Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6046515B2 - Method for manufacturing electrolyte retention matrix for fuel cells - Google Patents
[go: Go Back, main page]

JPS6046515B2 - Method for manufacturing electrolyte retention matrix for fuel cells - Google Patents

Method for manufacturing electrolyte retention matrix for fuel cells

Info

Publication number
JPS6046515B2
JPS6046515B2 JP55133714A JP13371480A JPS6046515B2 JP S6046515 B2 JPS6046515 B2 JP S6046515B2 JP 55133714 A JP55133714 A JP 55133714A JP 13371480 A JP13371480 A JP 13371480A JP S6046515 B2 JPS6046515 B2 JP S6046515B2
Authority
JP
Japan
Prior art keywords
matrix
electrolyte retention
retention matrix
binder
fuel cell
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.)
Expired
Application number
JP55133714A
Other languages
Japanese (ja)
Other versions
JPS5760670A (en
Inventor
篤夫 宗内
三司 上野
謙二 村田
保 城上
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
Tokyo Shibaura Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP55133714A priority Critical patent/JPS6046515B2/en
Publication of JPS5760670A publication Critical patent/JPS5760670A/en
Publication of JPS6046515B2 publication Critical patent/JPS6046515B2/en
Expired 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
    • H01M8/0289Means for holding the electrolyte
    • H01M8/0293Matrices for immobilising electrolyte solutions
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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)

Description

【発明の詳細な説明】 本発明は無機化合物とポリテトラフルオロエチレンで
形成される燃料電池の電解質保持マトリックスの製造方
法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an electrolyte retention matrix for a fuel cell formed of an inorganic compound and polytetrafluoroethylene.

周知の通り燃料電池たとえはりん酸電解液型燃料電池
は、対向して配置されたガス拡散電極の間に液体りん酸
を電解質として保持したマトリックスを配し、ガス拡散
電極にそれぞれ、水素を含有するガスを燃料ガスとして
、酸素を含有するたとえは空気を酸化剤として通流させ
て使用される。
As is well known, a fuel cell (for example, a phosphoric acid electrolyte fuel cell) has a matrix holding liquid phosphoric acid as an electrolyte between gas diffusion electrodes placed opposite each other, and each gas diffusion electrode contains hydrogen. It is used by passing a gas containing oxygen as a fuel gas and air, for example, containing oxygen, as an oxidizing agent.

ここで上記燃料電池を最適の状態で作動させるための
電解質保持マトリックスは次のような特性 を有する必
要がある。即ち(1)燃料電池作動条件下て安定である
。(2)親水性て液の保持性を有する。(3)燃料電池
内でのガスの交差、混合を阻止する。(4)電極との接
触が十分てあり、内部抵抗を最小限にするため、薄くし
かも充分な機械的強度をもつものである。 上記特性を
有する電解質保持マトリックスを従来の製造方法て製造
するためには種々の制限が生じる。
Here, in order to operate the fuel cell in an optimal state, the electrolyte retention matrix must have the following characteristics. That is, (1) it is stable under fuel cell operating conditions; (2) Hydrophilic and has liquid retention properties. (3) Prevent cross-crossing and mixing of gases within the fuel cell. (4) It should be thin and have sufficient mechanical strength to ensure sufficient contact with the electrode and minimize internal resistance. Various limitations arise in manufacturing electrolyte retention matrices having the above characteristics using conventional manufacturing methods.

化学的安定性の見地からマトリックス材料・を選定する
と無機化合物たとえは炭化けい素、酸化ジルコニウム、
五酸化タンタルが選定出来、結着剤としてふつ素系ポリ
マーが使用出来る従来このように選定されたマトリック
ス材料にふつ素系ポリマーの懸濁液を加え混合し、水分
を加熱除去して後所定の電解質保持マトリックスを形成
。ここで機械的強度を得めるためには結着剤の添加量を
増してマトリックス材料の結合を強固なものとならしめ
れば良い。しかし結着剤のふつ素系ポリマーは撥水性が
あるため機械的強度を増す為に結着剤の添加量を単に増
していくと電解質保持マトリックスとしての親水性およ
び電解液の保持性が悪くなる。また逆に結着剤のふつ素
系ポリマーの量を減らせば親水性は改善されるが機械的
強度が減少しそれのみかマトリックス材料が結合されな
いため、燃料電池内で気体の交差、混合が起こりやすく
なる。
When selecting matrix materials from the viewpoint of chemical stability, inorganic compounds such as silicon carbide, zirconium oxide,
Tantalum pentoxide can be selected, and a fluorine-based polymer can be used as a binder. Conventionally, a suspension of a fluorine-based polymer is added to and mixed with the matrix material selected in this way, and the moisture is removed by heating. Forms an electrolyte-retaining matrix. In order to obtain mechanical strength, the amount of binder added may be increased to strengthen the bond between the matrix materials. However, since the fluorine-based polymer used as a binder is water-repellent, simply increasing the amount of binder added to increase mechanical strength will deteriorate its hydrophilicity as an electrolyte retention matrix and its ability to retain electrolyte. . On the other hand, if the amount of fluorine-based polymer used as a binder is reduced, hydrophilicity will be improved, but the mechanical strength will be reduced and the matrix material will not be bonded, resulting in cross-crossing and mixing of gases within the fuel cell. It becomes easier.

