JPH09266007A - Fuel cell - Google Patents

Fuel cell

Info

Publication number
JPH09266007A
JPH09266007A JP8073392A JP7339296A JPH09266007A JP H09266007 A JPH09266007 A JP H09266007A JP 8073392 A JP8073392 A JP 8073392A JP 7339296 A JP7339296 A JP 7339296A JP H09266007 A JPH09266007 A JP H09266007A
Authority
JP
Japan
Prior art keywords
fuel
oxidant
oxidizer
cooling water
pipe
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
JP8073392A
Other languages
Japanese (ja)
Inventor
Katsumasa Araoka
勝政 荒岡
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP8073392A priority Critical patent/JPH09266007A/en
Publication of JPH09266007A publication Critical patent/JPH09266007A/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)

Abstract

PROBLEM TO BE SOLVED: To provide a lightweight and small fuel cell in which a surface contact force is kept appropriately to reduce electric and thermal surface resistance so as to prevent mixing of fuel with an oxidizer and leaking of the fuel and the oxidizer out of a single cell and in which end plates are made thinner and smaller. SOLUTION: A clamping rod 6 has a cooling water passage pipe 7, an oxidizer passage pipe 8, and a fuel passage pipe 9, through which cooling water, an oxidizer, and fuel, respectively, flow to the circulating part of the clamping rod 6, with the inlet and outlet of each pipe arranged in symmetry with respect to the center O of a clamping plate 4 on a Y-Z plane. The cooling water passage pipe 7 is connected to a cooling plate to supply and collect the cooling water. Similarly, the oxidizer passage pipe 8 supplies and collects the oxidizer to and from an oxidizer electrode, and the fuel passage pipe 9 is connected to a fuel electrode to supply and collect the fuel. A stacked body 1 is supported by such a clamping rod 6, with a spring 10 provided at one end of the clamping rod 6 so that the stacked body 1 is elastically supported on the clamping plate 4. Thus the clamping rod 6 serves also as the pipe through which a coolant and the like circulates and the pipe elastically supporting the stacked body 1, so that the fuel cell can be made smaller and lighter.

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、燃料電池に関す
る。
TECHNICAL FIELD The present invention relates to a fuel cell.

【0002】[0002]

【従来の技術】燃料電池とは、化学エネルギを直接電気
エネルギに変換する電池であり、具体的には軽油や工業
用燃料の気体と酸素とが電解質で化学反応を起こし、そ
の一部として電力を発生させるものである。
2. Description of the Related Art A fuel cell is a cell that directly converts chemical energy into electric energy. Specifically, gas of light oil or industrial fuel and oxygen cause a chemical reaction in an electrolyte, and as a part of it, electric power is generated. Is generated.

【0003】燃料電池のうち、電解質として水素イオン
伝導性を有する高分子電解質(Polymer Electrolyte Me
mbrane)を用いた固体高分子型燃料電池PEFC(Poly
Electrolyte Fuel Cell )は、コンパクトで高出力(高
電流密度)が得られ、かつ簡略なシステムで運転が可能
なことから、宇宙用や車両用等の電源として注目されて
いる。
Among fuel cells, a polymer electrolyte (polymer electrolyte) having hydrogen ion conductivity is used as an electrolyte.
polymer electrolyte fuel cell PEFC (Poly
Electrolyte Fuel Cell) is gaining attention as a power source for space and vehicles, because it is compact, has high output (high current density), and can be operated with a simple system.

【0004】高分子電解質膜として、スルホン酸基を持
つポリスチレン系の陽イオン交換膜、フルオロカーボン
スルホン酸とポリビニリデンフルオライドとの混合物
質、フルオロカーボンマトリックスにトリフルオロエチ
レンをグラフト化したもの等が知られている。最近で
は、パーフルオロカーボンスルホン酸膜(商品名;ナフ
ィオン:デュポン社製)等が用いられる。
Known polymer electrolyte membranes include polystyrene-based cation exchange membranes having sulfonic acid groups, mixed substances of fluorocarbon sulfonic acid and polyvinylidene fluoride, and grafted trifluoroethylene on a fluorocarbon matrix. ing. Recently, a perfluorocarbon sulfonic acid membrane (trade name; Nafion: manufactured by DuPont) is used.

