JPS61224272A - Electrode for molten carbonate fuel cell - Google Patents

Electrode for molten carbonate fuel cell

Info

Publication number
JPS61224272A
JPS61224272A JP60064290A JP6429085A JPS61224272A JP S61224272 A JPS61224272 A JP S61224272A JP 60064290 A JP60064290 A JP 60064290A JP 6429085 A JP6429085 A JP 6429085A JP S61224272 A JPS61224272 A JP S61224272A
Authority
JP
Japan
Prior art keywords
slurry
wire mesh
wire net
electrode
electrode according
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.)
Pending
Application number
JP60064290A
Other languages
Japanese (ja)
Inventor
Yukihiko Naka
幸彦 仲
Tatsumi Furukawa
古川 辰美
Kiichi Nagaya
長屋 喜一
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen 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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP60064290A priority Critical patent/JPS61224272A/en
Publication of JPS61224272A publication Critical patent/JPS61224272A/en
Pending 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
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/88Processes of manufacture
    • H01M4/8878Treatment steps after deposition of the catalytic active composition or after shaping of the electrode being free-standing body
    • H01M4/8882Heat treatment, e.g. drying, baking
    • H01M4/8885Sintering or firing
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/70Carriers or collectors characterised by shape or form
    • H01M4/80Porous plates, e.g. sintered carriers
    • 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
    • Y02E60/10Energy storage using batteries
    • 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

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Inert Electrodes (AREA)

Abstract

PURPOSE:To acquire an electrode having a reinforcement wire net only on one side in a simple method, by dissolving an organic binder in a mixed solution including an organic solvent, mixing and kneading the resultant binder solution and a metallic powder to make into a slurry, spreading the slurry on one side of a reinforcement wire net to hold the slurry, and baking up the slurry on the wire net into a porous body in a plate form. CONSTITUTION:In a mixed solvent consisting of water, methyl alcohol, isopropyl alcohol, and a nonionic surface active agent, methyl cellulose is dissolved, and the resultant binder solution and nickel powder are mixed and stirred at a reduced pressure, to make the powder into a slurry. After the resultant slurry S is put into a holder hopper 5, the slurry S is spread on the upper side of a wire net 1. After the wire net 1 holding the slurry S is removed from the slurry holder hopper and dried up, a filter paper 6 is removed from the wire net 1, and then the wire net 1 is placed in an electric furnace. After the air in the furnace is replaced with hydrogen, the slurry S is maintained in a steam flow and baked up into a porous body.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、溶融状態の炭酸塩を電解質とする溶融炭M
塩燃料電池に関し、さらに詳しくは同電池において電解
質体の両側に配置−られる一対の正負電極に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a molten coal M using molten carbonate as an electrolyte.
The present invention relates to a salt fuel cell, and more particularly to a pair of positive and negative electrodes arranged on both sides of an electrolyte body in the same cell.

発明の背m 溶融炭酸塩燃料電池における電極は通常650℃付近の
動作温度で溶融状態の炭酸3Bに接触した状態で使用さ
れる。そして同電極としては、ガスの透過性をJ:りす
るために、一般にニッケル系合金粉末を焼結して製造し
た板状の多孔質体よりなる電極が用いられている。しか
しこの電極を上記多孔質体のみで構成すると、電極の強
度が劣り、電極が発電中に変形することがある。強度を
増重には厚みを厚くすればよいのであるが、電極の厚み
は0.3〜1.0IIIIIIVl疫に限定されている
ため、多孔質板に補強材を沿わせることが必要となって
くる。補強材としてはステンレスu4製の金網が最も優
れているが、一般にステンレス鋼は溶融炭酸塩に接触す
ると腐食する。そのため腐食を防ぐには、金網を多孔質
板の片面のみに位置させた電極を製造して、金網が電極
と電解質の界面の反対側に来るように電極を配置する必
要がある。
BACKGROUND OF THE INVENTION Electrodes in molten carbonate fuel cells are typically used in contact with molten carbonic acid 3B at operating temperatures around 650°C. As the electrode, an electrode made of a plate-shaped porous body manufactured by sintering nickel-based alloy powder is generally used in order to improve gas permeability. However, if this electrode is composed only of the above porous material, the strength of the electrode will be poor and the electrode may deform during power generation. In order to increase the strength, it is sufficient to increase the thickness, but since the thickness of the electrode is limited to 0.3 to 1.0IIIIIIVl, it is necessary to run a reinforcing material along the porous plate. come. A wire mesh made of stainless steel U4 is the best reinforcing material, but stainless steel generally corrodes when it comes into contact with molten carbonate. Therefore, in order to prevent corrosion, it is necessary to manufacture an electrode in which the wire mesh is placed only on one side of the porous plate, and to arrange the electrode so that the wire mesh is on the opposite side of the interface between the electrode and the electrolyte.

