JP2003123781A - Solid polymer electrolyte fuel cell separator and method for producing the same - Google Patents
Solid polymer electrolyte fuel cell separator and method for producing the sameInfo
- Publication number
- JP2003123781A JP2003123781A JP2001312581A JP2001312581A JP2003123781A JP 2003123781 A JP2003123781 A JP 2003123781A JP 2001312581 A JP2001312581 A JP 2001312581A JP 2001312581 A JP2001312581 A JP 2001312581A JP 2003123781 A JP2003123781 A JP 2003123781A
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- JP
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- Prior art keywords
- stainless steel
- corrosion resistance
- film
- fuel cell
- polymer electrolyte
- Prior art date
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Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
- H01M8/0228—Composites in the form of layered or coated products
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0206—Metals or alloys
- H01M8/0208—Alloys
- H01M8/021—Alloys based on iron
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0215—Glass; Ceramic materials
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Ceramic Engineering (AREA)
- Composite Materials (AREA)
- Fuel Cell (AREA)
Abstract
(57)【要約】
【課題】 ステンレス鋼製セパレータの中でも、特に高
耐食性および良導電性を併有した固体高分子電解質型燃
料電池用セパレータを提供する。
【解決手段】 固体高分子電解質型燃料電池用セパレー
タを、耐全面腐食係数GI=[Cr%]+3.6[Ni%]
+4.7[Mo%]+11.5[Cu%]が90以上である
ステンレス鋼の表面に、金属窒化物や金属分散ダイヤモ
ンドライクカーボンなどの導電性化合物を被覆したもの
で構成する。皮膜を形成するときは、上記高耐食性ステ
ンレス鋼の表面に、イオンボンバーリングを前処理とし
て行い、次いで、イオンプレーティング加工によって導
電性化合物をコーティングする。そして、被覆部分で
は、この表面皮膜にて高耐食性と良導電性を確保し、非
被覆部分(ピンホールなどの欠陥部のある部分)では、
ステンレス鋼自体の不動態皮膜により高耐食性を担保す
る。(57) [Problem] To provide a separator for a solid polymer electrolyte fuel cell having particularly high corrosion resistance and good conductivity among stainless steel separators. SOLUTION: A solid polymer electrolyte fuel cell separator is provided with a general corrosion resistance GI = [Cr%] + 3.6 [Ni%].
It is configured by coating a surface of a stainless steel having +4.7 [Mo%] + 11.5 [Cu%] of 90 or more with a conductive compound such as metal nitride or metal-dispersed diamond-like carbon. When forming a film, ion bombing is performed as a pretreatment on the surface of the high corrosion-resistant stainless steel, and then a conductive compound is coated by ion plating. And, in the coated part, high corrosion resistance and good conductivity are secured by this surface film, and in the uncoated part (the part with a defect such as pinhole),
High corrosion resistance is ensured by the passive film of stainless steel itself.
Description
【0001】[0001]
【発明の属する技術分野】 本発明は、燃料電池に使用
するセパレータで、特に、固体高分子電解質型の燃料電
池用セパレータおよびその製造方法に関する。TECHNICAL FIELD The present invention relates to a separator used in a fuel cell, and more particularly to a solid polymer electrolyte type fuel cell separator and a method for producing the same.
【0002】[0002]
【従来の技術】 近年、固体高分子電解質型燃料電池
は、一般に、発電効率が大きく、しかも、SOxやNOxを排
出しない利点を有することから、家庭用や自動車用の小
規模な燃料電池として脚光を浴び、それぞれ定置式発電
や自動車用発電への利用が期待されている。従来、この
種の固体高分子電解質型燃料電池は、簡単に説明する
と、一般的に次のような構造からなっている。2. Description of the Related Art In recent years, solid polymer electrolyte fuel cells generally have the advantages of high power generation efficiency and no emission of SOx and NOx. Therefore, they are spotlighted as small-scale fuel cells for homes and automobiles. Therefore, they are expected to be used for stationary power generation and automobile power generation, respectively. Conventionally, this type of solid polymer electrolyte fuel cell generally has a structure described below.
