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
JPS6029190B2 - Method for impregnating electrolyte into the matrix of matrix fuel cells - Google Patents
[go: Go Back, main page]

JPS6029190B2 - Method for impregnating electrolyte into the matrix of matrix fuel cells - Google Patents

Method for impregnating electrolyte into the matrix of matrix fuel cells

Info

Publication number
JPS6029190B2
JPS6029190B2 JP53063091A JP6309178A JPS6029190B2 JP S6029190 B2 JPS6029190 B2 JP S6029190B2 JP 53063091 A JP53063091 A JP 53063091A JP 6309178 A JP6309178 A JP 6309178A JP S6029190 B2 JPS6029190 B2 JP S6029190B2
Authority
JP
Japan
Prior art keywords
matrix
fuel
electrolyte
electrode
gas
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
JP53063091A
Other languages
Japanese (ja)
Other versions
JPS54154045A (en
Inventor
博之 田島
正博 桜井
邦夫 水上
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.)
Fuji Electric Co Ltd
Furukawa Battery Co Ltd
Original Assignee
Fuji Electric Co Ltd
Furukawa Battery 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 Fuji Electric Co Ltd, Furukawa Battery Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP53063091A priority Critical patent/JPS6029190B2/en
Publication of JPS54154045A publication Critical patent/JPS54154045A/en
Publication of JPS6029190B2 publication Critical patent/JPS6029190B2/en
Expired 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)

Description

【発明の詳細な説明】 本発明はマトリックス型燃料電池のマトリックスへの電
解質含浸方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for impregnating an electrolyte into a matrix of a matrix fuel cell.

マトリックス型燃料電池は、燃料電極と酸化剤電極との
間に介在するマトリックスに液状電解質を含浸すること
により電池を構成するものであって、マトリックス中に
液状電解質を変質させずに含浸させることはマトリック
ス型燃料電池製作上、きわめて重要である。
Matrix fuel cells are constructed by impregnating a matrix interposed between a fuel electrode and an oxidizer electrode with a liquid electrolyte, and it is impossible to impregnate the liquid electrolyte into the matrix without altering its properties. This is extremely important in the production of matrix fuel cells.

従来、マトリックス型燃料電池のマトリックス中に液状
電解質を含浸させる方法として、電池組立時にマトリッ
クスに液状電解質を含浸させる方法がとられていたが、
この際に、電解質の吸湿性が強いために、外部から水分
を吸収し、電解質の濃度が変化するとともに、外部より
水分を吸収した分だけ、電解質の体積が増大し、電池組
立時に外部へ漏出する恐れがあった。
Conventionally, the method of impregnating liquid electrolyte into the matrix of a matrix fuel cell was to impregnate the matrix with liquid electrolyte during battery assembly.
At this time, since the electrolyte has strong hygroscopicity, it absorbs moisture from the outside, changing the concentration of the electrolyte, and the volume of the electrolyte increases by the amount of moisture absorbed from the outside, which leaks out when the battery is assembled. There was a fear that it would.

本発明は、上記u従来方法における欠点を除き、液状電
解質の濃度を変化させることなくマトリックス中に液状
電解質を含浸できる方法を提供することを目的とする。
An object of the present invention is to provide a method capable of impregnating a liquid electrolyte into a matrix without changing the concentration of the liquid electrolyte, eliminating the drawbacks of the conventional methods described above.