これらの問題を解決するための1つの方法としてマトリ
ックス材料に始めから繊維状のものを用い、この材料を
結着剤で結合させる方法が考えられるが繊維状の無機化
合物は材料価格が高く多量に使用する燃料電池に使用す
るには自ずと限界があり、一般的ではない。
One way to solve these problems is to use a fibrous matrix material from the beginning and bind this material with a binder, but fibrous inorganic compounds are expensive and require large quantities. There are naturally limits to its use in fuel cells, and it is not common.

本発明は、上記の問題を解決する為になされたもので、
結着剤を繊維化させ、この結着剤てマトリックス材料を
結合させて網目状の電解質保持マトリックスを形成させ
、燃料電池を最適状態で作動させることができ、かつ低
価格で実現できる電解質保持マトリックスの製造方法を
提供することを目的とする。
The present invention was made to solve the above problems.
The binder is made into fibers, and the matrix material is bonded with the binder to form a mesh-like electrolyte retention matrix, which enables fuel cells to operate in optimal conditions and can be realized at a low cost. The purpose is to provide a manufacturing method for.

即ち本発明に係る製造方法は結着剤としてふつ素系ポリ
マーの懸濁液を使用し、これを無機化合物でなるマトリ
ックス材料と混合し、この混合したものを加熱後たとえ
ばメタノールでなる添加剤を加えてさらに加熱し、その
後所定形状に成形する方法てある。以下、本発明に係る
製造方法について詳細に説明する。
That is, the manufacturing method according to the present invention uses a suspension of a fluorine-based polymer as a binder, mixes this with a matrix material made of an inorganic compound, and after heating the mixture, adds an additive such as methanol. In addition, there is a method of further heating and then molding it into a predetermined shape. Hereinafter, the manufacturing method according to the present invention will be explained in detail.

なお、実施例について説明する前に本発明の主要な工程
である2つの工程について説明する。ます第1の工程は
一般に知られている懸濁液は熱が加えられることにより
ミセルが破壊されて固相と液相に分離することを利用し
、ふつ素系ポリマーの懸濁液と無機化合物でなるマトリ
ックス材料との混合物を加熱し、固相のふつ素系ポリマ
ーを沈澱させてマトリックス材料にふつ素系ポリマーを
付着させる。第2の工程は第1の工程て加熱処理した混
合物にたとえばメタノールの添加剤を加え、混合物中に
残存したミセルを破壊せしめる。この時メタノールがミ
セル破壊剤として作用し、ふつ素系ポリマー粒子を覆つ
ていた界面活性剤が破壊してふつ素系ポリマー粒子が露
出し、粒子間での結合を起こし繊維化が進行する。加え
られたメタノールのうち余分となつたものはさらに加熱
することにより除去される。上記2工程により結着剤て
あるふつ素系ポリマーが充分繊維化され、これにマトリ
ックス材料の無機化合物が付着して網目状の所望の電解
質保持マトリックスが製造出来る。なお、添加剤として
メタノールを例示したがエタノール、プロパノール、イ
ソプロパノールおよびイソブチルアルコールのいずれで
もミセルの破壊が起こり、メタノールを使用した場合と
同様の結果が得られる。
Before describing the examples, two main steps of the present invention will be described. The first step takes advantage of the generally known fact that micelles in suspensions are destroyed and separated into a solid phase and a liquid phase when heat is applied, and a suspension of a fluorine-based polymer and an inorganic compound are The mixture with the matrix material is heated to precipitate the solid phase fluorine-based polymer, thereby adhering the fluorine-based polymer to the matrix material. In the second step, an additive such as methanol is added to the mixture heated in the first step to destroy micelles remaining in the mixture. At this time, methanol acts as a micelle-destroying agent, and the surfactant covering the fluorine-containing polymer particles is destroyed, exposing the fluorine-containing polymer particles, causing bonding between the particles and promoting fiberization. Excess methanol added is removed by further heating. Through the above two steps, the fluorine-based polymer serving as the binder is sufficiently fiberized, and the inorganic compound of the matrix material is attached to the fiber to produce the desired network-like electrolyte holding matrix. Although methanol is exemplified as an additive, micelle destruction occurs with any of ethanol, propanol, isopropanol, and isobutyl alcohol, and the same results as when methanol is used are obtained.