従来技術およびその問題点 従来、金網補強型多孔質板の製造法としては、有機バイ
ンダー溶液に金属粉末をiIP練してスラリー化し、1
qられたスラリーにステンレス鋼製の金網を浸漬し、つ
いで担持スラリーを焼成して板状の多孔質体とする方法
が知られているが、このやり方で得られた多孔質板はそ
の内部に金網を埋め込んだものであり、上記要望にこた
え得るような、多孔質板の片面にみに′金網を有した構
造のものは得られない。
Prior art and its problems Conventionally, as a method for manufacturing a wire mesh reinforced porous plate, metal powder is kneaded with an organic binder solution by iIP to form a slurry, and 1
A method is known in which a stainless steel wire gauze is immersed in a slurry that has been quenched, and then the supported slurry is fired to form a plate-shaped porous body. A wire mesh is embedded in the porous plate, and it is not possible to obtain a porous plate with a wire mesh on one side only, which can meet the above requirements.

また予めプレスによって成形した金属粉末に金網を接合
し、接合物を焼成して多孔質板を製造する方法もあるが
、この場合均一な厚さで面積の大きい製品を1昇ること
は困難である。
There is also a method of manufacturing porous plates by bonding metal mesh to metal powder that has been pre-formed by pressing and firing the bonded material, but in this case it is difficult to produce a product with a uniform thickness and a large area. .

この発明は、上記のような実情からなされたものであっ
て、片面のみに金網を有した多孔質板よりなる溶融炭酸
塩燃料電池用電極を提供することを目的とする。
The present invention was made in view of the above-mentioned circumstances, and an object of the present invention is to provide an electrode for a molten carbonate fuel cell made of a porous plate having a wire mesh on only one side.

問題点の解決手段 この発明による電極は、上記目的の達成のために、有機
溶媒を含む混合溶媒に有機バインダーを溶解し、得られ
たバインダー溶液と金属粉末を混練してスラリーとし、
得られたスラリーを補強用金網の片面に塗布して担持さ
け、担持スラリーを焼成して板状の多孔質体とすること
により製造され、片面のみに金網を有した多孔質板J:
りなることを特徴とする。
Means for Solving the Problems In order to achieve the above object, the electrode according to the present invention is made by dissolving an organic binder in a mixed solvent containing an organic solvent, and kneading the obtained binder solution and metal powder to form a slurry.
A porous plate J having a wire mesh on only one side is manufactured by coating the obtained slurry on one side of a reinforcing wire mesh to support it, and firing the supported slurry to form a plate-shaped porous body.
It is characterized by becoming.

この発明において上記バインダー溶液を用いる理由はつ
ぎのとおりである。金属粉末のような密度の人きい粉末
をバインダー溶液に安定かつ均一に分散さ1!るには、
粘度の大きいバインダー溶液を用いればよいのであるが
、粘度が高ずぎるとJJlつて分散性が悪くなって、ス
ラリー中に気泡が残留覆る原因となり、逆に粘度が低す
ぎると、金属粉末がバインダー溶液中に安定かつ均一に
分散しない。また金属粉末バインダー溶液にリイするス
ラリーは、金網上に塗布された後も長く流動性を保って
いると、金網から流出づ゛るおそれがあるので、金網上
への塗布担持複速やかに乾燥して固化するものでなけれ
ばならない。このような観点から、この発明の方法にお
いては、バインダー溶液として、有機溶媒を含む混合溶
媒に有機バインダーを溶解してなるバインダー溶液を用
いる。そしてこの溶液を用いると、金網にスラリーを塗
布する際スラリーが適度な流動性を有し、金網上へのス
ラリーの塗布担持後は、溶媒が速やかに揮発してスラリ
ーが固化し、その間にスラリーが変形をきた−   へ
   −−−1 すおそれが全くない。
The reason for using the binder solution in this invention is as follows. Stably and uniformly disperse powder with a density similar to metal powder in binder solution 1! To do this,
It is sufficient to use a binder solution with a high viscosity, but if the viscosity is too high, the dispersibility will be poor, causing air bubbles to remain in the slurry, and conversely, if the viscosity is too low, the metal powder will dissolve in the binder solution. It is not stably and uniformly dispersed in the liquid. In addition, if the slurry applied to the metal powder binder solution remains fluid for a long time after being applied onto the wire mesh, there is a risk that it will flow out from the wire mesh. It must be able to solidify. From this point of view, in the method of the present invention, a binder solution prepared by dissolving an organic binder in a mixed solvent containing an organic solvent is used as the binder solution. When this solution is used, the slurry has appropriate fluidity when it is applied to the wire mesh, and after the slurry is applied and supported on the wire mesh, the solvent quickly evaporates and the slurry solidifies. There is no risk of deformation.