次に本発明の実施例を図によって説明する。第1図は電
池の構成、第2図は電極の構造を示すもので、燃料電極
1は炭素繊維基村2とポリテトラフルオロェチレンとグ
ラフアィト粉末からなる溌水層3と、貴金属触媒を担持
した炭素質粉末と少量のポリテトラフルオ。エチレンを
混合した触媒層4からなる。溌水層3には第2図aから
判るように通路30が形成されており、この通路30は
親水性の触媒層4と同質の材料で満たされて触媒親水層
を炭素繊維基村に接触せしめている。また、酸化剤電極
5は炭素繊維基材6と溌水層7と触媒層8からなる。こ
れら電極の炭素繊維基材2および6はガス分離板9およ
び10とそれぞれ接触し、ガス区画室11および12を
形成する。ガス区画室11には燃料ガス供9溝口13、
排出口15が、またガス区画室12には酸化剤ガス供給
口14、排水口16がそれぞれ設けられている。また両
電極の触媒層4,8はノボロィド、酸化タンタル布、ア
スベスト紙等の多孔性繊維質のマトリックス17に接触
して、電解質区画18を形成している。このような構成
の燃料電池において、液状電解質を含浸していないマト
リックス17を燃料電極1、酸化剤電極5ではさみ、さ
らにガス分離板9,10で炭素繊維基村2,5側をはさ
み込み電池を組み立てた後、燃料ガス供給口13より燃
料ガス区画11に液状電解質(日3P04、WS04、
KOH、NaOH等)を満たし、燃料電極1のガス側層
から電極を通して、マトリックス17に液状電解質を含
浸させる。この含浸にあたっては前述の通路30が大き
な役割を果す。このとき酸化剤ガス区画12には乾燥し
た空気、窒素または不活性ガスを流しておく。第1表は
10仇W%の燐酸日3P04を2500の温度のもとで
燃料ガス区画室11に満たし、燃料電極の通路30を介
してマトリックス17に達する燐酸の移動距離を時間の
関係で調べたものである。この結果より高濃度(10仇
れ%)の燐酸は19比p(センチポアズ)もの高い粘度
を有するにもかかわらず、ゆるやかな速度でマトリック
スに浸透していくことがわかる。ちなみに、単セル当た
り1.球Wの出力を有する60×60(桝)面積に25
00の温度のもとで10仇れ%の燐酸を含浸する場合、
溌水層に電解液の通路を8柳ピッチで設けたものでは、
約2時間でマトリックスに所定の電解液を含浸すること
ができた。第1表十分に液状電解質をマトリックス17
に含浸させたのち、燃料ガス区画11に満たした余分の
液状電解質をガス排出口15より除き、燃料ガス区画1
1内に酸化剤ガス区画12と同様に、乾燥した空気、窒
素および不活性ガスを流し乾燥させる。
Next, embodiments of the present invention will be described with reference to the drawings. Figure 1 shows the structure of the battery, and Figure 2 shows the structure of the electrode.The fuel electrode 1 has a carbon fiber substrate 2, a water-repellent layer 3 made of polytetrafluoroethylene and graphite powder, and a noble metal catalyst supported. carbonaceous powder and a small amount of polytetrafluorocarbon. It consists of a catalyst layer 4 mixed with ethylene. As can be seen from FIG. 2a, a passage 30 is formed in the water repellent layer 3, and this passage 30 is filled with the same material as the hydrophilic catalyst layer 4 to bring the catalyst hydrophilic layer into contact with the carbon fiber matrix. It's forcing me. Further, the oxidizer electrode 5 is composed of a carbon fiber base material 6, a water repellent layer 7, and a catalyst layer 8. The carbon fiber substrates 2 and 6 of these electrodes are in contact with gas separation plates 9 and 10, respectively, forming gas compartments 11 and 12. The gas compartment 11 has a fuel gas supply 9 and a groove opening 13;
The gas compartment 12 is provided with an oxidizing gas supply port 14 and a drain port 16, respectively. Further, the catalyst layers 4 and 8 of both electrodes are in contact with a porous fibrous matrix 17 such as noboroid, tantalum oxide cloth, asbestos paper, etc. to form an electrolyte compartment 18. In a fuel cell having such a configuration, the matrix 17 not impregnated with liquid electrolyte is sandwiched between the fuel electrode 1 and the oxidizer electrode 5, and the carbon fiber base layers 2 and 5 sides are further sandwiched between the gas separation plates 9 and 10 to form a battery. After assembling, liquid electrolyte (Japanese 3P04, WS04,
(KOH, NaOH, etc.), and the matrix 17 is impregnated with a liquid electrolyte through the electrode from the gas side layer of the fuel electrode 1. The aforementioned passage 30 plays a major role in this impregnation. At this time, dry air, nitrogen, or an inert gas is allowed to flow through the oxidant gas section 12. Table 1 shows that the fuel gas compartment 11 is filled with 10W% phosphoric acid 3P04 at a temperature of 2500°C, and the distance traveled by the phosphoric acid reaching the matrix 17 through the passage 30 of the fuel electrode is investigated in relation to time. It is something that The results show that phosphoric acid at a high concentration (10%) permeates into the matrix at a slow rate, despite having a viscosity as high as 19 centipoise. By the way, 1.0 per single cell. 25 in the area of 60 x 60 (square) with the power of the sphere W
When impregnating with 10% phosphoric acid at a temperature of 0.00%,
In the case where the electrolyte passages are provided in the permeable water layer at 8 willow pitch,
The matrix was able to be impregnated with the specified electrolytic solution in about 2 hours. Table 1 Adequate liquid electrolyte matrix 17
After the liquid electrolyte is impregnated into the fuel gas compartment 11, the excess liquid electrolyte filled in the fuel gas compartment 11 is removed from the gas outlet 15, and the fuel gas compartment 1
Similarly to the oxidant gas compartment 12, dry air, nitrogen and inert gas are passed through the compartment 1 for drying.

