JPH0129308B2 - - Google Patents

Info

Publication number
JPH0129308B2
JPH0129308B2 JP57202527A JP20252782A JPH0129308B2 JP H0129308 B2 JPH0129308 B2 JP H0129308B2 JP 57202527 A JP57202527 A JP 57202527A JP 20252782 A JP20252782 A JP 20252782A JP H0129308 B2 JPH0129308 B2 JP H0129308B2
Authority
JP
Japan
Prior art keywords
electrode
electrolyte
central reaction
fuel
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
JP57202527A
Other languages
Japanese (ja)
Other versions
JPS5991671A (en
Inventor
Toshiaki Murahashi
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 JP57202527A priority Critical patent/JPS5991671A/en
Publication of JPS5991671A publication Critical patent/JPS5991671A/en
Publication of JPH0129308B2 publication Critical patent/JPH0129308B2/ja
Granted 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
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04276Arrangements for managing the electrolyte stream, e.g. heat exchange
    • H01M8/04283Supply means of electrolyte to or in matrix-fuel cells
    • 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
    • H01M8/0271Sealing or supporting means around electrodes, matrices or membranes
    • 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)
  • Inert Electrodes (AREA)
  • Fuel Cell (AREA)

Description

【発明の詳細な説明】 この発明は燃料電池、特にその電極部の構成に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fuel cell, and particularly to the structure of an electrode portion thereof.

従来この種の燃料電池として第1図に示すもの
があつた。図において、1はガス分離板で燃料流
路2と酸化剤流路3が両面に設けられている。4
は燃料電極であり、これに接して電解質マトリク
ス5があり、その上に酸化剤電極6がある。7は
シールのためのパツキングであり、8はガス分離
板1の周辺部分に設けられ電解質を保持する電解
質リザーバである。それぞれの番号のaがついた
部分は電池反応が生じる部分で、6の部分はシー
ル部であり不透気処理を施した部分である。
A conventional fuel cell of this type is shown in FIG. In the figure, reference numeral 1 denotes a gas separation plate, and a fuel flow path 2 and an oxidizer flow path 3 are provided on both sides of the plate. 4
is a fuel electrode, in contact with which is an electrolyte matrix 5, and above which is an oxidizer electrode 6. 7 is packing for sealing, and 8 is an electrolyte reservoir provided around the gas separation plate 1 to hold electrolyte. The parts marked with a in each number are the parts where the battery reaction occurs, and the part numbered 6 is the sealed part, which is treated to be air-impermeable.

次に動作について説明する。燃料流路2から供
給された燃料は燃料電極4で酸化され水素は陽イ
オンと電子になり、陽イオンは電解質マトリクス
5の反応部分5aを移動して酸化剤電極6に到達
し、酸化剤流路3から供給される酸化剤と反応し
て水を生成する。燃料電極4で生じた電子は外部
負荷(図示せず)を経て酸化剤電極6に達し、こ
こで還元反応に寄与する中で外部負荷において電
気エネルギーとなる。反応において電解質マトリ
クス5は常に電解質を保持している必要があり、
そのために電解質溜めとしての電解質リザーバ8
が設けられている。電解質リザーバ8から電解質
マトリクス5への電解質の供給およびガスシール
のため、電極4の周辺部分4bは電解質を浸み込
ませるために親水性となるように処理がなされて
いる。
Next, the operation will be explained. The fuel supplied from the fuel flow path 2 is oxidized at the fuel electrode 4, hydrogen becomes cations and electrons, and the cations move through the reaction part 5a of the electrolyte matrix 5 and reach the oxidizer electrode 6, where the oxidizer flow It reacts with the oxidizing agent supplied from path 3 to produce water. The electrons generated at the fuel electrode 4 pass through an external load (not shown) and reach the oxidizer electrode 6, where they contribute to a reduction reaction and become electrical energy in the external load. During the reaction, the electrolyte matrix 5 must always hold electrolyte,
For this purpose, an electrolyte reservoir 8 is used as an electrolyte reservoir.
is provided. In order to supply the electrolyte from the electrolyte reservoir 8 to the electrolyte matrix 5 and to seal the gas, the peripheral portion 4b of the electrode 4 is treated to be hydrophilic in order to allow the electrolyte to penetrate therein.

