JPH0656556A - Production of porous electrode - Google Patents
Production of porous electrodeInfo
- Publication number
- JPH0656556A JPH0656556A JP4209124A JP20912492A JPH0656556A JP H0656556 A JPH0656556 A JP H0656556A JP 4209124 A JP4209124 A JP 4209124A JP 20912492 A JP20912492 A JP 20912492A JP H0656556 A JPH0656556 A JP H0656556A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- raw material
- green sheet
- porous
- thickness direction
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 15
- 239000000835 fiber Substances 0.000 claims abstract description 25
- 239000002994 raw material Substances 0.000 claims abstract description 17
- 239000011230 binding agent Substances 0.000 claims abstract description 12
- 230000005686 electrostatic field Effects 0.000 claims abstract description 12
- 239000000843 powder Substances 0.000 claims abstract description 11
- 239000002904 solvent Substances 0.000 claims abstract description 7
- 229920000620 organic polymer Polymers 0.000 claims description 13
- 239000004020 conductor Substances 0.000 claims description 5
- 229920001778 nylon Polymers 0.000 abstract description 16
- 239000004677 Nylon Substances 0.000 abstract description 14
- 239000011148 porous material Substances 0.000 abstract description 12
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 abstract description 4
- 229910001928 zirconium oxide Inorganic materials 0.000 abstract description 4
- 239000007787 solid Substances 0.000 abstract description 3
- 229910000480 nickel oxide Inorganic materials 0.000 abstract description 2
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 abstract description 2
- 238000005868 electrolysis reaction Methods 0.000 abstract 1
- 229910052727 yttrium Inorganic materials 0.000 abstract 1
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 abstract 1
- 239000000446 fuel Substances 0.000 description 19
- 239000007789 gas Substances 0.000 description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000007784 solid electrolyte Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 229920005594 polymer fiber Polymers 0.000 description 5
- 238000010248 power generation Methods 0.000 description 5
- 238000010304 firing Methods 0.000 description 4
- 230000035699 permeability Effects 0.000 description 4
- 239000004014 plasticizer Substances 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 238000007606 doctor blade method Methods 0.000 description 3
- 229920002037 poly(vinyl butyral) polymer Polymers 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- BQENXCOZCUHKRE-UHFFFAOYSA-N [La+3].[La+3].[O-][Mn]([O-])=O.[O-][Mn]([O-])=O.[O-][Mn]([O-])=O Chemical compound [La+3].[La+3].[O-][Mn]([O-])=O.[O-][Mn]([O-])=O.[O-][Mn]([O-])=O BQENXCOZCUHKRE-UHFFFAOYSA-N 0.000 description 1
- 229910002113 barium titanate Inorganic materials 0.000 description 1
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
Classifications
-
- 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
- Conductive Materials (AREA)
- Inert Electrodes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、ガスセンサ、湿度セン
サ及び燃料電池等に用いられている多孔質電極の製造方
法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a porous electrode used in gas sensors, humidity sensors, fuel cells and the like.
【0002】[0002]
【従来の技術と課題】内部に気孔を有する多孔質電極
は、集電性能の他に、ガスを透過させる性能が要求され
る。この多孔質電極のガス透過性を向上させるために
は、電極内の気孔の配向方向を電極の厚み方向に揃えて
ガスの透過経路長を短くし、かつ、電極内の気孔のうち
閉気孔であるものの割合を少なくすればよい。2. Description of the Related Art A porous electrode having pores inside is required to have gas collection performance as well as gas permeation performance. In order to improve the gas permeability of this porous electrode, the gas permeation path length is shortened by aligning the orientation direction of the pores in the electrode with the thickness direction of the electrode, and the closed pores among the pores in the electrode are used. It is better to reduce the ratio of some.
