JPS632264A - Fuel cell - Google Patents

Fuel cell

Info

Publication number
JPS632264A
JPS632264A JP61145809A JP14580986A JPS632264A JP S632264 A JPS632264 A JP S632264A JP 61145809 A JP61145809 A JP 61145809A JP 14580986 A JP14580986 A JP 14580986A JP S632264 A JPS632264 A JP S632264A
Authority
JP
Japan
Prior art keywords
fuel
fuel cell
electrode
current
gas manifold
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.)
Granted
Application number
JP61145809A
Other languages
Japanese (ja)
Other versions
JPH0821416B2 (en
Inventor
Kenro Mitsuta
憲朗 光田
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric 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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP61145809A priority Critical patent/JPH0821416B2/en
Publication of JPS632264A publication Critical patent/JPS632264A/en
Publication of JPH0821416B2 publication Critical patent/JPH0821416B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0247Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/241Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
    • H01M8/2418Grouping by arranging unit cells in a plane
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465Details of groupings of fuel cells
    • H01M8/2484Details of groupings of fuel cells characterised by external manifolds
    • 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

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To eliminate reaction gas supply to each cell using gas separating plate and electrical connection between unit cells on a substrate to obtain a lightweight, compact fuel cell by arranging unit cells in a plurality of through holes installed in an insulating substrate, and connecting current terminals installed in gas manifolds. CONSTITUTION:A plurality of unit cells 5 are arranged in a substrate 1 and connected to current terminals 8 installed in gas manifolds 6, 7. Therefore, reaction gas supply to each cell using gas separating plate is unnecessary, and fuel gas and oxidizing agent gas only flows on each side of the substrate. Electrical connection between unit cells 5 on the substrate 1 is unnecessary, selection of parallel or series connection can be decided after connection of current terminals 8. Therefore, the cell is made lightweight and compact, and output current and output voltage can be optionally selected.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、小型軽量でコンパクトな燃料電池に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a small, lightweight, and compact fuel cell.

〔従来の技術〕[Conventional technology]

周知の通シ、燃料°1池は対向して配置仏された燃料電
極と酸化剤電極の間Kt電解質保持した電解質マ) I
Jラックス介在させ、燃料電極および酸化剤を極にそれ
ぞれ燃料2よび酸化剤を供給して運転される一種の発゛
底装置である。
As is well-known, a fuel cell is an electrolyte tank that holds a Kt electrolyte between a fuel electrode and an oxidizer electrode that are arranged opposite each other.
This is a type of bottom ignition device that is operated by supplying fuel 2 and oxidizer to the fuel electrode and oxidizer, respectively, with J-lux interposed between them.

燃料1池ては、■カルノーサイクルの制約がなく高い効
率が期待できる、■電池作動温度に近い比較的高温の有
効利用が容易な廃熱が得ら冗る・、■出力を変えても効
率はあまシ変わらない、■負荷変動に対する応答性に侵
れているなどの利点があシ、都市内もしくは都市近郊に
配電用変電所の規模で分配配置途する、あるいは火力発
電所の代替発電装置とするなどの利用形態が考えられて
いる。
As for one fuel tank, ■ High efficiency can be expected as there is no restriction of Carnot cycle, ■ Waste heat can be easily utilized effectively at a relatively high temperature close to the battery operating temperature, and ■ Efficiency can be achieved even if the output is changed. - There are no advantages such as poor responsiveness to load fluctuations, and it is necessary to distribute power in the city or near the city on the scale of a distribution substation, or as an alternative power generation device for thermal power plants. Various forms of use are being considered, such as:

燃料電池は用いられている’tMMの種類によって、ア
ルカリ型、リン酸壓、溶融炭酸塩型などに分類され、こ
れらは燃料として水素やメタンなどの気体を使用するが
、この他に液体を燃料とするメタノール直接改良型など
の燃料電池もある。
Fuel cells are classified into alkaline type, phosphoric acid bottle, molten carbonate type, etc. depending on the type of 'tMM used.These types use gases such as hydrogen and methane as fuel, but they also use liquid as fuel. There are also fuel cells such as the methanol direct improved type.

