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41. 发明授权

US07939212B2 Flux control apparatus and fuel cell system 有权
标题翻译：焊剂控制装置和燃料电池系统
公开(公告)号：US07939212B2
公开(公告)日：2011-05-10
申请号：US11294553
申请日：2005-12-06
申请人： Hiroaki Kato , Kazumasa Takada
发明人： Hiroaki Kato , Kazumasa Takada
IPC分类号： H01M8/04 , H01M8/06
CPC分类号： G05D7/0658 , B01J2219/00006 , B01J2219/00191 , C01B3/384 , C01B2203/0233 , C01B2203/0283 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0894 , C01B2203/1047 , C01B2203/1058 , C01B2203/1223 , C01B2203/1241 , C01B2203/127 , C01B2203/1276 , C01B2203/1604 , C01B2203/1619 , C01B2203/1633 , C01B2203/1685 , C01B2203/169 , C01B2203/1695 , H01M8/04089 , H01M8/04164 , H01M8/0618 , Y02P20/128 , Y10T137/2514
摘要： A flux control apparatus includes an outlet pressure detector for detecting an outlet pressure of a fluid at an outlet of a fluid flow apparatus driven by a drive source for feeding the fluid from an inlet of the fluid flow apparatus and letting the fluid flow out from the outlet of the fluid flow apparatus, a drive amount detector for detecting an amount of drive of the drive source, an estimated flux-calculating apparatus for calculating a flux of the fluid flowing from the fluid flow apparatus as an estimated flux on the basis of the pressure of the fluid and the amount of drive, a control amount-calculating apparatus for calculating an amount of control for the fluid flow apparatus on the basis of the estimated flux and a target flux, and a control apparatus for controlling the drive source on the basis of the amount of control.
摘要翻译：磁通控制装置包括出口压力检测器，用于检测由驱动源驱动的流体流动装置的出口处的流体的出口压力，用于从流体流动装置的入口供给流体，并使流体从流体流动装置的出口，用于检测驱动源的驱动量的驱动量检测器，用于计算从流体流动装置流动的流体的流量作为估计通量的估计通量计算装置，流体的压力和驱动量，基于估计的通量和目标通量计算流体流动装置的控制量的控制量计算装置，以及用于控制驱动源的控制装置控制量的基础。