【0003】しかし、従来の方法は、導電体粉末と、結
合剤と、有機溶剤と、多孔質にするための有機高分子と
からなる電極原料をセラミック基板に塗布し、焼き付け
るだけなので、作製された電極の気孔の配向方向及び閉
気孔の割合を少なくすることができなかった。そこで、
本発明の課題は、電極内の気孔の配向方向が電極の厚み
方向に揃い、かつ、閉気孔が殆どない多孔質電極を提供
することにある。However, according to the conventional method, an electrode raw material composed of a conductor powder, a binder, an organic solvent and an organic polymer for making it porous is applied to a ceramic substrate and baked, so that it is produced. It was not possible to reduce the orientation direction of pores of the electrode and the ratio of closed pores. Therefore,
An object of the present invention is to provide a porous electrode in which the orientation direction of the pores in the electrode is aligned with the thickness direction of the electrode and there are almost no closed pores.
【0004】[0004]
【課題を解決するための手段】以上の課題を解決するた
め、本発明に係る多孔質電極の製造方法は、(a)強誘
電体粉末と複合化して長さ方向に電気極性を有した有機
高分子繊維と、導電体粉末と、結合剤と、溶剤とを混合
して電極原料を作製する工程と、(b)前記電極原料に
静電場を印加して前記有機高分子繊維の配向方向を電極
の厚み方向に揃えた状態で、前記電極原料にて電極を成
形する工程と、(c)前記成形された電極を焼成して前
記有機高分子繊維を飛散させ、多孔質電極を作製する工
程と、を備えたことを特徴とする。In order to solve the above-mentioned problems, the method for producing a porous electrode according to the present invention comprises: (a) an organic compound which is compounded with a ferroelectric powder and has an electric polarity in the longitudinal direction. A step of preparing an electrode raw material by mixing a polymer fiber, a conductor powder, a binder, and a solvent; and (b) applying an electrostatic field to the electrode raw material to change the orientation direction of the organic polymer fiber. A step of forming an electrode with the electrode raw material in a state of being aligned in the thickness direction of the electrode; and (c) a step of firing the formed electrode to scatter the organic polymer fibers to produce a porous electrode. And are provided.
【0005】[0005]
【作用】以上の方法において、強誘電体粉末と複合化し
た有機高分子繊維は長さ方向に電気極性を有するものと
なる。この有機高分子繊維は電極原料に混ぜられた状態
では、その配向方向は無秩序にあらゆる方向に向いてい
る。この電極原料に静電場を印加すると、有機高分子繊
維は静電場の方向に配向する。従って、静電場を印加し
て、有機高分子繊維の配向方向を電極の厚み方向に揃
え、かつ、有機高分子繊維の長さを電極の厚みと略同じ
か若干長めの寸法にした場合、図2に示すように、高分
子繊維の両端部は成形された電極の表裏面に達する。そ
して、この成形された電極を焼成することにより、この
高分子繊維は飛散して高分子繊維跡に電極の厚み方向に
略配向している開気孔が形成されることになる。In the above method, the organic polymer fiber composited with the ferroelectric powder has an electric polarity in the length direction. When the organic polymer fibers are mixed with the electrode raw material, the orientation directions thereof are randomly oriented in all directions. When an electrostatic field is applied to this electrode raw material, the organic polymer fibers are oriented in the direction of the electrostatic field. Therefore, when an electrostatic field is applied so that the orientation direction of the organic polymer fibers is aligned with the thickness direction of the electrode, and the length of the organic polymer fibers is set to be approximately the same as or slightly longer than the thickness of the electrode, As shown in FIG. 2, both ends of the polymer fiber reach the front and back surfaces of the molded electrode. Then, by firing the formed electrode, the polymer fibers are scattered to form open pores in the traces of the polymer fibers which are substantially oriented in the thickness direction of the electrode.
【0006】[0006]
【実施例】以下、本発明に係る多孔質電極の製造方法の
一実施例を説明する。実施例として、固体電解質型燃料
電池の空気側電極及び燃料側電極の製造に適用した場合
について説明する。まず、燃料側電極のグリーンシート
製造方法について説明する。EXAMPLES An example of the method for producing a porous electrode according to the present invention will be described below. As an example, a case where the invention is applied to manufacture of an air side electrode and a fuel side electrode of a solid oxide fuel cell will be described. First, a method for manufacturing the green sheet for the fuel side electrode will be described.