燃料電池の基本構成単位は単電池すなわちセルであるが
、単電池の単子電圧は0.7 V程度と小さいため、単
電池を数十ないし数百セル積層して集合電池を構成する
0単電池および集合電池の構成については米圓特許嬉4
2’76355号において詳細に開示されている。
The basic structural unit of a fuel cell is a single cell, or a cell, but since the single cell voltage of a single cell is as low as about 0.7 V, it is difficult to stack tens or hundreds of single cells to form an aggregate battery. Regarding the structure of batteries and battery packs, please refer to Beien Patent Publication No. 4.
2'76355.

近年燃料電池の利用形態として自動車の動力源など小規
模での実用化も考えられているが、燃料電池は平方セン
ナメートルあたシ数百mAと高い電流が取り出せる反面
0.7v程度の低い電圧しか取り出せないという本質的
な特徴がある。これに対して小規模な用途からは逆に電
流は少なくてよいが、100ないし200■程度の高電
圧が必要とされる。従って、従来の燃料電池でこの様な
用途に応じるためには面積が1 % 100 am2程
度の単電池を150ないし300セル積層する必要があ
る。
In recent years, fuel cells have been considered for practical use on a small scale, such as as a power source for automobiles, but while fuel cells can draw a high current of several hundred mA per square centimeter, they have a low voltage of around 0.7V. It has an essential feature that it can only be taken out. On the other hand, for small-scale applications, a small current may be required, but a high voltage of about 100 to 200 μm is required. Therefore, in order to meet such uses with conventional fuel cells, it is necessary to stack 150 to 300 single cells with an area of about 1% 100 am2.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

上記のような従来の燃料電池では、単セルあたり最低5
ミリメートル程度の厚さを有するので集合電池は1m以
上の高さになシ、また四方にマニホールドを取シ付けな
ければならないので、かなりの大きさと重量を伴う。従
って、このような燃料電池の小規模での実用化は実現で
きていないという問題点がめった。
Conventional fuel cells, such as those mentioned above, require at least 5
Since the battery pack has a thickness of about a millimeter, the height of the battery pack must be more than 1 m, and manifolds must be attached on all sides, resulting in considerable size and weight. Therefore, there has been a problem that practical application of such fuel cells on a small scale has not been realized.

されたもので、小型軽量の燃料電池を得ることをこの発
明は、かかる問題点を解決するためにな目的とする。
The object of the present invention is to obtain a small and lightweight fuel cell in which the fuel cells have been used to solve the above problems.

〔問題点を解決するだめの手段〕[Failure to solve the problem]

に複数個の貫通穴を設け、これらの貫通孔に単電池をは
め込み、基盤の上下面に複数個の電流端子を有するガス
マニホールドを取り付け、各々の単電池と電流端子とを
電気的に接続したものである。
A plurality of through-holes were provided in the board, cells were fitted into these through-holes, a gas manifold having a plurality of current terminals was attached to the upper and lower surfaces of the board, and each cell and the current terminal were electrically connected. It is something.

〔作用〕[Effect]

この発明においては、1枚の基盤に複数個の単電池を配
置し、ガスマニホールドに設けた電流端子に接続したの
で、従来のようなガス分離板を用いた各セルごとの反応
ガスの供給が不要であり、基盤の表裏に燃料ガス及び酸
化剤ガス電流せばよく、また基盤上での単電池同士の電
気的接続が不要で単電池を直列にするか並列にするか、
などの組合せを電流端子以降の接続で任意に決定できる
ので軽量かつコンパクトで出力電流と出力電圧を任意に
選ぶことのできる燃料電池ができる。
In this invention, a plurality of cells are arranged on one board and connected to a current terminal provided on a gas manifold, so that the supply of reaction gas to each cell using a conventional gas separation plate is no longer possible. It is not necessary, and it is only necessary to apply fuel gas and oxidizing gas current to the front and back sides of the board, and there is no need to electrically connect the cells on the board, so it is possible to connect the cells in series or in parallel.
Combinations such as these can be determined arbitrarily by connections after the current terminal, so a lightweight and compact fuel cell can be created in which the output current and output voltage can be arbitrarily selected.

