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JP3611065B2 - Integrated fuel cell power generator - Google Patents

Integrated fuel cell power generator Download PDF

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Publication number
JP3611065B2
JP3611065B2 JP24283096A JP24283096A JP3611065B2 JP 3611065 B2 JP3611065 B2 JP 3611065B2 JP 24283096 A JP24283096 A JP 24283096A JP 24283096 A JP24283096 A JP 24283096A JP 3611065 B2 JP3611065 B2 JP 3611065B2
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Prior art keywords
fuel cell
reformer
fuel
gas
power generator
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JP24283096A
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JPH1092457A (en
Inventor
元基 吉野
信之 在間
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石川島播磨重工業株式会社
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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Description

【0001】
【発明の属する技術分野】
本発明は、主要機器を一体に構成し同一の格納容器内に収納した一体型燃料電池発電装置に関する。
【0002】
【従来の技術】
溶融炭酸塩型燃料電池は、高効率、かつ環境への影響が少ないなど、従来の発電装置にはない特徴を有しており、水力・火力・原子力に続く発電システムとして注目を集め、現在世界各国で鋭意研究開発が行われている。
【0003】
図3は、天然ガスを燃料とする溶融炭酸塩型燃料電池を用いた発電設備のフロー図であり、燃料予熱器10、改質器12、燃料電池14、及び触媒燃焼器16を備えている。燃料ガス1は燃料予熱器10で柚され改質器12の改質室Reに供給されて、水素を含むアノードガス2に改質され、燃料予熱器10で冷却後、燃料電池14のアノード側Aに供給され、ここでアノード反応により水素の大部分を消費してアノード排ガス4となり、触媒燃焼器16で未燃分を燃焼して高温の燃焼ガス5を発生し、改質器12のガス室Gに供給されて改質室Reを加熱した後、系外に排出される。一方、CO2 を含む空気3は、燃料電池14のカソード側Cに供給され、ここでカソード反応により一部の酸素を消費してカソード排ガス7となり、その一部が触媒燃焼器16に供給されてアノード排ガス4を燃焼させる。なお、カソード排ガス7の残部7aは系外に出て図示しない循環経路を経て空気3に混入され、カソード反応に必要なCO2 を循環供給するようになっている。
【0004】
【発明が解決しようとする課題】
上述した燃料電池発電装置は、加圧下で運転することにより、より高効率が得られ、かつ小型化することができる。しかし、従来の装置では、燃料予熱器10、改質器12、燃料電池14、及び触媒燃焼器16をそれぞれ別々の圧力容器内に格納し、各機器を配管で接続するため,特に比較的小出力の場合に設置面積が大きくなる問題点があった。
【0005】
また、各機器を連結する配管には、大量の高温ガスが流れるため大口径配管となり、その配管の曲げや保温が困難であり、放熱ロスが大きく、発電装置全体の効率が低下する問題点があった。
【0006】
本発明はかかる問題点を解決するために創案されたものである。すなわち本発明の目的は、小型で設置面積が小さく、かつ放熱ロスが少ない一体型燃料電池発電装置を提供することにある。
【0007】
【課題を解決するための手段】
本発明によれば、燃料予熱器、改質器、燃料電池、触媒燃焼器、及びこれらを格納する圧力容器からなり、燃料電池と改質器が積層され、
正面側において、改質器の燃焼ガス入口と燃料電池のカソード排ガス出口が同一の向きに配置され、
背面側において、改質器の燃焼ガス出口と燃料電池のカソードガス入口が同一の向きに配置され、
両側の側面において、改質器の燃料ガス入口と改質器の改質ガス出口が同一の向きに配置され、
改質器の燃焼ガス入口と燃料電池のカソード排ガス出口の間に複数の触媒燃焼器が配置され、
圧力容器への燃料ガス入口と改質器の改質ガス出口の間に複数の燃料予熱器が配置される、ことを特徴とする一体型燃料電池発電装置が提供される。
【0008】