次に実施例を説明する。Next, an example will be explained.

実施例1 マトリックス材料の炭化けい素100yに結着剤”のポ
リテトラフルオロエチレンの懸濁液即ち市販されている
6鍾量%のポリテトラフルオロエチレン粒子と6重量%
の界面活性剤て成るテフロン30一J(三井フロロケミ
カル社製)36ccと水30ccを加え攪拌混合し、こ
の混合したものを100℃〜150℃に加熱したオープ
ン中に2時間放置し水分の除去を行つた。
Example 1 A suspension of polytetrafluoroethylene as a binder in 100y of silicon carbide as a matrix material, i.e. commercially available 6% by weight polytetrafluoroethylene particles and 6% by weight.
36 cc of Teflon 301J (manufactured by Mitsui Fluorochemical Co., Ltd.), which is a surfactant, and 30 cc of water were added and mixed with stirring, and the mixture was left in an open oven heated to 100°C to 150°C for 2 hours to remove moisture. I went to

この水分除去を行つた混合物に次にメタノール20cc
を加えて攪拌後100℃のオープン中に入れ3紛間放置
し、メタノール水分の除去を行つた。これにより生じた
混合物質に水を添加しニーダー混練機で1紛間混練し、
この混練物をローラーでシート状に展関してマトリック
ス基材を成形した。このマトリックス基材に95%りん
酸液を含浸させて電解質保持マトリックスを得た。なお
上記製造工程においては炭化けい素100yに対し3〜
5重量%の結着剤で充分シート状に展関し得たが、メタ
ノールを添加しないでマトリックス材料と結着剤を混練
し、シート状に展関する場合には2呼量%の結着剤を要
し電解液の保持性が悪い。実施例2 上記実施例1て得られた混合物質に水を加え電極表面上
に直接塗布しマトリックス基材を形成せしめ、このマト
リックス基材に95%リン酸液を含浸させて電解質保持
マトリックスとなした。
Next, add 20 cc of methanol to the mixture from which water has been removed.
After stirring, the mixture was placed in an open chamber at 100°C and left to stand for 3 minutes to remove methanol water. Water was added to the resulting mixed material and kneaded into a single powder using a kneader kneader.
This kneaded material was rolled out into a sheet shape using a roller to form a matrix base material. This matrix base material was impregnated with a 95% phosphoric acid solution to obtain an electrolyte retention matrix. In addition, in the above manufacturing process, 3 to 100y of silicon carbide
Although 5% by weight of the binder was sufficient to spread into a sheet, if the matrix material and binder were kneaded without adding methanol and the binder was spread into a sheet, 2% by weight of the binder was added. Retention of electrolyte is poor. Example 2 Water was added to the mixed material obtained in Example 1 above and applied directly onto the electrode surface to form a matrix base material, and this matrix base material was impregnated with 95% phosphoric acid solution to form an electrolyte retention matrix. did.

