JPH0945349A - Fuel cell power generation device - Google Patents
Fuel cell power generation deviceInfo
- Publication number
- JPH0945349A JPH0945349A JP7192884A JP19288495A JPH0945349A JP H0945349 A JPH0945349 A JP H0945349A JP 7192884 A JP7192884 A JP 7192884A JP 19288495 A JP19288495 A JP 19288495A JP H0945349 A JPH0945349 A JP H0945349A
- Authority
- JP
- Japan
- Prior art keywords
- fuel cell
- reformed gas
- fuel
- power generation
- main body
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Fuel Cell (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、反応ガスを受けて
電気化学反応により発電する燃料電池発電装置の高熱利
用構成に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a high heat utilization configuration of a fuel cell power generator which receives a reaction gas and generates electricity by an electrochemical reaction.
【0002】[0002]
【従来の技術】燃料電池発電装置は燃料電池本体と燃料
改質器を主要機器として構成されており、反応ガスとし
て天然ガス等の燃料を燃料改質器で改質して得られた改
質ガスと空気とを燃料電池本体に送り、改質ガス中の水
素と空気中の酸素から電気化学反応によって電力を取り
出すものである。2. Description of the Related Art A fuel cell power generator is mainly composed of a fuel cell main body and a fuel reformer, and is a reformer obtained by reforming a fuel such as natural gas as a reaction gas in the fuel reformer. Gas and air are sent to the fuel cell body, and electric power is taken out from hydrogen in the reformed gas and oxygen in the air by an electrochemical reaction.
【0003】図3は、従来より用いられている燃料電池
発電装置の反応ガス系統の基本構成図である。図におい
て、燃料電池本体1は模式的に示されており、図示しな
い電解質層を燃料極と空気極とにより挟持する単セル
と、単セルを複数個積層する毎に配設される冷却管3を
有する冷却板2から構成されている。燃料は、水蒸気分
離器7より供給される水蒸気と一定の割合で混合されて
燃料改質器4へと送られ、燃料改質器4の触媒層を通っ
て水素濃度の高い改質ガスが生成され、燃料電池本体1
の燃料極へと供給される。一方の空気極へはブロア6に
よって空気が供給される。燃料電池本体1での電気化学
反応に寄与しなかった残余の水素を含んで燃料極より排
出される改質ガスは、燃料改質器4の改質器バーナー5
へと送られ、ブロア10によって送られる空気と反応し
て燃焼され、燃料改質器4を加熱し改質反応をサポート
するために用いられる。燃料電池本体1の冷却板2に埋
設された冷却管3には、冷却水循環ポンプ8により冷却
水熱回収用熱交換器9を介して水蒸気分離器7より送ら
れる冷却水が通流され、電気化学反応にともなう発熱が
除去され、燃料電池本体1の温度が一定に保持される。
加熱された冷却水は、水蒸気分離器7へと戻され、水と
水蒸気とに分離され、水蒸気の一部は上記のように燃料
の改質に用いられる。FIG. 3 is a basic configuration diagram of a reaction gas system of a conventional fuel cell power generator. In the figure, the fuel cell main body 1 is schematically shown. A unit cell in which an electrolyte layer (not shown) is sandwiched between a fuel electrode and an air electrode, and a cooling pipe 3 arranged every time a plurality of unit cells are stacked. Is composed of a cooling plate 2. The fuel is mixed with the steam supplied from the steam separator 7 at a constant ratio and sent to the fuel reformer 4, and a reformed gas having a high hydrogen concentration is generated through a catalyst layer of the fuel reformer 4. Fuel cell body 1
Is supplied to the fuel electrode. Air is supplied to one air electrode by the blower 6. The reformed gas discharged from the fuel electrode containing the residual hydrogen that has not contributed to the electrochemical reaction in the fuel cell body 1 is the reformer burner 5 of the fuel reformer 4.
Is used to heat and reform the fuel reformer 4 to support the reforming reaction. Cooling water sent from the steam separator 7 is passed through the cooling water circulation pump 8 through the cooling water heat recovery heat exchanger 9 to the cooling pipe 3 embedded in the cooling plate 2 of the fuel cell main body 1 to generate electricity. The heat generated by the chemical reaction is removed, and the temperature of the fuel cell body 1 is kept constant.
