JPS62200666A - Fuel cell - Google Patents
Fuel cellInfo
- Publication number
- JPS62200666A JPS62200666A JP61040479A JP4047986A JPS62200666A JP S62200666 A JPS62200666 A JP S62200666A JP 61040479 A JP61040479 A JP 61040479A JP 4047986 A JP4047986 A JP 4047986A JP S62200666 A JPS62200666 A JP S62200666A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- cell
- fuel cell
- series
- electrode
- 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
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 56
- 239000007800 oxidant agent Substances 0.000 claims abstract description 25
- 239000007789 gas Substances 0.000 claims abstract description 22
- 230000001590 oxidative effect Effects 0.000 claims abstract description 15
- 239000002737 fuel gas Substances 0.000 claims abstract description 14
- 239000000758 substrate Substances 0.000 claims abstract description 11
- 239000003792 electrolyte Substances 0.000 claims abstract description 10
- 239000011159 matrix material Substances 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 5
- 239000012495 reaction gas Substances 0.000 abstract 1
- 239000002184 metal Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000004043 responsiveness Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2457—Grouping of fuel cells, e.g. stacking of fuel cells with both reactants being gaseous or vaporised
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
- H01M8/2418—Grouping by arranging unit cells in a plane
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
- H01M8/2484—Details of groupings of fuel cells characterised by external manifolds
-
- 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
- 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
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
ものでるる。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a small, lightweight, and compact fuel cell.
周知の通シ、燃料電池は対向して配置された燃料電極と
酸化剤電極の間に電解質を保持した電解質マトリックス
を介在させ、燃料電極および酸化剤電極にそれぞれ燃料
および酸化剤を供給して運転される一種の発電装置でる
る。As is well known, a fuel cell operates by interposing an electrolyte matrix holding an electrolyte between a fuel electrode and an oxidizer electrode arranged opposite each other, and supplying fuel and oxidizer to the fuel electrode and the oxidizer electrode, respectively. It is a kind of power generation device.
燃料電池には、■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れる、■出力を変えても効率
はろまシ変わらない、■負荷変動に対する応答性に優れ
ているなどの利点があり、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
。Fuel cells have the following characteristics: ■ High efficiency can be expected as there is no Carnot cycle restriction; ■ Waste heat can be obtained at a relatively high temperature close to the cell operating temperature and can be used effectively; ■ Efficiency does not change much even if the output is changed. ■It has advantages such as excellent responsiveness to load fluctuations, and can be used in ways such as being distributed within or near cities on the scale of distribution substations, or as an alternative power generation device for thermal power plants. It is considered.
燃料電池は用いられている電解質の種類によつて、アル
カリ型、リン酸型、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 type, molten carbonate type, etc. depending on the type of electrolyte used, and these types use gases such as hydrogen and methane as fuel.
There are also other types of fuel cells, such as the methanol direct-improved type, which use liquid as fuel.
燃料電池の基本構成単位は単電池すなわちセルでるるか
、単電池の重子電圧は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
。単電池および集合電池の構成については米国特許第グ
、コクA、、? & 5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, and since the deuteron voltage of a single cell is as small as about 0.7 V, an assembled battery is constructed by stacking tens to hundreds of single cells. Regarding the structure of single cells and collective batteries, see US Patent No. G, Koku A, ? & 5 is disclosed in detail.
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
ナメートルめたシ数百mAと高い電流が取シ出せる反面
47V程度の低い電圧しか取シ出せないという本質的な
特徴がb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ないし一〇〇V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l〜100ctd楊度の単電
池を/10ないし300セル積層する必要がろる。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 centameter, they have a low voltage of around 47V. The essential feature is that it can only be taken out. On the other hand, for small-scale applications, the current may be small, but a high voltage of about 100 to 100 V is required. Therefore, in order to meet such uses with conventional fuel cells, it is necessary to stack 10 to 300 cells each having an area of 1 to 100 ctd.
上記のような従来の燃料電池では、琳セルろたシ最低5
ミリメートル程度の厚さを有するので集合電池は771
以上の高さになシ、また四方にマニホールドを取り付け
なければならないので、かなシの大きさと重量を伴う。In conventional fuel cells such as those mentioned above, the Rin cell filter must be at least 5.
Since it has a thickness of about a millimeter, the assembled battery has a thickness of 771 mm.
Since it is necessary to install manifolds on all sides at a height higher than that, the size and weight of the structure increase.
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。Therefore, there has been a problem that practical application of such fuel cells on a small scale has not been realized.
この発明は、かかる問題点を解決するためになされたも
ので、小型軽量の燃料電池を得ることを目的とする。This invention was made to solve this problem, and aims to obtain a small and lightweight fuel cell.