【0003】固体高分子電解質型燃料電池は、その固体
高分子電解質膜が、厚さ50μm程度であり、その電解
質膜の両面に電極が接合されている。電極は、白金の多
孔質体が基本であるが、カーボンブラックの微粒子に白
金微粒子を付着し、それを少量のテフロン(登録商標)
微粒子などの高分子と混合し、これを炭素繊維紙に薄く
塗布して黒鉛多孔質体と炭素繊維紙の2層構造となって
いる。そして、固体高分子電解質型燃料電池の単一のセ
ルは、この電極の黒鉛多孔質体側を、電解質膜の両面に
重ね、熱圧着して一体化した構造になっており、更に、
その電極の炭素繊維紙側にそれぞれ黒鉛製のセパレータ
を配置して単一のユニットが形成される。そうして、燃
料電池は、通常は、複数のユニットの積層体として使用
される。In the solid polymer electrolyte fuel cell, the solid polymer electrolyte membrane has a thickness of about 50 μm, and electrodes are bonded to both surfaces of the electrolyte membrane. The electrode is basically made of a platinum porous material, but platinum fine particles are attached to carbon black fine particles and a small amount of Teflon (registered trademark)
It is mixed with a polymer such as fine particles and thinly coated on carbon fiber paper to form a two-layer structure of a porous graphite body and carbon fiber paper. Then, a single cell of the solid polymer electrolyte fuel cell has a structure in which the graphite porous body side of this electrode is superposed on both surfaces of the electrolyte membrane and thermocompression-bonded to be integrated.
A single unit is formed by disposing graphite separators on the carbon fiber paper side of the electrode. Thus, fuel cells are typically used as a stack of units.
【0004】また、従来、固体高分子電解質型燃料電池
は、電極の両側にそれぞれ燃料ガスと酸化ガスが流れる
ことから、上記セパレータとして、通常、黒鉛に溝加工
を施した溝付セパレータが用いられている。黒鉛製溝付
セパレータは、流路基板として電極の両側を挟んで、そ
の両側に流路を形成し、燃料ガスと酸化ガスとが混合し
ないような構造になっている。そして、この黒鉛製溝付
セパレータは、各セルの仕切りとして、このように燃料
ガスと酸化ガスが混合することを防ぐと共に、各セルで
発生した電流の通路としての役割も担っている。Conventionally, in solid polymer electrolyte fuel cells, since a fuel gas and an oxidizing gas respectively flow on both sides of an electrode, a grooved separator made by grooving graphite is usually used as the separator. ing. The graphite grooved separator sandwiches both sides of the electrode as a flow channel substrate and forms flow channels on both sides of the electrode so that the fuel gas and the oxidizing gas are not mixed. The graphite grooved separator serves as a partition of each cell to prevent the fuel gas and the oxidizing gas from being mixed in this way, and also serves as a passage for an electric current generated in each cell.
【0005】しかし、黒鉛製セパレータは、材質上、壊
れやすいため、特に、自動車用燃料電池に使用する場合
に耐衝撃性に欠けるという問題がある。しかも、黒鉛の
溝加工には、切削加工が必要になるなど、余計に加工費
がかかり、その分だけ燃料電池がコスト高になるという
問題もあった。However, since the graphite separator is fragile in terms of material, there is a problem that impact resistance is insufficient particularly when it is used in a fuel cell for automobiles. Moreover, there is a problem in that the groove processing of graphite requires an additional processing cost such as a cutting process, and the fuel cell cost increases accordingly.