【0005】以下、従来の燃料電池の構成について、図
面を参照して説明する。図4は、積層体を分解した斜視
図で、図5は、燃料電池の斜視図である。例えば白金か
らなる燃料極101と白金からなる酸化剤極102とが
高分子電解質膜103を狭持し、燃料電池の起電部分1
04を構成する。燃料極101には、燃料配流板105
が、また酸化剤極102には、酸化剤配流板106が接
着される。燃料配流板105が燃料極101と接する面
には、燃料流路となる溝107が、酸化剤配流板106
が酸化剤極102と接する面には、酸化剤流路となる溝
108が設けられる。燃料配流板105と酸化剤配流板
106とは、集電体である。また、高分子電解質膜10
3と酸化剤配流板106との間には、酸化剤極102の
形状に切り欠いた穴が形成されるシートパッキング10
9が狭着される。燃料配流板105には、冷却板110
が接着される。冷却板110は、加湿水透過板111と
冷却水配流板112とが張り合わせて構成される。冷却
水配流板112の加湿水透過板111側の面には冷却水
が流通可能な溝113が設けられる。
The structure of a conventional fuel cell will be described below with reference to the drawings. FIG. 4 is an exploded perspective view of the stack, and FIG. 5 is a perspective view of the fuel cell. For example, the fuel electrode 101 made of platinum and the oxidant electrode 102 made of platinum sandwich the polymer electrolyte membrane 103, and the electromotive portion 1 of the fuel cell is formed.
Make up 04. The fuel distribution plate 105 is provided on the fuel electrode 101.
However, the oxidant distribution plate 106 is bonded to the oxidant electrode 102. On the surface of the fuel distribution plate 105 in contact with the fuel electrode 101, a groove 107 serving as a fuel flow path is provided with an oxidizer distribution plate 106.
A groove 108 that serves as an oxidant flow path is provided on the surface that contacts the oxidant electrode 102. The fuel distribution plate 105 and the oxidant distribution plate 106 are current collectors. In addition, the polymer electrolyte membrane 10
The sheet packing 10 in which a hole cut out in the shape of the oxidizer electrode 102 is formed between the oxidizer distributor 3 and the oxidizer distribution plate 106.
9 is narrowed down. The fuel distribution plate 105 includes a cooling plate 110.
Are adhered. The cooling plate 110 is configured by laminating a humidification water transmission plate 111 and a cooling water distribution plate 112. A groove 113 through which cooling water can flow is provided on the surface of the cooling water distribution plate 112 on the humidification water transmission plate 111 side.

【0006】また単セル114は、酸化剤配流板10
6、シートパッキング109、酸化剤極102、高分子
電解質膜103、燃料極101、燃料配流板105の順
に積層されて構成される。
Further, the single cell 114 is composed of the oxidant distributor plate 10.
6, a sheet packing 109, an oxidizer electrode 102, a polymer electrolyte membrane 103, a fuel electrode 101, and a fuel distribution plate 105 are laminated in this order.

【0007】単セル114と隣接する単セル114との
間に冷却板110を挿入し、それらを積層することで積
層体115を構成する。酸化剤配流板106とシートパ
ッキング109と高分子電解質膜103と燃料配流板1
05と加湿水透過板111と冷却水配流板112とに
は、互いに共通に貫通する複数の孔116が設けられ
る。孔116には燃料や酸化剤や冷却水が流通される。
燃料配流板105と酸化剤配流板106と加湿水透過板
111と冷却水配流板112とには、燃料や酸化剤や冷
却水の入口、出口となる連絡溝117が設けられる。
The cooling plate 110 is inserted between the single cell 114 and the adjacent single cell 114, and these are laminated to form a laminated body 115. Oxidizer distribution plate 106, sheet packing 109, polymer electrolyte membrane 103, and fuel distribution plate 1
05, the humidification water permeation plate 111, and the cooling water distribution plate 112 are provided with a plurality of holes 116 that pass through in common. Fuel, an oxidizer, and cooling water are circulated through the holes 116.
The fuel distribution plate 105, the oxidizer distribution plate 106, the humidification water permeation plate 111, and the cooling water distribution plate 112 are provided with communication grooves 117 serving as inlets and outlets of fuel, oxidizer, and cooling water.

【0008】シートパッキング109は、単セル114
を積層したときに燃料と酸化剤とが混合されることを防
ぐと共に、積層体115外部に漏れ出すことも防止して
いる。また、燃料配流板105と酸化剤配流板106と
が電気的に短絡されることも防ぐ。
The sheet packing 109 is a single cell 114.
It is possible to prevent the fuel and the oxidizer from being mixed when they are stacked, and also to prevent the fuel from leaking to the outside of the stacked body 115. It also prevents the fuel distribution plate 105 and the oxidant distribution plate 106 from being electrically short-circuited.

【0009】また、冷却板110は、起電反応によって
発生する熱を水の循環によって冷却する。積層体115
を積層させて、積層されたスタック126は、その両側
からエンドプレート118によって挟まれる。エンドプ
レート118には、発生した電力を燃料電池外部に取り
出すための端子119が設けられる。エンドプレート1
18は、絶縁物(テフロン等の樹脂)のシートを介して
SUSからなる締め付け板120によって挟まれ、複数
の締め付けロッド121とバネ122とで締め付けるこ
とによって一体に固定される。
The cooling plate 110 cools the heat generated by the electromotive reaction by circulating water. Laminate 115
The stacked stack 126 is sandwiched by the end plates 118 from both sides thereof. The end plate 118 is provided with a terminal 119 for taking out the generated electric power to the outside of the fuel cell. End plate 1
18 is sandwiched by a tightening plate 120 made of SUS via a sheet of an insulating material (resin such as Teflon), and is fixed integrally by tightening a plurality of tightening rods 121 and springs 122.

【0010】エンドプレート118と締め付け板120
とには、積層体115と同様に共通に貫通する孔116
が設けられる。孔116には燃料が燃料極101に供給
され、燃料極101から排出される燃料が通る管123
が、また酸化剤極102に酸化剤が供給され、回収され
る管124が、また冷却板110に冷却水を循環させる
管125が挿入される。図中矢印が媒体の流れる方向の
一例である。
End plate 118 and tightening plate 120
And a hole 116 that commonly penetrates through, similarly to the laminated body 115.
Is provided. A pipe 123 through which fuel is supplied to the fuel electrode 101 and through which fuel discharged from the fuel electrode 101 passes through the hole 116.
However, a pipe 124 for supplying and recovering the oxidant to the oxidant electrode 102 is inserted, and a pipe 125 for circulating cooling water is inserted in the cooling plate 110. The arrow in the figure is an example of the flow direction of the medium.