この発明に係る燃料電池は、電気絶縁性の基盤に複数個
の貫通穴を設げ、これらの貫通孔に単電池をはめ込み、
単電池を電気的に直列又は並列に接続したものである。The fuel cell according to the present invention includes a plurality of through holes provided in an electrically insulating base, a unit cell inserted into these through holes,
These are cells electrically connected in series or parallel.
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シ、単電池の数に依らず
、基盤の表裏に燃料ガス及び酸化剤ガスを流せばよいの
で軽量でコンパクトな燃料電池ができる。In this invention, since a plurality of cells are arranged on a single substrate, there is no need to supply reactive gas to each cell using a gas separation plate as in the past, and it is possible to First, since fuel gas and oxidizing gas only need to flow between the front and back sides of the substrate, a lightweight and compact fuel cell can be created.
第7図、第一図はこの発明の一実施例を示すそれぞれ断
面図、平面図でろシ、O)は電気絶縁性の基盤でろって
、複数個の貫通穴が設けられている。(−)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) IJソックス(4c)はこの電解質保持
マトリックス(3)に隣接して設けられた酸化剤電極で
めシ、これら燃料電極(,2)、電解質保持マ) IJ
ソックス3)、及び酸化剤電極(lI)によって単電池
(5)が構成され且つ上述した各貫通穴に配置される。FIG. 7 and FIG. 1 are a cross-sectional view and a plan view, respectively, showing an embodiment of the present invention. Reference numeral O) is an electrically insulating base having a plurality of through holes. (-) is the fuel electrode, (3) is the electrolyte holding matrix provided adjacent to this fuel electrode (2)) IJ sock (4c) is the oxidizing agent provided adjacent to this electrolyte holding matrix (3) These fuel electrodes (,2), electrolyte retainer) IJ
A unit cell (5) is constituted by the sock 3) and the oxidizer electrode (lI), and is arranged in each of the above-mentioned through holes.
(6)は燃料電極(2)及び酸化剤電極(4=)に接続
された集電板、(7)はこの集電板(6)に接続される
導電性の接合金具、(g)はこの接合金具(り)−個を
電気的に接続する導電性のピンでメジ、図に示す3個の
単電池(j)はこれらの集電板(6)、接合金具(ワ)
、及びピン(g)によって電気的に直列に接続されてい
る。(6) is a current collector plate connected to the fuel electrode (2) and oxidizer electrode (4=), (7) is a conductive joint metal fitting connected to this current collector plate (6), and (g) is The three cells (j) shown in the figure are connected to these current collecting plates (6) and the connecting metal fittings (wa).
, and are electrically connected in series by pin (g).
第3図及び第を図はM1図の単電池(5)の拡大図であ
シ、それぞれ#電池の組立前の分解した状態及び組立後
の状態を示す。これらの囚で、燃料電極(2)は燃料電
極基材(q)と燃料を極触煤層(10)からなシ、酸化
剤11極(4)は酸化剤電極基材(11)と酸化剤電極
触媒層(l2)からなることが示されている。Figures 3 and 3 are enlarged views of the unit cell (5) in Figure M1, showing the disassembled state before and after assembly of the # battery, respectively. In these cells, the fuel electrode (2) has a fuel electrode base material (q) and the fuel in contact with the soot layer (10), and the oxidizer 11 electrode (4) has the oxidizer electrode base material (11) and the oxidizer in contact with the soot layer (10). It is shown that it consists of an electrode catalyst layer (l2).
上記のように構成された燃料電池においては、燃料ガス
を基盤(1)の表面に流しく矢印(13))、酸化剤ガ
スを基盤(1)の裏面に流す(矢印(t<Q)ことによ
って、これらのガスの反応によシ生じた起電力は集電板
(6)、接合金具(7)、及びピン(f)を用いて取シ
出すことができる。In the fuel cell configured as described above, the fuel gas is caused to flow on the surface of the substrate (1) (arrow (13)), and the oxidizing gas is caused to flow on the back surface of the substrate (1) (arrow (t<Q)). Therefore, the electromotive force generated by the reaction of these gases can be taken out using the current collector plate (6), the joining metal fitting (7), and the pin (f).
