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JP2003109639A - Fuel cell system - Google Patents

Fuel cell system

Info

Publication number
JP2003109639A
JP2003109639A JP2001298130A JP2001298130A JP2003109639A JP 2003109639 A JP2003109639 A JP 2003109639A JP 2001298130 A JP2001298130 A JP 2001298130A JP 2001298130 A JP2001298130 A JP 2001298130A JP 2003109639 A JP2003109639 A JP 2003109639A
Authority
JP
Japan
Prior art keywords
fuel
fuel cell
reformer
reforming
cell system
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001298130A
Other languages
Japanese (ja)
Inventor
Hiroaki Takeuchi
弘明 竹内
Susumu Aikawa
進 相川
Masahiro Kuroishi
正宏 黒石
Satoshi Matsuoka
聡 松岡
Toshiya Abe
俊哉 阿部
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toto Ltd
Original Assignee
Toto Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toto Ltd filed Critical Toto Ltd
Priority to JP2001298130A priority Critical patent/JP2003109639A/en
Publication of JP2003109639A publication Critical patent/JP2003109639A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Fuel Cell (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a fuel cell system of high energy efficiency and high safety and having a reformer free from risk of deformation and fracture. SOLUTION: A heat supply method for reforming is improved by mounting a reformer in a combustion chamber for combusting an unused fuel and an unused oxidant from a fuel cell module. By improving an installation method of a reforming catalyst, the rapid progress of the reforming reaction at an inlet of a fuel passage of the reformer can be inhibited, and the generation of thermal stress caused by reforming can be also reduced.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は改質器を有する燃料
電池システムに関する。
TECHNICAL FIELD The present invention relates to a fuel cell system having a reformer.

【0002】[0002]

【従来の技術】燃料電池は、アノードに燃料を、カソー
ド側に酸化剤を供給し、電解質を介して燃料と酸化剤を
電気化学的に反応させることにより発電する発電素子で
ある。燃料電池の原燃料としては、都市ガス、メタノー
ル、ガソリンなどが代表的であり、原燃料中の水素原
子、炭素原子を、水蒸気や酸素との化学反応である改質
反応により、発電に適した水素や一酸化炭素を主成分と
する改質ガスとして供給するのが一般的である。
2. Description of the Related Art A fuel cell is a power generation element that supplies fuel to an anode and an oxidant to a cathode side and electrochemically reacts the fuel and the oxidant through an electrolyte to generate electricity. Typical raw fuels for fuel cells are city gas, methanol, gasoline, etc., and are suitable for power generation due to the reforming reaction that is a chemical reaction of hydrogen atoms and carbon atoms in raw fuels with water vapor and oxygen. It is generally supplied as a reformed gas containing hydrogen or carbon monoxide as a main component.

【0003】図6は、改質器を有する燃料電池システム
の従来技術の一例である。燃料電池モジュール3におい
ては、改質器1により改質された燃料がアノード側に、
酸化剤がカソード側に導入され、電解質を介して燃料と
酸化剤が電気化学的に反応し発電する。導入された燃料
および酸化剤は全量を発電では消費せず、未利用燃料5
および未利用酸化剤6が排出される。
FIG. 6 shows an example of a conventional technique of a fuel cell system having a reformer. In the fuel cell module 3, the fuel reformed by the reformer 1 is directed to the anode side,
The oxidant is introduced to the cathode side, and the fuel and the oxidant electrochemically react with each other through the electrolyte to generate electricity. All of the introduced fuel and oxidant are not consumed in power generation, and unused fuel 5
And the unused oxidant 6 is discharged.

【0004】改質の代表例としては、都市ガスの水蒸気
改質が挙げられ、その改質反応は、一般的に600℃を
こえる温度が必要であり、また、吸熱反応であるため、
改質器1においては、燃料および酸化剤を改質用バーナ
ー2などに供給し燃焼させ、改質に必要な熱量を供給し
ている。
A typical example of reforming is steam reforming of city gas. The reforming reaction generally requires a temperature higher than 600 ° C. and is an endothermic reaction.
In the reformer 1, the fuel and the oxidant are supplied to the reforming burner 2 and the like to be burned, and the amount of heat necessary for the reforming is supplied.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、図6に
示す従来の技術においては、発電反応以外で燃料を消費
するためシステムとしてのエネルギー効率が低いという
問題があった。また、改質器は改質の反応熱により大き
な温度分布が生じやすく、熱応力により変形、時には破
損するといった問題があった。改質器の変形、破損によ
り可燃性ガスが流出した場合、発電効率が低下するのみ
でなく、爆発などの危険性がある。
However, the conventional technique shown in FIG. 6 has a problem that the energy efficiency of the system is low because the fuel is consumed except for the power generation reaction. Further, the reformer has a problem that a large temperature distribution is likely to occur due to the reaction heat of the reforming, which causes deformation and sometimes damage due to thermal stress. When flammable gas flows out due to deformation and damage of the reformer, not only the power generation efficiency is lowered, but also there is a risk of explosion or the like.

