JP3430166B2 - Porous conductive plate - Google Patents
Porous conductive plateInfo
- Publication number
- JP3430166B2 JP3430166B2 JP2001295651A JP2001295651A JP3430166B2 JP 3430166 B2 JP3430166 B2 JP 3430166B2 JP 2001295651 A JP2001295651 A JP 2001295651A JP 2001295651 A JP2001295651 A JP 2001295651A JP 3430166 B2 JP3430166 B2 JP 3430166B2
- Authority
- JP
- Japan
- Prior art keywords
- porous conductive
- conductive plate
- titanium
- porosity
- gas atomized
- 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 - Fee Related
Links
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 53
- 239000002245 particle Substances 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 239000000446 fuel Substances 0.000 claims description 10
- 229920000642 polymer Polymers 0.000 claims description 10
- 239000007787 solid Substances 0.000 claims description 10
- 239000004020 conductor Substances 0.000 claims 1
- 239000007789 gas Substances 0.000 description 28
- 238000005245 sintering Methods 0.000 description 27
- 239000010936 titanium Substances 0.000 description 22
- 229910052719 titanium Inorganic materials 0.000 description 22
- 239000012528 membrane Substances 0.000 description 16
- 239000000835 fiber Substances 0.000 description 10
- 238000011049 filling Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- 239000000843 powder Substances 0.000 description 8
- 239000011362 coarse particle Substances 0.000 description 6
- 239000010419 fine particle Substances 0.000 description 6
- 238000005868 electrolysis reaction Methods 0.000 description 5
- 230000035699 permeability Effects 0.000 description 4
- 238000007750 plasma spraying Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000005518 polymer electrolyte Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 229910001069 Ti alloy Inorganic materials 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000013065 commercial product Substances 0.000 description 2
- 238000009689 gas atomisation Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000007606 doctor blade method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 150000003608 titanium Chemical class 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
- Fuel Cell (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Powder Metallurgy (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、固体高分子型水電
解槽における給電体又は固体高分子型燃料電池における
集電体として使用される多孔質導電板に関し、特に、チ
タン焼結体からなる多孔質導電板に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a porous conductive plate used as a power supply in a solid polymer water electrolyzer or as a current collector in a solid polymer fuel cell, and more particularly, it is composed of a titanium sintered body. The present invention relates to a porous conductive plate.
【0002】[0002]
【従来の技術】高分子電解質膜を用いて水素及び酸素を
製造する水電解セルは、いわゆるフィルタープレス型に
構成されている。具体的に説明すると、高分子電解質膜
の両面に触媒層を接合して構成された膜電極接合体の両
面側に給電体を配置してユニットを構成し、このユニッ
トを多数積層して、その両端側に電極を設けた構成が一
般に採用されている。2. Description of the Related Art A water electrolysis cell for producing hydrogen and oxygen using a polymer electrolyte membrane is of a so-called filter press type. Specifically, a unit is formed by disposing a power supply member on both sides of a membrane electrode assembly formed by joining catalyst layers on both sides of a polymer electrolyte membrane, and laminating a large number of these units. A configuration in which electrodes are provided on both end sides is generally adopted.
【0003】ここにおける給電体は、多孔質の導電板か
らなり、隣接する膜電極接合体に密に接して配置され
る。給電体として多孔質の導電板を使用するのは、電流
を通す必要があること、水電解反応のために水を供給す
る必要があること、水電解反応で生じたガスを速やかに
排出する必要があることなどによる。The power feeder here is made of a porous conductive plate and is arranged in close contact with an adjacent membrane electrode assembly. The use of a porous conductive plate as a power supply means that it is necessary to pass an electric current, it is necessary to supply water for the water electrolysis reaction, and it is necessary to quickly discharge the gas generated by the water electrolysis reaction. It depends on
【0004】また、高分子電解質膜を用いた燃料電池の
構造も水電解槽のそれと全く同じであり、膜電極接合体
の両面側には多孔質の導電板が配置されている。燃料電
池の場合は、水素を燃料として電力を得ることから、こ
の多孔質導電板は集電板と呼ばれている。The structure of the fuel cell using the polymer electrolyte membrane is exactly the same as that of the water electrolysis cell, and porous conductive plates are arranged on both sides of the membrane electrode assembly. In the case of a fuel cell, since hydrogen is used as fuel to obtain electric power, this porous conductive plate is called a current collector plate.
