实际尺寸之间的较小公差的管作为反应管，以长期稳定地进行高产率反应的多管反应器，将催化剂填充到反应管中，使得催化剂层的峰值温度部分反应管不与其与挡板的连接部分重叠，以有效地防止热点发生并且长时间稳定地进行反应而不会使反应管堵塞，允许热介质和材料气体流入逆流方向和特定类型的催化剂被填充到反应管中，使得从材料气体的入口向其出口开始活动增加，以防止产品的自动氧化反应，从而防止设备被损坏由于反应，并且在起始时，温度为100〜400℃的气体被引导到真空的外部以提高反应管的温度，并且在室温下，将固体热介质加热以使介质循环到反应管的外部，以有效启动反应器而不影响催化剂的活性。

64. 发明申请

WO02045838A1 COMPACT FUEL PROCESSOR FOR PRODUCING A HYDROGEN RICH GAS 审中-公开
标题翻译：用于生产氢气的紧凑燃料加工机
公开(公告)号：WO02045838A1
公开(公告)日：2002-06-13
申请号：PCT/US2001/047112
申请日：2001-12-05
IPC分类号： B01J8/00 , B01J8/02 , B01J8/04 , B01J8/06 , B01J19/00 , B01J19/24 , C01B3/16 , C01B3/38 , C01B3/48 , C01B3/58 , C10J1/207 , H01M8/04 , H01M8/06
CPC分类号： B01J8/0488 , B01J8/009 , B01J8/0278 , B01J8/0285 , B01J8/0423 , B01J8/0453 , B01J8/048 , B01J8/0492 , B01J8/0496 , B01J8/067 , B01J19/0013 , B01J19/2475 , B01J19/2485 , B01J2208/00141 , B01J2208/00176 , B01J2208/00194 , B01J2208/00203 , B01J2208/00407 , B01J2208/00415 , B01J2208/00716 , B01J2208/00814 , B01J2208/025 , B01J2219/0002 , B01J2219/00083 , B01J2219/00135 , B01J2219/182 , B01J2219/185 , B01J2219/1944 , C01B3/16 , C01B3/38 , C01B3/382 , C01B3/384 , C01B3/386 , C01B3/48 , C01B3/583 , C01B2203/0244 , C01B2203/0283 , C01B2203/0288 , C01B2203/044 , C01B2203/0455 , C01B2203/0465 , C01B2203/047 , C01B2203/0485 , C01B2203/0495 , C01B2203/066 , C01B2203/0805 , C01B2203/0844 , C01B2203/085 , C01B2203/0866 , C01B2203/0877 , C01B2203/0883 , C01B2203/0894 , C01B2203/1011 , C01B2203/1017 , C01B2203/1023 , C01B2203/1035 , C01B2203/1041 , C01B2203/1082 , C01B2203/1205 , C01B2203/1235 , C01B2203/1276 , C01B2203/142 , C01B2203/146 , C01B2203/147 , C01B2203/1604 , C01B2203/80 , C01B2203/82 , H01M8/04022 , H01M8/04037 , H01M8/04059 , H01M8/0612 , H01M8/0631 , H01M8/0668 , Y02P20/52
摘要： An apparatus (100) including a plurality of modules stacked end-to-end along a common axis and a multi-step process of converting hydrocarbon fuel (F) to a substantially pure hydrogen gas (P) using said apparatus (100). Each module includes a shell having an interior space defining a passeway for the flow of gas from a first end of the shell to a second end of the shell opposite the first end, and a processing core being contained within the interior space for effecting a chemical, thermal, or physical change to a gas stream passing axially through the module. In one embodiment, said plurality of modules including a first module (110) containing a partial oxidation catalyst and steam reforming catalyst, a seond module (120) containing a first heat exchanger (121), a third module (130) containing a desulfurization agent, a fourth module (140) containing an inert material for mixing components of gas stream passing there through, a fifth module (150) containing a water gas shift catalyst bed, a sixth module (160) containing a second heat exchanger (161) and a seventh module (170) containing a carbon monoxide oxidation catalyst bed.
摘要翻译：一种装置（100），包括沿公共轴线端对端堆叠的多个模块和使用所述装置（100）将烃燃料（F）转换成基本上纯的氢气（P）的多步骤过程。每个模块包括壳体，其具有限定用于从壳体的第一端到壳体的与第一端相对的第二端的气流的通道的内部空间，以及包含在内部空间内用于实现化学品的处理芯，对通过模块的气流的热或物理变化。在一个实施方案中，所述多个模块包括含有部分氧化催化剂和蒸汽重整催化剂的第一组件（110），含有第一热交换器（121）的第二组件（130），含有脱硫剂，包含用于混合通过其的气流的组分的惰性材料的第四模块（140），包含水煤气变换催化剂床的第五模块（150），包含第二热交换器（161）的第六模块（160）和含有一氧化碳氧化催化剂床的第七模块（170）。