混合溶媒として水と有機溶媒を所要割合で混合してなる
溶媒を用いて、スラリーの乾燥速度を調節することもで
きる。
The drying rate of the slurry can also be adjusted by using a solvent obtained by mixing water and an organic solvent in a required ratio as a mixed solvent.

有機バインダーとしては、メチルレルロースが好ましく
用いられるが、これは限定的なものではない。
As the organic binder, methyllerulose is preferably used, but it is not limited thereto.

金網の下面にシー1〜を重ねて配し、金網の上面にスラ
リーを塗布することもできる。この場合スラリーが金網
の下面から流出することが防止される。シートとじては
濾紙のような液吸収性のよいシートを用いると、これに
スラリー中の溶媒が吸収され、スラリーの乾燥が一層促
進される。
It is also possible to arrange Sea 1~ on the lower surface of the wire mesh and apply the slurry to the upper surface of the wire mesh. In this case, the slurry is prevented from flowing out from the underside of the wire mesh. If a sheet with good liquid absorbency, such as filter paper, is used as the sheet, the solvent in the slurry will be absorbed by the sheet, and the drying of the slurry will be further accelerated.

焼成は好ましくは還元雰囲気で行なわれる。Calcining is preferably carried out in a reducing atmosphere.

この発明による電極の製造において、スラリー担持工程
に直接使用されるスラリー担持装置は、金網を基台上に
沿って所要方向に移動させる金網牽引手段と、移動する
金網の上面にスラリーを塗布するスラリー塗布手段とよ
りなる。
In manufacturing the electrode according to the present invention, the slurry carrying device used directly in the slurry carrying step includes a wire mesh pulling means for moving the wire mesh in a desired direction along the base, and a slurry for applying slurry to the top surface of the moving wire mesh. It consists of a coating means.

スラリー塗布手段は、好ましくは、金網の土面どの間に
幅調節自在のスラリー出ロスリッ1〜を右するホッパー
よりなる。
The slurry application means preferably comprises a hopper having a width-adjustable slurry outlet slit 1 between the soil surface of the wire mesh.

スラリー塗布手段の後流側には、必要に応じて、金網の
上面との間に幅調節自在の塗膜補修スリブ1〜を右Jる
スラリー整形部材が設番プられる。同部祠は小ツバ−か
ら出たスラリー中に気泡が混入している揚台や、大ぎな
面積の多孔質板を得る場合に特に有用である。
On the downstream side of the slurry application means, a slurry shaping member is installed, if necessary, to form a coating film repairing sleeve 1 whose width can be adjusted freely between the slurry shaping member and the upper surface of the wire mesh. The same part is particularly useful when obtaining a platform where air bubbles are mixed in the slurry discharged from the small brim or when obtaining a porous plate with a large area.

発明の効果 以十の次第で、この発明によれば、片面のみに補強用金
網を有した多孔質板よりなる溶融炭酸塩燃料電池用電極
を簡単な操作でIl!J造することができる。したがっ
てこうして得られた電極を、金網が電極と電解質の界面
の反対側に来るようにMdすることにより、金網と溶融
炭M塩の接触をなくして金網の腐食を防止号−ることが
できる。こうして、この発明による溶融1:AM塩燃F
11電池用電極を用いることにより、電池の寿命を大幅
に延長することができる。
According to the present invention, an electrode for a molten carbonate fuel cell made of a porous plate having a reinforcing wire mesh on only one side can be made by a simple operation. It is possible to build J. Therefore, by Md-ing the thus obtained electrode so that the wire mesh is on the opposite side of the interface between the electrode and the electrolyte, it is possible to prevent corrosion of the wire mesh by eliminating contact between the wire mesh and the molten carbon M salt. Thus, the melting 1:AM salt fuel F according to this invention
By using the No. 11 battery electrode, the life of the battery can be significantly extended.