The heated cooling water is returned to the steam separator 7 and separated into water and steam, and a part of the steam is used for reforming the fuel as described above.
【0004】[0004]
【発明が解決しようとする課題】燃料電池本体1の発電
特性は反応ガスの供給量が増大するほど向上する。また
反応ガスの供給量が多量となるほど面内の均一度が向上
するので局部的な負担が軽減する。また、長寿命化を図
るためには反応ガスの供給量を増大して局部的な集中を
回避することが効果的であると考えられている。したが
って、これらの電池特性の向上の点においては燃料改質
ガスと空気の供給量の増大が望ましい。このうち空気に
ついては、供給量の増大にさしたる支障はなくすでに増
大が図られている。しかしながら、燃料改質ガスの供給
量を増大すると、改質器バーナー5へと送られる排出改
質ガスの量が増大し、燃料改質器4の温度が温度制御限
界を越えて上昇する恐れがある。したがって、これを避
けるために燃料極から排出される改質ガスの一部を改質
器バーナー5へ送ることなく外部へ排出する方法が採ら
れているが、この方法においては改質ガスが外部へ直接
排出されるので燃料電池発電装置の総合効率が低下して
しまうという難点があり、かつ可燃性の改質ガスが外部
へ直接排出されるので安全性が低下するという難点があ
る。The power generation characteristics of the fuel cell body 1 are improved as the supply amount of the reaction gas is increased. Further, as the supply amount of the reaction gas increases, the in-plane uniformity increases, so that the local burden is reduced. Further, in order to extend the life, it is considered effective to increase the supply amount of the reaction gas to avoid local concentration. Therefore, it is desirable to increase the supply amount of the fuel reforming gas and air in order to improve the cell characteristics. Of these, air has already been increased without any obstacle to the increase in supply. However, if the supply amount of the fuel reformed gas is increased, the amount of the exhausted reformed gas sent to the reformer burner 5 is increased, and the temperature of the fuel reformer 4 may rise above the temperature control limit. is there. Therefore, in order to avoid this, a method is adopted in which a part of the reformed gas discharged from the fuel electrode is discharged to the outside without being sent to the reformer burner 5. In this method, the reformed gas is discharged to the outside. However, there is a problem in that the overall efficiency of the fuel cell power generator is reduced because it is directly discharged to the outside, and there is a problem that the safety is deteriorated because the combustible reformed gas is directly discharged to the outside.
【0005】この発明の目的は、上記の難点を解消し
て、総合効率が高く、かつ安全で、電池特性の優れた燃
料電池発電装置を提供することにある。An object of the present invention is to solve the above problems and provide a fuel cell power generator having high overall efficiency, safety, and excellent cell characteristics.
【0006】[0006]
【課題を解決するための手段】上記の目的を達成するた
めに、本発明においては、燃料を水素濃度の高い改質ガ
スに改質する燃料改質器と、改質ガスと空気を導入して
電気化学反応により発電する燃料電池本体とを備え、燃
料電池本体より排出される改質ガスを燃料改質器の改質
エネルギーとして使用する燃料電池発電装置において、
燃料電池本体より排出される改質ガスの一部と燃料電池
本体より排出される空気の少なくとも一部を導入して燃
焼する触媒燃焼器と、燃焼により生じた熱を回収する熱
交換器を備えることとする。In order to achieve the above object, in the present invention, a fuel reformer for reforming a fuel into a reformed gas having a high hydrogen concentration, and a reformed gas and air are introduced. In a fuel cell power generation device that uses a reformed gas discharged from the fuel cell body as reforming energy of a fuel reformer,
A catalytic combustor for introducing and burning a part of the reformed gas discharged from the fuel cell body and at least a part of the air discharged from the fuel cell body, and a heat exchanger for recovering heat generated by the combustion I will.
【0007】このように構成すれば、燃料電池本体へ送
る改質ガスの供給量を増大して発電特性を向上させる場
合において、燃料電池本体より排出される改質ガスのう
ち改質器バーナーの能力を越えるものを触媒燃焼器を経
て熱交換器へ送ることとすれば、燃料改質器の温度が過
大となることはなく、かつ触媒燃焼器で空気と反応させ
て燃焼させ、生成熱を熱交換器で回収することにより効
果的に熱利用される。また、本構成では改質ガスは燃焼
させたのち排出されるので安全である。According to this structure, when the amount of reformed gas sent to the fuel cell main body is increased to improve the power generation characteristics, the reformer burner out of the reformed gas discharged from the fuel cell main body is used. If the excess of capacity is sent to the heat exchanger through the catalytic combustor, the temperature of the fuel reformer will not become excessive and the catalytic combustor will react with air to burn and generate heat. The heat is effectively used by recovering it with the heat exchanger. Further, in this configuration, the reformed gas is discharged after being burned, which is safe.