マトリックス17内の電解質の量が不足していれば同様
の操作を繰り返す。この不足は酸化剤電極側における燃
料電極側からのガス漏洩をガスロマトグラフ、ガス検知
器等で検知することにより確認することができる。電解
質の含浸の際、ガス区画11内に満たされた液状電解質
は炭素繊維基材2を通り、ざらに溌水層3内に間隙を置
いて設けられた触媒親水層4の突出部分(通路30)か
ら触媒親水層4を経て、マトIJックス17内に達する
。なお、燐酸は常温では粘度が高いもののこれを高温に
加熱すれば粘度は低下する。
If the amount of electrolyte in the matrix 17 is insufficient, repeat the same operation. This deficiency can be confirmed by detecting gas leakage from the fuel electrode side on the oxidizer electrode side using a gas chromatograph, gas detector, etc. During electrolyte impregnation, the liquid electrolyte filled in the gas compartment 11 passes through the carbon fiber base material 2 and passes through the protruding portions (passages 30 ), passes through the catalyst hydrophilic layer 4, and reaches the inside of the MATO IJ box 17. Although phosphoric acid has a high viscosity at room temperature, the viscosity decreases when it is heated to a high temperature.

例えば第6図に示すように、10肌t%の燐酸では30
℃で15比pの粘度を有するものが100qCで16p
となり約1/10に粘度を下げることができる。したが
って、あらかじめ燐酸電解液の温度を高めて粘度を低く
した状態で燃料ガス区画室に供給すれば、比較的容易に
電解液をマトリックスに含浸することができる。この場
合、燐酸だけを加熱したのでは電池内部で燐酸の温度は
下がってしまうので、電池を炉内に置くなどして加熱す
ることが望ましい。また、燐酸はその濃度を下げれば粘
度は低下する。例えば第2表に示すように、2500の
燐酸の場合、10肌t%では約19比pの粘度を有する
ものが8仇れ%では27.位pとなる。したがって、あ
らかじめ低濃度の燐酸電解液をマトリックスに含浸させ
たのち、電池を作動温度近くまで加熱する操作を繰り返
すことによっても、所定濃度の電解液を得ることができ
る。第2表 この燃料電極1における通路30の作り方を第3図〜第
5図に基づいて説明する。
For example, as shown in Figure 6, with 10 skin t% phosphoric acid, 30
A substance with a viscosity of 15 specific p at °C has a viscosity of 16 p at 100 qC.
Therefore, the viscosity can be reduced to about 1/10. Therefore, by supplying the phosphoric acid electrolyte to the fuel gas compartment in a state in which the temperature of the phosphoric acid electrolyte is raised to lower its viscosity, the matrix can be impregnated with the electrolyte relatively easily. In this case, if only the phosphoric acid is heated, the temperature of the phosphoric acid will drop inside the battery, so it is desirable to heat the battery by placing it in a furnace or the like. Furthermore, the viscosity of phosphoric acid decreases when its concentration is lowered. For example, as shown in Table 2, in the case of 2500 phosphoric acid, it has a viscosity of about 19 ratio p at 10 t%, but 27. The position becomes p. Therefore, an electrolytic solution with a predetermined concentration can also be obtained by repeatedly impregnating a matrix with a phosphoric acid electrolytic solution of a low concentration and then heating the battery to near the operating temperature. Table 2 How to make the passage 30 in this fuel electrode 1 will be explained based on FIGS. 3 to 5.