【0006】そこで、従来、このような黒鉛製セパレー
タに代えて、最近、金属製セパレータが提案されてい
る。セパレータが金属製であれば、耐衝撃性に富むこと
は勿論、切削加工を施す必要がなく、プレス加工により
成形が可能であるため、加工費が安くなり、しかも、体
積効率が良好なために、コンパクト化も図れる利点があ
るからである。Therefore, in place of such a graphite separator, a metal separator has been proposed recently. If the separator is made of metal, it will not only have high impact resistance, but it does not need to be cut and can be formed by pressing, so the processing cost will be low and the volume efficiency will be good. This is because there is an advantage that it can be made compact.
【0007】[0007]
【発明が解決しようとする課題】 ところで、固体高分
子電解質型燃料電池において、そもそも固体高分子電解
質膜は、テフロンと同じ主鎖を有し、末端にスルホン基
を有する構造をなし、そのスルホン基がイオン化し、プ
ロトンがイオン伝導性を示す。このため、固体高分子電
解質膜は、酸性を示し、電極およびセパレータに、酸に
対する耐食性が要求される。特に、セパレータとして、
耐食性の低い金属材料を使用した場合には、溶出した金
属イオンが電解質膜と反応し、その膜のイオン伝導性が
損なわれ、発電能力の低下をもたらすことになる。した
がって、金属製セパレータには、まず高耐食性を有する
ことが必要である。By the way, in the solid polymer electrolyte fuel cell, the solid polymer electrolyte membrane originally has the same main chain as Teflon and has a structure having a sulfone group at the terminal. Is ionized, and the proton exhibits ionic conductivity. Therefore, the solid polymer electrolyte membrane exhibits acidity, and the electrodes and the separator are required to have corrosion resistance against acid. Especially as a separator,
When a metal material having low corrosion resistance is used, the eluted metal ions react with the electrolyte membrane, impairing the ion conductivity of the membrane, resulting in a decrease in power generation capacity. Therefore, the metal separator must first have high corrosion resistance.
【0008】次に、そもそもセパレータは、上述のよう
に各セル同士の境界を形成し、燃料ガスと酸化ガスとが
混合するのを防止するだけでなく、各セルで発生した電
流の通路となるものであるから、十分な導電性を有する
ことが必要である。Next, in the first place, the separator not only prevents the fuel gas and the oxidizing gas from mixing with each other by forming the boundary between the cells as described above, but also serves as a passage for the electric current generated in each cell. Therefore, it is necessary to have sufficient conductivity.
【0009】そこで、従来、これら高耐食性および良導
電性の要件を満足する可能性が高い金属製セパレータと
して、ステンレス鋼製セパレータが注目されている。Therefore, stainless steel separators have hitherto attracted attention as metal separators that are highly likely to satisfy the requirements of high corrosion resistance and good conductivity.
【0010】ところが、ステンレス鋼は、確かに、優れ
た耐食性を有することで知られ、その耐食性は、表面に
形成される不動態皮膜により維持されるが、一方で、不
動態皮膜は絶縁性であり、導電性を阻害する。したがっ
て、従来、ステンレス鋼製のセパレータを提供する場合
には、セパレータの機能を確保する観点から、表面の不
動態皮膜により耐食性が担保される一方で、その不動態
皮膜が原因で導電性が阻害される弊害を解消する必要が
あるという課題があった。However, stainless steel is known to have excellent corrosion resistance, and the corrosion resistance is maintained by the passivation film formed on the surface, while the passivation film is insulating. Yes, impedes conductivity. Therefore, conventionally, when providing a separator made of stainless steel, from the viewpoint of ensuring the function of the separator, while the corrosion resistance is secured by the passivation film on the surface, the conductivity is hindered by the passivation film. There is a problem that it is necessary to eliminate the harmful effects.
【0011】そこで、本発明の目的は、上述した従来の
課題を解決し、ステンレス鋼製セパレータの中でも、特
に高耐食性および良導電性を併有した固体高分子電解質
型燃料電池用セパレータを提供することにある。Therefore, an object of the present invention is to solve the above-mentioned conventional problems, and to provide a separator for a solid polymer electrolyte fuel cell, which has particularly high corrosion resistance and good conductivity among the stainless steel separators. Especially.