上記本発明の構成によれば、設置面積の大きい燃料電池と改質器が積層されるので、比較的小出力の場合でも設置面積を小さくすることができる。また、改質器の燃焼ガス入口と燃料電池のカソード排ガス出口、及び改質器の燃焼ガス出口と燃料電池のカソードガス入口がそれぞれ同一の向きに配置されるので、流量の大きいカソードガス及び燃焼ガスの配管をほぼ直線の短い配管にすることができる。また、改質器の燃焼ガス入口と燃料電池のカソード排ガス出口の間に複数(例えば2系統)の触媒燃焼器が配置されるので、触媒燃焼器とその配管を小型化できる。更に、圧力容器への燃料ガス入口と改質器の改質ガス出口が同一の向きに配置され、その間に複数(例えば2系統)の燃料予熱器が配置されるので、比較的流量の小さいアノードガスラインもほぼ直線の短い配管にすることができ、かつ燃料予熱器も小型化できる。
【0009】
従って、積層した燃料電池と改質器を圧力容器に収めた状態で、残る空間に小型化した触媒燃焼器と燃料予熱器を効率良く格納することができ、容器内の空間を有効に活用することができる。また、小口径配管の利用が可能となり,容器内配管が容易となり、結果として、陸上輸送できる大きさの圧力容器内(例えば直径約2m程度)に比較的大出力(例えば500KW前後)の一体型燃料電池発電装置を格納することが可能となる。
【0010】
【発明の実施の形態】
以下、本発明の好ましい実施形態を図面を参照して説明する。なお、各図において共通する部分には同一の符号を付し重複した説明を省略する。
図1は、本発明による一体型燃料電池発電装置の正面斜視図であり、図2は、本発明による一体型燃料電池発電装置の背面斜視図である。
【0011】
本発明の一体型燃料電池発電装置は、燃料予熱器10、改質器12、燃料電池14、触媒燃焼器16、及びこれらを格納する圧力容器(図示せず)からなる。燃料予熱器10は、隔壁式熱交換器(好ましくは、プレートフィン熱交換器)であり、燃料ガス1とアノードガス2との熱交換により、アノードガス2を燃料電池14に適した温度(例えば約600〜650℃)まで冷却すると共に、燃料ガス1を予熱し熱効率を高めるようになっている。
【0012】
改質器12は、水平な隔壁を隔ててガス室Gと改質室Reが対峙したプレート型改質器であり、改質室Reには改質触媒が充填され、ガス室Gにはガスの流れを均一化するように分散用粒子が充填されている。ガス室Gには触媒燃焼器16で発生した高温の燃焼ガス5が供給/排出され、改質室Reには水蒸気を含む燃料ガス1が供給され、ガス室Gからの伝熱で加熱され、改質触媒により水素を含むアノードガス2に改質するようになっている。
【0013】
燃料電池14は、2枚の平板状電極(アノードとカソード)の間に電解質板(タイル)を挟持した単セルを導電性の水平なセパレータ板の間に挟持して積層した積層電池(スタック)である。燃料電池14は、この例では溶融炭酸塩を電解質とする溶融炭酸塩型燃料電池であり、約650℃前後の温度で運転され、水素を含むカノードガス2と酸素を含むカソードガス3とをそれぞれアノードとカソードに供給し、電気を発電するようになっている。触媒燃焼器16は、内部に燃焼触媒が充填され、燃料電池14を出たアノード排ガス4をカソード排ガス7で触媒燃焼させ、高温(例えば約750〜850℃)の燃焼ガス5を発生するようになっている。
【0014】
図1に示すように、本発明の一体型燃料電池発電装置では、燃料電池14の上に改質器12が同一位置に積層される。また、図中の18は、締付け装置であり、上下の締付け板18aの間に、燃料電池14と改質器12を挟持し、複数のコンロッド18bを介してその間を圧縮して燃料電池14と改質器12に所定の面圧を付加すると同時に、燃料電池14と改質器12を一体化している。この構成により、構成機器のうち特に設置面積の大きい燃料電池14と改質器12が積層されるので、比較的小出力の場合でも設置面積を小さくすることができる。
【0015】
また、図1に示すように、改質器12の燃焼ガス5の入口部と燃料電池14のカソード排ガス7の出口部が同一の向きに配置され、同様に、図2に示すように、改質器12の燃焼ガス5の出口部と燃料電池14のカソードガス3の入口部が同一の向きに配置されている。なお、各配管の出入口は、図の下方に位置する図示しない圧力容器の鏡板に設けられている。また、燃料電池14のカソード排ガス7の出口部は、上向き及び下向きに設けられ、下向きの出口部から一部のカソード排ガス7aを直接系外に排出するようになっている。かかる構成により、流量の大きいカソードガス3,カソード排ガス7及び燃焼ガス5の配管をほぼ直線の短い配管にすることができる。
【0016】
更に図1に示すように、複数(この例では、2系統)の触媒燃焼器16が、改質器12の燃焼ガス5の入口部と燃料電池14のカソード排ガス7の出口部の間に配置されている。この構成により、触媒燃焼器16とその配管5,7を小型化でき、容器内空間を有効に活用することができる。
【0017】
また、図1及び図2に示すように、燃料ガス1の入口部と改質器12の改質ガス2の出口部が同一の向きに配置されており、その間に複数(この例では、2系統)の燃料予熱器10が配置されている。この構成により、比較的流量の小さいアノードガスラインもほぼ直線の短い配管にすることができ、かつ燃料予熱器10も小型化できる。
【0018】
なお、本発明は上述した実施形態に限定されず、本発明の要旨を逸脱しない範囲で種々に変更できることは勿論である。
【0019】
【発明の効果】