まず製膜用枠体19に囲まれた炭素繊維基材2の表面に
格子状の型20〜22を薄く。型20は格子状をなして
おり型厚が綾水層3の厚さに相当するものである。この
型20を置いた後ポリテトラフルオロェチレンとグラフ
アィト混合物をスクリーン印刷法、スプレィ法等で炭素
繊維基材2上に0.3〜0.5肋の厚さに塗布する。塗
布後、型を除くことによって第2図aの通路30が形成
される。さらにこの上に貴金属触媒を担持した炭素質粉
末とポリテトラフルオロェチレンの混合物をスクリーン
印刷法やスプレィ法等で塗布し、触媒親水層4とする。
型を除いた部分には触媒親水層4が入り込むため、触媒
親水層4が炭素繊維基材2に接触する。これを乾燥後加
熱焼成して炭素繊維基材、穣水層、触媒親水層の3層か
らなる燃料電極を作る。この場合に結着剤として用いら
れるポリテトラフルオロェチレンの量は、溌水層におい
ては液状電解質で漏れないようにするため30〜80重
量%親水層では逆に0.1%から最大1の重量%までで
ある。第4図および第5図は第3図と異なる形状の型を
用いた例を示すもので、第4図の型21は細長矩形でこ
れを複数個間隔を置いて並べてある。
First, lattice-shaped molds 20 to 22 are thinly formed on the surface of the carbon fiber base material 2 surrounded by the film forming frame 19. The mold 20 has a lattice shape, and the mold thickness corresponds to the thickness of the twill water layer 3. After placing the mold 20, a mixture of polytetrafluoroethylene and graphite is applied onto the carbon fiber substrate 2 to a thickness of 0.3 to 0.5 ribs by screen printing, spraying, or the like. After application, the mold is removed to form the passageway 30 of FIG. 2a. Furthermore, a mixture of carbonaceous powder supporting a noble metal catalyst and polytetrafluoroethylene is applied thereon by screen printing, spraying, or the like to form the catalyst hydrophilic layer 4.
Since the catalyst hydrophilic layer 4 enters the portion excluding the mold, the catalyst hydrophilic layer 4 comes into contact with the carbon fiber base material 2 . After drying, this is heated and fired to produce a fuel electrode consisting of three layers: a carbon fiber base material, a filtrated water layer, and a catalyst hydrophilic layer. In this case, the amount of polytetrafluoroethylene used as a binder is 30 to 80% by weight in the water-repellent layer to prevent leakage of the liquid electrolyte.On the contrary, the amount of polytetrafluoroethylene used as a binder in the hydrophilic layer is 0.1% to a maximum of 1%. up to % by weight. FIGS. 4 and 5 show an example in which a mold having a shape different from that in FIG. 3 is used. The mold 21 in FIG. 4 is an elongated rectangle, and a plurality of molds are arranged at intervals.