従来の燃料電池は以上のように構成されている
ので、電極4の親水性周辺部分4bから電極4の
中央反応部分4aへの電解質の浸み込みが生じる
問題点があつた。電極4の中央反応部分4aは
PTFE(ポリテトラフルオロエチレン)を用いた
撥水処理が施されているが、あまり強度に撥水処
理を行なうと電極基材の気孔が埋まるためガス透
気性が悪くなり、ガス拡散電極としての機能が損
われる。このように電極4の周辺部分4bから中
央反応部分4aへの電解質が浸み込むと、ガス透
気性が悪くなり、その結果ガス拡散電極としての
機能が損われる欠点があつた。
Since the conventional fuel cell is constructed as described above, there is a problem in that the electrolyte permeates from the hydrophilic peripheral portion 4b of the electrode 4 into the central reaction portion 4a of the electrode 4. The central reaction part 4a of the electrode 4 is
Water-repellent treatment is applied using PTFE (polytetrafluoroethylene), but if the water-repellent treatment is applied too strongly, the pores in the electrode base material will be filled, resulting in poor gas permeability, making it difficult to function as a gas diffusion electrode. is damaged. When the electrolyte permeates from the peripheral portion 4b of the electrode 4 into the central reaction portion 4a in this way, gas permeability deteriorates, resulting in a disadvantage that the function as a gas diffusion electrode is impaired.

この発明は上記のような従来のものの欠点を除
去するためになされたもので、電解質リザーバに
対向する電極の周辺部分を親水性にすると共に、
上記電極の親水性周辺部分と中央反応部分との間
に上記中央反応部分よりも撥水性な部分を設ける
ことにより、親水性の上記電極周辺部分から中央
反応部分への電解質の移動を抑制し、燃料電池の
正常な反応を持続することを目的としている。
This invention was made in order to eliminate the drawbacks of the conventional ones as described above, and it makes the peripheral part of the electrode facing the electrolyte reservoir hydrophilic, and
By providing a portion between the hydrophilic peripheral portion of the electrode and the central reaction portion that is more water repellent than the central reaction portion, electrolyte movement from the hydrophilic peripheral portion of the electrode to the central reaction portion is suppressed; The purpose is to maintain the normal reaction of the fuel cell.

以下、この発明の一実施例を図をもとに説明す
る。第2図はこの発明にかかわる燃料電池の断面
図である。図において、4,6はそれぞれ燃料電
極および酸化剤電極であり、厚さ400〜500μmの
カーボンペーパーに触媒層を塗布したものであ
る。4bは燃料電極4の周辺部分で平均粒径1〜
5μm程度の微細な炭化珪素粒子を充填してある。
9はこの電極周辺部分4bと触媒を塗布した中央
反応部分4aとの間に設けられた中央反応部分4
aよりも撥水性な部分で、幅5〜15mmの層であ
り、混合するPTFEの量を中央反応部分より多く
することにより得られる。
An embodiment of the present invention will be described below with reference to the drawings. FIG. 2 is a sectional view of a fuel cell according to the present invention. In the figure, numerals 4 and 6 are a fuel electrode and an oxidizer electrode, respectively, which are carbon paper with a thickness of 400 to 500 μm coated with a catalyst layer. 4b is the peripheral part of the fuel electrode 4 with an average particle size of 1 to
It is filled with fine silicon carbide particles of about 5 μm.
Reference numeral 9 denotes a central reaction portion 4 provided between this electrode peripheral portion 4b and the central reaction portion 4a coated with a catalyst.
This part is more water repellent than A, and is a layer with a width of 5 to 15 mm, and is obtained by mixing a larger amount of PTFE than the central reaction part.

電極周辺部分4bはガスシールのため十分に電
解質が保持されていなければならないが、その電
解質が隣接する中央反応部分4aへ移動すると中
央反応部分4aのガス拡散性が悪くなり電極機能
が低下する。従つてガスシールの役割を果す電極
周辺部分4bと中央反応部分4aとの間に強い撥
水性を有する境界層9を設けることにより、電極
周辺部分4bに含有される電解質の中央反応部分
4aへの移動を抑制することができる。一般に、
電極反応部分4aの電極基材であるカーボンペー
パーは撥水処理が適度に施されているが、それは
電解質マトリクス5からの電解質がこれも若干の
撥水性を持つ触媒層を経て侵入するのを軽減する
ためになされているのであり、あまり強度の撥水
性処理を行なうことはガス透気性を損ない電極4
aの反応性を阻害するので行なわれない。その意
味で電極周辺部分4bからの中央反応部分4aへ
の電解質の侵入に対しては従来の構造では十分に
対処し得ず、この発明による電極の中央反応部分
4aよりも強い撥水性を有する境界層9が重要と
なる。
Electrolyte must be sufficiently retained in the electrode peripheral portion 4b for gas sealing, but if the electrolyte moves to the adjacent central reaction portion 4a, the gas diffusivity of the central reaction portion 4a will deteriorate and the electrode function will deteriorate. Therefore, by providing a boundary layer 9 having strong water repellency between the electrode peripheral part 4b and the central reaction part 4a, which serves as a gas seal, the electrolyte contained in the electrode peripheral part 4b is prevented from flowing into the central reaction part 4a. Movement can be suppressed. in general,
The carbon paper that is the electrode base material of the electrode reaction part 4a is appropriately water-repellent treated, which reduces the intrusion of the electrolyte from the electrolyte matrix 5 through the catalyst layer, which also has some water repellency. However, applying too strong a water repellent treatment will impair gas permeability and the electrode 4
This is not done because it inhibits the reactivity of a. In this sense, the conventional structure cannot sufficiently deal with the intrusion of electrolyte from the electrode peripheral part 4b into the central reaction part 4a. Layer 9 is important.