【0005】このような固体高分子型水電解槽における
給電体又は固体高分子型燃料電池における集電体として
使用される多孔質導電板に関しては、酸化性雰囲気で使
用できる特性も必要なため、カーボンと共にチタン材が
検討されており、チタン材のなかでも特に焼結体が、表
面が平滑で、隣接する膜電極接合体を損傷させ難いこと
や適正な空隙率を得やすいことなどから注目されてい
る。As for the porous conductive plate used as a power supply in such a solid polymer type water electrolyzer or as a current collector in a solid polymer type fuel cell, it is necessary to have a characteristic that it can be used in an oxidizing atmosphere. Titanium materials have been studied together with carbon.Among the titanium materials, especially the sintered body has a smooth surface, and it attracts attention because it is difficult to damage the adjacent membrane electrode assembly and it is easy to obtain an appropriate porosity. ing.
【0006】そして、チタン焼結体からなる多孔質導電
板としては、スポンジチタンの破砕粉末やスポンジチタ
ンを水素化脱水素により粉砕して製造された粉末を焼結
したチタン粉末焼結板と、チタン繊維を圧縮成形して焼
結したチタン繊維焼結板とがあり、チタン繊維焼結板の
表面に更に金属チタンのプラズマ溶射層を形成したもの
も、特開平11−302891号公報により提示されて
いる。As the porous conductive plate made of a titanium sintered body, a crushed powder of titanium sponge or a titanium powder sintered plate obtained by sintering powder produced by pulverizing sponge titanium by hydrodehydrogenation, Japanese Patent Laid-Open No. 11-302891 discloses a titanium fiber sintered plate obtained by compression-molding and sintering titanium fibers, and a titanium fiber sintered plate on which a plasma sprayed layer of titanium metal is further formed. ing.
【0007】[0007]
【発明が解決しようとする課題】しかしながら、これら
の従来のチタン焼結体からなる多孔質導電板には、次の
ような問題がある。However, the conventional porous conductive plates made of these titanium sintered bodies have the following problems.
【0008】チタン粉末焼結体は、表面が平滑で、隣接
する膜電極接合体を損傷させない利点があるものの、プ
レス成形性が悪く、割れやすいため、薄型で大面積のも
のを製造できないという致命的な制約がある。一方、チ
タン繊維焼結板は、成形性が良好で、薄型で大面積のも
のを製造できるが、表面に鋭角の起伏があり、繊維間の
間隔も大きい。このため、隣接する膜電極接合体に圧接
した場合に膜電極接合体を損傷させる危険性が高い。ま
た、膜電極接合体との接触抵抗が増加する問題がある。Although the titanium powder sintered body has the advantage that the surface is smooth and does not damage the adjacent membrane electrode assembly, it has poor press formability and is easily cracked, so that it is fatal that a thin product having a large area cannot be manufactured. There are some restrictions. On the other hand, the titanium fiber sintered plate has good formability and can be manufactured thin and having a large area, but has a sharp undulation on the surface and a large fiber interval. Therefore, there is a high risk of damaging the membrane electrode assembly when it is pressed against the adjacent membrane electrode assembly. In addition, there is a problem that the contact resistance with the membrane electrode assembly increases.
【0009】これらに対し、特開平11−302891
号公報により提示されたチタン繊維焼結板は、チタン繊
維焼結板の表面に金属チタンのプラズマ溶射層を形成す
ることにより、チタン繊維焼結板で問題となる表面の鋭
角の起伏や大きな繊維間隔を解消したものであり、成形
性及び膜電極接合体との接触性の両方に共に優れたもの
と言える。In contrast to these, Japanese Patent Laid-Open No. 11-302891
The titanium fiber sintered plate disclosed in Japanese Patent Laid-Open Publication No. 2003-242242 has a plasma sprayed layer of titanium metal formed on the surface of the titanium fiber sintered plate. Since the gap is eliminated, it can be said that the moldability and the contact with the membrane electrode assembly are both excellent.