第5図は網状の型22を炭素繊維基材2上に置いたもの
である。型21、型22はいづれも型20と同様に触媒
親水層の突出部分を形成する型となるものである。酸化
剤電極5は第2図bに示すように燃料電極1と同様の三
層構造になっているもので、燃料電極1と同様に炭素繊
維基村6に綾水層7、触媒親水層8が順次塗布され、加
熱焼成して製造される。
In FIG. 5, a mesh mold 22 is placed on the carbon fiber base material 2. In FIG. Like the mold 20, the molds 21 and 22 are both molds for forming the protruding portions of the catalyst hydrophilic layer. The oxidizer electrode 5 has a three-layer structure similar to the fuel electrode 1, as shown in FIG. are sequentially coated and heated and fired.

酸化剤電極5は燃料電極1に比べ分極の程度がはるかに
大きく、酸化剤電極5に第2図aの通路30を設けて反
応面積を減少するのは電池の特性上好ましくない。以上
のように、本発明によれば燃料電極を酸化剤電極と共に
マトリックスを介挿して粗合せた後、燃料電極側から液
状電解質を注入することができるので、電解液が吸湿に
よって変質したり、体積を増大したりすることないこ所
望の電解質濃度で所要量を含浸することが可能となるも
ので、作動中に電解質の補給が容易にできるという付加
的な効果も得られ、実用に供して多大の利点が得られる
ものである。
The degree of polarization of the oxidant electrode 5 is much greater than that of the fuel electrode 1, and it is not preferable to reduce the reaction area by providing the passage 30 in FIG. As described above, according to the present invention, the liquid electrolyte can be injected from the fuel electrode side after the fuel electrode and the oxidizer electrode are roughly combined by inserting a matrix, so that the electrolyte does not change in quality due to moisture absorption. This makes it possible to impregnate the required amount of electrolyte at the desired concentration without increasing the volume, and has the added effect of making it easy to replenish electrolyte during operation, making it suitable for practical use. This provides many advantages.

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

第1図は本発明によるマトリックス型燃料電池の縦断断
面図、第2図aは燃料電極、bは酸化剤電極のそれぞれ
の縦断面図、第3図、第4図および第5図は燃料電極の
製造のための型を示す斜視図、第6図は濃度の異なる燐
酸の温度と粘度の関係を示すグラフである。 1……燃料電極、2,6……炭素繊維基材、3,7・・
・・・・溌水層、4,8・・・・・・触媒親水層、5・
・・・・・酸化剤電極、9,10・・・・・・ガス分離
板、11,12……ガス区画、13,14……ガス供給
口、15,16・・・・・・ガス排出口、17・・・・
・・マトリックス、18・・・・・・電解質区画、19
…・・・製膜用枠体、20,21,22・・・・・・型
。 第1図 第2図 第3図 第4図 第5図 第6図
FIG. 1 is a longitudinal sectional view of a matrix fuel cell according to the present invention, FIG. 2 a is a longitudinal sectional view of a fuel electrode, and FIG. 2 b is a longitudinal sectional view of an oxidizer electrode. FIGS. FIG. 6 is a graph showing the relationship between temperature and viscosity of phosphoric acid with different concentrations. 1...Fuel electrode, 2,6...Carbon fiber base material, 3,7...
... Water repellent layer, 4,8... Catalyst hydrophilic layer, 5.
... Oxidizer electrode, 9, 10 ... Gas separation plate, 11, 12 ... Gas compartment, 13, 14 ... Gas supply port, 15, 16 ... Gas exhaust Exit, 17...
... Matrix, 18 ... Electrolyte compartment, 19
...Filming frame, 20, 21, 22...Model. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 Figure 6

Claims (1)