【0012】[0012]
【課題を解決するための手段】 本発明者らは、鋭意研
究を重ねた結果、上述した技術的課題を解決する手段と
して、まずは、ステンレス鋼にイオンプレーティングな
どの表面処理を施すことにより、高耐食性および良導電
性を併有した導電性化合物の皮膜を形成する構成を見い
出した。なお、本発明において、単に「皮膜」とは、特
に断らない限り、イオンプレーティング等の表面処理に
よって下地ステンレス鋼表面に形成された被覆層を指
す。Means for Solving the Problems As a result of intensive studies, the inventors of the present invention have found that as a means for solving the above-mentioned technical problems, first, by subjecting stainless steel to a surface treatment such as ion plating, We have found a structure that forms a film of a conductive compound having both high corrosion resistance and good conductivity. In the present invention, the term “coating” simply refers to a coating layer formed on the surface of the underlying stainless steel by surface treatment such as ion plating unless otherwise specified.
【0013】また、ステンレス鋼は、不動態皮膜がその
含有成分であるクロム等の水酸化物などを主成分とする
ため、クロムやモリブデンを多く含有するほど、表面の
不動態皮膜により高い耐食性を維持する一方、イオンプ
レーティング等によって形成される皮膜には、不可避的
にピンホール等の欠陥部が発生することが知られてい
る。これら欠陥部は、皮膜形成処理中にゴミ等が付着し
て発生したり、皮膜の粒界に起因して微細な割れが発生
したりすることなど、様々なことが原因で発生するた
め、欠陥部の存在しない皮膜を作製することは不可能で
ある。ピンホール等の欠陥部が存在すると、皮膜自体の
耐食性が如何に優れたものであっても、皮膜のないピン
ホール等から下地の金属イオンが溶出し、それが電解質
膜と反応して電解質膜のイオン伝導性が阻害される結果
となる。そこで、下地のステンレス鋼は、皮膜にピンホ
ール等の欠陥部が発生しても、少なくとも下地の金属イ
オンが溶出しないことが必要であることに着目し、これ
を解決する手段として、下地金属に所要の高耐食性ステ
ンレス鋼を用いることを見い出し、以下のような構成の
本発明を完成するに至った。Further, in stainless steel, since the passivation film is mainly composed of a hydroxide such as chromium, which is a contained component, the higher the content of chromium and molybdenum, the higher the corrosion resistance of the surface passivation film. On the other hand, it is known that a film formed by ion plating or the like inevitably has a defective portion such as a pinhole while being maintained. These defects are caused by various factors such as dust adhering during the film formation process and fine cracks caused by the grain boundaries of the film. It is not possible to make a film without parts. If there are defects such as pinholes, no matter how excellent the corrosion resistance of the coating itself is, the underlying metal ions will elute from the pinholes without coating, which react with the electrolyte membrane to cause electrolyte membrane As a result, the ionic conductivity of is impaired. Therefore, we focused on the fact that the underlying stainless steel requires that at least the underlying metal ions do not elute even if defects such as pinholes occur in the film. It was found that the required high corrosion resistance stainless steel was used, and the present invention having the following constitution was completed.