【0007】図1は燃料側電極の原料2Aを示す組成図
である。ナイロン材料と強誘電体粉末であるチタン酸バ
リウムとを混ぜ、電場を射出方向に印加しながら射出成
形し、50μmの長さに裁断して、長さ方向に電気極性
を有するナイロン短繊維2cを作製する。次に、粉末状
のセラミックス材料である酸化ニッケルとイットリウム
安定化酸化ジルコニウムとを同重量ずつ混合して導電体
粉末2aとした後、前記ナイロン短繊維2cを所定量加
えて混合する。そして、得られた混合物100重量%に
対して、15重量%の結合剤(例えば、ポリビニルブチ
ラール系バインダ)、溶剤(エタノール、トルエン)及
び可塑剤等(これらをまとめて図中2bで表示する)を
適当量加えてスラリー(泥しょう)とする。この状態で
は、各ナイロン短繊維2cの配向方向は無秩序にあらゆ
る方向に向いている。FIG. 1 is a composition diagram showing a raw material 2A for the fuel side electrode. Nylon material and ferroelectric powder barium titanate are mixed, injection molded while applying an electric field in the injection direction, cut into 50 μm lengths, and nylon short fibers 2c having electrical polarity in the length direction are obtained. Create. Next, nickel oxide, which is a powdery ceramic material, and yttrium-stabilized zirconium oxide are mixed in equal weights to form a conductor powder 2a, and then a predetermined amount of the nylon short fibers 2c is added and mixed. Then, with respect to 100% by weight of the obtained mixture, 15% by weight of a binder (for example, polyvinyl butyral binder), a solvent (ethanol, toluene), a plasticizer, etc. (these are collectively indicated by 2b in the figure) Add an appropriate amount to make a slurry. In this state, the nylon short fibers 2c are randomly oriented in all directions.
【0008】次に、図2に示すように、このスラリー状
の原料2AにX方向の静電場を印加しながら、ドクター
ブレード法によって厚み40μmの燃料側電極のグリー
ンシート2Bを作製した。このとき、グリーンシート2
Bは静電場に対して、その厚み方向が平行な状態で作製
される。従って、グリーンシート2Bに含まれている各
ナイロン短繊維2cは、グリーンシート2Bの厚み方向
に略配向している。しかも、ナイロン短繊維2cの長さ
寸法はグリーンシート2Bの厚み寸法より若干長いの
で、ナイロン短繊維2cの両端部はグリーンシート2B
の表裏面に達している。Next, as shown in FIG. 2, while applying an electrostatic field in the X direction to the slurry-like raw material 2A, a 40 μm thick fuel-side electrode green sheet 2B was prepared by the doctor blade method. At this time, green sheet 2
B is manufactured in a state where its thickness direction is parallel to the electrostatic field. Therefore, each nylon short fiber 2c included in the green sheet 2B is substantially oriented in the thickness direction of the green sheet 2B. Moreover, since the length of the nylon short fiber 2c is slightly longer than the thickness of the green sheet 2B, both ends of the nylon short fiber 2c are green sheet 2B.
Has reached the front and back.
【0009】次に、空気側電極のグリーンシート製造方
法について説明する。燃料側電極のグリーンシート製造
方法と同様に、粉末状のランタンマンガナイトに前記ナ
イロン短繊維を所定量加えて混合する。そして、得られ
た混合物100重量%に対して15重量%の結合剤(例
えば、ポリビニルブチラール系バインダ)及び溶剤(エ
タノール、トルエン)、可塑剤等を適当量加えてスラリ
ー状の空気側電極の原料とする。この状態では、各ナイ
ロン短繊維の配向方向は無秩序にあらゆる方向に向いて
いる。このスラリー状の原料に静電場を印加しながら、
ドクターブレード法によって厚み40μmの空気側電極
のグリーンシートを作製した。このとき、グリーンシー
トは静電場に対して、その厚み方向が平行な状態で作製
される。従って、グリーンシートに含まれている各ナイ
ロン短繊維はグリーンシートの厚み方向に略配向してい
る。Next, a method of manufacturing the green sheet for the air side electrode will be described. Similar to the method for producing the green sheet for the fuel side electrode, a predetermined amount of the above nylon short fibers is added to and mixed with powdered lanthanum manganite. Then, an appropriate amount of a binder (for example, polyvinyl butyral binder), a solvent (ethanol, toluene), a plasticizer, etc., of 15% by weight with respect to 100% by weight of the obtained mixture is added, and a raw material for an air-side electrode in a slurry state. And In this state, the orientation directions of the respective nylon short fibers are randomly oriented in all directions. While applying an electrostatic field to this slurry-like raw material,
A 40 μm thick air side electrode green sheet was prepared by the doctor blade method. At this time, the green sheet is produced with its thickness direction parallel to the electrostatic field. Therefore, each nylon short fiber contained in the green sheet is substantially oriented in the thickness direction of the green sheet.