【0010】しかし、プラズマ溶射に余分のコストがか
かる上に、チタン繊維焼結板とその表面のプラズマ溶射
層とでは、空隙率及びチタン材の形状が異なるため、両
者の接合界面で電気抵抗が増大し、多孔質導電板として
の電気抵抗が見掛けの空隙率以上に高くなる。その結
果、例えば1〜3A/cm2 の高電流密度で用いる水電
解セルにおいては、大きな損失電圧を生じることにな
る。また、このような損失電圧が燃料電池でも容易に許
されるはずのないことは言うまでもない。However, in addition to the extra cost of plasma spraying, the titanium fiber sintered plate and the plasma sprayed layer on the surface thereof have different porosities and shapes of the titanium material, so that the electrical resistance is increased at the joint interface between them. As a result, the electric resistance of the porous conductive plate becomes higher than the apparent porosity. As a result, a large loss voltage is generated in a water electrolysis cell used at a high current density of, for example, 1 to 3 A / cm 2 . Further, it goes without saying that such a loss voltage cannot be easily allowed even in a fuel cell.
【0011】更に、接合界面での空隙率の大きな変化
は、通液性や通気性にも悪影響を及ぼすことが懸念され
る。Further, it is feared that a large change in the porosity at the bonding interface may adversely affect the liquid permeability and the air permeability.
【0012】本発明の目的は、成形性に優れるのは勿論
のこと、プラズマ溶射のようなコーティングを行わずと
も、表面の平滑性に優れ、更には製造が容易で経済性に
も優れる多孔質導電板を提供することにある。The object of the present invention is not only excellent in moldability, but also excellent in surface smoothness without coating such as plasma spraying, and moreover, it is easy to manufacture and is excellent in economical efficiency. To provide a conductive plate.
【0013】[0013]
【課題を解決するための手段】上記目的を達成するため
に、本発明者らは、球状ガスアトマイズチタン粉末に注
目した。球状ガスアトマイズチタン粉末とは、ガスアト
マイズ法により製造されたチタン又はチタン合金の粉末
であり、個々の粒子は、チタン又はチタン合金の溶融飛
沫が飛散中に凝固してできたものであるから、表面が滑
らかな球形をしている。また、粒径は例えば平均で10
0μm以下と非常に微細にできる。In order to achieve the above object, the present inventors have paid attention to spherical gas atomized titanium powder. Spherical gas atomized titanium powder is a powder of titanium or titanium alloy produced by the gas atomization method, the individual particles, since the molten droplets of titanium or titanium alloy is solidified during scattering, the surface is It has a smooth spherical shape. The particle size is, for example, 10 on average.
It can be made extremely fine with 0 μm or less.
【0014】ちなみに、スポンジチタンの破砕や水素化
脱水素により製造されたチタン粉末の粒子形状は不定形
である。また、球状チタン粉末は回転電極法によっても
製造可能であるが、得られる平均粒度は一般に400μ
m以上である。By the way, the particle shape of titanium powder produced by crushing titanium sponge or hydrodehydrogenation is irregular. Spherical titanium powder can also be produced by the rotating electrode method, but the average particle size obtained is generally 400 μm.
It is m or more.
【0015】本発明者らは、このような特徴を有する球
状ガスアトマイズチタン粉末を用いて、固体高分子型水
電解槽における給電体や固体高分子型燃料電池における
集電体を想定した焼結板を試験的に製造し、その特性等
を評価した。その結果、以下のことが明らかになった。The present inventors have made use of the spherical gas atomized titanium powder having the above-mentioned characteristics to assume a sintered plate for a power supply in a solid polymer type water electrolyzer and a current collector in a solid polymer type fuel cell. Was experimentally manufactured, and its characteristics and the like were evaluated. As a result, the following was revealed.
【0016】球状ガスアトマイズチタン粉末は流動性に
優れ、焼結容器内に投入すると、加圧なしでも十分な密
度に充填される。そして、これを焼結すると、薄型大
面積の場合も十分な機械的強度が確保される。給電体
や集電体として好ましい空隙率が、格別の操作なしで簡
単に得られる。表面は平滑性が高く、プラズマ溶射等
によるコーティングを行うわずとも、隣接する膜電極接
合体に密着し且つ膜電極接合体を損傷させるおそれがな
い。従って、接合界面での抵抗増大による損失電圧も、
また通液性や通気性への悪影響も回避される。The spherical gas atomized titanium powder has excellent fluidity, and when it is placed in a sintering container, it is filled to a sufficient density without applying pressure. Then, when this is sintered, sufficient mechanical strength is secured even in the case of a thin and large area. The porosity preferable as the power supply and the current collector can be easily obtained without any special operation. The surface has high smoothness, and even if it is not coated by plasma spraying or the like, there is no possibility of adhering to an adjacent membrane electrode assembly and damaging the membrane electrode assembly. Therefore, the loss voltage due to the increased resistance at the junction interface is also
Also, adverse effects on liquid permeability and air permeability are avoided.