【0011】この様に構成される燃料電池は、不活性ガ
スが封入される図示しない圧力容器内に収納される。そ
して、冷却板110と単セル114とからなる積層体1
15を締め付けロッド121とバネ122とを用いて所
望の接触力をもって、電気抵抗および熱的面抵抗が小さ
くなるように圧接される。そして、純水素や天然ガスや
メタノールやナトリウムや炭化水素や一酸化炭素等の改
質ガスとなる燃料、および純酸素や空気等の酸化剤、お
よび冷却水をそれぞれの装置各部へ供給する。供給する
時の燃料と酸化剤と冷却材の圧力は高く設定し、燃料電
池の動作圧力を上げ、電気を発生させている。
The fuel cell thus constructed is housed in a pressure vessel (not shown) in which an inert gas is sealed. Then, the laminated body 1 including the cooling plate 110 and the single cell 114
The fastening rod 15 and the spring 122 are pressed against each other with a desired contact force so as to reduce the electric resistance and the thermal surface resistance. Then, fuel such as pure hydrogen, natural gas, reformed gas such as methanol, sodium, hydrocarbon, carbon monoxide, etc., oxidant such as pure oxygen, air, etc., and cooling water are supplied to respective parts of the apparatus. The pressures of the fuel, oxidant and coolant at the time of supply are set high, and the operating pressure of the fuel cell is raised to generate electricity.

【0012】また、燃料電池は、不活性ガスが充満され
る図示しない圧力容器内に配置される。ここで、燃料電
池の動作圧力は、単セル114から燃料や酸化剤が漏出
することを防止するために圧力容器内の不活性ガスの圧
力と同一にしてある。また、苛性ソーダから得られる水
素を燃料として使用することも可能である。
Further, the fuel cell is arranged in a pressure vessel (not shown) filled with an inert gas. Here, the operating pressure of the fuel cell is the same as the pressure of the inert gas in the pressure vessel in order to prevent the fuel and the oxidant from leaking out from the single cell 114. It is also possible to use hydrogen obtained from caustic soda as a fuel.

【0013】[0013]

【発明が解決しようとする課題】しかしながら、上記の
様な構成をする燃料電池では、電池性能を向上させるた
めに電池の動作圧力を大きくする必要があるが、動作圧
力を上げるとそれに伴ってエンドプレートや締め付け板
の厚みを厚くし剛性を上げる必要があり、また締め付け
ロッドとバネも大きく多数用いなければならず、装置の
大きさが大形化し、重さも増加するという欠点がある。
However, in the fuel cell having the above-mentioned structure, it is necessary to increase the operating pressure of the cell in order to improve the cell performance. It is necessary to increase the thickness of the plate and the tightening plate to increase the rigidity, and also to use a large number of tightening rods and springs, resulting in an increase in size of the device and an increase in weight.

【0014】また、電池性能を向上させるために、単セ
ルの起電部の面積を大きくすることも可能であるが、装
置が大形化し、重さも増加するといった問題も生じる。
また、単セルを構成する酸化剤極等の各構成要素ごとの
面接触力を所望の力に均一にすることは容易ではなく、
電気的・熱的性質の問題や燃料と酸化剤との混合によ
り、単セル外部に漏れ出す等の問題もあった。
Further, in order to improve the battery performance, it is possible to increase the area of the electromotive portion of the single cell, but there is a problem that the device becomes large and the weight also increases.
Further, it is not easy to make the surface contact force of each constituent element such as the oxidizer electrode constituting the single cell uniform to a desired force,
There were also problems with electrical and thermal properties, and with the mixture of fuel and oxidizer, there were problems such as leakage to the outside of the single cell.

【0015】そこで、本発明は上記従来の問題点に鑑み
てなされたもので、面接触力を良好に保ち、電気的・熱
的な面抵抗を小さくし、燃料と酸化剤とが混合すること
や単セル外部に燃料や酸化剤が漏れ出すことを防ぎ、か
つエンドプレートを薄く、小さくして軽量で小形な燃料
電池の提供を目的とする。
Therefore, the present invention has been made in view of the above-mentioned problems of the prior art, in which the surface contact force is kept good, the electrical / thermal surface resistance is reduced, and the fuel and the oxidizer are mixed. Another object of the present invention is to provide a small and lightweight fuel cell by preventing fuel and oxidant from leaking out of the unit cell and by making the end plate thin and small.