第5図は基盤に72個の曜電池(&)を直列に配置した
燃料電池の平面図、第6図は基盤に75−個の単電池(
j)を直列に配置した燃料電池の平面図でめシ、第6図
では接合金具(7)及びピン(&)は簡略化して示して
るる。(15)は定流ソケット、(弓)はこの電流ソケ
ット(tS)に設けられたプラス側接続部、(17)は
同じく電流ソケット(lり)K設けられたマイナス側接
続部である。これらの燃料電池では、基盤(1)の表面
に燃料ガスを、裏面に酸化剤ガスをそれぞれ流して動作
させることができる。生じた起電力は電流ソケット(t
S)によって外部配線と容易に接続することができる。Figure 5 is a plan view of a fuel cell with 72 day cells (&) arranged in series on the base, and Figure 6 is a plan view of a fuel cell with 75 single cells (&) arranged on the base.
Fig. 6 is a plan view of a fuel cell in which 6 j) are arranged in series. In Fig. 6, the connecting fittings (7) and pins (&) are shown in a simplified manner. (15) is a constant current socket, (bow) is a positive side connection portion provided on this current socket (tS), and (17) is a negative side connection portion similarly provided on the current socket (l) K. These fuel cells can be operated by flowing fuel gas onto the front surface of the substrate (1) and flowing oxidant gas onto the back surface thereof. The generated electromotive force is the current socket (t
S) allows easy connection to external wiring.
また、第6図の燃料電池では単電池lセルめたp o、
t、 rV程度の出力電圧が得られるので、燃料電池
全体としては約10OVの直流電圧が得られる。In addition, in the fuel cell shown in Fig. 6, the single cell p o,
Since an output voltage of about t, rV can be obtained, the entire fuel cell can obtain a DC voltage of about 10 OV.
第7図、第5図は第3図又は第6図の燃料電池にマニホ
ールドを取シ付けたそれぞれ概略平面図、正面図でるる
。(/1)は基盤(1)の上面に設けられた燃料ガスマ
ニホールド、(19)は基盤(1)の下面に設けられた
酸化剤ガスマニホールド、(2θ)は燃料ガスマニホー
ルド(/l)に設けられた燃料ガスの供給接続プラグ、
(St)は同じく燃料ガスマニホールド(lt)に設け
られた燃料ガスの排出プラグ、(2λ)は酸化剤ガスマ
ニホールド(19)に設けられた酸化剤ガスの供給接続
プラグ、(23)は同じく酸化剤ガスマニホールド(1
9)に設けられた酸化剤ガスの排出プラグである。燃料
ガスは燃料ガスマニホールド(lざ)の供給接続プラグ
(20)から供給され排出プラグOt)から排出される
。一方、酸化剤ガスは酸化剤ガスマニホールド(19)
の供給接続プラグ(コ2)から供給され排出プラグ(コ
3)から排出される。このような燃料電池は非常にコン
パクトで燃料電池カードとも呼びうるものでsb、外部
配線・配管への接続部も簡単な構造でらり、家庭の電気
のソケットのように簡離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sbさまざまな小規模発
電に適用できる。7 and 5 are a schematic plan view and a front view, respectively, of the fuel cell shown in FIG. 3 or 6 with a manifold attached thereto. (/1) is the fuel gas manifold provided on the top surface of the base (1), (19) is the oxidizer gas manifold provided on the bottom surface of the base (1), (2θ) is the fuel gas manifold (/l) Fuel gas supply connection plug provided,
(St) is also a fuel gas discharge plug provided in the fuel gas manifold (lt), (2λ) is an oxidizing gas supply connection plug provided in the oxidizing gas manifold (19), and (23) is also an oxidizing gas discharge plug provided in the oxidizing gas manifold (19). agent gas manifold (1
9) is an oxidant gas discharge plug provided in Fuel gas is supplied from the supply connection plug (20) of the fuel gas manifold (lza) and discharged from the exhaust plug (Ot). On the other hand, the oxidizing gas is in the oxidizing gas manifold (19)
It is supplied from the supply connection plug (K2) and discharged from the discharge plug (K3). This kind of fuel cell is very compact and can be called a fuel cell card.The connection to external wiring and piping is simple, and it can be easily connected like a household electric socket. It can generate electricity. Therefore, it is easy to carry and can be applied to various types of small-scale power generation.
なお、上記実施例では単電池を電気的に直列に接続した
場合について示したが、数個の単電池を並列に接続して
電気的に並列になった単電池群を形成した上で、この単
電池群を直列に接続してもよい。In addition, although the above example shows the case where the single cells are electrically connected in series, this example is performed by connecting several single cells in parallel to form a group of electrically parallel single cells. Groups of cells may be connected in series.