上述したように、本発明の一体型燃料電池発電装置は、積層した燃料電池と改質器を圧力容器に収めた状態で、残る空間に小型化した触媒燃焼器と燃料予熱器を効率良く格納することができ、容器内空間を有効に活用することができる。また、小口径配管の利用が可能となり,容器内配管が容易となり、結果として、陸上輸送できる大きさの圧力容器内に比較的大出力(例えば500KW前後)の一体型燃料電池発電装置を格納することが可能となる。
【0020】
従って、本発明の一体型燃料電池発電装置は、小型で設置面積が小さく、かつ放熱ロスが少ない、等の優れた効果を有する。
【図面の簡単な説明】
【図1】本発明による一体型燃料電池発電装置の正面斜視図である。
【図2】本発明による一体型燃料電池発電装置の背面斜視図である。
【図3】天然ガスを燃料とする溶融炭酸塩型燃料電池発電設備のフロー図である。
【符号の説明】
1 燃料ガス
2 アノードガス
3 空気
4 アノード排ガス
5 燃焼ガス
7 カソード排ガス
10 燃料予熱器
12 改質器
14 燃料電池
16 触媒燃焼器
18 締付け装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an integrated fuel cell power generation apparatus in which main devices are integrated and housed in the same containment vessel.
[0002]
[Prior art]
Molten carbonate fuel cells have characteristics that are not found in conventional power generators, such as high efficiency and low environmental impact, and are attracting attention as a power generation system following hydropower, thermal power, and nuclear power. Intensive research and development is conducted in each country.
[0003]
FIG. 3 is a flowchart of a power generation facility using a molten carbonate fuel cell using natural gas as a fuel, and includes a fuel preheater 10, a reformer 12, a fuel cell 14, and a catalytic combustor 16. . The fuel gas 1 is drowned by the fuel preheater 10, supplied to the reforming chamber Re of the reformer 12, reformed to the anode gas 2 containing hydrogen, cooled by the fuel preheater 10, and then the anode side of the fuel cell 14. A is supplied to A, where most of the hydrogen is consumed by the anodic reaction to become the anode exhaust gas 4, the unburned portion is burned in the catalytic combustor 16 to generate the high-temperature combustion gas 5, and the gas in the reformer 12 After being supplied to the chamber G and heating the reforming chamber Re, it is discharged out of the system. On the other hand, the air 3 containing CO 2 is supplied to the cathode side C of the fuel cell 14, where a part of oxygen is consumed by the cathode reaction to become the cathode exhaust gas 7, and a part thereof is supplied to the catalytic combustor 16. The anode exhaust gas 4 is burned. The remaining portion 7a of the cathode exhaust gas 7 comes out of the system and is mixed into the air 3 through a circulation path (not shown) so as to circulate and supply CO2 required for the cathode reaction.