【0006】本発明は、このような従来技術の問題点に
鑑み、燃料電池からの未利用燃料および未利用酸化剤を
有効利用して燃料を改質することができ、変形、破損と
いった危険性の少ない改質器を有した燃料電池システム
を提供することを目的とする。
In view of the above problems of the prior art, the present invention can effectively utilize the unused fuel and the unused oxidizer from the fuel cell to reform the fuel, and there is a risk of deformation and damage. An object of the present invention is to provide a fuel cell system having a reformer with less fuel consumption.

【0007】[0007]

【課題を解決するための手段】前記課題を解決するため
に、第1の発明では、改質器を燃焼室に設置した改質器
を備えた燃料電池システムを提供する。前記燃焼室にお
いて生成する燃焼ガスを改質の熱源とし、未利用燃料と
未利用酸化剤の持つ熱エネルギーを有効に利用してい
る。
In order to solve the above problems, the first invention provides a fuel cell system having a reformer in which a reformer is installed in a combustion chamber. The combustion gas generated in the combustion chamber is used as a heat source for reforming, and the thermal energy of the unused fuel and the unused oxidant is effectively used.

【0008】また、第2の発明では、改質器の燃料流路
内に設置する改質触媒の活性を、触媒設置範囲の燃料入
口付近で低く、燃料出口付近で高い改質器を備えた燃料
電池システムを提供する。このようにすることにより、
改質器の燃料流路入口で改質反応が急激に進行すること
を抑制し、熱応力の発生を小さくしている。
According to the second aspect of the invention, the reforming catalyst installed in the fuel passage of the reformer has a low activity near the fuel inlet of the catalyst installation range and a high activity near the fuel outlet. Provide a fuel cell system. By doing this,
It suppresses the rapid progress of the reforming reaction at the fuel flow path inlet of the reformer, and reduces the generation of thermal stress.

【0009】また、第3の発明では、改質器の燃料流路
内に設置する改質触媒の触媒設置位置を、燃料流れ方向
において不連続とし、かつ、触媒が設置されない空間
を、燃料出口から入口に向かうに従い大きくした改質器
を備えた燃料電池システムを提供する。このようにする
ことにより、改質器の燃料流路入口で改質反応が急激に
進行することを抑制し、熱応力の発生を小さくしてい
る。
Further, according to the third aspect of the invention, the catalyst installation position of the reforming catalyst installed in the fuel passage of the reformer is discontinuous in the fuel flow direction, and the space where the catalyst is not installed is defined as the fuel outlet. Provided is a fuel cell system including a reformer which is enlarged from the inlet to the inlet. By doing so, it is possible to prevent the reforming reaction from rapidly advancing at the fuel flow path inlet of the reformer and reduce the generation of thermal stress.

【0010】また、第4の発明では、改質器の燃料流路
が互いに平行な複数の流路である場合、改質触媒の燃料
流れ方向の設置位置が、近隣の関係にある燃料流路の間
で同一位置とならないように空隙を持って、改質触媒を
配置した改質器を備えた燃料電池システムを提供する。
このようにすることにより、、改質反応が起こる場所を
流路間で分散させて、熱応力の発生が集中しないように
している。
Further, in the fourth aspect of the invention, when the fuel passages of the reformer are a plurality of passages parallel to each other, the installation positions of the reforming catalyst in the fuel flow direction are in a neighborhood relationship. Provided is a fuel cell system including a reformer in which a reforming catalyst is arranged with a gap so as not to be in the same position between them.
By doing so, the locations where the reforming reaction occurs are dispersed between the flow paths, and the generation of thermal stress is not concentrated.