【0016】[0016]

【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、本発明の燃料電池は、酸化剤が供給される酸化剤
極と、水素ガスが供給される燃料極と、前記酸化剤極と
前記燃料極とに挟持され、水素ガスと酸化剤との化学反
応により電気を発生する電解質膜とから構成される単セ
ルが該単セルを冷却する冷却部と交互に積層された積層
体と、前記積層体に設けられた穿設部に挿入され、該積
層体の積層方向に対して該積層体を支持し、燃料あるい
は酸化剤が該積層体に供給され回収される流通部を持つ
支持手段とから構成される。
In order to achieve the above-mentioned object, a fuel cell of the present invention comprises an oxidant electrode to which an oxidant is supplied, a fuel electrode to which hydrogen gas is supplied, and the oxidant electrode. And a laminated body in which a single cell sandwiched between the fuel electrode and an electrolyte membrane that generates electricity by a chemical reaction between hydrogen gas and an oxidant is alternately laminated with a cooling unit that cools the single cell. A support having a circulation portion that is inserted into a perforated portion provided in the laminated body, supports the laminated body in the laminating direction of the laminated body, and supplies or recovers a fuel or an oxidant to the laminated body. And means.

【0017】[0017]

【発明の実施の形態】以下、本発明の実施例を図面を参
照しながら説明する。図1は、燃料電池の斜視図で、図
2は、燃料電池の締め付けロッド周辺の概略断面図であ
る。図1及び図2中の矢印は冷却水あるいは酸化剤ある
いは燃料の流れる方向の一例を示す。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a perspective view of a fuel cell, and FIG. 2 is a schematic cross-sectional view around a fastening rod of the fuel cell. The arrows in FIGS. 1 and 2 show an example of the flow direction of the cooling water, the oxidant, or the fuel.

【0018】発電に必要な燃料と酸化剤との化学反応に
より電気を発生させる単セルの基本的な構成は、前述し
た図4に示した構成とほぼ同一であり、酸化剤配流板、
シートパッキング、酸化剤極、高分子電解質膜(電解質
膜)、燃料極、燃料配流板の順で積層されている。また
単セルの内、燃料極と高分子電解質膜と酸化剤極とが積
層されて一体となる部分は起電部分となる。
The basic structure of the unit cell for generating electricity by the chemical reaction between the fuel necessary for power generation and the oxidant is almost the same as the structure shown in FIG.
The sheet packing, the oxidizer electrode, the polymer electrolyte membrane (electrolyte membrane), the fuel electrode, and the fuel distribution plate are laminated in this order. Further, in the single cell, a portion where the fuel electrode, the polymer electrolyte membrane and the oxidizer electrode are laminated and integrated with each other becomes an electromotive portion.

【0019】この様な単セルを積層させ、隣接する単セ
ルと単セルとの間に加湿水透過板と冷却水配流板とから
なる冷却板(冷却部)を挿入して積層体1を構成する。
積層体1は、積層体1の積層方向にエンドプレート2に
よって狭持され、エンドプレート2の一部には化学反応
によって作られる電力を取り出すための端子3が設けら
れる。エンドプレート2の外側には、絶縁物からなる締
め付け板4(挟持部)を設ける。
A stack 1 is constructed by stacking such single cells and inserting a cooling plate (cooling section) consisting of a humidifying water permeation plate and a cooling water distribution plate between adjacent single cells. To do.
The laminated body 1 is sandwiched by the end plates 2 in the laminating direction of the laminated body 1, and a part of the end plate 2 is provided with a terminal 3 for taking out electric power generated by a chemical reaction. On the outside of the end plate 2, a tightening plate 4 (holding part) made of an insulating material is provided.

【0020】エンドプレート2と締め付け板4と積層体
1を構成する酸化剤配流板、シートパッキング、高分子
電解質膜、燃料配流板、加湿水透過板及び冷却水配流板
とには、互いに共通した貫通口5(穿設部)を複数、起
電部分の周辺に均等に穿設する(図1中の貫通口5は6
口)。
The end plate 2, the tightening plate 4, and the oxidant distribution plate, sheet packing, polymer electrolyte membrane, fuel distribution plate, humidifying water permeation plate, and cooling water distribution plate that constitute the laminate 1 are common to each other. A plurality of through holes 5 (piercing portions) are evenly formed around the electromotive portion (the through holes 5 in FIG.
mouth).

【0021】貫通口5には円筒状のSUSからなる締め
付けロッド6(支持手段)が挿入される。締め付けロッ
ド6には、締め付けロッド6の媒体流通部に冷却水が流
れる冷却水流路管7、酸化剤が流れる酸化剤流路管8、
燃料が流れる燃料流路管9がある。各管の供給管11
(供給側)と回収管13(回収側)とは締め付け板4の
YZ面での中心部O(中心)に対して対称的に配置され
る。冷却水流路管7は、冷却板に接続され冷却水を供
給、回収している。同様に酸化剤流路管8は酸化剤極に
酸化剤を供給、回収し、燃料流路管9は燃料極に接続さ
れ燃料を供給、回収している。
A cylindrical tightening rod 6 (supporting means) made of SUS is inserted into the through hole 5. The tightening rod 6 includes a cooling water flow path pipe 7 through which cooling water flows, a oxidant flow path pipe 8 through which an oxidant flows, in a medium circulating portion of the tightening rod 6.
There is a fuel flow tube 9 through which the fuel flows. Supply pipe 11 for each pipe
The (supply side) and the recovery pipe 13 (recovery side) are arranged symmetrically with respect to the central portion O (center) on the YZ plane of the fastening plate 4. The cooling water flow path pipe 7 is connected to a cooling plate to supply and collect cooling water. Similarly, the oxidant flow pipe 8 supplies and collects the oxidant to the oxidant electrode, and the fuel flow pipe 9 is connected to the fuel electrode and supplies and collects the fuel.