[0004]
[Problems to be solved by the invention]
The above-described fuel cell power generator can be made more efficient and downsized by operating under pressure. However, in the conventional apparatus, the fuel preheater 10, the reformer 12, the fuel cell 14, and the catalyst combustor 16 are housed in separate pressure vessels, and each device is connected by piping. In the case of output, there is a problem that the installation area becomes large.
[0005]
In addition, the piping connecting each device is a large-diameter piping due to the flow of a large amount of high-temperature gas, making it difficult to bend or keep the piping warm, resulting in a large heat dissipation loss and a decrease in the efficiency of the entire generator. there were.
[0006]
The present invention has been made to solve such problems. That is, an object of the present invention is to provide an integrated fuel cell power generator that is small in size, has a small installation area, and has a small heat dissipation loss.
[0007]
[Means for Solving the Problems]
According to the present invention, the fuel preheater, the reformer, the fuel cell, the catalytic combustor, and the pressure vessel for storing them, the fuel cell and the reformer are stacked,
On the front side, the combustion gas inlet to the reformer and the cathode exhaust gas outlet of the fuel cell are arranged in the same direction,
On the back side, the combustion gas outlet of the reformer and the cathode gas inlet to the fuel cell are arranged in the same direction,
On both sides , the fuel gas inlet to the reformer and the reformer outlet of the reformer are arranged in the same direction,
A plurality of catalytic combustors are disposed between the combustion gas inlet to the reformer and the cathode exhaust gas outlet of the fuel cell,
An integrated fuel cell power generator is provided, wherein a plurality of fuel preheaters are disposed between a fuel gas inlet to the pressure vessel and a reformed gas outlet of the reformer.
[0008]
According to the configuration of the present invention, since the fuel cell and the reformer having a large installation area are stacked, the installation area can be reduced even when the output is relatively small. Further, the combustion gas inlet and the fuel cell cathode exhaust outlet to the reformer, and since the cathode gas inlet to the combustion gas outlet and a fuel cell reformer is arranged in the same direction respectively, the flow rate of the larger cathode gas In addition, the combustion gas piping can be a short straight tube. In addition, since a plurality of (for example, two systems) catalyst combustors are disposed between the combustion gas inlet to the reformer and the cathode exhaust gas outlet of the fuel cell, the catalyst combustor and its piping can be reduced in size. Further, the fuel gas inlet to the pressure vessel and the reformer gas outlet of the reformer are arranged in the same direction, and a plurality of (for example, two systems) fuel preheaters are arranged between them. The gas line can also be a short straight pipe, and the fuel preheater can be downsized.
[0009]
Therefore, in a state where the stacked fuel cell and the reformer are housed in the pressure vessel, it is possible to efficiently store the downsized catalyst combustor and the fuel preheater in the remaining space, and effectively use the space in the vessel. be able to. In addition, it is possible to use small-diameter piping, which facilitates piping within the container. As a result, a relatively large output (for example, around 500 kW) is integrated into a pressure vessel (for example, about 2 m in diameter) that can be transported by land. The fuel cell power generator can be stored.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings. In addition, the same code | symbol is attached | subjected to the common part in each figure, and the overlapping description is abbreviate | omitted.
FIG. 1 is a front perspective view of an integrated fuel cell power generator according to the present invention, and FIG. 2 is a rear perspective view of the integrated fuel cell power generator according to the present invention.
[0011]
The integrated fuel cell power generator of the present invention comprises a fuel preheater 10, a reformer 12, a fuel cell 14, a catalytic combustor 16, and a pressure vessel (not shown) for storing them. The fuel preheater 10 is a partition wall heat exchanger (preferably a plate fin heat exchanger), and the heat exchange between the fuel gas 1 and the anode gas 2 causes the anode gas 2 to be heated to a temperature suitable for the fuel cell 14 (for example, In addition, the fuel gas 1 is preheated to increase the thermal efficiency.