【0008】[0008]
【発明の実施の形態】図1は、この発明の実施の形態を
示す燃料電池発電装置の反応ガス系統の基本構成図であ
る。本図において、図3に示した従来の形態と同一の機
能を有する構成部品には同一符号を付して重複する説明
は略する。本図の図3との相違点は、燃料電池本体1の
燃料極と空気極から排出される排出改質ガスの一部と排
出空気の一部が、それぞれ制御弁11と手動弁14を介
して触媒燃焼器12に送られ、さらに熱交換器13に送
られたのち排出されるように構成されていることにあ
る。したがって、本構成においては、電池特性を向上さ
せるために改質ガスの供給量を増大する際にも、改質器
バーナーに対して過剰となる排出改質ガスは全て触媒燃
焼器12へ送られて燃焼され、熱交換器13で生成熱が
回収されるので燃料電池発電装置の総合効率が向上する
こととなり、かつ可燃性ガスが放出されることがないの
で安全である。FIG. 1 is a basic configuration diagram of a reaction gas system of a fuel cell power generator showing an embodiment of the present invention. In this figure, components having the same functions as those of the conventional embodiment shown in FIG. 3 is different from FIG. 3 in that a part of the exhaust reformed gas discharged from the fuel electrode and the air electrode of the fuel cell main body 1 and a part of the exhaust air pass through the control valve 11 and the manual valve 14, respectively. Is sent to the catalytic combustor 12, is further sent to the heat exchanger 13, and is then discharged. Therefore, in this configuration, even when the supply amount of the reformed gas is increased in order to improve the battery characteristics, all the exhausted reformed gas that is excessive with respect to the reformer burner is sent to the catalytic combustor 12. The heat generated by the heat exchanger 13 is recovered by the heat exchanger 13, so that the overall efficiency of the fuel cell power generator is improved, and the combustible gas is not released, which is safe.
【0009】図2は、この発明の他の実施の形態を示す
燃料電池発電装置の反応ガス系統の基本構成図である。
図2の図1との相違点は、燃料電池本体1の空気極から
排出される排出空気が全て触媒燃焼器12に送られ、熱
交換器13を経て排出されるように構成されている点に
ある。本構成においても、図1の場合と同様に、過剰な
排出改質ガスは全て触媒燃焼器12へ送られて燃焼さ
れ、熱交換器13で生成熱が回収されることとなる。FIG. 2 is a basic configuration diagram of a reaction gas system of a fuel cell power generator showing another embodiment of the present invention.
2 is different from FIG. 1 in that all the exhaust air discharged from the air electrode of the fuel cell body 1 is sent to the catalytic combustor 12 and is discharged via the heat exchanger 13. It is in. Also in this configuration, as in the case of FIG. 1, all the excess reformed reformed gas is sent to the catalytic combustor 12 and burned, and the heat generated by the heat exchanger 13 is recovered.
【0010】[0010]
【発明の効果】上述のごとく、本発明においては、燃料
を水素濃度の高い改質ガスに改質する燃料改質器と、改
質ガスと空気を導入して電気化学反応により発電する燃
料電池本体とを備え、燃料電池本体より排出される改質
ガスを燃料改質器の改質エネルギーとして使用する燃料
電池発電装置において、燃料電池本体より排出される改
質ガスの一部と燃料電池本体より排出される空気の少な
くとも一部を導入して燃焼する触媒燃焼器と、燃焼によ
り生じた熱を回収する熱交換器を備えることとしたの
で、電池特性を向上させるために改質ガスの供給量を増
大する際にも効果的に熱利用が図られ、総合効率が高
く、かつ安全で電池特性の優れた燃料電池発電装置が得
られることとなった。As described above, according to the present invention, a fuel reformer for reforming a fuel into a reformed gas having a high hydrogen concentration, and a fuel cell for introducing a reformed gas and air to generate electricity by an electrochemical reaction. In a fuel cell power generator including a main body and using reformed gas discharged from the fuel cell main body as reforming energy of a fuel reformer, a part of the reformed gas discharged from the fuel cell main body and the fuel cell main body Since it is equipped with a catalytic combustor that introduces and combusts at least a portion of the air that is exhausted from it, and a heat exchanger that recovers the heat generated by combustion, the supply of reformed gas to improve the battery characteristics Even when the amount is increased, the heat can be effectively utilized, and it is possible to obtain a fuel cell power generator having high overall efficiency, safety, and excellent cell characteristics.