〔実施例〕〔Example〕

以下、この発明の一実施例を図について説明する。第1
図は断面図であり、(1)は電気絶縁性の基盤であって
、複数個の貫通穴が設けられている。
An embodiment of the present invention will be described below with reference to the drawings. 1st
The figure is a cross-sectional view, and (1) is an electrically insulating substrate, in which a plurality of through holes are provided.

(2)は燃料電極、(3)はこの燃料電極(2)に隣接
して設けられた電解質保持マトリックス、(4)はこの
戚解質保持マトリックス(3)に隣接して設けられZζ
酸化剤電極であシ、これら燃料電極(2)、゛電解質保
持マトリックス(3)、および酸化剤電極(4)によっ
て単電池(5)が構成され且つ上述した各貫通式に配置
される。(6)は燃料ガスマニホールド、(7)は酸化
剤ガスマニホールド、(8)はガスマニホールドに取り
付けられた電流端子、(9)は集電金具、00は電流端
子をガスマニホールドに取り付ける為のバッキング材、
(9)は燃料ガス室、@は酸化剤ガス室である。
(2) is a fuel electrode, (3) is an electrolyte retention matrix provided adjacent to this fuel electrode (2), and (4) is an electrolyte retention matrix provided adjacent to this electrolyte retention matrix (3).
The fuel electrode (2), the electrolyte holding matrix (3), and the oxidant electrode (4) constitute a unit cell (5), which is arranged in the above-mentioned through-hole manner. (6) is the fuel gas manifold, (7) is the oxidizer gas manifold, (8) is the current terminal attached to the gas manifold, (9) is the current collector, and 00 is the backing for attaching the current terminal to the gas manifold. wood,
(9) is a fuel gas chamber, and @ is an oxidant gas chamber.

第2図、第3図は単電池の拡大図を示すそれぞれ平面図
、および断面図である。これらの図で、α力は基盤(1
)の突起部であり単電池を支持する為のものである。第
2図で六角形をした単電池の燃料電極(2)はガス透気
性の燃料電極基材Q]と燃料電極触媒層Q4)からなり
、酸化剤電極(4)は酸化剤電極基材OGと酸化剤電極
触媒層(至)からなることが第3図の断面図で示されて
いる。
FIG. 2 and FIG. 3 are a plan view and a cross-sectional view, respectively, showing an enlarged view of a unit cell. In these figures, the α force is the base (1
) is a protrusion that supports the cell. In Fig. 2, the fuel electrode (2) of the hexagonal unit cell is composed of a gas-permeable fuel electrode base material Q] and a fuel electrode catalyst layer Q4), and the oxidant electrode (4) is composed of an oxidant electrode base material OG. The cross-sectional view of FIG. 3 shows that the oxidizing agent electrode catalyst layer is composed of an oxidizing agent electrode catalyst layer and an oxidizing agent electrode catalyst layer.