[0012]
The reformer 12 is a plate type reformer in which the gas chamber G and the reforming chamber Re face each other across a horizontal partition, the reforming chamber Re is filled with a reforming catalyst, and the gas chamber G is filled with a gas. The particles for dispersion are packed so as to make the flow of water uniform. The gas chamber G is supplied / exhausted with the high-temperature combustion gas 5 generated in the catalytic combustor 16, the fuel gas 1 containing water vapor is supplied to the reforming chamber Re, and is heated by heat transfer from the gas chamber G. The reforming catalyst reforms the anode gas 2 containing hydrogen.
[0013]
The fuel cell 14 is a stacked battery (stack) in which a single cell having an electrolyte plate (tile) sandwiched between two flat electrodes (anode and cathode) is sandwiched between conductive horizontal separator plates. . In this example, the fuel cell 14 is a molten carbonate fuel cell using molten carbonate as an electrolyte, and is operated at a temperature of about 650 ° C., and the anode gas 2 containing hydrogen gas and the cathode gas 3 containing oxygen are respectively used as anodes. And is supplied to the cathode to generate electricity. The catalytic combustor 16 is filled with a combustion catalyst, and the anode exhaust gas 4 exiting the fuel cell 14 is catalytically combusted with the cathode exhaust gas 7 to generate high-temperature (for example, about 750 to 850 ° C.) combustion gas 5. It has become.
[0014]
As shown in FIG. 1, in the integrated fuel cell power generator of the present invention, the reformer 12 is stacked on the fuel cell 14 at the same position. Reference numeral 18 in the figure denotes a clamping device, which sandwiches the fuel cell 14 and the reformer 12 between upper and lower clamping plates 18a and compresses the fuel cell 14 and the reformer 12 via a plurality of connecting rods 18b. At the same time as applying a predetermined surface pressure to the reformer 12, the fuel cell 14 and the reformer 12 are integrated. With this configuration, since the fuel cell 14 and the reformer 12 having a particularly large installation area among the constituent devices are stacked, the installation area can be reduced even when the output is relatively small.
[0015]
Further, as shown in FIG. 1, the inlet portion of the combustion gas 5 of the reformer 12 and the outlet portion of the cathode exhaust gas 7 of the fuel cell 14 are arranged in the same direction. Similarly, as shown in FIG. The outlet part of the combustion gas 5 of the mass device 12 and the inlet part of the cathode gas 3 of the fuel cell 14 are arranged in the same direction. In addition, the entrance / exit of each piping is provided in the end plate of the pressure vessel which is not shown in the figure located in the downward direction. Further, the outlet of the cathode exhaust gas 7 of the fuel cell 14 is provided upward and downward, and a part of the cathode exhaust 7a is directly discharged out of the system from the downward outlet. With such a configuration, the pipes of the cathode gas 3, the cathode exhaust gas 7 and the combustion gas 5 having a large flow rate can be made into a substantially straight short pipe.
[0016]
Further, as shown in FIG. 1, a plurality of (in this example, two systems) catalytic combustors 16 are disposed between the inlet portion of the combustion gas 5 of the reformer 12 and the outlet portion of the cathode exhaust gas 7 of the fuel cell 14. Has been. With this configuration, the catalytic combustor 16 and its pipes 5 and 7 can be downsized, and the space in the container can be effectively utilized.
[0017]
Further, as shown in FIGS. 1 and 2, the inlet portion of the fuel gas 1 and the outlet portion of the reformed gas 2 of the reformer 12 are arranged in the same direction, and a plurality of (in this example, 2 System) fuel preheater 10 is arranged. With this configuration, the anode gas line with a relatively small flow rate can be made into a substantially straight short pipe, and the fuel preheater 10 can be downsized.
[0018]
In addition, this invention is not limited to embodiment mentioned above, Of course, it can change variously in the range which does not deviate from the summary of this invention.