【0014】すなわち、本発明の固体高分子電解質型燃
料電池用セパレータは、質量%で示すと、[Cr%]+
3.6[Ni%]+4.7[Mo%]+11.5[Cu%]の
耐全面腐食係数が90以上であるステンレス鋼の表面
に、導電性化合物を被覆してなることを特徴とする。こ
のようにステンレス鋼の表面を導電性化合物で被覆すれ
ば、被覆部分には、皮膜と下地金属の間に不動態皮膜が
存在しないため、良好な導電性が担保される一方、耐食
性についても、被覆部分は、皮膜自身の耐食性により高
い耐食性が担保され、非被覆部分(ピンホールなどの欠
陥部のある部分)は、下地である高耐食性ステンレス鋼
自体の不動態皮膜により担保される。これによって、高
耐食性および良導電性を併有した固体高分子電解質型燃
料電池用セパレータが提供され、本発明の目的が達成さ
れる。That is, the solid polymer electrolyte fuel cell separator of the present invention is [Cr%] +
It is characterized in that the surface of stainless steel having a general corrosion resistance coefficient of 3.6 [Ni%] + 4.7 [Mo%] + 11.5 [Cu%] of 90 or more is coated with a conductive compound. . If the surface of the stainless steel is coated with a conductive compound in this way, the coated portion does not have a passivation film between the film and the underlying metal, and thus good conductivity is ensured, while also regarding corrosion resistance, The coated portion has a high corrosion resistance secured by the corrosion resistance of the coating itself, and the non-coated portion (the portion having a defective portion such as a pinhole) is secured by the passivation coating of the high corrosion resistant stainless steel itself which is the base. As a result, a solid polymer electrolyte fuel cell separator having both high corrosion resistance and good conductivity is provided, and the object of the present invention is achieved.
【0015】本発明の固体高分子電解質型燃料電池用セ
パレータにおいて、前記導電性化合物は、高耐食性と良
導電性を併せ持つものであれば何でもよいが、たとえば
窒化クロム、窒化チタン等の金属窒化物であることが好
ましい。In the solid polymer electrolyte fuel cell separator of the present invention, the conductive compound may be any one having both high corrosion resistance and good conductivity. For example, metal nitrides such as chromium nitride and titanium nitride. Is preferred.
【0016】また、本発明において、前記導電性化合物
は、ダイヤモンドライクカーボンに金属を分散して導電
性を付与した物質である、金属分散ダイヤモンドライク
カーボンであることも好ましい。なぜなら、金属分散ダ
イヤモンドライクカーボンの皮膜は、耐酸性に優れてい
るが絶縁体であるダイヤモンドライクカーボンに、金属
の添加により導電性を付与したものだからである。In the present invention, the conductive compound is also preferably metal-dispersed diamond-like carbon, which is a substance in which a metal is dispersed in diamond-like carbon to impart conductivity. This is because the film of the metal-dispersed diamond-like carbon has excellent acid resistance, but conductivity is imparted to the diamond-like carbon, which is an insulator, by adding a metal.
【0017】さらに、本発明において、ステンレス鋼の
表面に導電性化合物の皮膜を形成するときは、耐全面腐
食係数が90以上の前記高耐食性ステンレス鋼を下地金
属とし、該ステンレス鋼の表面にイオンボンバーリング
を前処理として行い、次いで、イオンプレーティング加
工によって前記導電性化合物をコーティングすることが
好ましい。Further, in the present invention, when a film of a conductive compound is formed on the surface of stainless steel, the above-mentioned highly corrosion resistant stainless steel having a general corrosion resistance of 90 or more is used as a base metal, and ions are formed on the surface of the stainless steel. It is preferable to perform bomber ring as a pretreatment and then coat the conductive compound by ion plating.
【0018】[0018]
【発明の実施の形態】 以下、本発明の実施の形態につ
いて詳細に説明する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described in detail.
【0019】本発明の固体高分子電解質型燃料電池用セ
パレータは、下地金属として高耐食性ステンレス鋼を用
い、そのステンレス鋼の表面に、導電性化合物を被覆し
た構成になっている。The solid polymer electrolyte fuel cell separator of the present invention has a structure in which highly corrosion-resistant stainless steel is used as a base metal, and the surface of the stainless steel is coated with a conductive compound.