65. 发明申请

WO00076651A1 COMPACT, LIGHT WEIGHT METHANOL FUEL GAS AUTOTHERMAL REFORMER ASSEMBLY 审中-公开
标题翻译：轻量甲醇燃料气体自动转换器总成
公开(公告)号：WO00076651A1
公开(公告)日：2000-12-21
申请号：PCT/US2000/016290
申请日：2000-06-14
IPC分类号： B01J8/02 , B01J8/04 , B01J12/00 , B01J23/02 , B01J23/40 , B01J23/745 , B01J23/89 , B01J35/00 , B01J35/04 , C01B3/32 , C01B3/38 , C01B3/40 , H01M8/04 , H01M8/06 , B01J8/002
CPC分类号： C01B3/323 , B01J8/025 , B01J8/0278 , B01J8/0285 , B01J8/0449 , B01J8/0492 , B01J8/0496 , B01J12/007 , B01J23/02 , B01J23/40 , B01J23/745 , B01J23/8906 , B01J35/0006 , B01J35/04 , B01J2208/00203 , B01J2208/00212 , B01J2208/00415 , B01J2208/0053 , B01J2208/00716 , B01J2208/025 , C01B3/382 , C01B3/40 , C01B2203/0244 , C01B2203/0283 , C01B2203/066 , C01B2203/0844 , C01B2203/085 , C01B2203/0883 , C01B2203/1011 , C01B2203/1017 , C01B2203/1023 , C01B2203/1029 , C01B2203/1041 , C01B2203/1047 , C01B2203/1052 , C01B2203/1064 , C01B2203/1076 , C01B2203/1082 , C01B2203/1094 , C01B2203/1223 , C01B2203/1276 , C01B2203/142 , C01B2203/1604 , C01B2203/82 , Y02P20/52 , Y10S165/395 , Y10S165/396 , Y10S165/397
摘要： A fuel gas-steam reformer assembly, preferably an autothermal reformer assembly (3), for use in a fuel cell power plant, includes a catalyst bed (2) which is formed from a cylindrical monolithic open cell foam body. The foam body is preferably formed from a high temperature material such as stainless steel, nickel alloys and iron-aluminum alloys, or from a ceramic material. The foam body includes open cells or pores (6) which are contained within the metal or ceramic lattice (4). The lattice (4) is coated with a porous wash coat which serves as a high surface area substrate onto which catalysts used in the reformer (3) are applied. The foam body has an inlet end (8) into which a mixture of fuel steam and air is fed to begin the reforming process. An inlet portion (48) of the foam body may be provided with an iron oxide and/or noble metal catalyst and the reminder of the foam body (50) may be provided with a copper, copper/zinc and/or noble metal catalyst.
摘要翻译：一种用于燃料电池发电厂的燃料气体 - 蒸汽重整器组件，优选为自热重整器组件（3），包括由圆柱形单片开孔泡沫体形成的催化剂床（2）。泡沫体优选由诸如不锈钢，镍合金和铁 - 铝合金的高温材料或陶瓷材料形成。泡沫体包括容纳在金属或陶瓷晶格（4）内的开孔或孔（6）。格子（4）涂覆有多孔洗涤涂层，其用作高表面积底物，在其上施加用于重整器（3）中的催化剂。泡沫体具有入口端（8），燃料蒸汽和空气的混合物供入入口端（8）以开始重整过程。泡沫体的入口部分（48）可以设置有氧化铁和/或贵金属催化剂，并且泡沫体（50）的提醒可以设置有铜，铜/锌和/或贵金属催化剂。