この塗布法で得た電解質保持マトリックスでは包圧力が
0.7kg/d〜1.05k9/d得られたのに対し、
メタノールを添加しないでマトリックス材料と結着剤混
練した場合には0.14k9/d〜0.21k9/Cl
.にしかならなかつた。また上述の2つの実施例に示し
たマトリックス基材を厚さ0.3〜0.5朗200順角
のシール状にして一端部を保持して吊り下げたところ自
重による破壊はなく、充分な機械的強度が得られたのに
対し、メタノールを添加しないで前記と同寸法のマトリ
ックス基材のシートを形成し吊り下けたところ自重によ
り破壊した。さらに上述の実施例に示した電解質保持マ
トリックスを用いて、第1図に示した単セルの大きさが
200Wr1n角の燃料電池を組み立ててその特性を検
討した。
With the electrolyte retention matrix obtained by this coating method, the envelope pressure was obtained from 0.7 kg/d to 1.05 k9/d.
When matrix material and binder are kneaded without adding methanol, 0.14k9/d to 0.21k9/Cl
.. It just turned out to be. Furthermore, when the matrix substrate shown in the above two examples was made into a seal with a thickness of 0.3 to 0.5 200 mm and hung by holding one end, it did not break due to its own weight, and the While mechanical strength was obtained, when a sheet of the matrix base material with the same dimensions as above was formed without adding methanol and suspended, it broke under its own weight. Further, using the electrolyte retention matrix shown in the above-mentioned example, a fuel cell having a unit cell size of 200 Wr1n square as shown in FIG. 1 was assembled and its characteristics were investigated.

図において符号1は電解質保持マトリックスで、この電
解質保持マトリックス1の両面にそれせろ白金触媒を有
する燃料極2、空気極3が配され、さらに各極の上にカ
ーボンベーパー4が配され、このカーボンベーパー4の
上に燃料通路5、空気通路6を形成する双極性隔離板7
が配置されている。このように構成された燃料電池に水
素ガスおよび空気をそれぞれの通路に供給し通流させた
時の通電特性は第2図に示した通りである。
In the figure, reference numeral 1 denotes an electrolyte holding matrix, and a fuel electrode 2 and an air electrode 3 each having a platinum catalyst are arranged on both sides of the electrolyte holding matrix 1, and a carbon vapor 4 is arranged on each electrode. A bipolar separator 7 forming a fuel passage 5 and an air passage 6 above the vapor 4
is located. The energization characteristics when hydrogen gas and air are supplied to the respective passages of the fuel cell constructed in this way and made to flow are as shown in FIG. 2.

この図で符号1,■はそれぞれ上述の実施例1、実施例
2て示した電解質保持マトリックスを有する燃料電池の
特性曲線であり、■は電解質保持マトリックスに従来の
ものを用いた燃料電池の特性曲線てある。図から判明す
るように本発明による電解質保持マトリックスを用いた
燃料電池の電流密度に対する電圧降下は大巾に改善され
る。このように本発明によれば化学的に安定した低価格
のマトリックス材料と少ない結着剤を用いて親水性、電
解液の保持性が優れ、充分な機械強度等を有し、電池特
性が大巾に改善される電解質保持マトリックスが簡易な
工程により得られる利点を有する。
In this figure, symbols 1 and ■ are the characteristic curves of the fuel cell having the electrolyte retention matrix shown in Example 1 and Example 2, respectively, and ■ is the characteristic curve of the fuel cell using the conventional electrolyte retention matrix. It has a curve. As can be seen from the figure, the voltage drop versus current density of the fuel cell using the electrolyte retention matrix according to the present invention is greatly improved. As described above, according to the present invention, by using a chemically stable, low-cost matrix material and a small amount of binder, it has excellent hydrophilicity and electrolyte retention, sufficient mechanical strength, etc., and excellent battery characteristics. It has the advantage that an electrolyte retention matrix that is greatly improved in width can be obtained through a simple process.

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

第1図は本発明による電解質保持マトリックスを用いた
燃料電池の概略を示す断面図、第2図は本発明に係る燃
料電池の通電特性を示す特性図である。 1・・・・・・電解質保持マトリックス、2・・・・・
・燃料極、3・・・・・・空気極。
FIG. 1 is a cross-sectional view schematically showing a fuel cell using an electrolyte retention matrix according to the present invention, and FIG. 2 is a characteristic diagram showing the current conduction characteristics of the fuel cell according to the present invention. 1... Electrolyte retention matrix, 2...
・Fuel electrode, 3... Air electrode.