【0020】すなわち、本発明は、高耐食性ステンレス
鋼の表面に、後述するイオンプレーティングにて表面処
理を施すことにより、高耐食性および良導電性を併有す
る導電性化合物の皮膜を形成する。導電性化合物は、高
耐食性および良導電性を併有する、例えば窒化クロム、
窒化チタン等のような金属窒化物であることが好まし
い。また、斯かる導電性化合物の皮膜としては、窒化物
皮膜コーティングの前処理として、金属コーティングし
たもの、例えば皮膜を金属クロムと窒化クロムの2層構
造としたもの、或いは、金属チタンと窒化チタンの2層
構造としたものであることが、耐食性をより高める上で
効果的である。That is, the present invention forms a film of a conductive compound having both high corrosion resistance and good conductivity by subjecting the surface of high corrosion resistance stainless steel to surface treatment by the ion plating described later. The conductive compound has both high corrosion resistance and good conductivity, for example, chromium nitride,
It is preferably a metal nitride such as titanium nitride. Further, as the film of such a conductive compound, as a pretreatment of the nitride film coating, a metal coating, for example, a film having a two-layer structure of metal chromium and chromium nitride, or a film of metal titanium and titanium nitride is used. Having a two-layer structure is effective in further increasing the corrosion resistance.
【0021】本発明における導電性化合物の皮膜は、金
属分散ダイヤモンドライクカーボンを被覆したものであ
っても有効である。金属分散ダイヤモンドライクカーボ
ンの皮膜としては、炭化タングステン皮膜に金属タング
ステンを分散させたものや、炭化タンタル皮膜に金属タ
ンタルを分散させたもの等がある。炭化タングステンや
炭化タンタルなどのダイヤモンドライクカーボンは、耐
酸性は優れているが、絶縁体であるため、金属の添加に
より導電性を付与しているのである。The conductive compound film of the present invention is effective even if it is coated with metal-dispersed diamond-like carbon. Examples of the film of the metal-dispersed diamond-like carbon include a tungsten carbide film in which metallic tungsten is dispersed, a tantalum carbide film in which metallic tantalum is dispersed, and the like. Diamond-like carbon such as tungsten carbide and tantalum carbide has excellent acid resistance, but since it is an insulator, conductivity is imparted by adding a metal.
【0022】下地のステンレス鋼に対する皮膜の厚さに
限定はないが、特に耐食性確保の観点から、2〜3μm
以上が望ましい。The thickness of the coating on the underlying stainless steel is not limited, but from the viewpoint of ensuring corrosion resistance, it is 2 to 3 μm.
The above is desirable.
【0023】ここで、本発明に用いる高耐食性ステンレ
ス鋼として、具体的にどのようなステンレス鋼が下地金
属として有効かを検討した結果を述べる。本発明者ら
は、各種成分組成を有するステンレス鋼について、10
%硫酸および20%硫酸中80℃での腐食減量を測定し
た。この結果を、耐全面腐食係数(以下「GI」とい
う)について整理したところ、図1のようにGIと腐食
減量との間には、明らかな相関が認められた。ここにお
いて、GIは、質量%を使用してGI=[Cr%]+3.
6[Ni%]+4.7[Mo%]+11.5[Cu%]により
求められる指数である。この関係から、GIが90以上
であれば、十分な耐食性が得られることが判明した。Here, the results of a study of what kind of stainless steel is particularly effective as the base metal as the high corrosion resistant stainless steel used in the present invention will be described. The present inventors have found that for stainless steels having various component compositions, 10
The corrosion weight loss was measured at 80 ° C. in% sulfuric acid and 20% sulfuric acid. When this result was arranged for the general corrosion resistance (hereinafter referred to as "GI"), a clear correlation was observed between GI and the corrosion weight loss as shown in FIG. Here, GI is GI = [Cr%] + 3.
It is an index obtained by 6 [Ni%] + 4.7 [Mo%] + 11.5 [Cu%]. From this relationship, it was found that if GI is 90 or more, sufficient corrosion resistance can be obtained.
【0024】したがって、本発明の固体高分子電解質型
燃料電池用セパレータは、下地金属として、質量%で示
すと、[Cr%]+3.6[Ni%]+4.7[Mo%]+1
1.5[Cu%]の耐全面腐食係数が90以上である高耐
食性ステンレス鋼を選択し、そのステンレス鋼の表面
に、前記導電性化合物を被覆して構成してなる。Therefore, in the solid polymer electrolyte fuel cell separator of the present invention, when expressed in mass% as a base metal, [Cr%] + 3.6 [Ni%] + 4.7 [Mo%] + 1
A highly corrosion resistant stainless steel having a general corrosion resistance of 1.5 [Cu%] of 90 or more is selected, and the surface of the stainless steel is coated with the conductive compound.