なお、上記実施例では酸化剤電極6はガスシー
ルとしてパツキング7を用いる方式について示し
たが、燃料電極4と同じ様に電解質を充填したガ
スシールを行なつてもよく、その場合は酸化剤電
極6についても中央反応部分6aよりも撥水性な
部分9を中央反応部分6aとガスシール部分との
間に設けてもよい。またこの場合は燃料電極4は
パツキングを用いたガスシールを行なつてもよ
い。
In the above embodiment, the oxidant electrode 6 uses the packing 7 as a gas seal, but it is also possible to use a gas seal filled with electrolyte in the same way as the fuel electrode 4, in which case the oxidant electrode 6 as well, a portion 9 that is more water repellent than the central reaction portion 6a may be provided between the central reaction portion 6a and the gas seal portion. Further, in this case, the fuel electrode 4 may be gas-sealed using packing.

以上のように、この発明によれば電解質リザー
バに対向する電極の周辺部分を親水性にすると共
に、上記電極の親水性周辺部分と中央反応部分と
の間に上記中央反応部分よりも撥水性な部分を設
けたので、親水性の上記電極周辺部分から中央反
応部分への電解質の移動を抑制し、燃料電池の正
常な反応を持続できる効果がある。
As described above, according to the present invention, the peripheral part of the electrode facing the electrolyte reservoir is made hydrophilic, and the area between the hydrophilic peripheral part of the electrode and the central reaction part is more water repellent than the central reaction part. The provision of this section has the effect of suppressing the movement of electrolyte from the hydrophilic peripheral area of the electrode to the central reaction area, thereby sustaining the normal reaction of the fuel cell.

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

第1図は従来の燃料電池の主要部を示す断面
図、第2図はこの発明にかかわる燃料電池の主要
部を示す断面図である。 図において、1はガス分離板、4は燃料電極、
4aは中央反応部分、4bは周辺部分、5は電解
質マトリクス、6は酸化剤電極、8は電解質リザ
ーバ、9は中央反応部分4aよりも撥水性な部分
である。なお、図中同一符号は同一または相当部
分を示すものとする。
FIG. 1 is a cross-sectional view showing the main parts of a conventional fuel cell, and FIG. 2 is a cross-sectional view showing the main parts of a fuel cell according to the present invention. In the figure, 1 is a gas separation plate, 4 is a fuel electrode,
4a is a central reaction part, 4b is a peripheral part, 5 is an electrolyte matrix, 6 is an oxidizing agent electrode, 8 is an electrolyte reservoir, and 9 is a part more water repellent than the central reaction part 4a. Note that the same reference numerals in the figures indicate the same or corresponding parts.

Claims (1)

【特許請求の範囲】[Claims] 1 周辺部分に電解質リザーバを備えたガス分離
板、燃料電極、電解質マトリクスおよび酸化剤電
極を順次積層して構成する燃料電池において、上
記電解質リザーバに対向する上記電極の周辺部分
を親水性にすると共に、上記電極の親水性周辺部
分と中央反応部分との間に上記中央反応部分より
も撥水性な部分を設けたことを特徴とする燃料電
池。
1. In a fuel cell configured by sequentially stacking a gas separation plate, a fuel electrode, an electrolyte matrix, and an oxidizer electrode with an electrolyte reservoir in the peripheral part, the peripheral part of the electrode facing the electrolyte reservoir is made hydrophilic, and , A fuel cell characterized in that a portion more water repellent than the central reaction portion is provided between the hydrophilic peripheral portion of the electrode and the central reaction portion.
JP57202527A 1982-11-16 1982-11-16 Fuel cell Granted JPS5991671A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57202527A JPS5991671A (en) 1982-11-16 1982-11-16 Fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57202527A JPS5991671A (en) 1982-11-16 1982-11-16 Fuel cell

Publications (2)

Publication Number Publication Date
JPS5991671A JPS5991671A (en) 1984-05-26
JPH0129308B2 true JPH0129308B2 (en) 1989-06-09

Family

ID=16458965

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57202527A Granted JPS5991671A (en) 1982-11-16 1982-11-16 Fuel cell

Country Status (1)

Country Link
JP (1) JPS5991671A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4978591A (en) * 1989-09-11 1990-12-18 The United States Of America As Represented By The United States Department Of Energy Corrosion free phosphoric acid fuel cell

Also Published As

Publication number Publication date
JPS5991671A (en) 1984-05-26

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