【0022】締め付けロッド6の一端にはバネ10が設
けられ、締め付け板4に対して積層体1を弾性支持して
いる。次に、締め付けロッド6の詳細な構成について説
明する(図2参照)。
A spring 10 is provided at one end of the tightening rod 6 to elastically support the laminated body 1 with respect to the tightening plate 4. Next, a detailed configuration of the tightening rod 6 will be described (see FIG. 2).

【0023】締め付けロッド6の一端には、冷却水(あ
るいは燃料あるいは酸化剤)の供給口11が設けられ、
他端には締め付けロッド6に対して螺旋状に巻かれたバ
ネ10が設けられ、締め付け板4に対して積層体1を弾
性支持する。また、締め付けロッド6の媒体流通部は、
冷却水(あるいは燃料あるいは酸化剤)が流通する連通
部12(流通部)であり、図示しない冷却板(あるいは
燃料極あるいは酸化剤極)に接続される。冷却板(ある
いは燃料極あるいは酸化剤極)を流通した冷却水は、締
め付けロッド6と対向配置される別の締め付けロッド6
の連通部13に接続され、冷却水の回収口13に接続さ
れる。締め付けロッド6が、締め付け板4と接触する部
分にはシール部材14が設けられる。
A supply port 11 for cooling water (or fuel or oxidant) is provided at one end of the tightening rod 6.
A spring 10 spirally wound around the tightening rod 6 is provided at the other end, and elastically supports the laminated body 1 with respect to the tightening plate 4. Further, the medium circulating portion of the tightening rod 6 is
It is a communication part 12 (flow part) through which cooling water (or fuel or oxidant) flows, and is connected to a cooling plate (or fuel electrode or oxidizer electrode) not shown. The cooling water that has circulated through the cooling plate (or the fuel electrode or the oxidizer electrode) is attached to another tightening rod 6 facing the tightening rod 6.
Is connected to the communication part 13 and is connected to the cooling water recovery port 13. A seal member 14 is provided at a portion where the tightening rod 6 contacts the tightening plate 4.

【0024】この様に構成される燃料電池の動作につい
て説明する。純水素等の燃料が締め付けロッド6を兼ね
る燃料流路管9の供給管11から燃料極に供給される。
また、空気等の酸化剤が締め付けロッド6を兼ねる酸化
剤流路管8の供給管11から酸化剤極に供給される。供
給された空気と純水素とは高分子電解質膜で化学反応を
起こし水を生成する。その化学反応によって発生した直
流の電気は、直流の電気を交流に変換する図示しない直
交変換装置に送られる。化学反応後の燃料や酸化剤は、
燃料流路管9あるいは酸化剤流路管8の回収管13か
ら、積層体1外部に排出される。
The operation of the fuel cell thus configured will be described. Fuel such as pure hydrogen is supplied to the fuel electrode from the supply pipe 11 of the fuel flow pipe 9 that also serves as the tightening rod 6.
Further, an oxidant such as air is supplied to the oxidant electrode from the supply pipe 11 of the oxidant flow passage pipe 8 which also serves as the tightening rod 6. The supplied air and pure hydrogen cause a chemical reaction in the polymer electrolyte membrane to generate water. Direct current electricity generated by the chemical reaction is sent to an orthogonal converter (not shown) that converts direct current electricity into alternating current. After the chemical reaction, the fuel and oxidant are
The fuel flow pipe 9 or the recovery pipe 13 of the oxidant flow pipe 8 discharges the laminate 1 to the outside.

【0025】この時化学反応による単セルの温度は、1
00℃程度に昇温する。昇温した単セルの温度を冷却す
るために、冷却水は締め付けロッド6を兼ねる冷却水流
路管7の供給管11から冷却板に流通し、単セルから熱
を奪い取って冷却し、回収管13を通って積層体1外部
に放出される。
At this time, the temperature of the single cell due to the chemical reaction is 1
Raise the temperature to about 00 ° C. In order to cool the temperature of the raised single cell, the cooling water flows from the supply pipe 11 of the cooling water flow passage pipe 7 which also serves as the tightening rod 6 to the cooling plate, takes heat from the single cell and cools it, and the recovery pipe 13 And is discharged to the outside of the laminated body 1.

【0026】以上述べた様に第1実施例によれば、酸化
剤配流板、シートパッキング、高分子電解質膜、燃料配
流板、加湿水透過板、および冷却水配流板に共通に貫通
する貫通口5に燃料、酸化剤、および冷却水の入口、出
口を持つ締め付けロッド6を設け、バネ10を用いて全
体を両側から締め付けることにより、積層体1を所望の
接触力で均一に確実に締め付けることができ、シール性
能が大幅に向上し、例えば、燃料と酸化剤とが混合する
ことによって電池性能を低下させない。
As described above, according to the first embodiment, the oxidant distribution plate, the sheet packing, the polymer electrolyte membrane, the fuel distribution plate, the humidification water permeation plate, and the cooling water distribution plate have through-holes that commonly penetrate therethrough. 5 is provided with a tightening rod 6 having an inlet and an outlet for fuel, oxidant, and cooling water, and the spring 10 is used to tighten the whole body from both sides, so that the laminated body 1 is securely and uniformly tightened with a desired contact force. Therefore, the sealing performance is significantly improved and, for example, the fuel performance and the oxidizer are not mixed so that the battery performance is not deteriorated.