42. 发明申请

US20110046244A1 NATURAL GAS STEAM REFORMING METHOD WITH LINEAR COUNTERCURRENT HEAT EXCHANGER 有权
标题翻译：具有线性逆流换热器的天然气蒸汽重整方法
公开(公告)号：US20110046244A1
公开(公告)日：2011-02-24
申请号：US12943834
申请日：2010-11-10
申请人： Robert M. Zubrin , Sam G. Michael , Gevorg Sargsyan
发明人： Robert M. Zubrin , Sam G. Michael , Gevorg Sargsyan
IPC分类号： C01B3/38 , C10L3/06 , C07C1/04
CPC分类号： E21B43/168 , C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0405 , C01B2203/0415 , C01B2203/0475 , C01B2203/06 , C01B2203/0816 , C01B2203/0894 , C01B2203/1058 , C01B2203/1241 , C01B2203/1247 , C01B2203/1252 , C01B2203/127 , C01B2203/1294 , C01B2203/169 , C01B2203/82 , C01B2203/84 , C01B2203/86 , Y02E20/16 , Y02P20/129 , Y02P30/30
摘要： The present invention is a natural gas steam reforming method for generating an output gas mixture of carbon dioxide and hydrogen, including the following steps. (1) Combusting a portion of the natural gas with an oxidizing agent to generate heat, superheated steam, and a gas mixture of carbon dioxide, carbon monoxide, and hydrogen. (2) Steam reforming the gas mixture with additional superheated steam under steam-rich conditions to transform a remaining portion of the natural gas into carbon dioxide, carbon monoxide, and hydrogen. (3) Water-gas-shifting any residual carbon monoxide into additional carbon dioxide and additional hydrogen by utilizing a water-gas-shift catalyst downstream of the steam reforming step, thereby producing an effluent gas mixture that is predominantly carbon dioxide and hydrogen. (4) Boiling water in a top-to-bottom linear countercurrent heat exchanger to generate the superheated steam by transferring heat released in the water-gas-shifting step, where as the water is gravitationally and thermally stratified from top to bottom with a top portion boiling into steam, the steam continues to rise and is additionally heated in the top-to-bottom linear countercurrent heat exchanger. (5) And, utilizing the superheated steam produced as a reactant in the steam reforming step and the water-gas-shifting step to assist in reformation of the natural gas into carbon dioxide and hydrogen.
摘要翻译：本发明是用于产生二氧化碳和氢气的输出气体混合物的天然气蒸汽重整方法，包括以下步骤。（1）用氧化剂燃烧一部分天然气以产生热量，过热蒸汽以及二氧化碳，一氧化碳和氢气的混合气体。（2）在富含蒸汽的条件下用另外的过热蒸汽对气体混合物进行蒸汽重整，以将剩余部分的天然气转化为二氧化碳，一氧化碳和氢气。（3）通过在蒸汽重整步骤下游利用水煤气变换催化剂将任何残留的一氧化碳进行水煤气转移到另外的二氧化碳和另外的氢气中，从而产生主要是二氧化碳和氢气的流出气体混合物。（4）在顶部到底部的线性逆流热交换器中的沸腾水，通过传递在水煤气变换步骤中释放的热量来产生过热蒸汽，其中水由上而下重力和热分层，顶部部分沸腾成蒸汽，蒸汽继续上升，并在顶部至底部的线性逆流热交换器中另外加热。（5）利用在蒸汽重整工序和水煤气变换工序中作为反应物生成的过热蒸汽，有助于将天然气重整成二氧化碳和氢气。

43. 发明申请

US20110042619A1 OPERATION METHOD OF SYNTHESIS GAS REFORMER IN GTL PLANT 有权
标题翻译： GTL工厂合成气转化器的运行方法
公开(公告)号：US20110042619A1
公开(公告)日：2011-02-24
申请号：US12736256
申请日：2009-03-30
申请人： Yasumasa Morita , Kenichi Kawazuishi
发明人： Yasumasa Morita , Kenichi Kawazuishi
IPC分类号： C01B3/24
CPC分类号： C01B3/384 , C01B2203/0233 , C01B2203/0238 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0495 , C01B2203/062 , C01B2203/0811 , C01B2203/0827 , C01B2203/0894 , C01B2203/1058 , C01B2203/1258 , C01B2203/148 , C01B2203/1614 , C01B2203/1628 , C01B2203/169 , C01B2203/1695
摘要： An operation method of a synthesis gas reformer of a GTL (gas to liquids) plant is provided with: setting an operation condition of the synthesis gas reformer; determining control target values of a flow rate of the light hydrocarbon gas, the steam, and the CO2, and an amount of heat needed for the synthesis gas reformer; controlling operation load of the synthesis gas reformer; setting a furnace efficiency of the synthesis gas reformer; calculating a combustion load of a burner of the synthesis gas reformer; calculating a lower heating value of the fuel gas based on a composition measurement of the fuel gas of the burner; determining a control target value of the pressure of the fuel gas; calculating a deviation between the control target value of the pressure of the fuel gas and a measured value of the pressure of the fuel gas; and controlling the temperature of the synthesis gas at the outlet of the synthesis gas reformer by adjusting a pressure control valve provided at an inlet of the burner to compensate for the deviation.
摘要翻译：提供了一种GTL（气 - 液）设备的合成气重整器的操作方法，其特征在于：设置合成气重整器的操作条件; 确定轻烃气体，蒸汽和CO 2的流量的控制目标值和合成气重整器所需的热量; 控制合成气重整器的运行负荷; 设定合成气重整炉的炉效; 计算合成气重整器的燃烧器的燃烧负荷; 基于燃烧器的燃料气体的组成测量值计算燃料气体的较低的热值; 确定燃料气体的压力的控制目标值; 计算燃料气体的压力的控制目标值和燃料气体的压力的测量值之间的偏差; 以及通过调节设置在燃烧器入口处的压力控制阀来控制合成气在重整器出口处的温度，以补偿偏差。