l@4図、第5図は、それぞれ第2図、第3図の単電池
に燃料ガスマニホールドに設けられた電流端子を配設し
たものである。三本足の集電金具(9)は電流端子(8
)と燃料電極(2)との電気的接触を得る為のものであ
シ、バネのような弾力性によって、ガスマニホールド(
6)と基盤(1)との間隔が多少変化した場合でも電気
的接触を保つことができ、また、電極(2)に圧力を与
えるととくよって電池を基盤(1)K密着させる役割を
する。バッキング材(J■は電流端子(8)をガスマニ
ホールド責6)に支持すると為に燃料ガスが燃料ガス室
0υからガスマニホールド(6)ト電流端子(8)との
すき間を通って外部へ漏れるのを防ぐ。また、ガスマニ
ホールド(6)が電気絶縁体ではなく、金属などで形成
されている場合には電気絶縁の役割も果たす。酸化剤電
極への電流端子の配役も同様である。第1図は3つの単
電池を並設した所を示しているが、このように構成され
た燃料電池においては、燃料ガスを燃料ガス室に流し、
酸化剤ガスを酸化剤ガス室に流すことによって、これら
のガスの反応によって生じた起電力は集電金具(9)、
電流端子α0を通じて取シ出すことができる0 第6図は基盤(1)に32個の単電池(5)を配設した
燃料電池の平面図であシ、第7図は第6図の燃料電池の
燃料ガスマニホールドの平面図である。Q’Jは外部配
線と接続するための電流ソケットであり、(ト)は電流
端子(8)と電流ソケットとをつなぐリード線である。
1@4 and FIG. 5 show the unit cells shown in FIGS. 2 and 3, respectively, with a current terminal provided in the fuel gas manifold. The three-legged current collector (9) is connected to the current terminal (8
) and the fuel electrode (2), and its spring-like elasticity allows it to connect to the gas manifold (
Even if the distance between the electrode (6) and the substrate (1) changes slightly, electrical contact can be maintained, and when pressure is applied to the electrode (2), the electrode (2) cracks and serves to bring the battery into close contact with the substrate (1). . Because the backing material (J) supports the current terminal (8) to the gas manifold (6), fuel gas leaks from the fuel gas chamber 0υ to the outside through the gap between the gas manifold (6) and the current terminal (8). prevent Furthermore, when the gas manifold (6) is made of metal or the like instead of an electrical insulator, it also serves as an electrical insulator. The same applies to the arrangement of current terminals to the oxidizer electrodes. Figure 1 shows three unit cells arranged side by side. In a fuel cell configured in this way, fuel gas is flowed into the fuel gas chamber,
By flowing the oxidizing gas into the oxidizing gas chamber, the electromotive force generated by the reaction of these gases is collected by the current collector (9),
Figure 6 is a plan view of a fuel cell in which 32 cells (5) are arranged on a base (1), and Figure 7 shows the fuel cell shown in Figure 6. FIG. 2 is a plan view of a fuel gas manifold of a battery. Q'J is a current socket for connecting to external wiring, and (G) is a lead wire connecting the current terminal (8) and the current socket.

また、翰は燃料ガスマニホールド(6)に設けられた燃
料ガスの供給接続プラグ、?υは同じく燃料ガスマニホ
ールド責6)に設けられた燃料ガスの排出プラグである
Also, the handle is the fuel gas supply connection plug installed in the fuel gas manifold (6). Similarly, υ is a fuel gas discharge plug provided in the fuel gas manifold 6).

リード線O印は第8図のようにガスマニホールド(6)
の外側に設けてもよく(イ)、内側に設けてもよい翰、
また内蔵していてもよい。
The lead wire marked O is connected to the gas manifold (6) as shown in Figure 8.
A fence that may be provided on the outside (a) or on the inside,
It may also be built-in.

また、ガスマニホールドが金属のような導電性のもので
あれば、第9図、第10図に示すようにアルミナやシリ
カのような絶縁物(ハ)を塗布した後にリード線を配設
するのがよい。また、第11図のようにガスマニホール
ド(6)の外側からすでにリード線(至)の配設された
プリント基盤@を隣接させて電流端子(8)に接触させ
てもよい。
Also, if the gas manifold is made of conductive material such as metal, the lead wires should be installed after coating with an insulating material (c) such as alumina or silica, as shown in Figures 9 and 10. Good. Alternatively, as shown in FIG. 11, a printed circuit board on which lead wires (to) are already arranged from the outside of the gas manifold (6) may be brought into contact with the current terminals (8).

第7図ではリード線(至)は各単電池について電流ソケ
ット09までプリントされており、電流ソケツ。
In Figure 7, the lead wires (to) are printed up to the current socket 09 for each cell.