この発明は以上説明したとおシ、電気絶縁性の基盤に設
けられた複数個の貫通穴に、燃料W池とと酸化剤電極と
電解質保持マトリックスとからなる単電池をそれぞれ配
置し、これら単電池を電気的に直列、並列又は直並列に
接続したので、従来のようなガス分離板を用いた各単電
池ごとの反応ガスの供給が不要でろ)、単電池の数に限
らず基盤の表裏に燃料ガス及び酸化剤ガスを流せばよく
、小型軽量でコンパクトな燃料電池が得られる効果がる
る。As described above, the present invention includes a plurality of through holes provided in an electrically insulating substrate, each of which has unit cells each consisting of a fuel W pond, an oxidizer electrode, and an electrolyte retention matrix, and which are electrically connected in series, parallel, or series-parallel, so there is no need to supply reactant gas to each cell using a gas separation plate as in the past), regardless of the number of cells. It is sufficient to flow the fuel gas and the oxidant gas, and the effect is that a small, lightweight, and compact fuel cell can be obtained.
第1図、第2図はこの発明の一実施例を示すそれぞれ断
面図、平面図、第3図、第7図は第1図中の単電池のそ
れぞれ組立前1組立後の拡大図、第3図は基盤に7.2
個の単電池を配置した燃料電池の平面図、第6図は基盤
にlり2個の単電池を配置した燃料電池の平面図、第7
図、第3図は第tJて。
5図又は第6図の燃料電池にマニホールド−取付1則
けられた燃料電池のそれぞれ概略平面図、平面図である
。
図において(1)は基盤、(2)は燃料電極、(3)は
電解質保持マトリックス、(lI)は酸化剤電極、(よ
)は単電池、(6)は集電板、(7)は接合金具、(1
)はピン、(9)は燃料電極基材、(10)は燃料電極
触媒層、(11)は酸化剤電極基材、(tX)は酸化剤
電極触媒層、(lり)は電流ソケット、(16)ス
はプラグ側接続部、(/7)はマイナス側接続部、(/
1)は燃料ガスマニホールド、(/9)は酸化剤ガスマ
ニホールド、(20) 、 (22)は供給接続プラグ
、(2/)、(コ3)は排出プラグでるる。゛なお、各
図中、同一符号は同−又は相当部分を示す。
1・、“・[I
代埋入 曾 我 道 6.1[===
コニニニーー二、二゛E二ニーEXJk 612・諌L
I’l電狗11諜層
尾5図
15゛、電浚ソケ町ト
16: プラス便J欅鏝部1 and 2 are a sectional view and a plan view, respectively, showing an embodiment of the present invention, and FIGS. 3 and 7 are enlarged views of the cell shown in FIG. 1 before and after assembly, respectively. Figure 3 shows 7.2 on the base.
Figure 6 is a plan view of a fuel cell with two single cells arranged on a base, and Figure 7 is a plan view of a fuel cell with two single cells arranged on a base.
Figure 3 is tJ. FIG. 6 is a schematic plan view and a plan view, respectively, of a fuel cell in which a manifold is attached to the fuel cell of FIG. 5 or FIG. 6; In the figure, (1) is the substrate, (2) is the fuel electrode, (3) is the electrolyte holding matrix, (lI) is the oxidizer electrode, (yo) is the unit cell, (6) is the current collector plate, and (7) is Joining metal fittings, (1
) is the pin, (9) is the fuel electrode base material, (10) is the fuel electrode catalyst layer, (11) is the oxidizer electrode base material, (tX) is the oxidizer electrode catalyst layer, (l) is the current socket, (16) is the plug side connection, (/7) is the negative side connection, (/
1) is the fuel gas manifold, (/9) is the oxidant gas manifold, (20) and (22) are the supply connection plugs, and (2/) and (3) are the discharge plugs.゛In each figure, the same reference numerals indicate the same or corresponding parts. 1., “・[I substitution 6.1 [===
Koninini 2, 2゛E 2nie EXJk 612・Isa L
I'l Dengu 11 intelligence layer tail 5 figure 15゛, Densokecho To 16: Plus delivery J Keyaki Kobe
Claims (4)
、燃料電極と酸化剤電極と電解質保持マトリックスとか
らなる単電池をそれぞれ配置し、これら単電池を電気的
に直列、並列又は直並列に接続したことを特徴とする燃
料電池。(1) A single cell consisting of a fuel electrode, an oxidizer electrode, and an electrolyte holding matrix is placed in a plurality of through holes provided in an electrically insulating substrate, and these single cells are electrically connected in series, parallel, or A fuel cell characterized by being connected in series and parallel.
ト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。(2) The fuel cell according to claim 1, wherein a current socket is provided at the terminal to which the cell is electrically connected.