44. 发明申请

US20110039172A1 HYDROGEN GENERATOR, FUEL CELL SYSTEM INCLUDING HYDROGEN GENERATOR, AND METHOD FOR OPERATING HYDROGEN GENERATOR 有权
标题翻译：氢发生器，包括氢发生器的燃料电池系统，以及氢发生器运行方法
公开(公告)号：US20110039172A1
公开(公告)日：2011-02-17
申请号：US12989780
申请日：2010-03-02
申请人： Yukimune Kani , Kunihiro Ukai , Yuji Mukai
发明人： Yukimune Kani , Kunihiro Ukai , Yuji Mukai
IPC分类号： H01M8/06 , B01J19/00 , C01B3/02
CPC分类号： C01B3/384 , C01B2203/0233 , C01B2203/0283 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/1282 , C01B2203/1288 , C01B2203/1294 , C01B2203/1609 , C01B2203/1619 , C01B2203/169 , H01M8/04776 , H01M8/0612 , Y02E60/50
摘要： A hydrogen generator of the present invention includes: a raw material supplying device (4) configured to supply a raw material; a water supplying device (3) configured to supply water; an evaporator (23) configured to evaporate the water supplied from the water supplying device (3) to generate steam; a reformer (20) having a reforming catalyst which generates a hydrogen-containing gas by a reforming reaction using the raw material and the steam; a valve (12) disposed on a gas passage to cause the reformer (20) to be communicated with an atmosphere and block the reformer (20) from the atmosphere, the gas passage being located downstream of the reformer (20); and a controller (11) configured to stop supplying the water from the water supplying device (3), then continue to supply the raw material from the raw material supplying device (4) with the valve (12) open, and stop supplying the raw material from the raw material supplying device (4) and close the valve (12) before an inside of the reformer (20) is purged with the raw material.
摘要翻译：本发明的氢发生器包括：原料供给装置（4），其构造成供给原料; 供水装置（3），其构造成供水; 蒸发器（23），被配置为蒸发从供水装置（3）供应的水以产生蒸汽; 重整器（20），其具有通过使用所述原料和所述蒸汽的重整反应产生含氢气体的重整催化剂; 设置在气体通道上以使重整器（20）与大气连通并将重整器（20）从大气中阻断的阀（12），气体通道位于重整器（20）的下游; 以及控制器（11），其被配置为停止从供水装置（3）供应水，然后继续从原料供给装置（4）供应源于阀（12）的原料，并停止供应原料来自原料供给装置（4）的材料，并且在重整器（20）的内部被原料清除之前关闭阀（12）。