【0017】即ち、球状ガスアトマイズチタン粉末を用
いた焼結体は、製造過程で加圧さえも行わず、また製造
後に表面コートを行わずとも、固体高分子型水電解槽に
おける給電体又は固体高分子型燃料電池における集電体
として、性能及び経済性の両面から極めて優れた適性を
示すものとなる。That is, the sintered body using the spherical gas atomized titanium powder does not even have to be pressurized in the manufacturing process and is not surface-coated after the manufacturing process. As a current collector in a molecular fuel cell, it exhibits extremely excellent suitability in terms of both performance and economy.
【0018】本発明の多孔質導電板は、かかる知見に基
づいて開発されたもので、固体高分子型水電解槽におけ
る給電体又は固体高分子型燃料電池における集電体とし
て使用される多孔質導電板であって、球状ガスアトマイ
ズチタン粉末の焼結体から構成されるものである。The porous conductive plate of the present invention was developed on the basis of such findings, and is a porous material used as a power supply in a solid polymer type water electrolyzer or a current collector in a solid polymer type fuel cell. The conductive plate is composed of a sintered body of spherical gas atomized titanium powder.
【0019】球状ガスアトマイズチタン粉末としては、
例えば粒径範囲によって区分された次の3種類が市販さ
れている。即ち、45μm以下の細粒、45〜150μ
mの粗粒、更に粗い150μm以上の3種類であり、平
均粒径は細粒で約25μm、粗粒で約80μmである。As the spherical gas atomized titanium powder,
For example, the following three types classified according to the particle size range are commercially available. That is, fine particles of 45 μm or less, 45 to 150 μm
There are three types of coarse particles of m and 150 μm or more, which are coarser.
【0020】本発明の多孔質導電板に使用される球状ガ
スアトマイズチタン粉末の粒径は、特に限定せず、上述
の市販品レベルで何ら問題はないが、ガスアトマイズ法
と言えども極端な細粒を歩留りよく工業的に生産するこ
とは困難である。また、粗粒の場合は、薄型の多孔質体
を製造した場合に多孔質体の厚みに対するチタン粉末間
の接触点数が少なくなるために強度不足が懸念される。
よって、粒径は平均で10〜150μmが好ましい。The particle size of the spherical gas atomized titanium powder used in the porous conductive plate of the present invention is not particularly limited, and there is no problem at the level of the above-mentioned commercial products, but even in the gas atomization method, extremely fine particles can be obtained. It is difficult to industrially produce with high yield. Further, in the case of coarse particles, when a thin porous body is manufactured, the number of contact points between titanium powders with respect to the thickness of the porous body is reduced, so that there is a fear of insufficient strength.
Therefore, the average particle size is preferably 10 to 150 μm.
【0021】多孔質導電板の空隙率については、球状ガ
スアトマイズチタン粉末として市販品を使用し、且つ充
填時や焼結時に加圧を行わずとも、35〜55%の空隙
率が得られる。本発明者らによる調査によれば、この空
隙率は、チタン粉末焼結体からなる多孔質導電板では電
気的・機械的特性等の面から好ましいものである。な
お、充填時や焼結時に加圧を行ったり、焼結条件の選択
によっては、空隙率を35%以下に調整することも可能
である。Regarding the porosity of the porous conductive plate, a commercially available spherical gas atomized titanium powder is used, and a porosity of 35 to 55% can be obtained without applying pressure during filling or sintering. According to the investigation by the present inventors, this porosity is preferable in terms of electrical / mechanical characteristics in the porous conductive plate made of a titanium powder sintered body. It should be noted that it is also possible to apply pressure during filling or sintering, or adjust the porosity to 35% or less depending on the selection of sintering conditions.