[0019]
【The invention's effect】
As described above, the integrated fuel cell power generator according to the present invention efficiently stores the miniaturized catalyst combustor and the fuel preheater in the remaining space while the stacked fuel cell and the reformer are housed in the pressure vessel. It is possible to effectively use the space in the container. In addition, it is possible to use small-diameter piping, which facilitates piping inside the container. As a result, the integrated fuel cell power generator having a relatively large output (for example, around 500 KW) is stored in a pressure vessel of a size that can be transported by land. It becomes possible.
[0020]
Therefore, the integrated fuel cell power generator of the present invention has excellent effects such as small size, a small installation area, and a small heat loss.
[Brief description of the drawings]
FIG. 1 is a front perspective view of an integrated fuel cell power generator according to the present invention.
FIG. 2 is a rear perspective view of an integrated fuel cell power generator according to the present invention.
FIG. 3 is a flow diagram of a molten carbonate fuel cell power generation facility using natural gas as fuel.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Fuel gas 2 Anode gas 3 Air 4 Anode exhaust gas 5 Combustion gas 7 Cathode exhaust gas 10 Fuel preheater 12 Reformer 14 Fuel cell 16 Catalytic combustor 18 Tightening device

Claims (1)

燃料予熱器、改質器、燃料電池、触媒燃焼器、及びこれらを格納する圧力容器からなり、燃料電池と改質器が積層され、
正面側において、改質器の燃焼ガス入口と燃料電池のカソード排ガス出口が同一の向きに配置され、
背面側において、改質器の燃焼ガス出口と燃料電池のカソードガス入口が同一の向きに配置され、
両側の側面において、改質器の燃料ガス入口と改質器の改質ガス出口が同一の向きに配置され、
改質器の燃焼ガス入口と燃料電池のカソード排ガス出口の間に複数の触媒燃焼器が配置され、
圧力容器への燃料ガス入口と改質器の改質ガス出口の間に複数の燃料予熱器が配置される、ことを特徴とする一体型燃料電池発電装置。
It consists of a fuel preheater, a reformer, a fuel cell, a catalytic combustor, and a pressure vessel for storing them, and the fuel cell and the reformer are stacked,
On the front side, the combustion gas inlet to the reformer and the cathode exhaust gas outlet of the fuel cell are arranged in the same direction,
On the back side, the combustion gas outlet of the reformer and the cathode gas inlet to the fuel cell are arranged in the same direction,
On both sides , the fuel gas inlet to the reformer and the reformer outlet of the reformer are arranged in the same direction,
A plurality of catalytic combustors are disposed between the combustion gas inlet to the reformer and the cathode exhaust gas outlet of the fuel cell,
An integrated fuel cell power generator, wherein a plurality of fuel preheaters are disposed between a fuel gas inlet to a pressure vessel and a reformed gas outlet of a reformer.
JP24283096A 1996-09-13 1996-09-13 Integrated fuel cell power generator Expired - Fee Related JP3611065B2 (en)

Priority Applications (1)

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Application Number Priority Date Filing Date Title
JP24283096A JP3611065B2 (en) 1996-09-13 1996-09-13 Integrated fuel cell power generator

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JP3611065B2 true JP3611065B2 (en) 2005-01-19

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Publication number Priority date Publication date Assignee Title
JP4598508B2 (en) * 2004-12-22 2010-12-15 本田技研工業株式会社 Fuel cell system
JP4641182B2 (en) * 2004-12-22 2011-03-02 本田技研工業株式会社 Fuel cell system
JP4598510B2 (en) * 2004-12-22 2010-12-15 本田技研工業株式会社 Fuel cell system
US7687172B2 (en) 2004-12-22 2010-03-30 Honda Motor Co., Ltd. Fuel cell system
US7947407B2 (en) * 2005-04-27 2011-05-24 Lilliputian Systems, Inc. Fuel cell apparatus having a small package size
JP5248829B2 (en) * 2007-09-19 2013-07-31 日本電信電話株式会社 Fuel cell module
JP5254588B2 (en) * 2007-10-12 2013-08-07 日本特殊陶業株式会社 Solid oxide fuel cell module
JP5356903B2 (en) * 2009-04-24 2013-12-04 日本特殊陶業株式会社 Solid oxide fuel cell

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