45. 发明申请

US20110014088A1 COMPACT NATURAL GAS STEAM REFORMER WITH LINEAR COUNTERCURRENT HEAT EXCHANGER 有权
标题翻译：具有线性逆向热交换器的紧凑型天然气蒸汽转化器
公开(公告)号：US20110014088A1
公开(公告)日：2011-01-20
申请号：US12902143
申请日：2010-10-11
申请人： Robert M Zubrin , Sam G. Michael , Gevorg Sargsyan
发明人： Robert M Zubrin , Sam G. Michael , Gevorg Sargsyan
IPC分类号： B01J19/00
CPC分类号： E21B43/168 , C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0405 , C01B2203/0415 , C01B2203/0475 , C01B2203/06 , C01B2203/0816 , C01B2203/0894 , C01B2203/1058 , C01B2203/1241 , C01B2203/1247 , C01B2203/1252 , C01B2203/127 , C01B2203/1294 , C01B2203/169 , C01B2203/82 , C01B2203/84 , C01B2203/86 , Y02E20/16 , Y02P20/129 , Y02P30/30
摘要： The present invention is natural gas steam reforming apparatus for generating an output gas mixture of carbon dioxide and hydrogen. The apparatus is made from two enclosures. A first enclosure contains a source of water, superheated steam, and channels, located within a lower portion of the first enclosure, which contain a water-gas-shift catalyst for converting CO into CO2 and H2. The heat from hot gas flowing through the channels is released into the first enclosure to boil the water to generate the superheated steam. A second enclosure, contained within an upper portion of the first enclosure, includes a steam inlet for receiving the superheated steam from the first enclosure; a combustion chamber; and a reformation chamber. The combustion chamber is used for combusting a portion of the natural gas to generate additional steam, heat, and a hot gas mixture of CO2, CO, and H2. The reformation chamber is used for steam reforming a remaining portion of the natural gas to generate additional hot gas mixture of CO2, CO, and H2. The hot gas mixture is directed through the channels installed in the first enclosure in which the water-gas-shift catalyst converts residual CO into additional CO2 and additional H2, to produce an output gas mixture of carbon dioxide and hydrogen. In the present invention, the first and second enclosures function as a top-to-bottom linear countercurrent heat exchanger. In one embodiment of the present invention, an external third enclosure containing a combustion chamber and a boiler for combusting natural gas with ambient air may be used to boil additional water into superheated steam which is then fed into the first enclosure.
摘要翻译：本发明是用于产生二氧化碳和氢气的输出气体混合物的天然气蒸汽重整装置。该设备由两个外壳制成。第一壳体包含位于第一外壳下部的水源，过热蒸汽和通道，其包含用于将CO转化成CO 2和H 2的水煤气变换催化剂。来自流经通道的热气体的热量被释放到第一外壳中以使水沸腾以产生过热蒸汽。包含在第一外壳的上部内的第二外壳包括用于从第一外壳接收过热蒸汽的蒸汽入口; 燃烧室; 和改造室。燃烧室用于燃烧一部分天然气以产生额外的蒸汽，热量和CO 2，CO和H 2的热气体混合物。重整室用于蒸汽重整天然气的剩余部分，以产生CO 2，CO和H 2的另外的热气体混合物。热气体混合物通过安装在第一壳体中的通道引导，其中水煤气变换催化剂将残余CO转化成另外的CO 2和另外的H 2，以产生二氧化碳和氢气的输出气体混合物。在本发明中，第一和第二外壳用作顶部到底部的线性逆流热交换器。在本发明的一个实施例中，可以使用包含用于将天然气与环境空气一起燃烧的燃烧室和锅炉的外部第三壳体，以将额外的水沸腾到过热蒸汽中，然后将其进料到第一外壳中。

46. 发明申请

US20100329952A1 REACTION DEVICE, HEAT-INSULATING CONTAINER, FUEL CELL DEVICE, AND ELECTRONIC APPARATUS 有权
标题翻译：反应装置，绝热容器，燃料电池装置和电子装置
公开(公告)号：US20100329952A1
公开(公告)日：2010-12-30
申请号：US12877580
申请日：2010-09-08
申请人： Osamu NAKAMURA , Masatoshi Nomura
发明人： Osamu NAKAMURA , Masatoshi Nomura
IPC分类号： B01J19/24
CPC分类号： H01M8/0618 , B01J19/0093 , B01J19/249 , B01J2219/00153 , B01J2219/00155 , B01J2219/00783 , B01J2219/00835 , B01J2219/00873 , B01J2219/2453 , B01J2219/2458 , B01J2219/2465 , B01J2219/2467 , B01J2219/2479 , B01J2219/2496 , C01B3/323 , C01B3/384 , C01B2203/0233 , C01B2203/0261 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/085 , C01B2203/1035 , C01B2203/1076 , C01B2203/1211 , C01B2203/1223 , C01B2203/1229 , C01B2203/1247 , C01B2203/1288 , C01B2203/169 , H01M8/0668 , H01M2250/30 , Y02B90/18 , Y02P20/128
摘要： Disclosed is a reaction device that includes a reaction device main body that includes a first reaction unit and a second reaction unit, a container to house the reaction device main body and a first region that corresponds to at least the first reaction unit and a second region that corresponds to the second reaction unit, the first and second regions being provided to the container or internal side of the container. The first reaction unit is set to a temperature higher than that of the second reaction unit, and the first region has a higher reflectivity than that of the second region, with respect to a heat ray that is radiated from the reaction device main body.
摘要翻译：公开了一种反应装置，其包括反应装置主体，其包括第一反应单元和第二反应单元，容纳反应装置主体的容器和至少对应于第一反应单元的第一区域和第二区域对应于第二反应单元，第一和第二区域设置在容器的容器或内侧。相对于从反应装置主体辐射的热射线，第一反应单元被设定为高于第二反应单元的温度，并且第一区域具有比第二区域的反射率更高的反射率。