【特許請求の範囲】[Claims] 1 マトリツクスを挾んで燃料電極と酸化剤電極とを配
設し、燃料電極と酸化剤電極の前記マトリツクスと反対
側の方からそれぞれ燃料ガスおよび酸化剤ガスを供給す
るマトリツクス型燃料電池において、炭素繊維基材と撥
水層と触媒親水層とを順次積層して成る燃料電極の撥水
層に、これを貫通する通路を設けて炭素繊維基材と触媒
親水層とを接触せしめ、燃料電池を組立てたのちに燃料
電極を通して燃料ガス区画室側から液状電解質を含浸さ
せることを特徴とするマトリツクス型燃料電池のマトリ
ツクスへの電解質含浸方法。
1. In a matrix type fuel cell in which a fuel electrode and an oxidizer electrode are disposed with a matrix sandwiched between them, and a fuel gas and an oxidant gas are supplied from the opposite side of the fuel electrode and the oxidizer electrode, respectively, the carbon fiber A fuel cell is assembled by providing a passage through the water-repellent layer of a fuel electrode, which is formed by sequentially laminating a base material, a water-repellent layer, and a catalyst hydrophilic layer, and bringing the carbon fiber base material into contact with the catalyst hydrophilic layer. 1. A method for impregnating a matrix of a matrix fuel cell with an electrolyte, which comprises subsequently impregnating a liquid electrolyte from the fuel gas compartment side through a fuel electrode.
JP53063091A 1978-05-26 1978-05-26 Method for impregnating electrolyte into the matrix of matrix fuel cells Expired JPS6029190B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53063091A JPS6029190B2 (en) 1978-05-26 1978-05-26 Method for impregnating electrolyte into the matrix of matrix fuel cells

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53063091A JPS6029190B2 (en) 1978-05-26 1978-05-26 Method for impregnating electrolyte into the matrix of matrix fuel cells

Publications (2)

Publication Number Publication Date
JPS54154045A JPS54154045A (en) 1979-12-04
JPS6029190B2 true JPS6029190B2 (en) 1985-07-09

Family

ID=13219290

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53063091A Expired JPS6029190B2 (en) 1978-05-26 1978-05-26 Method for impregnating electrolyte into the matrix of matrix fuel cells

Country Status (1)

Country Link
JP (1) JPS6029190B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0640493B2 (en) * 1985-09-02 1994-05-25 株式会社東芝 Fuel cell

Also Published As

Publication number Publication date
JPS54154045A (en) 1979-12-04

Similar Documents

Publication Publication Date Title
US4125676A (en) Carbon foam fuel cell components
US4615955A (en) Fuel cell
JPH05283094A (en) Fuel cell
JPH02234358A (en) Fuel cell
JPS6047702B2 (en) Fuel cell assembly and its manufacturing method
JP3022528B1 (en) Polymer electrolyte fuel cell
JPH0652871A (en) Polymer electrolyte fuel cell
JP2022553451A (en) Gas diffusion layer, manufacturing method thereof, membrane electrode assembly, and fuel cell
WO1989006055A1 (en) Gas-permeable and ion-permeable membrane for electrochemical system
JP3502508B2 (en) Direct methanol fuel cell
US7867668B2 (en) Electrolyte layer for fuel cell, fuel cell, and method of manufacturing electrolyte layer for fuel cell
JP2010129309A (en) Gas diffusion layer for fuel cell, and manufacturing method thereof
JPH06103983A (en) Solid polymer electrolyte fuel cell and method for manufacturing the electrode thereof
JPS6029190B2 (en) Method for impregnating electrolyte into the matrix of matrix fuel cells
JPH10334922A (en) Polymer electrolyte fuel cell and method of manufacturing the polymer electrolyte fuel cell
JP2003173788A (en) Gas diffusion layer for polymer electrolyte fuel cell, electrolyte membrane-electrode assembly using the same, and polymer electrolyte fuel cell
JPS5848366A (en) Fuel cell
JPS5968171A (en) Electrodes for fuel cells
US4751062A (en) Fuel cell with electrolyte matrix assembly
JP2657015B2 (en) Electrolyte for impregnation of phosphoric acid fuel cell
Blanco Study of selected water management strategies for proton exchange membrane fuel cells
JPS58103784A (en) Fuel cell
JPH0640493B2 (en) Fuel cell
JPS6340025B2 (en)
JPH08264192A (en) Fuel cell electrode base material and method for manufacturing the same