【0025】GIが90以上のステンレス鋼には、例え
ばJIS鋼種ではSUS317、SUS310S等があり、その他の商用
鋼種としてNTK30AC(C≦0.07、Cr:19.00〜21.00、Ni:
32.00〜38.00、Mo:2.00〜3.00、Cu:3.00〜4.00、Nb:
8xC%〜10xC%)、NTK30A(C≦0.020、Cr:19.00〜21.0
0、Ni:28.00〜30.00、Mo:2.00〜3.00、Cu:3.00〜4.0
0、Mn:2.50〜3.50)、NTK22A(C≦0.020、Cr:19.00〜
21.00、Ni:21.00〜23.00、Mo:1.75〜2.75、Cu:1.75
〜2.75、Mn:2.50〜3.50)等がある。しかし、本発明
は、下地の高耐食性ステンレス鋼として、上記に列挙し
た鋼種に限定されるものではない。Stainless steels having a GI of 90 or more include, for example, JIS steel types such as SUS317 and SUS310S, and other commercial steel types include NTK30AC (C ≦ 0.07, Cr: 19.00 to 21.00, Ni:
32.00 ~ 38.00, Mo: 2.00 ~ 3.00, Cu: 3.00 ~ 4.00, Nb:
8xC% ~ 10xC%), NTK30A (C ≤ 0.020, Cr: 19.00 ~ 21.0
0, Ni: 28.00 to 30.00, Mo: 2.00 to 3.00, Cu: 3.00 to 4.0
0, Mn: 2.50 ~ 3.50), NTK22A (C ≤ 0.020, Cr: 19.00 ~
21.00, Ni: 21.00-23.00, Mo: 1.75-2.75, Cu: 1.75
~ 2.75, Mn: 2.50 ~ 3.50) etc. However, the present invention is not limited to the steel types listed above as the high corrosion-resistant stainless steel of the base.
【0026】さて次に、下地の高耐食性ステンレス鋼に
表面処理を施して導電性化合物の皮膜を形成する方法に
ついて説明する。Next, a method for forming a film of a conductive compound by subjecting the high corrosion-resistant stainless steel as a base to a surface treatment will be described.
【0027】本発明は、上述したGIが90以上の高耐
食性ステンレス鋼を下地金属とし、該ステンレス鋼の表
面に、好ましくはイオンボンバーリングを前処理として
行い、次いで、イオンプレーティング加工によって金属
窒化物や金属分散ダイヤモンドライクカーボンのような
導電性化合物をコーティングする。In the present invention, the above-mentioned highly corrosion resistant stainless steel having a GI of 90 or more is used as a base metal, and the surface of the stainless steel is preferably subjected to ion bombarding as a pretreatment, and then metal nitriding is performed by ion plating. Or a conductive compound such as metal-dispersed diamond-like carbon.