47. 发明授权

US07857875B2 Autothermal reforming in a fuel processor utilizing non-pyrophoric shift catalyst 有权
标题翻译：使用非自燃变换催化剂的燃料处理器中的热重整
公开(公告)号：US07857875B2
公开(公告)日：2010-12-28
申请号：US11432068
申请日：2006-05-11
申请人： W. Spencer Wheat , Vesna R. Mirkovic , Kevin H. Nguyen , Curtis L. Krause , James F. Stevens , Daniel G. Casey
发明人： W. Spencer Wheat , Vesna R. Mirkovic , Kevin H. Nguyen , Curtis L. Krause , James F. Stevens , Daniel G. Casey
IPC分类号： C01B3/36 , C10J3/46 , C10J3/54 , H01M8/06 , H01M8/04 , F23N5/20 , F23N5/22 , F23N5/00 , F23D11/38
CPC分类号： B01J8/0453 , B01J8/025 , B01J8/0496 , B01J19/0013 , B01J19/0033 , B01J19/24 , B01J2208/00132 , B01J2208/00141 , B01J2208/00203 , B01J2208/00398 , B01J2208/00415 , B01J2208/0053 , B01J2208/00646 , B01J2208/00716 , B01J2208/00849 , B01J2219/00263 , C01B3/382 , C01B3/48 , C01B2203/0244 , C01B2203/0283 , C01B2203/066 , C01B2203/0844 , C01B2203/127 , C01B2203/1604 , C01B2203/1609 , C01B2203/1619 , C01B2203/169 , H01M8/0618 , H01M8/0668 , H01M2008/1095
摘要： A method for start-up and shut down of a fuel processor including an autothermal reformer employing a non-pyrophoric shift catalyst is disclosed. Also disclosed are a computer programmed to start-up or shut down a fuel processor including an autothermal reformer employing a non-pyrophoric shift catalyst or a program storage medium encoded with instruction that, when executed by a computer, start-up or shut down a fuel processor including an autothermal reformer employing a non-pyrophoric shift catalyst.
摘要翻译：公开了一种用于启动和关闭包括使用非自发变换催化剂的自热重整器的燃料处理器的方法。还公开了一种被编程为启动或关闭燃料处理器的计算机，该燃料处理器包括采用非自燃变换催化剂的自热重整器或编码有指令的程序存储介质，当由计算机执行时，启动或关闭燃料处理器包括采用非自燃变换催化剂的自热重整器。