【0022】この空隙率は、焼結温度の調節、粒径の選
択、加圧等により制御可能である。一般的な傾向とし
て、焼結温度が高くなると、接触面積が増大することか
ら、空隙率が低下する。同様に、粒径が小さくなった場
合も、接触面積が増大することから、空隙率が低下する
傾向となる。また、充填時や焼結時に加圧を行えば、空
隙率は低下する。また、多孔質導電板の板厚に対して粒
径が大きくなると、空隙率が増大する傾向となる。これ
らの組み合わせにより、空隙率は比較的広い範囲で任意
に制御される。なお、空隙率の極端な低減や増大は、反
応における水やガスの受給効率の悪化や多孔質導電板の
強度不足の原因になる。The porosity can be controlled by adjusting the sintering temperature, selecting the particle size, pressurizing, and the like. As a general tendency, as the sintering temperature increases, the contact area increases, and the porosity decreases. Similarly, when the particle size is small, the contact area increases, and the porosity tends to decrease. If pressure is applied during filling or sintering, the porosity will decrease. Further, when the particle diameter becomes large relative to the plate thickness of the porous conductive plate, the porosity tends to increase. With these combinations, the porosity is arbitrarily controlled within a relatively wide range. It should be noted that the extreme reduction or increase in the porosity causes deterioration in the efficiency of receiving water or gas in the reaction and insufficient strength of the porous conductive plate.
【0023】多孔質導電板の寸法は、製造される給電体
や集電体の寸法に応じて適宜選択される。The size of the porous conductive plate is appropriately selected according to the sizes of the power supply body and the current collector to be manufactured.
【0024】[0024]
【発明の実施の形態】以下、図面を参照して本発明の実
施形態を説明する。図1〜図3は球状ガスアトマイズ粉
末の充填形態を示す断面図である。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. 1 to 3 are cross-sectional views showing a filling form of spherical gas atomized powder.
【0025】まず、図1に示すように、所定粒径の球状
ガスアトマイズチタン粉末1を高密度アルミナ製の焼結
容器2に無加圧で充填する。焼結容器2の内形は、製造
すべき多孔質導電板の形状に対応する薄板形状である。
次いで、焼結容器2内に充填された球状ガスアトマイズ
チタン粉末1を無加圧で真空焼結する。First, as shown in FIG. 1, a spherical gas atomized titanium powder 1 having a predetermined particle size is filled in a sintering container 2 made of high density alumina without pressure. The inner shape of the sintering container 2 is a thin plate shape corresponding to the shape of the porous conductive plate to be manufactured.
Next, the spherical gas atomized titanium powder 1 filled in the sintering container 2 is vacuum-sintered without pressure.
【0026】焼結温度は、チタンの融点よりはるかに低
い850〜1200℃が好ましい。焼結温度が850℃
未満の場合は、十分な焼結が行われない。1200℃を
超えると、無加圧の場合でも、焼結部分が個々の粒子同
士の接触部にとどまらず、粒子同士が溶け合うため、適
正な空隙率を確保できなくなるおそれがある。The sintering temperature is preferably 850 to 1200 ° C., which is much lower than the melting point of titanium. Sintering temperature is 850 ℃
If it is less than, sufficient sintering is not performed. If the temperature exceeds 1200 ° C., even if no pressure is applied, the sintered portion is not limited to the contact portion between the individual particles and the particles are fused to each other, so that it may not be possible to ensure an appropriate porosity.
【0027】このような方法で50mm角×1mm厚、
0.5mm厚、0.2mm厚の寸法をもつ3種類の多孔
質導電板を、本発明の実施例として製造した。With such a method, 50 mm square × 1 mm thick,
Three types of porous conductive plates having dimensions of 0.5 mm thickness and 0.2 mm thickness were manufactured as examples of the present invention.
【0028】球状ガスアトマイズチタン粉末は、前述し
た市販品で、1mm厚及び0.5mm厚のものでは粗粒
(45〜150μm)を使用し、0.2mm厚のもので
は細粒(45μm以下)を使用した。真空焼結での真空
度は7×10-3Pa、焼結温度は粗粒に対しては約10
00℃、細粒に対しては約900℃とした。また、温度
保持時間は、粗粒、細粒とも約15分間とした。製造さ
れた多孔質導電板の空隙率はいずれも約45%であっ
た。The spherical gas atomized titanium powder is the above-mentioned commercial product, and coarse particles (45 to 150 μm) are used for 1 mm thickness and 0.5 mm thickness, and fine particles (45 μm or less) for 0.2 mm thickness. used. The degree of vacuum in vacuum sintering is 7 × 10 −3 Pa, and the sintering temperature is about 10 for coarse particles.