該基盤の下面に酸化剤ガスマニホールドが設けられ、且
つそれぞれのマニホールドに供給接続プラグ及び排出プ
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。(3) A fuel gas manifold is provided on the top surface of the base,
Claim 1, characterized in that an oxidant gas manifold is provided on the lower surface of the base, and each manifold is provided with a supply connection plug and a discharge plug.
Fuel cell as described in Section.
なり、酸化剤電極が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。(4) Claim 1, characterized in that the fuel electrode consists of a fuel electrode base material and a fuel electrode catalyst layer, and the oxidizer electrode consists of an oxidizer electrode base material and an oxidizer electrode catalyst layer. fuel cell.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61040479A JPH0828234B2 (en) | 1986-02-27 | 1986-02-27 | Fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61040479A JPH0828234B2 (en) | 1986-02-27 | 1986-02-27 | Fuel cell |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62200666A true JPS62200666A (en) | 1987-09-04 |
JPH0828234B2 JPH0828234B2 (en) | 1996-03-21 |
Family
ID=12581749
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61040479A Expired - Lifetime JPH0828234B2 (en) | 1986-02-27 | 1986-02-27 | Fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0828234B2 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07169499A (en) * | 1985-04-19 | 1995-07-04 | Ivac Corp | Plate-shaped multiple-junction type electrochemical cell |
JP2002216803A (en) * | 2001-01-19 | 2002-08-02 | Sony Corp | Fuel cell, its manufacturing method and method of use |
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 |
JP2002329514A (en) * | 2001-05-01 | 2002-11-15 | Nissan Motor Co Ltd | Single cell for fuel cell and solid electrolyte fuel cell |
JP2002329513A (en) * | 2001-05-01 | 2002-11-15 | Nissan Motor Co Ltd | Single cell for fuel cell and solid electrolyte fuel cell |
JP2005038671A (en) * | 2003-07-18 | 2005-02-10 | Kyocera Corp | Electronics |
JP2005285709A (en) * | 2004-03-31 | 2005-10-13 | Minoru Umeda | Film electrode element, manufacturing method thereof, and fuel cell |
JP2009016364A (en) * | 2008-10-22 | 2009-01-22 | Minoru Umeda | Membrane electrode element manufacturing method, membrane electrode element, and fuel cell |
JP2009512169A (en) * | 2005-10-18 | 2009-03-19 | ミシュラン ルシェルシュ エ テクニーク ソシエテ アノニム | Integrated fluid management fuel cell |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53122739A (en) * | 1977-03-31 | 1978-10-26 | Shin Kobe Electric Machinery | Gas fuel battery |
JPS53122740A (en) * | 1977-03-31 | 1978-10-26 | Shin Kobe Electric Machinery | Gas fuel battery |
JPS59134571A (en) * | 1983-01-24 | 1984-08-02 | Shin Kobe Electric Mach Co Ltd | Fuel cell structure |
-
1986
- 1986-02-27 JP JP61040479A patent/JPH0828234B2/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53122739A (en) * | 1977-03-31 | 1978-10-26 | Shin Kobe Electric Machinery | Gas fuel battery |
JPS53122740A (en) * | 1977-03-31 | 1978-10-26 | Shin Kobe Electric Machinery | Gas fuel battery |
JPS59134571A (en) * | 1983-01-24 | 1984-08-02 | Shin Kobe Electric Mach Co Ltd | Fuel cell structure |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07169499A (en) * | 1985-04-19 | 1995-07-04 | Ivac Corp | Plate-shaped multiple-junction type electrochemical cell |
JP2002216803A (en) * | 2001-01-19 | 2002-08-02 | Sony Corp | Fuel cell, its manufacturing method and method of use |
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 |
JP2002329514A (en) * | 2001-05-01 | 2002-11-15 | Nissan Motor Co Ltd | Single cell for fuel cell and solid electrolyte fuel cell |
JP2002329513A (en) * | 2001-05-01 | 2002-11-15 | Nissan Motor Co Ltd | Single cell for fuel cell and solid electrolyte fuel cell |
JP2005038671A (en) * | 2003-07-18 | 2005-02-10 | Kyocera Corp | Electronics |
JP4518755B2 (en) * | 2003-07-18 | 2010-08-04 | 京セラ株式会社 | Electronic equipment and fuel cell containers |
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 |
JP2009512169A (en) * | 2005-10-18 | 2009-03-19 | ミシュラン ルシェルシュ エ テクニーク ソシエテ アノニム | Integrated fluid management fuel cell |
JP2013127978A (en) * | 2005-10-18 | 2013-06-27 | Michelin Recherche & Technique Sa | 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 |
---|---|
JPH0828234B2 (en) | 1996-03-21 |
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Legal Events
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EXPY | Cancellation because of completion of term |