48. 发明申请

US20100310951A1 FUEL CELL SYSTEM AND METHOD FOR STARTING UP THE SAME 失效
标题翻译：燃料电池系统及其启动方法
公开(公告)号：US20100310951A1
公开(公告)日：2010-12-09
申请号：US12675161
申请日：2008-08-11
申请人： Susumu Hatada
发明人： Susumu Hatada
IPC分类号： H01M8/06
CPC分类号： H01M8/04268 , C01B3/38 , C01B3/382 , C01B3/386 , C01B2203/0227 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/066 , C01B2203/085 , C01B2203/1288 , C01B2203/1604 , C01B2203/1619 , C01B2203/169 , H01M8/04223 , H01M8/04302 , H01M8/04373 , H01M8/04753 , H01M8/0618 , H01M8/2425 , H01M8/2457 , H01M2008/1293
摘要： Provided is a method for starting up a fuel cell system, in which reforming can be reliably performed from an early stage to more reliably prevent the oxidative degradation of the anode. A method for starting up a fuel cell system including a reformer having a reforming catalyst layer, for reforming a hydrocarbon-based fuel to produce a hydrogen-containing gas, and a high temperature fuel cell for generating electric power using the hydrogen-containing gas, including: a) increasing the temperature of the reforming catalyst layer, while measuring the temperature of the reforming catalyst layer; b) calculating the flow rate of the hydrocarbon-based fuel that can be reformed in the reforming catalyst layer, based on the measured temperature of the reforming catalyst layer; and c) supplying the hydrocarbon-based fuel at the calculated flow rate to the reforming catalyst layer to reform the hydrocarbon-based fuel, and supplying the obtained reformed gas to the anode of the high temperature fuel cell, wherein the feed rate of the hydrocarbon-based fuel to the reforming catalyst layer is increased, while the steps b and c are repeated, until the feed rate of the hydrocarbon-based fuel to the reforming catalyst layer becomes a flow rate at completion of start-up. Also provided is a fuel cell system appropriate for this method.
摘要翻译：提供一种启动燃料电池系统的方法，其中可以从早期可靠地进行重整，以更可靠地防止阳极的氧化降解。一种用于启动燃料电池系统的方法，包括具有重整催化剂层的重整器，用于重整烃系燃料以产生含氢气体，以及使用含氢气体产生电力的高温燃料电池，包括：a）在测量重整催化剂层的温度的同时提高重整催化剂层的温度; b）基于重整催化剂层的测量温度计算重整催化剂层中能够重整的烃类燃料的流量; 以及c）以计算的流量将烃基燃料供给到重整催化剂层以重整烃基燃料，并将获得的重整气体供应到高温燃料电池的阳极，其中烃的进料速率提高了重整催化剂层的燃料，同时重复步骤b和c，直到烃类燃料与重整催化剂层的进料速率成为启动完成时的流量。还提供了适用于该方法的燃料电池系统。