実  施  例 つぎに上記効果を実証するためにこの発明の実施例を挙
げる。
EXAMPLES Next, examples of the present invention will be given to demonstrate the above effects.

実施例1 第1図において、スラリー担持装部は、ステンレス鋼(
SUS316)製の120メツシユの金網(1)を、こ
れの下面に重ねて配した濾紙(6)とともに、基台(2
)の上面に沿って牽引モーター(3)で左方向に一定速
度で移動さける金網牽引手段と、移動する金網(1)の
上面にスラリー(S)を塗布するスラリー塗布手段どよ
りなる。スラリー塗布手段は、スラリー塗布厚調節用の
可動壁(4)を備えたホッパー(5)よりなる。そして
可動壁(4)の高さを設定することによりポツパー(5
)のスラリー出ロスリット(7)の幅が調節せられる。
Example 1 In FIG. 1, the slurry carrying device is made of stainless steel (
A 120-mesh wire mesh (1) made of SUS316) is placed on the base (2) along with filter paper (6) stacked on the underside of the wire mesh (1).
) consists of a wire mesh traction means that moves at a constant speed to the left by a traction motor (3), and a slurry application means that applies slurry (S) to the top surface of the moving wire mesh (1). The slurry application means consists of a hopper (5) equipped with a movable wall (4) for adjusting the slurry application thickness. Then, by setting the height of the movable wall (4), the height of the movable wall (4) is set.
) The width of the slurry outlet loss slit (7) is adjusted.

上記構成のスラリー担持装置においてつきの操作を行な
った。水15Q、メチルアルコール150、イソプロピ
ルアルコール0.30および非イオン性活面活性剤0.
10よりなる混合溶媒にメチルセルロース2gを溶解し
、得られたバインダー溶液とニッケル粉末(米用インコ
社製123型)1000を減圧下に撹拌混練し、同粉末
をスラリー化した。
The following operations were performed on the slurry supporting device having the above configuration. 15 Q of water, 150 Q of methyl alcohol, 0.30 Q of isopropyl alcohol, and 0.0 Q of nonionic surfactant.
2 g of methylcellulose was dissolved in a mixed solvent consisting of 10, and the resulting binder solution and nickel powder (model 123, manufactured by Inco Inc.) 1000 were stirred and kneaded under reduced pressure to form a slurry.

得られたスラリー(S)をスラリー担持装置のポツパー
(5)に投入し、金網(1)と濾紙(6)を基台(2)
上に沿って牽引モーター(3)で15cm/minの速
度で移動させ、可動壁(4)の調節によりポツパー(5
)のスラリー出ロスリット(7)の幅をQ、4mmとし
、金網(1)の上面にスラリー(S)を塗布した。
The obtained slurry (S) is put into the popper (5) of the slurry supporting device, and the wire mesh (1) and filter paper (6) are placed on the base (2).
The traction motor (3) moves along the top at a speed of 15 cm/min, and the movable wall (4) is adjusted to move the popper (5
), the width of the slurry outlet slit (7) was Q, 4 mm, and the slurry (S) was applied to the top surface of the wire mesh (1).

こうしてスラリー(S)を担持した金網(1)をスラリ
ー担持装置からはずしてスラリーを乾燥させた後、金網
(1)から濾紙(6)を剥離し、ついで金網(1)を電
気炉に入れて炉内空気を水素で置換した後、水素気流中
で温度400℃で1時間、950℃で1時間それぞれ保
持し、スラリー(S)を焼成して多孔質化した。
After removing the wire mesh (1) supporting the slurry (S) from the slurry supporting device and drying the slurry, the filter paper (6) is peeled off from the wire mesh (1), and then the wire mesh (1) is placed in an electric furnace. After the air in the furnace was replaced with hydrogen, the slurry (S) was held at a temperature of 400° C. for 1 hour and at 950° C. for 1 hour in a hydrogen stream, and the slurry (S) was fired to make it porous.

こうして得られた多孔質板よりなる電極は多孔度60%
および厚さ0.35m1Ilのものであって、第2図に
示す顕微鏡写真から明ら□′かなように、片面のみに補
強用金網を有したものであった。
The electrode made of the porous plate thus obtained has a porosity of 60%.
It had a thickness of 0.35 ml and had a reinforcing wire mesh on only one side, as shown in the micrograph shown in FIG.