【0027】また、単セルの起電部分周囲を均等に締め
付けるため、燃料や酸化剤が積層外に漏れ出すことを確
実に防ぎ、積層された各セル部品の間の面接触を良好に
保ち、電気的・熱的面抵抗を小さくでき、燃料電池の性
能の向上が図れる。
Further, since the periphery of the electromotive portion of the unit cell is evenly tightened, the fuel and the oxidizer are surely prevented from leaking out of the stack, and good surface contact between the stacked cell parts is maintained, The electrical and thermal surface resistance can be reduced and the performance of the fuel cell can be improved.

【0028】また、締め付けロッド6内を流通する媒体
の入口、出口は中心部Oに対して、対称的に配置される
ため、例えば燃料極に供給される燃料を燃料極全体に浸
透させることができるため、燃料極全体で化学反応が起
こり高効率となり、燃料電池の出力も高出力となる。
Further, since the inlet and outlet of the medium flowing through the tightening rod 6 are arranged symmetrically with respect to the central portion O, for example, the fuel supplied to the fuel electrode can permeate the entire fuel electrode. Therefore, a chemical reaction occurs in the entire fuel electrode, resulting in high efficiency and high output of the fuel cell.

【0029】さらに、締め付けロッド6やバネ10等の
締め付け構造品が各流路管を兼ねるため、締め付け板4
等の大きさ(YZ面の面積)を小さくでき、締め付け板
4も薄くできる。それにより小形軽量化が可能となる。
Further, since the tightening structure such as the tightening rod 6 and the spring 10 also serves as each flow path tube, the tightening plate 4
The size (area of the YZ plane) can be made small, and the tightening plate 4 can be made thin. This makes it possible to reduce the size and weight.

【0030】また、締め付けロッド6中に、燃料あるい
は酸化剤あるいは冷却水の各流路管を設けることによ
り、燃料電池の小形軽量化と共にコスト低減ができる。
また、単セルの面積を増加させ、発電量を増加させるこ
ともできる。
Further, by providing each passage pipe of the fuel, the oxidizer or the cooling water in the tightening rod 6, the fuel cell can be made compact and lightweight and the cost can be reduced.
Further, the area of the unit cell can be increased to increase the amount of power generation.

【0031】次に、本発明の第2実施例の構成について
図面を参照しながら説明する。なお、第2実施例におい
て第1実施例と同一構成要素は同一符号を付し、重複す
る説明は省略する。
Next, the configuration of the second embodiment of the present invention will be described with reference to the drawings. In the second embodiment, the same components as those in the first embodiment are designated by the same reference numerals, and the duplicated description will be omitted.

【0032】図3は、燃料電池の第2実施例の断面図で
ある。第2実施例の特徴は、冷却水(あるいは燃料ある
いは酸化剤)を積層体1に供給する供給部18と、積層
体1から冷却水(あるいは燃料あるいは酸化剤)を回収
する回収部19とが、同一の締め付けロッド6内に設け
られることであり、締め付けロッド6の個数を少なくす
ることができ、小型軽量化が達成できる。
FIG. 3 is a sectional view of a second embodiment of the fuel cell. The feature of the second embodiment is that a supply unit 18 that supplies cooling water (or fuel or oxidizer) to the stack 1 and a recovery unit 19 that recovers cooling water (or fuel or oxidizer) from the stack 1. Since they are provided in the same tightening rod 6, the number of tightening rods 6 can be reduced, and the size and weight can be reduced.

【0033】積層体1の冷却部15には、冷却水が循環
する溝16が設けられ、冷却部15の外周には冷却部枠
17がある。冷却部枠17には溝16に冷却水を供給す
る供給部18と、冷却水を回収する回収部19とを兼ね
備えた冷却水流路管7が設けられる。
A groove 16 through which cooling water circulates is provided in the cooling section 15 of the laminate 1, and a cooling section frame 17 is provided on the outer periphery of the cooling section 15. The cooling part frame 17 is provided with a cooling water passage pipe 7 that has both a supply part 18 that supplies cooling water to the groove 16 and a recovery part 19 that recovers the cooling water.

【0034】この様な構成からなる燃料電池の動作につ
いて説明する。単セル内で起こる燃料と酸化剤との化学
反応によって、単セルは100℃程度の温度になる。単
セルから発生する熱を冷却するために冷却部15の溝1
6に冷却水を循環させて冷却を行う。冷却水の循環は、
冷却水が締め付けロッド6を兼ねた冷却水流路管7内の
供給部18、溝16、回収部19の順に循環し、溝16
を通過する際に冷却部15から単セルの熱を吸収する。
The operation of the fuel cell having such a structure will be described. Due to the chemical reaction between the fuel and the oxidant that occurs in the unit cell, the temperature of the unit cell is about 100 ° C. The groove 1 of the cooling unit 15 for cooling the heat generated from the single cell
Cooling water is circulated in 6 for cooling. The circulation of cooling water is
The cooling water circulates in the order of the supply part 18, the groove 16 and the recovery part 19 in the cooling water flow path pipe 7 which also serves as the tightening rod 6, and the groove 16
The heat of the single cell is absorbed from the cooling unit 15 when passing through the.