【0011】また、第5の発明では、燃料電池の種類を
作動温度が高い溶融炭酸塩型燃料電池あるいは固体酸化
物型燃料電池とした改質器を備えた燃料電池システムを
提供する。燃料電池を溶融炭酸塩型燃料電池あるいは固
体酸化物型燃料電池とし、燃焼ガスの温度を高くするこ
とにより、改質反応の速度を向上させ、必要な改質触媒
の量が少なくコンパクトな改質器とすることができる。
The fifth aspect of the present invention provides a fuel cell system including a reformer in which the type of fuel cell is a molten carbonate fuel cell or a solid oxide fuel cell having a high operating temperature. The fuel cell is a molten carbonate fuel cell or a solid oxide fuel cell, and by raising the temperature of the combustion gas, the speed of the reforming reaction is improved, and the amount of required reforming catalyst is small and compact reforming is performed. It can be a bowl.

【0012】[0012]

【発明の実施の形態】以下に本発明の実施の形態を添付
図面に基づいて説明する。図1は本発明に係る改質器を
有する燃料電池システム構成図の一例である。燃料電池
モジュール3は、電解質の両側にアノード及びカソード
を備えた燃料電池素子を複数接続した集合体であり、燃
料がアノードに酸化剤がカソードに供給され、燃料と酸
化剤が電解質を介して電気化学的に反応し発電する。発
電で消費されなかった未利用燃料5および未利用酸化剤
6は燃料電池モジュール3に隣接する燃焼室4において
燃焼し、燃焼室4に設置された燃焼室改質器7で燃料を
改質するための熱源となる。以上のような構成とするこ
とにより、未利用燃料5、未利用酸化剤6の持つ熱エネ
ルギーを損失することなく、改質の熱源とすることがで
きるので、従来の技術と比較して高効率な燃料電池シス
テムとすることができる。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is an example of a configuration diagram of a fuel cell system having a reformer according to the present invention. The fuel cell module 3 is an assembly in which a plurality of fuel cell elements each having an anode and a cathode on both sides of an electrolyte are connected to each other. The fuel is supplied to the anode and the oxidant is supplied to the cathode, and the fuel and the oxidant are electrically supplied via the electrolyte. Reacts chemically to generate electricity. The unused fuel 5 and the unused oxidant 6 which have not been consumed in the power generation burn in the combustion chamber 4 adjacent to the fuel cell module 3 and reform the fuel in the combustion chamber reformer 7 installed in the combustion chamber 4. It becomes a heat source for. With the above-described configuration, the heat energy of the unused fuel 5 and the unused oxidant 6 can be used as a heat source for reforming without loss, so that the efficiency is higher than that of the conventional technology. Fuel cell system.

【0013】燃料としては、都市ガス、メタノール、ガ
ソリンなどが使用可能であり、酸化剤としては空気を用
いるのが一般的である。
City gas, methanol, gasoline or the like can be used as the fuel, and air is generally used as the oxidizer.

【0014】図2は本発明に係る改質器の一例を示して
おり、図2の(a)、(b)、(c)はそれぞれ燃焼室
改質器7の正面外観図、側面外観図、上面外観図であ
り、プレートフィン型熱交換器の燃料流路21に改質触
媒20を設置している。未利用燃料と未利用酸化剤が燃
焼した燃焼ガスは燃焼ガス流路22を通り、また、燃料
は燃料流路21を通り、燃焼ガスの持つ熱エネルギーを
改質の熱源とする。また、改質器は改質反応に伴う反応
熱のため温度分布を生じ、熱応力により改質器の変形、
破損を生じやすい。熱応力を緩和するためには、改質反
応を制御することが必要であり、本発明に係る改質器に
おいては、図3、図4、図5のように改質触媒を設置し
ている。
FIG. 2 shows an example of a reformer according to the present invention, and FIGS. 2 (a), 2 (b) and 2 (c) are front and side views of the combustion chamber reformer 7, respectively. FIG. 4 is an external view of the upper surface, and the reforming catalyst 20 is installed in the fuel flow path 21 of the plate fin type heat exchanger. The combustion gas obtained by burning the unused fuel and the unused oxidant passes through the combustion gas flow path 22, and the fuel passes through the fuel flow path 21, and the thermal energy of the combustion gas is used as the heat source for reforming. In addition, the reformer produces a temperature distribution due to the reaction heat associated with the reforming reaction, and the thermal stress causes deformation of the reformer,
It is easily damaged. In order to reduce the thermal stress, it is necessary to control the reforming reaction. In the reformer according to the present invention, the reforming catalyst is installed as shown in FIGS. 3, 4 and 5. .