49. 发明申请

US20100300382A1 FUEL REFORMING APPARATUS 有权
标题翻译：燃油改造设备
公开(公告)号：US20100300382A1
公开(公告)日：2010-12-02
申请号：US12744691
申请日：2009-01-26
申请人： Hideo Yahagi , Isamu Nakada , Keiichiro Aoki , Takanori Sasaki
发明人： Hideo Yahagi , Isamu Nakada , Keiichiro Aoki , Takanori Sasaki
IPC分类号： F02B43/08 , B01J8/00
CPC分类号： F02D41/1441 , C01B3/323 , C01B3/384 , C01B2203/0233 , C01B2203/0238 , C01B2203/025 , C01B2203/0435 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0844 , C01B2203/1052 , C01B2203/1058 , C01B2203/1064 , C01B2203/107 , C01B2203/1076 , C01B2203/1229 , C01B2203/1247 , C01B2203/148 , C01B2203/1619 , C01B2203/1676 , C01B2203/169 , F01N3/2889 , F01N5/02 , F01N13/009 , F01N2240/30 , F01N2560/025 , F01N2610/03 , F02D19/0623 , F02D19/0634 , F02D19/0644 , F02D19/0671 , F02D19/0692 , F02D19/084 , F02D41/0025 , F02D41/0027 , F02D41/0065 , F02D41/1439 , F02D41/1454 , F02D2041/147 , F02M26/36 , G01N33/005 , Y02P20/128 , Y02P20/142 , Y02T10/16 , Y02T10/36 , Y02T10/47
摘要： Fuel reforming catalysts 28 generate a hydrogen-containing reformed gas when they come into contact with exhaust gas that contains a reforming fuel. Upstream and downstream air-fuel ratio sensors 58, 60 are respectively installed upstream and downstream of the fuel reforming catalysts 28. The upstream air-fuel ratio sensor 58 outputs a upstream sensor signal in accordance with oxygen concentration. The downstream air-fuel ratio sensor 60 outputs a downstream sensor signal in accordance with oxygen concentration and hydrogen concentration by using zirconia's oxygen detection capability and a change of a diffusion layer's hydrogen-concentration-dependent oxygen detection capability. An ECU 50 detects the hydrogen concentration without being affected by the oxygen concentration through the use of the upstream sensor signal in which only the oxygen concentration is reflected and the downstream sensor signal in which the oxygen concentration and hydrogen concentration are reflected. This makes it possible to establish a hydrogen concentration detection system with the common air-fuel ratio sensors 58, 60.
摘要翻译：当燃料重整催化剂28与含重整燃料的废气接触时，产生含氢重整气体。上游和下游空燃比传感器58,60分别安装在燃料重整催化剂28的上游和下游。上游空燃比传感器58根据氧浓度输出上游传感器信号。下游空燃比传感器60通过使用氧化锆的氧检测能力和扩散层的氢浓度依赖性氧检测能力的变化，根据氧浓度和氢浓度输出下游传感器信号。 ECU50通过使用仅反映氧浓度的上游传感器信号和反映氧浓度和氢浓度的下游传感器信号，检测氢浓度而不受氧浓度的影响。这使得可以建立具有共用空燃比传感器58,60的氢浓度检测系统。

50. 发明授权

US07811341B2 Reaction device, heat-insulating container, fuel cell device, and electronic apparatus 有权
标题翻译：反应装置，绝热容器，燃料电池装置和电子装置
公开(公告)号：US07811341B2
公开(公告)日：2010-10-12
申请号：US11646030
申请日：2006-12-27
申请人： Osamu Nakamura , Masatoshi Nomura
发明人： Osamu Nakamura , Masatoshi Nomura
IPC分类号： B01J7/00 , H01M8/06 , B01J8/00 , B01J8/04 , B01J10/00 , B01J19/00
CPC分类号： H01M8/0618 , B01J19/0093 , B01J19/249 , B01J2219/00153 , B01J2219/00155 , B01J2219/00783 , B01J2219/00835 , B01J2219/00873 , B01J2219/2453 , B01J2219/2458 , B01J2219/2465 , B01J2219/2467 , B01J2219/2479 , B01J2219/2496 , C01B3/323 , C01B3/384 , C01B2203/0233 , C01B2203/0261 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/085 , C01B2203/1035 , C01B2203/1076 , C01B2203/1211 , C01B2203/1223 , C01B2203/1229 , C01B2203/1247 , C01B2203/1288 , C01B2203/169 , H01M8/0668 , H01M2250/30 , Y02B90/18 , Y02P20/128
摘要： Disclosed is a reaction device that includes a reaction device main body that includes a first reaction unit and a second reaction unit, a container to house the reaction device main body and a first region that corresponds to at least the first reaction unit and a second region that corresponds to the second reaction unit, the first and second regions being provided to the container or internal side of the container. The first reaction unit is set to a temperature higher than that of the second reaction unit, and the first region has a higher reflectivity than that of the second region, with respect to heat ray that is radiated from the reaction device main body.
摘要翻译：公开了一种反应装置，其包括反应装置主体，其包括第一反应单元和第二反应单元，容纳反应装置主体的容器和至少对应于第一反应单元的第一区域和第二区域对应于第二反应单元，第一和第二区域设置在容器的容器或内侧。第一反应单元设定为高于第二反应单元的温度，并且第一区域相对于从反应装置主体辐射的热射线具有比第二区域更高的反射率。

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