【0010】さらに、固体電解質となるイットリウム安
定化酸化ジルコニウムのグリーンシートを作製した。す
なわち、粉末状のイットリウム安定化酸化ジルコニウム
100重量%に対して15重量%の結合剤(例えばポリ
ビニルブチラール系バインダ)及び溶剤(エタノール、
トルエン)、可塑剤等を適当量加えてスラリー化し、ド
クターブレード法によって、このスラリーから固体電解
質グリーンシートを作製した。Further, a green sheet of yttrium-stabilized zirconium oxide as a solid electrolyte was prepared. That is, 15 wt% of a binder (for example, polyvinyl butyral binder) and a solvent (ethanol, 15 wt% to 100 wt% of powdery yttrium-stabilized zirconium oxide).
Toluene), a plasticizer, etc. were added in appropriate amounts to form a slurry, and a solid electrolyte green sheet was produced from this slurry by the doctor blade method.
【0011】作製された固体電解質グリーンシートを適
当枚数重ねたものに、燃料側電極のグリーンシートと空
気側電極のグリーンシートをそれぞれ上下から重ねて圧
着し、所定の大きさに裁断して成形体を得た。この成形
体を400℃の温度下で3時間にわたって加熱して結合
剤を飛散させた後、毎分1℃の速度で1300℃まで昇
温し、この温度下で2時間焼成した。この焼成によっ
て、ナイロン短繊維は飛散して、ナイロン短繊維跡に成
形体の厚み方向に略配向している開気孔が形成されるこ
ととなる。この後、室温まで冷却することによって、多
孔質電極である燃料側電極2と空気側電極3を表裏面に
設けた固体電解質1を得た(図3参照)。A green sheet for the fuel side electrode and a green sheet for the air side electrode are respectively stacked from above and below on a stack of an appropriate number of the produced solid electrolyte green sheets, and the sheets are cut into a predetermined size to form a molded body. Got The molded body was heated at a temperature of 400 ° C. for 3 hours to scatter the binder, then heated to 1300 ° C. at a rate of 1 ° C./min, and baked at this temperature for 2 hours. By this firing, the short nylon fibers are scattered, and open pores that are substantially oriented in the thickness direction of the molded body are formed in the traces of the short nylon fibers. Then, by cooling to room temperature, a solid electrolyte 1 having a fuel side electrode 2 and an air side electrode 3 which are porous electrodes provided on the front and back surfaces was obtained (see FIG. 3).
【0012】こうして得られた2種類の実施例品1,2
を気孔率及び発電能力について評価した。評価結果を表
1に示す。比較のために、グリーンシート作製時に静電
場を印加しないということ以外は、前記製造方法と同様
の方法で作製した従来品1,2の評価結果も合わせて示
す。Two types of example products 1 and 2 thus obtained
Was evaluated for porosity and power generation capacity. The evaluation results are shown in Table 1. For comparison, the evaluation results of the conventional products 1 and 2 produced by the same method as the above-described production method are also shown except that the electrostatic field is not applied during the production of the green sheet.