【0015】図3は改質触媒設置の一例であり、図2に
おける燃焼室改質器7の断面Aを上面より見た図であ
る。燃料流路21に設置される改質触媒20は、燃料入
口付近に活性の低い触媒を配置し、出口に向かうに従い
活性の高い触媒を配置することにより、燃料入口付近で
偏って起こる改質による熱応力を緩和している。
FIG. 3 is an example of installation of a reforming catalyst, and is a view of a cross section A of the combustion chamber reformer 7 in FIG. 2 as viewed from above. The reforming catalyst 20 installed in the fuel flow path 21 has a catalyst with low activity near the fuel inlet and a catalyst with high activity toward the outlet, which causes uneven reforming near the fuel inlet. Relieves thermal stress.

【0016】また、図4は改質触媒設置の一例であり、
図2における燃焼室改質器7の断面Aを上面より見た図
である。燃料流路21に改質触媒20を設置しない部分
を設け、さらには、その触媒を設置しない部分を、燃料
入口付近で広く、燃料出口付近で狭くすることにより、
燃料入口で偏って起こる改質による熱応力を緩和してい
る。
FIG. 4 shows an example of installing a reforming catalyst,
It is the figure which looked at the cross section A of the combustion chamber reformer 7 in FIG. 2 from the upper surface. By providing a portion where the reforming catalyst 20 is not installed in the fuel flow path 21 and further widening the portion where the catalyst is not installed near the fuel inlet and narrow near the fuel outlet,
It reduces the thermal stress due to reforming that occurs unevenly at the fuel inlet.

【0017】また、図5は改質触媒設置の一例であり、
図2における燃焼室改質器7の断面Aを上面より見た図
である。燃料流路21に改質触媒20を、燃料流れ方向
に空隙を持って配置し、さらには、隣り合う燃料流路で
は、燃料流れ方向で触媒の設置位置が同一でないように
することにより、改質反応が起こる場所を分散させ、熱
応力を緩和している。
FIG. 5 shows an example of installing a reforming catalyst,
It is the figure which looked at the cross section A of the combustion chamber reformer 7 in FIG. 2 from the upper surface. By arranging the reforming catalyst 20 in the fuel flow passage 21 with a gap in the fuel flow direction, and by disposing the catalyst installation positions in adjacent fuel flow passages in the fuel flow direction not to be the same, Disperses the places where quality reactions occur and relaxes thermal stress.

【0018】図2から図5における本発明の実施例にお
いては、改質器は触媒を設置したプレートフィン型の熱
交換器であるが、これは改質のための熱供給の効率を高
める手段の一つであり、他の熱交換手段によっても同様
の効果は期待できる。例えば、改質触媒を内部に設置し
たチューブに熱交換効率向上のためのフィンを設置した
改質器なども考えられる。また、本発明の燃料電池シス
テムにおいては、燃料電池の種類を作動温度が高く、未
利用燃料および未利用酸化剤も高温となる溶融炭酸塩型
燃料電池あるいは固体酸化物型燃料電池を適用すること
により、改質の反応速度を向上させ、改質器を小型化す
ることが可能となる。
In the embodiment of the present invention shown in FIGS. 2 to 5, the reformer is a plate fin type heat exchanger provided with a catalyst, which is a means for increasing the efficiency of heat supply for reforming. The same effect can be expected by other heat exchange means. For example, a reformer in which a fin for improving heat exchange efficiency is installed in a tube in which a reforming catalyst is installed may be considered. Further, in the fuel cell system of the present invention, a molten carbonate fuel cell or a solid oxide fuel cell in which the operating temperature is high and the unused fuel and the unused oxidant are also high in temperature is applied to the fuel cell system of the present invention. Thereby, it becomes possible to improve the reaction speed of reforming and downsize the reformer.