66. 发明申请

WO98044298A1 ROTARY REGENERATIVE OXIDIZER 审中-公开
标题翻译：旋转式再生氧化剂
公开(公告)号：WO98044298A1
公开(公告)日：1998-10-08
申请号：PCT/US1998/005533
申请日：1998-03-19
IPC分类号： B01D53/86 , B01D53/88 , B01J19/24 , B01J19/28 , B01J35/04 , F23G7/06 , F23G7/07
CPC分类号： F23G7/07 , B01D53/864 , B01D53/8668 , B01D53/885 , B01J19/24 , B01J19/2485 , B01J19/28 , B01J35/04 , B01J2208/00716 , B01J2219/00135 , B01J2219/00157 , B01J2219/00243 , F23G7/068 , Y02E20/12
摘要： A system for the abatement of industrial process gases utilizes a rotary regenerative oxidizer (10) comprised of one or more heat exchange beds (14), each bed comprised of a parallel, axial, and longitudinal array of heat regenerative channels that thermally and/or catalytically oxidize contaminated gases. Utilizing a rotary regenerative oxidizer, and if desired, a plurality of heat regenerative beds incorporated therein, facilitates the use of regenerative technology at lower gas flow rates, increases thermal efficiency and significantly reduces the floor space normally required when implementing fixed-bed nonrotary regenerative oxidizers. The heat exchange channels may be catalytically treated to enhance oxidation of the pollutants at a lower temperature.
摘要翻译：用于减少工业过程气体的系统使用由一个或多个热交换床（14）组成的旋转再生氧化器（10），每个床由平行，轴向和纵向阵列的热再生通道组成，热和/或催化氧化污染气体。利用旋转式再生氧化器，如果需要，其中并入的多个热再生床有助于以更低的气体流量使用再生技术，提高热效率并且显着降低了在实施固定床非旋转再生氧化剂时通常需要的占地面积。可以对热交换通道进行催化处理以在较低温度下增强污染物的氧化。