The temperature was set to 00 ° C and to 900 ° C for fine particles. The temperature holding time was about 15 minutes for both coarse particles and fine particles. The porosity of each manufactured porous conductive plate was about 45%.
【0029】製造された多孔質導電板の電気抵抗を4端
子法で測定したところ、1mm厚のもので10mΩ、
0.5mm厚のもので15mΩとなり、0.2mm厚の
ものでは細粒の使用により12mΩとなった。性状につ
いては、球状ガスアトマイズチタン粉末が焼結容器の底
部上面に沿って揃うことにより、表面が平坦化された。
また、球状ガスアトマイズチタン粉末の流動性の良さか
ら、多孔質導電板全体で比較的均一な空隙率が得られ
た。The electric resistance of the produced porous conductive plate was measured by the four-terminal method, and it was 10 mΩ with a thickness of 1 mm.
The thickness of 0.5 mm was 15 mΩ, and the thickness of 0.2 mm was 12 mΩ by using fine particles. Regarding the properties, the spherical gas atomized titanium powder was aligned along the upper surface of the bottom portion of the sintering container, whereby the surface was flattened.
Further, due to the good fluidity of the spherical gas atomized titanium powder, a relatively uniform porosity was obtained over the entire porous conductive plate.
【0030】比較のために、水素化脱水素チタン粉末の
市販品(粒径範囲50〜150μm、平均粒径100μ
m)を焼結して、50mm角×1mm厚、0.5mm厚
で空隙率が45%の多孔質導電板を製造した。45%の
空隙率を得るためにプレスによる成形を必要とした。電
気抵抗は実施例と同等であったが、強度が不十分であっ
た。これは、不規則形状粒子を使用しているために、チ
タン粉末同士の結合が均一に行われていないことが原因
と推定される。それが、多孔質導電板全体での空隙率の
バラツキに現れている。For comparison, a commercial product of hydrodehydrogenated titanium powder (particle size range 50 to 150 μm, average particle size 100 μ)
m) was sintered to produce a porous conductive plate having a size of 50 mm square × 1 mm thickness, 0.5 mm thickness and a porosity of 45%. Press molding was required to obtain a porosity of 45%. The electric resistance was equivalent to that of the example, but the strength was insufficient. It is presumed that this is because the titanium powder particles are not bonded uniformly because the irregularly shaped particles are used. This appears in the variation in the porosity of the entire porous conductive plate.
【0031】一方、チタン繊維焼結板の市販品(厚み
0.8mm)は、空隙率が60%と大きく、電気抵抗は
30mΩと高抵抗であった。強度は十分であったが、表
面は膜電極接合体に圧接させることができない程度に微
細な尖りがあった。このチタン繊維焼結体の片側の表面
に、前記市販の球状ガスアトマイズチタン粉末をアルゴ
ンガス中で0.2mmの厚みにプラズマ溶射して、全体
の厚みを1mmとした。全体の空隙率は45%となり、
表面は平坦化されたが、電気抵抗は20mΩと依然大き
く、実施例の2倍であった。On the other hand, the commercially available titanium fiber sintered plate (thickness 0.8 mm) had a large porosity of 60% and a high electric resistance of 30 mΩ. Although the strength was sufficient, the surface had minute sharpness to the extent that it could not be pressed into contact with the membrane electrode assembly. On one surface of this titanium fiber sintered body, the commercially available spherical gas atomized titanium powder was plasma-sprayed in argon gas to a thickness of 0.2 mm to make the total thickness 1 mm. The overall porosity is 45%,
Although the surface was flattened, the electric resistance was still as high as 20 mΩ, which was twice that of the example.
【0032】前記実施例では、粗粒に対する焼結温度を
約1000℃としたが、この焼結温度を1100℃とす
れば空隙率は約40%に低下した。また、焼結温度を9
00℃とすれば空隙率は約50%に増大した。いずれの
多孔質導電板も、高強度で表面の平滑性に優れ、且つ低
抵抗であった。In the above-mentioned embodiment, the sintering temperature for coarse particles was set to about 1000 ° C., but if this sintering temperature was set to 1100 ° C., the porosity decreased to about 40%. Also, the sintering temperature is 9
The porosity increased to about 50% at a temperature of 00 ° C. All porous conductive plates had high strength, excellent surface smoothness, and low resistance.