【0019】[0019]

【発明の効果】以上に説明したように、本発明の燃料電
池システムによれば、改質器を燃焼室に設置することに
より、未利用燃料と未利用酸化剤の持つ熱エネルギーを
有効利用することが可能となり、エネルギー効率を高く
することが可能となる。また、本発明の燃料電池システ
ムによれば、改質器に異なる活性の触媒を設置する、あ
るいは、触媒設置位置を工夫することにより、改質器に
発生する熱応力を緩和し、安全性の高い改質器を有する
システムとすることが可能となる。
As explained above, according to the fuel cell system of the present invention, the reformer is installed in the combustion chamber to effectively utilize the thermal energy of the unused fuel and the unused oxidant. It becomes possible to increase energy efficiency. Further, according to the fuel cell system of the present invention, different active catalysts are installed in the reformer, or the catalyst installation position is devised to reduce the thermal stress generated in the reformer and improve safety. A system having a high reformer can be obtained.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明に係る改質器を有する燃料電池システム
の一例
FIG. 1 is an example of a fuel cell system having a reformer according to the present invention.

【図2】本発明に係る改質器の一例FIG. 2 shows an example of a reformer according to the present invention.

【図3】本発明に係る改質器の触媒設置の一例FIG. 3 is an example of installing a catalyst in a reformer according to the present invention.

【図4】本発明に係る改質器の触媒設置の一例FIG. 4 is an example of installing a catalyst in a reformer according to the present invention.

【図5】本発明に係る改質器の触媒設置の一例FIG. 5 shows an example of installing a catalyst in the reformer according to the present invention.

【図6】従来の改質器を有する燃料電池システムの一例FIG. 6 shows an example of a fuel cell system having a conventional reformer.

【符号の説明】[Explanation of symbols]

1:改質器 2:改質用バーナー 3:燃料電池モジュール 4:燃焼室 5:未利用燃料 6:未利用酸化剤 7:燃焼室改質器 20:改質触媒 21:燃料流路 22:燃焼ガス流路 1: reformer 2: reforming burner 3: Fuel cell module 4: Combustion chamber 5: Unused fuel 6: Unused oxidizer 7: Combustion chamber reformer 20: Reforming catalyst 21: Fuel flow path 22: Combustion gas flow path

───────────────────────────────────────────────────── フロントページの続き (72)発明者 黒石 正宏 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 松岡 聡 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 阿部 俊哉 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 Fターム(参考) 4G040 EA02 EA03 EA06 EB44 EC07 5H026 AA05 AA06 5H027 AA05 AA06 BA09 BA10    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Masahiro Kuroishi             2-1-1 Nakajima, Kokurakita-ku, Kitakyushu City, Fukuoka Prefecture             No. Totoki Equipment Co., Ltd. (72) Inventor Satoshi Matsuoka             2-1-1 Nakajima, Kokurakita-ku, Kitakyushu City, Fukuoka Prefecture             No. Totoki Equipment Co., Ltd. (72) Inventor Toshiya Abe             2-1-1 Nakajima, Kokurakita-ku, Kitakyushu City, Fukuoka Prefecture             No. Totoki Equipment Co., Ltd. F-term (reference) 4G040 EA02 EA03 EA06 EB44 EC07                 5H026 AA05 AA06                 5H027 AA05 AA06 BA09 BA10