Claims (1)

【特許請求の範囲】[Claims] 1 無機化合物粉末とポリテトラフルオロエチレンの懸
濁液とを混合し、この混合したものを加熱し、この加熱
したものにメタノール、エタノール、プロパノール、イ
ソプロパノールおよびイソブチルアルコールの中から選
ばれた少なくとも1種の添加剤を混合し、さらにこの混
合したものを加熱して前記添加剤及び水分を除去し、生
じた物質を所定の薄板状に成形することを特徴とする燃
料電池の電解質保持マトリックスの製造方法。
1 Mix an inorganic compound powder and a suspension of polytetrafluoroethylene, heat the mixture, and add at least one kind selected from methanol, ethanol, propanol, isopropanol, and isobutyl alcohol to the heated mixture. A method for producing an electrolyte retention matrix for a fuel cell, comprising: mixing additives, heating the mixture to remove the additives and moisture, and forming the resulting material into a predetermined thin plate shape. .
JP55133714A 1980-09-27 1980-09-27 Method for manufacturing electrolyte retention matrix for fuel cells Expired JPS6046515B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55133714A JPS6046515B2 (en) 1980-09-27 1980-09-27 Method for manufacturing electrolyte retention matrix for fuel cells

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55133714A JPS6046515B2 (en) 1980-09-27 1980-09-27 Method for manufacturing electrolyte retention matrix for fuel cells

Publications (2)

Publication Number Publication Date
JPS5760670A JPS5760670A (en) 1982-04-12
JPS6046515B2 true JPS6046515B2 (en) 1985-10-16

Family

ID=15111175

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55133714A Expired JPS6046515B2 (en) 1980-09-27 1980-09-27 Method for manufacturing electrolyte retention matrix for fuel cells

Country Status (1)

Country Link
JP (1) JPS6046515B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6238612U (en) * 1985-08-22 1987-03-07

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4898631A (en) * 1988-01-15 1990-02-06 California Institute Of Technology Method for fabricating ceramic filaments and high density tape casting method
US5057362A (en) * 1988-02-01 1991-10-15 California Institute Of Technology Multilayer ceramic oxide solid electrolyte for fuel cells and electrolysis cells
US4957673A (en) * 1988-02-01 1990-09-18 California Institute Of Technology Multilayer ceramic oxide solid electrolyte for fuel cells and electrolysis cells and method for fabrication thereof
US5879828A (en) * 1997-10-10 1999-03-09 Minnesota Mining And Manufacturing Company Membrane electrode assembly
US5879827A (en) * 1997-10-10 1999-03-09 Minnesota Mining And Manufacturing Company Catalyst for membrane electrode assembly and method of making
US6136412A (en) * 1997-10-10 2000-10-24 3M Innovative Properties Company Microtextured catalyst transfer substrate
US6042959A (en) * 1997-10-10 2000-03-28 3M Innovative Properties Company Membrane electrode assembly and method of its manufacture
JPH11204121A (en) * 1998-01-19 1999-07-30 Aisin Seiki Co Ltd Solid polymer electrolyte fuel cell

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5229938A (en) * 1975-09-02 1977-03-07 Pioneer Electronic Corp Detection apparatus for the operation of electric machiens

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6238612U (en) * 1985-08-22 1987-03-07

Also Published As

Publication number Publication date
JPS5760670A (en) 1982-04-12

Similar Documents

Publication Publication Date Title
RU2182387C2 (en) Bipolar separator plate of fuel cell with proton-exchange membrane
JP7387905B2 (en) Gas diffusion layer, manufacturing method thereof, membrane electrode assembly and fuel cell
WO2000011741A1 (en) Fuel cell and method of menufacture thereof
US4529671A (en) Fuel cell
JPS6046515B2 (en) Method for manufacturing electrolyte retention matrix for fuel cells
JP2001155744A (en) Proton conductor
JP2004296274A (en) Fuel cell, method of manufacturing the same, and fuel cell
JP2002313371A (en) Cell unit of fuel cell
JP2002075406A (en) Fuel battery cell unit and manufacturing method
JPH0548581B2 (en)
JP5987766B2 (en) Fuel cell
JPH0574190B2 (en)
JPS6282652A (en) Manufacture of gas diffusion electrode
JPH04218267A (en) Solid electrolyte type fuel cell
JPS6340264A (en) Manufacture of electrolyte retaining matrix for phosphoric acid fuel cell
JP2569769B2 (en) Phosphoric acid fuel cell
JPS60133660A (en) Manufacture of electrode substrate of fuel cell
JPH01204366A (en) Manufacture of electrolyte retaining matrix for fuel cell
JP2003178773A (en) Fuel-cell unit
JPS6332865A (en) Electrolyte holding matrix for fuel cell
JPS61259460A (en) Matrix for phosphoric-acid fuel cell
JPH02170362A (en) Fuel cell
JPS62154572A (en) Manufacture of molten carbonate fuel cell
JPS633421B2 (en)
JPS58100369A (en) Electrolyte matrix for fuel cell