【0035】以上述べた様に第2実施例によれば、酸化
剤配流板、シートパッキング、高分子電解質膜、燃料配
流板、加湿水透過板、および冷却水配流板に共通に貫通
する貫通口5に燃料、酸化剤、および冷却水の入口、出
口を持つ締め付けロッド6を設け、バネ10を用いて全
体を両側から締め付けることにより、積層体1を所望の
接触力で均一に確実に締め付けることができ、シール性
能が大幅に向上し、例えば、燃料と酸化剤とが混合して
電池性能を低下させることがない。
As described above, according to the second embodiment, the oxidant distribution plate, the sheet packing, the polymer electrolyte membrane, the fuel distribution plate, the humidification water permeation plate, and the cooling water distribution plate are commonly penetrated. 5 is provided with a tightening rod 6 having an inlet and an outlet for fuel, oxidant, and cooling water, and the spring 10 is used to tighten the whole body from both sides, so that the laminated body 1 is securely and uniformly tightened with a desired contact force. Therefore, the sealing performance is significantly improved, and, for example, the fuel and the oxidant are not mixed with each other and the cell performance is not deteriorated.

【0036】また、単セルの起電部分周囲を均等に締め
付けるため、燃料や酸化剤が積層外に漏れ出すことを確
実に防ぎ、積層された各セル部品の間の面接触を良好に
保ち、電気的・熱的面抵抗を小さくでき、燃料電池の性
能の向上が図れる。
Further, since the periphery of the electromotive portion of the single cell is evenly tightened, it is possible to reliably prevent the fuel and the oxidizer from leaking out of the stack, and to keep the surface contact between the stacked cell parts in good condition. The electrical and thermal surface resistance can be reduced and the performance of the fuel cell can be improved.

【0037】さらに、締め付けロッド6やバネ10等の
締め付け構造品が各流路管を兼ねるため、締め付け板4
等の大きさ(YZ面の面積)を小さくでき、強いては締
め付け板4も薄くできる。それにより小形軽量化が可能
となる。
Further, since the tightening structure such as the tightening rod 6 and the spring 10 also serves as each flow path tube, the tightening plate 4
The size (area of the YZ plane) can be reduced, and the tightening plate 4 can be thinned. This makes it possible to reduce the size and weight.

【0038】また、冷却水あるいは燃料が積層体1内を
流通する際に、それらを積層体1内に供給する管と回収
する管との2本が一組となって、各流路管を構成する必
要がなく、1本で供給と回収とができるため、流路管の
積層体1内に占有する面積を減少させることができ小形
軽量化が達成できる。また、流路管の減少する面積分だ
け起電部分の面積を増加させれば、電池能力が向上す
る。
Further, when the cooling water or the fuel flows through the laminated body 1, two pipes for supplying the cooling water or the fuel into the laminated body 1 and a pipe for collecting the cooling water form one set to form each flow passage pipe. Since it is not necessary to configure and supply and recovery can be performed by one pipe, the area occupied by the flow path pipe in the laminated body 1 can be reduced and the size and weight can be reduced. Further, if the area of the electromotive portion is increased by the decreasing area of the flow passage tube, the battery capacity is improved.

【0039】また、冷却水を冷却部15内の溝16に循
環させることで、積層体1の熱を効率良く冷却すること
ができる。なお、本発明は上記実施例に限定されず、そ
の主旨を逸脱しない範囲で種々変形して実施できること
はいうまでもない。例えば、各流路管の本数や形状につ
いては、少なくとも各流路管を流れる媒体が流通すれば
良い。また、溝の形状は少なくとも溝を流れる媒体が流
通すれば良い。
Further, by circulating the cooling water through the groove 16 in the cooling section 15, the heat of the laminate 1 can be efficiently cooled. Needless to say, the present invention is not limited to the above-described embodiments, and various modifications can be made without departing from the spirit of the invention. For example, as for the number and shape of each flow tube, at least the medium flowing through each flow tube should circulate. Further, the shape of the groove may be at least that the medium flowing through the groove circulates.

【0040】[0040]

【発明の効果】以上説明した様に本発明によれば、マニ
ホールドを構成する各構成要素ごとの面接触力を良好に
保ち、電気的・熱的な面抵抗を小さくし、燃料と酸化剤
とが混合することや単セル外部に燃料や酸化剤が漏れ出
すことを防ぎ、かつエンドプレートを薄く小さくできる
ため小形軽量化ができる。
As described above, according to the present invention, the surface contact force of each component constituting the manifold is kept good, the electrical / thermal surface resistance is reduced, and the fuel and the oxidant are mixed. It is possible to reduce the size and weight of the fuel cell and the oxidizer by preventing them from mixing with each other and leaking the fuel and the oxidizer to the outside of the single cell and by making the end plate thin and small.

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

【図1】 本発明の燃料電池の第1実施例の斜視図FIG. 1 is a perspective view of a first embodiment of a fuel cell of the present invention.

【図2】 本発明の燃料電池の第1実施例の締め付けロ
ッド周辺の概略断面図
FIG. 2 is a schematic cross-sectional view around a tightening rod of the first embodiment of the fuel cell of the present invention.

【図3】 本発明の燃料電池の第2実施例の断面図FIG. 3 is a sectional view of a second embodiment of the fuel cell of the present invention.