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 電解質の両側にアノード及びカソードを
備えた燃料電池を複数接合した燃料電池モジュールと、
前記燃料電池モジュールに酸化剤を供給する酸化剤供給
手段と、前記燃料電池モジュールに改質可能な燃料を供
給する燃料供給手段と、前記燃料供給手段より供給され
た燃料を改質して前記燃料電池モジュールに改質ガスを
供給する改質触媒を具備した改質器と、前記燃料電池モ
ジュールから排出される未利用燃料と未利用酸化剤を燃
焼させる燃焼室と、を備えた燃料電池システムであっ
て、前記改質器が前記燃焼室に設置されることを特徴と
する燃料電池システム。
1. A fuel cell module in which a plurality of fuel cells having an anode and a cathode on both sides of an electrolyte are joined together,
An oxidant supply means for supplying an oxidant to the fuel cell module, a fuel supply means for supplying a reformable fuel to the fuel cell module, and a fuel supplied from the fuel supply means for reforming the fuel. A fuel cell system including a reformer having a reforming catalyst for supplying reformed gas to a cell module, and a combustion chamber for burning unused fuel and unused oxidant discharged from the fuel cell module. A fuel cell system, wherein the reformer is installed in the combustion chamber.
【請求項2】 前期改質器の燃料流路内に設置される改
質触媒の活性が、触媒設置範囲の燃料入口付近で低く、
燃料出口付近で高いことを特徴とする請求項1記載の燃
料電池システム。
2. The activity of the reforming catalyst installed in the fuel passage of the former reformer is low near the fuel inlet of the catalyst installation range,
The fuel cell system according to claim 1, wherein the fuel cell system is high near the fuel outlet.
【請求項3】 前期改質器の燃料流路内に設置される改
質触媒の触媒設置位置が、燃料流れ方向において不連続
であり、かつ、触媒が設置されない空間が、燃料入口か
ら出口に向かうに従い、小さくなることを特徴とする請
求項1記載の燃料電池システム。
3. The catalyst installation position of the reforming catalyst installed in the fuel passage of the former reformer is discontinuous in the fuel flow direction, and the space where the catalyst is not installed is from the fuel inlet to the outlet. The fuel cell system according to claim 1, wherein the fuel cell system is reduced in size as it goes.
【請求項4】 前期改質器の燃料流路が互いに平行な複
数の流路であり、改質触媒の燃料流れ方向の設置位置
が、近隣の関係にある燃料流路の間で、同一位置となら
ないように空隙を持って、改質触媒が配置されることを
特徴とする請求項1記載の燃料電池システム。
4. The fuel passages of the former reformer are a plurality of passages that are parallel to each other, and the installation positions of the reforming catalysts in the fuel flow direction are the same in the neighboring fuel passages. The fuel cell system according to claim 1, wherein the reforming catalyst is arranged so as to have a void so as not to occur.
【請求項5】 前記燃料電池が溶融炭酸塩型燃料電池あ
るいは固体酸化物型燃料電池であることを特徴とする請
求項1〜4いずかれ一項に記載の燃料電池システム。
5. The fuel cell system according to any one of claims 1 to 4, wherein the fuel cell is a molten carbonate fuel cell or a solid oxide fuel cell.
JP2001298130A 2001-09-27 2001-09-27 Fuel cell system Pending JP2003109639A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001298130A JP2003109639A (en) 2001-09-27 2001-09-27 Fuel cell system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001298130A JP2003109639A (en) 2001-09-27 2001-09-27 Fuel cell system

Publications (1)

Publication Number Publication Date
JP2003109639A true JP2003109639A (en) 2003-04-11

Family

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Family Applications (1)

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Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005340075A (en) * 2004-05-28 2005-12-08 Kyocera Corp Operation stopping method of fuel cell
JP2006273635A (en) * 2005-03-29 2006-10-12 Idemitsu Kosan Co Ltd Reformer and fuel cell system
JP2007290900A (en) * 2006-04-24 2007-11-08 Toyota Central Res & Dev Lab Inc Heat exchange-type reformer
US8114546B2 (en) 2006-09-29 2012-02-14 Hitachi, Ltd. Fuel cell power generation system and method of operating thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08102326A (en) * 1994-09-30 1996-04-16 Osaka Gas Co Ltd Fuel cell power generating system
JPH0930801A (en) * 1995-07-19 1997-02-04 Mitsubishi Electric Corp Reformation reactor
JPH09249402A (en) * 1996-03-15 1997-09-22 Mitsubishi Electric Corp Modifying equipment
JP2001080904A (en) * 1999-09-08 2001-03-27 Fuji Electric Co Ltd Fuel reformer

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08102326A (en) * 1994-09-30 1996-04-16 Osaka Gas Co Ltd Fuel cell power generating system
JPH0930801A (en) * 1995-07-19 1997-02-04 Mitsubishi Electric Corp Reformation reactor
JPH09249402A (en) * 1996-03-15 1997-09-22 Mitsubishi Electric Corp Modifying equipment
JP2001080904A (en) * 1999-09-08 2001-03-27 Fuji Electric Co Ltd Fuel reformer

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005340075A (en) * 2004-05-28 2005-12-08 Kyocera Corp Operation stopping method of fuel cell
JP2006273635A (en) * 2005-03-29 2006-10-12 Idemitsu Kosan Co Ltd Reformer and fuel cell system
JP2007290900A (en) * 2006-04-24 2007-11-08 Toyota Central Res & Dev Lab Inc Heat exchange-type reformer
US8114546B2 (en) 2006-09-29 2012-02-14 Hitachi, Ltd. Fuel cell power generation system and method of operating thereof
US8377600B2 (en) 2006-09-29 2013-02-19 Hitachi, Ltd. Fuel cell power generation system and method of operating thereof

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