実施例2 第3図において、実施例1で用いたものと同じスラリー
担持装置のホッパー(5)の後流側に、塗膜被修用の可
動壁よりなるスラリー整形部材(8)を設け、その高さ
を設定することにより、金網(1)の−L而との間の塗
膜補修スリット(9)の幅を調節する。
Example 2 In FIG. 3, a slurry shaping member (8) consisting of a movable wall for coating is provided on the downstream side of the hopper (5) of the same slurry carrying device as used in Example 1, By setting the height, the width of the coating film repair slit (9) between -L and wire mesh (1) is adjusted.

上記構成のスラリー担持装置においてつきの操作を行な
った。水14q1メチルアル]−ル120、イソプロピ
ルアルコール0.30および非イオン性活面活性剤0.
10よりなる混合溶媒にメチルセルロース1.5gを溶
解し、得られたバインダー溶液とニッケル系合金粉末に
ッケル90重量%」−クロム10重石%、粒径5〜30
IIII)100qを減圧下に撹拌混練し、同粉末をス
ラリー化した。
The following operations were performed on the slurry supporting device having the above configuration. 14q1 of water, 120% of methylal]-al, 0.30% of isopropyl alcohol, and 0.0% of nonionic surfactant.
1.5 g of methyl cellulose was dissolved in a mixed solvent consisting of 10%, and the resulting binder solution and nickel-based alloy powder were mixed with 90% by weight of nickel - 10% of chromium, particle size 5 to 30%.
III) 100q was stirred and kneaded under reduced pressure to form the powder into a slurry.

得られたスラリー(S)をスラリー担持装置のホッパー
(5)に投入し、金網(1)と濾紙(6)を基台(2)
上に沿って牽引モーター(3)でi 5 cn+/mi
nの速度で移動させ、可動壁(4)の調節にJ:リボツ
バ−(5)のスラリー出「1スリツh(7)の幅をQ、
9+++n+とじ、塗膜補修スリッ1−(9)の幅を0
.8n+mとし、金網(1)の上面にスラリー(S)を
塗布した。
The obtained slurry (S) is put into the hopper (5) of the slurry carrying device, and the wire mesh (1) and filter paper (6) are placed on the base (2).
i 5 cn+/mi with traction motor (3) along the top
Move at a speed of n, adjust the movable wall (4) by setting the width of the slurry output of the revolving tube (5) to Q,
9+++n+ binding, set the width of paint film repair slit 1-(9) to 0
.. 8n+m, and the slurry (S) was applied to the top surface of the wire mesh (1).

こうしてスラリー(S)を担持した金網(1)をスラリ
ー担持装置からはずしてスラリーを乾燥さけた後、金網
(1)から濾紙(6)を剥離し、ついで金網(1)を電
気炉に入れて炉内空気を水素で置換した後、水素気流中
で温度400℃で1時間、1000℃で12時間それぞ
れ保持し、スラリー(S)を焼成して多孔質化しlこ 
After removing the wire mesh (1) supporting the slurry (S) from the slurry supporting device to avoid drying the slurry, the filter paper (6) is peeled off from the wire mesh (1), and then the wire mesh (1) is placed in an electric furnace. After replacing the air in the furnace with hydrogen, the slurry (S) was held in a hydrogen stream at a temperature of 400°C for 1 hour and at 1000°C for 12 hours, and the slurry (S) was fired to make it porous.
.

こうして1qられた多孔質板よりなる電極は多孔度58
%おにび厚さQ、3mmのものであって、その断面の顕
微鏡写真による観察の結束、やはり片面のみに補強用金
網を有したものであった。
The electrode made of the porous plate thus prepared has a porosity of 58
% rice thickness Q was 3 mm, and the cross-section observed through a microscopic photograph showed that it also had a reinforcing wire mesh on only one side.