【0033】表面の平滑性を更に高める方法としては、
例えば、球状ガスアトマイズチタン粉末を、振動を付与
しながら必要寸法の焼結容器に充填する方法がある。こ
の振動充填によると、図2に示すように、焼結容器2の
底部上面に接する表面だけでなく、開口側の表面の平滑
性が向上し、空隙率の更なる均一化も図られる。また、
図3に示すように、焼結容器2を、内側の板状空間が縦
向きとなるように構成するのも有効である。内側の板状
空間が縦向きになると、充填された球状ガスアトマイズ
チタン粉末1が両側の側面から自重による板厚方向の荷
重を受け、両表面の平滑性が向上する。いずれの方法で
も、充填率が増大することによる空隙率の低減を伴い、
両者を併用することも可能である。As a method for further improving the smoothness of the surface,
For example, there is a method in which spherical gas atomized titanium powder is filled into a sintering container having a required size while applying vibration. According to this vibration filling, as shown in FIG. 2, not only the surface in contact with the upper surface of the bottom of the sintering container 2 but also the surface on the opening side is improved in smoothness, and the porosity is further homogenized. Also,
As shown in FIG. 3, it is also effective to configure the sintering container 2 so that the inner plate-shaped space is oriented vertically. When the inner plate-shaped space is oriented vertically, the filled spherical gas atomized titanium powder 1 receives a load in the plate thickness direction due to its own weight from both side surfaces, and the smoothness of both surfaces is improved. In either method, the porosity is reduced by increasing the filling rate,
Both can be used together.
【0034】成形方法としては、自然充填・真空焼結の
他、球状ガスアトマイズチタン粉末をバインダに混練し
たものを、ドクターブレード法、射出成形法、押し出し
法等でグリーン体を成形し、その後、バインダを除去し
て焼結してもよい。焼結後の多孔質導電板を圧延した
り、グリーン体を圧延して表面の更なる平滑化や空隙率
の調整を行うことも可能である。また、球状ガスアトマ
イズチタン粉末の粒度分布を小さくすることも表面の平
滑化に有効である。As a molding method, in addition to natural filling and vacuum sintering, a spherical gas atomized titanium powder kneaded with a binder is molded into a green body by a doctor blade method, an injection molding method, an extrusion method or the like, and then the binder is formed. May be removed and sintered. It is also possible to roll the porous conductive plate after sintering or roll the green body to further smooth the surface and adjust the porosity. Further, reducing the particle size distribution of the spherical gas atomized titanium powder is also effective for smoothing the surface.
【0035】[0035]
【発明の効果】以上に説明したとおり、本発明の多孔質
導電板は、球状ガスアトマイズチタン粉末の焼結体によ
り構成されることにより、成形性に優れるので、薄型大
面積の製品を簡単に製造できる。プラズマ溶射のような
コーティングを行わずとも、表面の平滑性に優れるの
で、電気抵抗の増大を伴うことなく、膜電極接合体に対
する保護性及び接触性を改善でき、経済性にも優れる。
これらにより、高性能な給電体や集電体を安価に提供で
きる。As described above, since the porous conductive plate of the present invention is made of a sintered body of spherical gas atomized titanium powder and has excellent formability, a thin and large area product can be easily manufactured. it can. Even if the coating such as plasma spraying is not performed, the surface is excellent in smoothness, so that the protection property and contact property with respect to the membrane electrode assembly can be improved without increasing the electric resistance, and the economy is also excellent.
With these, a high-performance power supply and current collector can be provided at low cost.
【図1】球状ガスアトマイズ粉末の充填形態の1例を示
す断面図である。FIG. 1 is a cross-sectional view showing an example of a filling form of spherical gas atomized powder.
【図2】球状ガスアトマイズ粉末の充填形態の他の例を
示す断面図である。FIG. 2 is a cross-sectional view showing another example of a filling form of spherical gas atomized powder.
【図3】球状ガスアトマイズ粉末の充填形態の更に他の
例を示す断面図である。FIG. 3 is a cross-sectional view showing still another example of a filling form of spherical gas atomized powder.