トQI Kつながる外部配線での接続方法によって、(
a)〜(ff)までの32個の単電池を並列でも直列で
も自由に選ぶことができる。従って、任意の出力電圧、
出力電流を得ることができ用途に応じて外部配線で選択
して決めることができる。
Depending on how the external wiring is connected,
The 32 cells a) to (ff) can be freely selected in parallel or series. Therefore, for any output voltage,
Output current can be obtained and determined by external wiring depending on the application.

また、単電池を並列又は直列にガスマニホールド(61
、(7)やプリント基盤輸上で結線しておくこともでき
る。さらにまたe、n、w、ffの単電池は予備として
おき、過負荷:Cなった場合に外部配線で結線して出力
をとることもできる。
In addition, unit cells can be connected in parallel or in series to a gas manifold (61
, (7) or by importing a printed circuit board. Furthermore, the e, n, w, and ff cells can be kept as spares, and in case of overload: C, they can be connected with external wiring to obtain output.

第12図、第13図は第6図の燃料電池てガスマニホー
ルドを取り付けたそれぞれ概略平面図、および正面図で
ある。図において、□□□は酸化剤ガスの供給プラグ、
翰は燃料ガスの排出プラグである。
12 and 13 are a schematic plan view and a front view, respectively, of the fuel cell shown in FIG. 6 with a gas manifold attached thereto. In the figure, □□□ is the oxidizing gas supply plug,
The handle is a fuel gas discharge plug.

燃料ガスは燃料ガスマニホールド(6)の供給接続プラ
グ艶から供給され排出プラグQ1)から排出される。
Fuel gas is supplied from the supply connection plug of the fuel gas manifold (6) and discharged from the discharge plug Q1).

−方、酸化剤ガスは酸化剤ガスマニホールド(7)の供
給接続プラグ(ホ)から供給され排出プラグ(ト)から
排出される。このような燃料電池は非常てコンパクトで
燃料電池カードとも呼びうるものであシ、外部配線・配
管への接続部も簡単な構造でちり、家庭の電気のソケッ
トのように簡単に接続して発電することができる。従っ
て、持ち運びが容易であシさまざまな小規模発電に適用
できる。
- On the other hand, the oxidant gas is supplied from the supply connection plug (E) of the oxidant gas manifold (7) and is discharged from the discharge plug (G). This kind of fuel cell is very compact and can be called a fuel cell card, and the connection to external wiring and piping is simple, so it can be easily connected like a household electric socket and generate electricity. can do. Therefore, it is easy to carry and can be applied to various small-scale power generation applications.

な2、上記実施例では32個の単電池を配設したものを
示したが、100個以上でもよい。また、100個程度
の単電池を配設した燃料電池カードを数個用いることK
よって、100〜200 Vの直流電圧も容易に得られ
る。
2. In the above embodiment, 32 single cells were arranged, but the number may be 100 or more. It is also possible to use several fuel cell cards each containing about 100 single cells.
Therefore, a DC voltage of 100 to 200 V can be easily obtained.

〔発明の効果〕〔Effect of the invention〕

この発明は以上説明したとお夛、電気絶縁性の基盤に設
けられた複数個の貫通穴に、単電池を配賦し、ガスマニ
ホールドに設けた電流端子に接続したので、従来のよう
なガス分離板を用いた各セルごとの反応ガスの供給が不
要であり、また、基盤上での単電池同士の電気的接続が
不要になシ、小型軽量でコンパクトな燃料電池が得られ
る効果がある。
In addition to the above explanation, this invention has single cells arranged in a plurality of through holes provided in an electrically insulating substrate and connected to a current terminal provided in a gas manifold, thereby eliminating the need for conventional gas separation. It is not necessary to supply reactant gas to each cell using a plate, and there is no need to electrically connect the cells to each other on the substrate, so that a small, lightweight, and compact fuel cell can be obtained.