【0013】[0013]
【表1】 [Table 1]
【0014】電極2,3の気孔率は、電極断面のSEM
写真を撮り、その写真を画像解析することにより算出し
た。また、図4に示すように、電極2,3にそれぞれ燃
料ガス供給管7a,空気供給管7bを取り付けて燃料電
池を作製した。この燃料電池を測定回路19に接続し、
発電能力を測定した。すなわち、燃料電池を1000℃
の温度に保持しながら、燃料ガスと空気をそれぞれ電極
2,3に供給し、固体電解質1を介して電極反応を起こ
させ、かつ、電流計11にて観察しながら単位電極面積
当たり0.3A/cm2の電流が流れる状態下の燃料電
池に発生する電圧値を電圧計10で測定した。なお、8
a,8bは白金線、9は可変抵抗器である。この発電能
力の値が大きいほど電極のガス透過性が優れ、かつ、電
池としての性能も優れていることになる。表1は、実施
例品1,2が従来例品1,2より大きな発電能力を有し
ていることが示されている。The porosities of the electrodes 2 and 3 are determined by the SEM of the electrode cross section.
It was calculated by taking a picture and analyzing the picture. Further, as shown in FIG. 4, a fuel gas supply pipe 7a and an air supply pipe 7b were attached to the electrodes 2 and 3, respectively, to fabricate a fuel cell. Connect this fuel cell to the measuring circuit 19,
The power generation capacity was measured. That is, the fuel cell at 1000 ° C
Fuel gas and air are supplied to the electrodes 2 and 3, respectively, while maintaining the temperature of 3 A to cause an electrode reaction through the solid electrolyte 1, and 0.3 A per unit electrode area while observing with an ammeter 11. The voltage value generated in the fuel cell under the condition that a current of / cm 2 flows was measured by the voltmeter 10. 8
Reference numerals a and 8b are platinum wires, and 9 is a variable resistor. The larger the value of this power generation capacity, the better the gas permeability of the electrode and the better the performance as a battery. Table 1 shows that the example products 1 and 2 have a larger power generation capacity than the conventional example products 1 and 2.
【0015】以上のことから、実施例品1,2の方が電
極2,3のガス透過性に優れていることがわかる。な
お、本発明に係る多孔質電極の製造方法は前記実施例に
限定するものではなく、その要旨の範囲内で種々に変形
することができる。特に、前記実施例では固体電解質型
燃料電池の燃料側電極及び空気側電極に適用した場合を
説明したが、これ以外、例えばガスセンサや湿度センサ
の多孔質電極に適用してもよい。From the above, it can be seen that the products of Examples 1 and 2 are superior in gas permeability of the electrodes 2 and 3. The method for manufacturing the porous electrode according to the present invention is not limited to the above-mentioned embodiment, but can be variously modified within the scope of the gist. In particular, in the above-mentioned embodiment, the case where it is applied to the fuel side electrode and the air side electrode of the solid oxide fuel cell has been described, but other than this, it may be applied to, for example, a porous electrode of a gas sensor or a humidity sensor.
【0016】[0016]
【発明の効果】以上の説明で明らかなように、本発明に
よれば、静電場の印加によって、電極の厚み方向に揃え
られ有機高分子繊維を、焼成の際に飛散させて高分子繊
維跡に電極の厚み方向に略配向している開気孔を形成す
ることができる。従って、電極のガス透過性を従来より
アップさせることができ、かつ、集電性にも優れた多孔
質電極を得ることができる。As is apparent from the above description, according to the present invention, the organic polymer fibers aligned in the thickness direction of the electrode due to the application of the electrostatic field are scattered during firing to leave traces of the polymer fibers. It is possible to form open pores that are substantially oriented in the thickness direction of the electrode. Therefore, the gas permeability of the electrode can be improved as compared with the conventional one, and a porous electrode excellent in current collecting property can be obtained.
【0017】この結果、ガスセンサ、湿度センサ及び燃
料電池等の性能を向上させることが可能になる。As a result, it becomes possible to improve the performance of the gas sensor, the humidity sensor, the fuel cell and the like.
【図1】本発明に係る多孔質電極の製造方法の一実施例
を示す製造手順を説明するための組成図。FIG. 1 is a composition diagram for explaining a manufacturing procedure showing an embodiment of a method for manufacturing a porous electrode according to the present invention.
【図2】図1に続く製造手順を説明するための組成図。FIG. 2 is a composition diagram for explaining a manufacturing procedure subsequent to FIG.