67. 发明申请

WO1997026079A1 FLUID REACTOR WITH CATALYST ON FLOATING TUBESHEET 审中-公开
标题翻译：具有催化剂的流体反应器在浮动管上
公开(公告)号：WO1997026079A1
公开(公告)日：1997-07-24
申请号：PCT/US1997000521
申请日：1997-01-14
申请人： E.I. DU PONT DE NEMOURS AND COMPANY
发明人： E.I. DU PONT DE NEMOURS AND COMPANY , GARNER, John, Byron , HESTER, James, Olden , SMITH, Geoffry, Wallar
IPC分类号： B01J08/06
CPC分类号： B01J8/0285 , B01D53/8631 , B01D53/885 , B01J8/008 , B01J8/067 , B01J2208/00194 , B01J2208/00716 , B01J2208/0084 , B01J2208/00884 , B01J2219/00777 , F28F9/0229 , F28F9/0241 , F28F9/22
摘要： A fluid-reactor, heat-exchange device (11) and method of reacting a fluid in the device. The device (11) embodies a bundle of heat-exchange tubes (14) mounted internally of an elongated reactor shell (10) to a stationary tubesheet (16) attached to the reactor shell (10) near one end of the shell. The heat-exchange tubes (14) are also mounted to a floating tubesheet (24) which is located near the other end of the shell (10). Attached to the floating tubesheet (24) is a catalyst basket (26) which when the device (11) is in operation will contain catalyst (72). The catalyst (72) is supported in the basket (26), and the fluid to be reacted will enter the shell (10) near the point of attachment to the stationary tubesheet (16), where it will contact the heat-exchange tubes (14). The fluid will flow along the outside of the tubes (70) and into the catalyst basket (26) where it will contact the catalyst (72) and react. The fluid will then pass into the heat-exchange tubes (14) and finally be removed from the device near the end (30) of the reactor where it was introduced.
摘要翻译：流体反应器，热交换装置（11）和使装置中的流体反应的方法。装置（11）包括一束热量交换管（14），该热交换管（14）安装在细长的反应器壳体（10）的内部，靠近壳体的一端附接到反应器壳体（10）上的固定管板（16）。热交换管（14）也安装在位于壳体（10）的另一端附近的浮动管板（24）上。附着在浮动管板（24）上的是催化剂篮（26），当装置（11）运行时，其将包含催化剂（72）。催化剂（72）被支撑在篮子（26）中，待反应的流体将在靠近固定管板（16）的点附近进入壳体（10），在那里它将接触热交换管 14）。流体将沿着管（70）的外部流动并进入催化剂篮（26），在那里它将与催化剂（72）接触并进行反应。然后流体将进入热交换管（14），并最终从其被引入的反应器的端部（30）附近的装置移除。

68. 发明申请

WO1994029254A1 PROCESS FOR THE PREPARATION OF 3-(METHYLTHIO)PROPANAL 审中-公开
标题翻译：制备3-（甲基）丙酰胺的方法
公开(公告)号：WO1994029254A1
公开(公告)日：1994-12-22
申请号：PCT/US1993008552
申请日：1993-09-09
申请人： NOVUS INTERNATIONAL, INC.
发明人： NOVUS INTERNATIONAL, INC. , HSU, Yung, C. , RUEST, Dennis, A.
IPC分类号： C07C47/02
CPC分类号： C07C319/18 , B01J2208/00716 , C07C45/35 , C07C45/783 , C07C45/81 , C07C47/22 , C07C323/22
摘要： A process for the continuous preparation of 3-(methylthio)propanal. A liquid reaction medium is contacted with a gaseous acrolein feed stream in a gas/liquid contact zone. The reaction medium contains 3-(methylthio)propanal, methyl mercaptan and a catalyst for the reaction between methyl mercaptan and acrolein. The gaseous acrolein feed stream comprises acrolein vapor and non-condensable gas. Acrolein is transferred from the acrolein feed stream to the reaction medium and reacts with methyl mercaptan in that medium to produce a liquid reaction product containing 3-(methylthio)propanal. The non-condensable gas is separated from the liquid reaction product. The reaction product is divided into a product fraction and a circulating fraction, and the circulating fraction is recycled to the gas/liquid contact zone.
摘要翻译：连续制备3-（甲硫基）丙醛的方法。液体反应介质与气/液接触区中的气态丙烯醛进料流接触。反应介质含有3-（甲硫基）丙醛，甲硫醇和用于甲硫醇与丙烯醛反应的催化剂。气态丙烯醛进料流包含丙烯醛蒸气和不可冷凝气体。丙烯醛从丙烯醛进料流转移到反应介质中并与该介质中的甲硫醇反应，生成含有3-（甲硫基）丙醛的液体反应产物。不可冷凝气体与液体反应产物分离。将反应产物分成产物级分和循环级分，循环级分再循环至气/液接触区。