【図1】この発明の実施の形態を示す燃料電池発電装置
の反応ガス系統の基本構成図FIG. 1 is a basic configuration diagram of a reaction gas system of a fuel cell power generator showing an embodiment of the present invention.
【図2】この発明の他の実施の形態を示す燃料電池発電
装置の反応ガス系統の基本構成図FIG. 2 is a basic configuration diagram of a reaction gas system of a fuel cell power generator showing another embodiment of the present invention.
【図3】従来より用いられている燃料電池発電装置の反
応ガス系統の基本構成図FIG. 3 is a basic configuration diagram of a reaction gas system of a conventional fuel cell power generator.
1 燃料電池本体 2 冷却板 4 燃料改質器 5 改質器バーナー 6 ブロア 7 水蒸気分離器 10 ブロア 11 制御弁 12 触媒燃焼器 13 熱交換器 14 手動弁 1 Fuel Cell Main Body 2 Cooling Plate 4 Fuel Reformer 5 Reformer Burner 6 Blower 7 Steam Separator 10 Blower 11 Control Valve 12 Catalytic Combustor 13 Heat Exchanger 14 Manual Valve
Claims (1)
燃料改質器と、改質ガスと空気を導入して電気化学反応
により発電する燃料電池本体とを備え、燃料電池本体よ
り排出される改質ガスを燃料改質器の改質エネルギーと
して使用する燃料電池発電装置において、燃料電池本体
より排出される改質ガスの一部と燃料電池本体より排出
される空気の少なくとも一部を導入して燃焼する触媒燃
焼器と、燃焼により生じた熱を回収する熱交換器が備え
られていることを特徴とする燃料電池発電装置。1. A fuel reformer for reforming a fuel into a reformed gas having a high hydrogen concentration, and a fuel cell main body for introducing reformed gas and air to generate electricity by an electrochemical reaction. In a fuel cell power generator that uses the discharged reformed gas as reforming energy for a fuel reformer, at least part of the reformed gas discharged from the fuel cell body and at least part of the air discharged from the fuel cell body A fuel cell power generation device comprising: a catalytic combustor that introduces and combusts a gas, and a heat exchanger that recovers heat generated by the combustion.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7192884A JPH0945349A (en) | 1995-07-28 | 1995-07-28 | Fuel cell power generation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7192884A JPH0945349A (en) | 1995-07-28 | 1995-07-28 | Fuel cell power generation device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0945349A true JPH0945349A (en) | 1997-02-14 |
Family
ID=16298587
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7192884A Pending JPH0945349A (en) | 1995-07-28 | 1995-07-28 | Fuel cell power generation device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0945349A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010287426A (en) * | 2009-06-11 | 2010-12-24 | Clearedge Power Inc | Reformer for fixed type power generation plant, fuel cell, and battery managing system |
US8092953B2 (en) | 2007-08-28 | 2012-01-10 | Honda Motor Co., Ltd. | Fuel cell system and method of operating the fuel cell system |
US8980489B2 (en) | 2006-03-27 | 2015-03-17 | Casio Computer Co., Ltd. | Fuel cell type power generation device, electronic apparatus and treatment method of fuel |
-
1995
- 1995-07-28 JP JP7192884A patent/JPH0945349A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8980489B2 (en) | 2006-03-27 | 2015-03-17 | Casio Computer Co., Ltd. | Fuel cell type power generation device, electronic apparatus and treatment method of fuel |
US8092953B2 (en) | 2007-08-28 | 2012-01-10 | Honda Motor Co., Ltd. | Fuel cell system and method of operating the fuel cell system |
JP2010287426A (en) * | 2009-06-11 | 2010-12-24 | Clearedge Power Inc | Reformer for fixed type power generation plant, fuel cell, and battery managing system |
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