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

第1図おにび第3図は実施例1および2でそれぞれ用い
たスラリー担持装置を示す垂直縦断面図、第2図は実施
例1により得られた多孔質板の粒子構造を示す顕微鏡写
真(倍率60倍)である。 (1)・・・金網、(2)・・・基台、(3)・・・牽
引モーター、(4)・・・可動壁、(5)・・・ホッパ
ー、(6)・・・濾紙、(7)・・・スリット、(8)
・・・スラリー整形部材、(9)・・・スリツI〜、(
S)・・・スラリー。 以  」二
Figures 1 and 3 are vertical cross-sectional views showing the slurry supporting devices used in Examples 1 and 2, respectively, and Figure 2 is a micrograph showing the particle structure of the porous plate obtained in Example 1. (Magnification: 60 times). (1)...wire mesh, (2)...base, (3)...traction motor, (4)...movable wall, (5)...hopper, (6)...filter paper , (7)...slit, (8)
...Slurry shaping member, (9)...Suritsu I~, (
S)...Slurry. ``2''

Claims (6)

【特許請求の範囲】[Claims] (1)有機溶媒を含む混合溶媒に有機バインダーを溶解
し、得られたバインダー溶液と金属粉末を混練してスラ
リーとし、得られたスラリーを補強用金網の片面に塗布
して担持させ、担持スラリーを焼成して板状の多孔質体
とすることにより製造され、片面のみに金網を有した多
孔質板よりなることを特徴とする溶融炭酸塩燃料電池用
電極。
(1) Dissolve an organic binder in a mixed solvent containing an organic solvent, knead the obtained binder solution and metal powder to form a slurry, apply the obtained slurry to one side of a reinforcing wire mesh to support it, and make a supported slurry. 1. An electrode for a molten carbonate fuel cell, characterized in that the porous plate is manufactured by firing a porous body into a plate-like porous body, and has a wire mesh on only one side.
(2)混合溶媒として水と有機溶媒を所要割合で混合し
てなる溶媒を用いて、スラリーの乾燥速度を調節する、
特許請求の範囲第1項記載の電極。
(2) Adjusting the drying speed of the slurry by using a solvent made by mixing water and an organic solvent in a required ratio as a mixed solvent.
An electrode according to claim 1.
(3)有機バインダーとしてメチルセルロースを用いる
、特許請求の範囲第1または2項記載の電極。
(3) The electrode according to claim 1 or 2, wherein methylcellulose is used as the organic binder.
(4)金網の下面にシートを重ねて配し、金網の上面に
スラリーを塗布する、特許請求の範囲第1〜3項のうち
いずれか1項記載の電極。
(4) The electrode according to any one of claims 1 to 3, wherein sheets are stacked and arranged on the lower surface of the wire mesh, and the slurry is applied to the upper surface of the wire mesh.
(5)シートとして液吸収性のよいものを用いる、特許
請求の範囲第4項記載の電極。
(5) The electrode according to claim 4, wherein a sheet having good liquid absorption properties is used.
(6)焼成を還元雰囲気で行なう、特許請求の範囲第1
〜5項のうちいずれか1項記載の電極。
(6) Claim 1, in which the firing is performed in a reducing atmosphere.
The electrode according to any one of items 1 to 5.
JP60064290A 1985-03-27 1985-03-27 Electrode for molten carbonate fuel cell Pending JPS61224272A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60064290A JPS61224272A (en) 1985-03-27 1985-03-27 Electrode for molten carbonate fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60064290A JPS61224272A (en) 1985-03-27 1985-03-27 Electrode for molten carbonate fuel cell

Publications (1)

Publication Number Publication Date
JPS61224272A true JPS61224272A (en) 1986-10-04

Family

ID=13253954

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60064290A Pending JPS61224272A (en) 1985-03-27 1985-03-27 Electrode for molten carbonate fuel cell

Country Status (1)

Country Link
JP (1) JPS61224272A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012505510A (en) * 2008-12-30 2012-03-01 ドゥサン ヘヴィー インダストリーズ アンド コンストラクション カンパニー リミテッド Method for producing fuel electrode for in-situ sintering of molten carbonate fuel cell
CN114142046A (en) * 2021-11-22 2022-03-04 东睦新材料集团股份有限公司 Method for manufacturing metal support plate for fuel cell

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012505510A (en) * 2008-12-30 2012-03-01 ドゥサン ヘヴィー インダストリーズ アンド コンストラクション カンパニー リミテッド Method for producing fuel electrode for in-situ sintering of molten carbonate fuel cell
US8633122B2 (en) 2008-12-30 2014-01-21 Doosan Heavy Industries & Construction Co., Ltd. Method of manufacturing anode for in-situ sintering for molten carbonate fuel cell
CN114142046A (en) * 2021-11-22 2022-03-04 东睦新材料集团股份有限公司 Method for manufacturing metal support plate for fuel cell

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