69. 发明申请

WO2017029581A1 A METHOD OF OPERATING A SLURRY BUBBLE COLUMN REACTOR 审中-公开
标题翻译：一种浆料泡沫反应器的操作方法
公开(公告)号：WO2017029581A1
公开(公告)日：2017-02-23
申请号：PCT/IB2016/054806
申请日：2016-08-10
申请人： SASOL TECHNOLOGY PROPRIETARY LIMITED
发明人： BOOYSEN, Willem, Adriaan , OORTMAN, Ruben
IPC分类号： C10G2/00 , B01J8/18
CPC分类号： C10G2/342 , B01J8/22 , B01J2208/00716 , C10G2/344 , C10G2300/4031
摘要： A method for starting a slurry bubble column reactor that includes a reactor vessel holding a settled or slumped bed of particles and a liquid phase from which the particles have settled includes introducing a flow of a re-suspension liquid into the settled or slumped bed to loosen the settled or slumped bed. The introduction of the re-suspension liquid takes place before the introduction of any gas into the settled or slumped bed, or together with feeding of gas into the settled or slumped bed, provided that, if gas is fed together with the re-suspension liquid into the settled or slumped bed before the settled or slumped bed has been loosened, the gas has a superficial gas velocity in the reactor below 10 cm/s. Once the settled or slumped bed has been loosened by at least the re-suspension liquid, gas is passed at a superficial gas velocity above 10 cm/s through the liquid phase.
摘要翻译：一种用于启动浆液鼓泡塔反应器的方法，该反应器包括容纳沉淀或坍落的颗粒床的反应器容器和颗粒已经沉降的液相，包括将再悬浮液体流引入沉降或塌落的床中以松开定居或坍塌的床。重新悬浮液体的引入是在将任何气体引入沉降或塌陷的床之前进行的，或者连同气体进入沉降的或坍落的床中一样，条件是如果气体与再悬浮液一起进料在沉降或塌陷的床被松开之前，进入沉降的或塌落的床，气体在反应器中的表面气体速度低于10cm / s。一旦通过至少再悬浮液体使沉降或塌落的床已经松动，气体以10cm / s以上的表观气体速度通过液相。

70. 发明申请

WO2015008806A1 FUEL CELL MODULE 审中-公开
标题翻译：燃料电池模块
公开(公告)号：WO2015008806A1
公开(公告)日：2015-01-22
申请号：PCT/JP2014/068968
申请日：2014-07-10
申请人： HONDA MOTOR CO., LTD.
发明人： OGAWA, Tetsuya , YOSHIMINE, Yuki
IPC分类号： H01M8/06
CPC分类号： H01M8/0631 , B01J8/065 , B01J8/067 , B01J2208/00194 , B01J2208/00212 , B01J2208/00221 , B01J2208/0053 , B01J2208/00716 , B01J2208/00902 , C01B3/34 , C01B2203/0233 , C01B2203/066 , C01B2203/0811 , C01B2203/1205 , C01B2203/1241 , C01B2203/1258 , C01B2203/1294 , C01B2203/141 , C01B2203/16 , C01B2203/1604 , C01B2203/1619 , H01M8/04022 , H01M8/04074 , H01M8/04126 , H01M2008/1293
摘要： A fuel cell module (12) includes a fuel cell stack (24) and FC peripheral equipment (38). The FC peripheral equipment (38) includes an evaporator (42). At least one of evaporation pipes (90) of the evaporator (42) connects a water vapor discharge chamber (98b) and an inlet of a reformer (40) to form an evaporation return pipe (106) as a passage of water vapor. A raw fuel pipe (107) is inserted into the evaporation return pipe (106) for allowing a raw fuel to flow from the downstream side to the upstream side of the evaporation return pipe (106).
摘要翻译：燃料电池模块（12）包括燃料电池堆（24）和FC外围设备（38）。 FC外围设备（38）包括蒸发器（42）。蒸发器（42）的蒸发管道（90）中的至少一个连接水蒸汽排放室（98b）和重整器（40）的入口，以形成作为水蒸汽通道的蒸发返回管（106）。原料燃料管（107）被插入到蒸发回流管（106）中，用于使原料燃料从蒸发返回管（106）的下游侧流动到上游侧。

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