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

第1図はこの発明の一実施例による燃料電池を・示す断
面図、第2図〜第5図はそれぞれ第1図中の単電池を拡
大したものであり、第2図、第4図は平面図、第3図、
第5図は断面図、第6図、第7図はそれぞれ基盤に32
個の単電池を配置した燃料電池の平面図、第8図〜第1
1図はリード線の配設を示す断間図、第12図、第13
図は第6図の燃料電池にマニホールドが取り付けられた
燃料電池のそれぞれ概略平面図、および側面図である。 閃において、(1)は基盤、(2)は燃料電極、(3)
は電解質保持マトリックス、(4)は酸化剤電極、(5
)は単電池、(6)は燃料ガスマニホールド、(7)は
酸化剤ガスマニホールド、(8)は電流端子、(9)は
集電金具、(IcIは電流ソケットである。 なお、各図中、同一符号は同−又は相当部分を示す。
FIG. 1 is a sectional view showing a fuel cell according to an embodiment of the present invention, FIGS. 2 to 5 are enlarged views of the single cell in FIG. 1, and FIGS. Plan view, Figure 3,
Figure 5 is a cross-sectional view, Figures 6 and 7 are 32 mm on the base, respectively.
A plan view of a fuel cell in which single cells are arranged, Figures 8 to 1
Figure 1 is a cutaway view showing the arrangement of lead wires, Figures 12 and 13.
The figures are a schematic plan view and a side view, respectively, of the fuel cell shown in FIG. 6 with a manifold attached thereto. In flash, (1) is the base, (2) is the fuel electrode, (3)
is an electrolyte retention matrix, (4) is an oxidizer electrode, and (5
) is a single cell, (6) is a fuel gas manifold, (7) is an oxidizer gas manifold, (8) is a current terminal, (9) is a current collector, (IcI is a current socket. Note that in each figure , the same reference numerals indicate the same or equivalent parts.

Claims (8)

【特許請求の範囲】[Claims] (1)電気絶縁性の基盤に設けられた複数個の貫通穴に
、燃料電極と酸化剤電極と電解質マトリックスとからな
る単電池をそれぞれ配置し、上記基盤の上面と下面に、
それぞれ燃料ガスマニホールドと酸化剤ガスマニホール
ドが設けられた燃料電池において、上記燃料ガスマニホ
ールドと酸化剤ガスマニホールドにはそれぞれ複数個の
電流端子を設け、各々の単電池は、燃料電極が燃料ガス
マニホールドに設けられた電流端子に電気的に接続され
、酸化剤電極が酸化剤ガスマニホールドに設けられた電
流端子に電気的に接続されていることを特徴とする燃料
電池。
(1) Single cells each consisting of a fuel electrode, an oxidizer electrode, and an electrolyte matrix are arranged in a plurality of through holes provided in an electrically insulating substrate, and on the upper and lower surfaces of the substrate,
In a fuel cell equipped with a fuel gas manifold and an oxidizing gas manifold, each of the fuel gas manifold and the oxidizing gas manifold is provided with a plurality of current terminals, and each unit cell has a fuel electrode connected to the fuel gas manifold. A fuel cell characterized in that the oxidant electrode is electrically connected to a current terminal provided on an oxidant gas manifold.
(2)ガスマニホールドに設けられた複数個の電流端子
と電気的に接続されている電流ソケットを有することを
特徴とする特許請求の範囲第1項記載の燃料電池。
(2) The fuel cell according to claim 1, further comprising a current socket electrically connected to a plurality of current terminals provided on the gas manifold.
(3)電流ソケットと電流端子との接続は、ガスマニホ
ールドの内面、外面、およびガスマニホールドの外側の
何れかに配置されたプリント基盤を介してなされている
ことを特徴とする特許請求の範囲第2項記載の燃料電池
(3) The connection between the current socket and the current terminal is made through a printed circuit board placed on the inner surface, outer surface, or outside of the gas manifold. 2. The fuel cell according to item 2.
(4)電流ソケットと電流端子との接続の途中で、単電
池が直列、並列、および直並列の何れかに接続されてい
ることを特徴とする特許請求の範囲第2項または第3項
記載の燃料電池。
(4) Claim 2 or 3, characterized in that the cells are connected in series, parallel, or series-parallel in the middle of the connection between the current socket and the current terminal. fuel cell.
(5)電流ソケットまでの単電池の電気的接続において
電気的に直列にも並列にも接続されていない単電池が複
数個存在することを特徴とする特許請求の範囲第2項な
いし第4項の何れかに記載の燃料電池。
(5) Claims 2 to 4 characterized in that in the electrical connection of the cells to the current socket, there are a plurality of cells that are not electrically connected in series or in parallel. The fuel cell according to any one of.
(6)マニホールドには供給接続プラグおよび排出プラ
グが設けられたことを特徴とする特許請求の範囲第1項
記載の燃料電池。
(6) The fuel cell according to claim 1, wherein the manifold is provided with a supply connection plug and a discharge plug.
(7)燃料電極が、ガス透気性の燃料電極基材と燃料電
極触媒層とからなり、酸化剤電極が、ガス透気性の酸化
剤電極基材と酸化剤電極触媒層とからなることを特徴と
する特許請求の範囲第1項記載の燃料電池。
(7) The fuel electrode is comprised of a gas permeable fuel electrode base material and a fuel electrode catalyst layer, and the oxidant electrode is comprised of a gas permeable oxidant electrode base material and an oxidant electrode catalyst layer. A fuel cell according to claim 1.
(8)電流端子と燃料電極又は酸化剤電極との電気的接
触はバネのごとき弾力性を有する集電金具によつてなさ
れることを特徴とする特許請求の範囲第1項記載の燃料
電池。
(8) The fuel cell according to claim 1, wherein electrical contact between the current terminal and the fuel electrode or the oxidizer electrode is made by a resilient current collector fitting such as a spring.
JP61145809A 1986-06-20 1986-06-20 Fuel cell Expired - Lifetime JPH0821416B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61145809A JPH0821416B2 (en) 1986-06-20 1986-06-20 Fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61145809A JPH0821416B2 (en) 1986-06-20 1986-06-20 Fuel cell