【図4】 従来の積層体の分解斜視図FIG. 4 is an exploded perspective view of a conventional laminated body.

【図5】 従来の燃料電池の斜視図FIG. 5 is a perspective view of a conventional fuel cell.

【符号の説明】[Explanation of symbols]

1 積層体 2 エンドプレート 3 端子 4 締め付け板(挟持部) 5 貫通口(穿設部) 6 締め付けロッド(支持手段) 7 冷却水流路管 8 酸化剤流路管 9 燃料流路管 10 バネ 11 供給口(供給側) 12 連通部(流通部) 13 回収口(回収側) 14 シール部材 15 冷却部 16 溝 17 冷却部枠 18 供給部 19 回収部 DESCRIPTION OF SYMBOLS 1 Laminated body 2 End plate 3 Terminal 4 Tightening plate (clamping part) 5 Through hole (piercing part) 6 Tightening rod (supporting means) 7 Cooling water flow pipe 8 Oxidizer flow pipe 9 Fuel flow pipe 10 Spring 11 Supply Port (supply side) 12 Communication part (circulation part) 13 Recovery port (recovery side) 14 Seal member 15 Cooling part 16 Groove 17 Cooling part frame 18 Supply part 19 Recovery part

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】酸化剤が供給される酸化剤極と、水素ガス
が供給される燃料極と、前記酸化剤極と前記燃料極とに
挟持され、水素ガスと酸化剤との化学反応により電気を
発生する電解質膜とから構成される単セルが該単セルを
冷却する冷却部と交互に積層された積層体と、前記積層
体に設けられた穿設部に挿入され、該積層体の積層方向
に対して該積層体を支持し、燃料あるいは酸化剤が該積
層体に供給され回収される流通部を持つ支持手段とから
構成されることを特徴とする燃料電池。
1. An oxidant electrode supplied with an oxidant, a fuel electrode supplied with hydrogen gas, and an oxidant electrode sandwiched between the oxidant electrode and the fuel electrode, and the hydrogen gas and the oxidant chemically react to generate electricity. A laminated body in which a single cell composed of an electrolyte membrane that generates a layer is alternately laminated with a cooling unit that cools the unit cell, and a perforated portion provided in the laminated body, and the laminated body is laminated. 1. A fuel cell, comprising: a supporting unit that supports the laminate in a direction, and has a circulation unit that supplies or recovers a fuel or an oxidant to the laminate.
【請求項2】前記支持手段は、燃料あるいは酸化剤ある
いは冷却水を前記積層体に供給する供給側と、供給され
た燃料あるいは酸化剤あるいは冷却水を該積層体から回
収する回収側とからなり、該供給側と該回収側とが該積
層体を挟持する挟持部の中心に対して対称配置すること
を特徴とする請求項1記載の燃料電池。
2. The supporting means comprises a supply side for supplying fuel, oxidant or cooling water to the laminate, and a recovery side for recovering the supplied fuel, oxidant or cooling water from the laminate. 2. The fuel cell according to claim 1, wherein the supply side and the recovery side are symmetrically arranged with respect to the center of a sandwiching part that sandwiches the laminated body.
JP8073392A 1996-03-28 1996-03-28 Fuel cell Pending JPH09266007A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8073392A JPH09266007A (en) 1996-03-28 1996-03-28 Fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8073392A JPH09266007A (en) 1996-03-28 1996-03-28 Fuel cell

Publications (1)

Publication Number Publication Date
JPH09266007A true JPH09266007A (en) 1997-10-07

Family

ID=13516890

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8073392A Pending JPH09266007A (en) 1996-03-28 1996-03-28 Fuel cell

Country Status (1)

Country Link
JP (1) JPH09266007A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020058857A (en) * 2000-12-30 2002-07-12 이계안 A fuel cell for vehicles
US6521368B2 (en) 2000-02-29 2003-02-18 Aisin Seiki Kabushiki Kaisha Fuel cell
JP2005203189A (en) * 2004-01-14 2005-07-28 Sanyo Electric Co Ltd Polymer electrolyte fuel cell
JP2006054117A (en) * 2004-08-12 2006-02-23 Sony Corp Fuel battery device and its operation method
JP2010287501A (en) * 2009-06-12 2010-12-24 Ngk Spark Plug Co Ltd Fuel cell system
CN110925094A (en) * 2019-11-28 2020-03-27 四川泛华航空仪表电器有限公司 Cooling structure of ignition device

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6521368B2 (en) 2000-02-29 2003-02-18 Aisin Seiki Kabushiki Kaisha Fuel cell
KR20020058857A (en) * 2000-12-30 2002-07-12 이계안 A fuel cell for vehicles
JP2005203189A (en) * 2004-01-14 2005-07-28 Sanyo Electric Co Ltd Polymer electrolyte fuel cell
JP2006054117A (en) * 2004-08-12 2006-02-23 Sony Corp Fuel battery device and its operation method
JP2010287501A (en) * 2009-06-12 2010-12-24 Ngk Spark Plug Co Ltd Fuel cell system
CN110925094A (en) * 2019-11-28 2020-03-27 四川泛华航空仪表电器有限公司 Cooling structure of ignition device
CN110925094B (en) * 2019-11-28 2021-10-22 四川泛华航空仪表电器有限公司 Cooling structure of ignition device

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