1 球状ガスアトマイズチタン粉末 2 焼結容器 1 Spherical gas atomized titanium powder 2 Sintering container
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI H01M 8/10 H01M 8/10 (72)発明者 加藤 雅通 兵庫県尼崎市東浜町1番地 株式会社住 友シチックス尼崎内 (56)参考文献 特開2000−328279(JP,A) 特開 平8−333605(JP,A) 特開 平8−269761(JP,A) (58)調査した分野(Int.Cl.7,DB名) C25B 11/10 B22F 1/00 B22F 5/00 C25B 1/00 - 15/08 H01M 8/02 H01M 8/10 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification symbol FI H01M 8/10 H01M 8/10 (72) Inventor Masamichi Kato 1 Higashihama-cho, Amagasaki-shi, Hyogo Sumitomo Sitix Amagasaki (56 ) Reference JP 2000-328279 (JP, A) JP 8-333605 (JP, A) JP 8-269761 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) ) C25B 11/10 B22F 1/00 B22F 5/00 C25B 1/00-15/08 H01M 8/02 H01M 8/10
Claims (3)
は固体高分子型燃料電池における集電体として使用さ
れ、且つ、球状ガスアトマイズチタン粉末の焼結体から
なることを特徴とする多孔質導電板。1. A porous conductive material which is used as a power supply in a solid polymer type water electrolyzer or as a current collector in a solid polymer type fuel cell, and is composed of a sintered body of spherical gas atomized titanium powder. Board.
記載の多孔質導電板。2. The porous conductive plate according to claim 1, which has a porosity of 35 to 55%.
径が10〜150μmである請求項1又は2に記載の多
孔質導電板。3. The porous conductive plate according to claim 1, wherein the spherical gas atomized titanium powder has an average particle size of 10 to 150 μm.
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| JP2001006405 | 2001-01-15 | ||
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| JP4501342B2 (en) * | 2002-12-06 | 2010-07-14 | 三菱マテリアル株式会社 | Method for producing separator of polymer electrolyte fuel cell |
| JP4165655B2 (en) | 2005-02-25 | 2008-10-15 | 本田技研工業株式会社 | Electrolytic device, electrochemical reaction membrane device, and porous conductor |
| JP2009252399A (en) * | 2008-04-02 | 2009-10-29 | Sanyo Special Steel Co Ltd | Metallic porous separator for fuel, cell and manufacturing method therefor |
| JP5099017B2 (en) * | 2009-01-13 | 2012-12-12 | 三菱マテリアル株式会社 | Solid polymer fuel cell separator |
| JP5573110B2 (en) * | 2009-11-06 | 2014-08-20 | 三菱マテリアル株式会社 | Sintered metal sheet material for electrochemical member and method for producing sintered metal sheet material for electrochemical member |
| JP5519299B2 (en) * | 2010-01-08 | 2014-06-11 | 奇▲こう▼科技股▲ふん▼有限公司 | Heat sink manufacturing method |
| JP5431182B2 (en) * | 2010-01-21 | 2014-03-05 | 山陽特殊製鋼株式会社 | Method for producing sheet-like porous metal member and member thereof |
| JP5966782B2 (en) * | 2012-08-30 | 2016-08-10 | 株式会社大阪ソーダ | Insoluble anode |
| EP4189144A4 (en) | 2020-07-27 | 2024-10-16 | Ohmium International, Inc. | Porous electrolyzer gas diffusion layer and method of making thereof |
| US12308484B2 (en) | 2020-09-04 | 2025-05-20 | Infinity Fuel Cell And Hydrogen, Inc. | Methods of manufacturing a gas diffusion layer and an electrochemical cell incorporating the same |
| US20230374627A1 (en) | 2020-10-05 | 2023-11-23 | Toho Titanium Co., Ltd. | Method for Manufacturing Porous Metal Body, and Porous Metal Body |
| JP7267391B1 (en) | 2021-12-27 | 2023-05-01 | 東邦チタニウム株式会社 | Titanium porous body and method for producing titanium porous body |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000328279A (en) | 1999-05-25 | 2000-11-28 | Fuji Electric Co Ltd | Method of manufacturing power supply for electrochemical cell |
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2001
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Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000328279A (en) | 1999-05-25 | 2000-11-28 | Fuji Electric Co Ltd | Method of manufacturing power supply for electrochemical cell |
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