【図3】図1に示した多孔質電極を表裏面に設けた固体
電解質の構造図。FIG. 3 is a structural diagram of a solid electrolyte in which the porous electrodes shown in FIG. 1 are provided on the front and back surfaces.
【図4】図1に示した多孔質電極を備えた燃料電池の発
電能力を測定するための測定回路を示す電気回路図。FIG. 4 is an electric circuit diagram showing a measuring circuit for measuring the power generation capacity of the fuel cell provided with the porous electrode shown in FIG.
2…燃料側電極 2A…燃料側電極原料 2B…燃料側電極グリーンシート 2a…導電体粉末 2b…結合剤、溶剤及び可塑剤等 2c…ナイロン短繊維(有機高分子繊維) 2 ... Fuel side electrode 2A ... Fuel side electrode raw material 2B ... Fuel side electrode green sheet 2a ... Conductor powder 2b ... Binder, solvent, plasticizer, etc. 2c ... Nylon short fiber (organic polymer fiber)
Claims (1)
気極性を有した有機高分子繊維と、導電体粉末と、結合
剤と、溶剤とを混合して電極原料を作製する工程と、 前記電極原料に静電場を印加して前記有機高分子繊維の
配向方向を電極の厚み方向に揃えた状態で、前記電極原
料にて電極を成形する工程と、 前記成形された電極を焼成して前記有機高分子繊維を飛
散させ、多孔質電極を作製する工程と、 を備えたことを特徴とする多孔質電極の製造方法。1. A step of preparing an electrode raw material by mixing an organic polymer fiber composited with a ferroelectric powder and having electric polarity in the length direction, a conductor powder, a binder, and a solvent. The step of forming an electrode with the electrode raw material in a state where the orientation direction of the organic polymer fibers is aligned with the thickness direction of the electrode by applying an electrostatic field to the electrode raw material, and the formed electrode is fired. And a step of scattering the organic polymer fibers to produce a porous electrode, the method for producing a porous electrode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4209124A JPH0656556A (en) | 1992-08-05 | 1992-08-05 | Production of porous electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4209124A JPH0656556A (en) | 1992-08-05 | 1992-08-05 | Production of porous electrode |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0656556A true JPH0656556A (en) | 1994-03-01 |
Family
ID=16567687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4209124A Pending JPH0656556A (en) | 1992-08-05 | 1992-08-05 | Production of porous electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0656556A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10189012A (en) * | 1996-12-20 | 1998-07-21 | Toyota Motor Corp | Electrode and power generation layer for fuel cell and method for producing the same |
| JP2007250337A (en) * | 2006-03-15 | 2007-09-27 | Toppan Printing Co Ltd | Electrode catalyst layer for solid polymer electrolyte fuel cell, method for producing the same, and solid polymer electrolyte fuel cell |
| US9322457B2 (en) | 2012-02-22 | 2016-04-26 | Mitsubishi Heavy Industries Compressor Corporation | Turning device and rotating machine |
| JP2019519904A (en) * | 2016-07-25 | 2019-07-11 | ロベルト・ボッシュ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツングRobert Bosch Gmbh | Method of manufacturing current collector for fuel cell and fuel cell |
-
1992
- 1992-08-05 JP JP4209124A patent/JPH0656556A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10189012A (en) * | 1996-12-20 | 1998-07-21 | Toyota Motor Corp | Electrode and power generation layer for fuel cell and method for producing the same |
| JP2007250337A (en) * | 2006-03-15 | 2007-09-27 | Toppan Printing Co Ltd | Electrode catalyst layer for solid polymer electrolyte fuel cell, method for producing the same, and solid polymer electrolyte fuel cell |
| US9322457B2 (en) | 2012-02-22 | 2016-04-26 | Mitsubishi Heavy Industries Compressor Corporation | Turning device and rotating machine |
| JP2019519904A (en) * | 2016-07-25 | 2019-07-11 | ロベルト・ボッシュ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツングRobert Bosch Gmbh | Method of manufacturing current collector for fuel cell and fuel cell |
| US10862137B2 (en) | 2016-07-25 | 2020-12-08 | Robert Bosch Gmbh | Method for producing a current collector for a fuel cell, and fuel cell |
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