Publications (2)

Publication Number Publication Date
JPS632264A true JPS632264A (en) 1988-01-07
JPH0821416B2 JPH0821416B2 (en) 1996-03-04

Family

ID=15393639

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61145809A Expired - Lifetime JPH0821416B2 (en) 1986-06-20 1986-06-20 Fuel cell

Country Status (1)

Country Link
JP (1) JPH0821416B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002216803A (en) * 2001-01-19 2002-08-02 Sony Corp Fuel cell, its manufacturing method and method of use
JP2005285709A (en) * 2004-03-31 2005-10-13 Minoru Umeda Film electrode element, manufacturing method thereof, and fuel cell
JP2005322452A (en) * 2004-05-07 2005-11-17 Nissan Motor Co Ltd Cell plate for solid oxide fuel cell, and solid oxide fuel cell
JP2009016364A (en) * 2008-10-22 2009-01-22 Minoru Umeda Membrane electrode element manufacturing method, membrane electrode element, and fuel cell

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002237325A (en) * 2001-02-07 2002-08-23 Sony Corp Fuel cell module and electric equipment as well as electric equipment equipped with fuel cell module

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53122739A (en) * 1977-03-31 1978-10-26 Shin Kobe Electric Machinery Gas fuel battery

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53122739A (en) * 1977-03-31 1978-10-26 Shin Kobe Electric Machinery Gas fuel battery

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002216803A (en) * 2001-01-19 2002-08-02 Sony Corp Fuel cell, its manufacturing method and method of use
JP2005285709A (en) * 2004-03-31 2005-10-13 Minoru Umeda Film electrode element, manufacturing method thereof, and fuel cell
JP4674789B2 (en) * 2004-03-31 2011-04-20 実 梅田 Membrane electrode element manufacturing method, membrane electrode element and fuel cell
JP2005322452A (en) * 2004-05-07 2005-11-17 Nissan Motor Co Ltd Cell plate for solid oxide fuel cell, and solid oxide fuel cell
JP2009016364A (en) * 2008-10-22 2009-01-22 Minoru Umeda Membrane electrode element manufacturing method, membrane electrode element, and fuel cell

Also Published As

Publication number Publication date
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