【0028】イオンプレーティング加工においては、皮
膜密着性の向上を図るために、加工前に、イオンボンバ
ーリング処理を施すことが行われる。イオンボンバーリ
ング処理は、アルゴンイオンなどを加速して被処理物の
表面に衝突させ、表面の不純物や酸化皮膜を除去するこ
とにより表面を清浄とし、引き続き行うコーティング処
理によって形成される皮膜と、下地金属との密着性を向
上させるものである。このイオンボンバーリング処理に
よって、ステンレス鋼の表面に存在する不動態皮膜が予
め除去される。従って、イオンプレーティング処理に先
だって、前処理としてイオンボンバーリングを行うと、
皮膜が形成された被覆部分には、皮膜と下地金属の間に
不動態皮膜は存在せず、その結果、ステンレス鋼自体お
よび皮膜の有する導電性は担保される。なお、耐食性に
ついても、この被覆部分は、皮膜自身の耐食性によって
高い耐食性が担保される。In the ion plating process, in order to improve the film adhesion, an ion bomber ring process is performed before the process. The ion bombarding process cleans the surface by accelerating argon ions etc. to collide with the surface of the object to be treated and removes the impurities and oxide film on the surface, and the film formed by the subsequent coating process and the substrate. It improves the adhesion to metal. By this ion bombarding treatment, the passivation film existing on the surface of stainless steel is removed in advance. Therefore, if ion bombarding is performed as a pretreatment before the ion plating treatment,
In the coated portion where the coating is formed, there is no passivation coating between the coating and the underlying metal, and as a result, the conductivity of the stainless steel itself and the coating is ensured. With respect to the corrosion resistance, the high corrosion resistance of this coating portion is ensured by the corrosion resistance of the film itself.
【0029】一方、皮膜の形成されていないピンホール
等の欠陥(非被覆部分)は、下地のステンレス鋼が直接
外部に曝されるが、ステンレス鋼の不動態皮膜は、大気
中の水分や酸素と接触することにより自然に形成される
ので、耐食性も担保される。以上の皮膜形成方法によっ
て、高耐食性および良導電性を併有した固体高分子電解
質型燃料電池用セパレータが作製され、本発明の目的が
達成される。On the other hand, defects (uncoated portions) such as pinholes in which a film is not formed expose the underlying stainless steel directly to the outside, but the passive film of the stainless steel has a moisture and oxygen content in the atmosphere. Corrosion resistance is also ensured because it is formed naturally by contact with. By the above film forming method, a solid polymer electrolyte fuel cell separator having both high corrosion resistance and good conductivity is produced, and the object of the present invention is achieved.
【0030】皮膜の形成方法としては、本発明の目的を
達成できる方法、即ち、ステンレス鋼の表面に高耐食性
と良導電性を併有する皮膜の形成方法であれば、特に上
記方法に限定されるものではないが、イオンプレーティ
ングは最適な方法のひとつである。また、前処理とし
て、イオンボンバーリングというステンレス鋼の不導態
皮膜を予め除去するステップを含む構成にすることによ
って、より好ましい結果が得られる。The method for forming a film is not particularly limited to the above method as long as it can achieve the object of the present invention, that is, a method for forming a film having both high corrosion resistance and good conductivity on the surface of stainless steel. Although not a thing, ion plating is one of the best methods. Further, as a pretreatment, a more preferable result can be obtained by adopting a configuration including a step of previously removing the non-conductive coating of stainless steel called ion bomber ring.
【0031】[0031]
【実施例】次に、以下に示す実施例に基づいて、本発明
を更に詳細かつ具体的に説明するが、本発明は、この実
施例に限定されるものでないことは、勿論である。EXAMPLES Next, the present invention will be explained in more detail and specifically based on the following examples, but it goes without saying that the present invention is not limited to these examples.
【0032】(1)試料の作製
ステンレス板(厚さ0.2mm、鋼種NTK30AC)に対
し、マルチアークイオンプレーティング装置を用いて窒
化クロムをコーティングした。その場合、まず、前処理
として、5〜10x10−2Paのアルゴンガスを流しな
がら、電圧400Vを印加してイオンボンバーリングを
行った。次いで、電極にクロムを用い、チャンバー内
に、0.5Paの圧力となるように窒素ガスを流し、電圧
200V、電流80Aで電極とチャンバー壁面にアークを
発生させ、試料板を回転させながら、窒化クロムを5μ
mコーティングした(以下、「CrN皮膜材」という)。(1) Preparation of Sample A stainless steel plate (thickness: 0.2 mm, steel type: NTK30AC) was coated with chromium nitride using a multi-arc ion plating device. In that case, first, as a pretreatment, while applying an argon gas of 5 to 10 × 10 −2 Pa, a voltage of 400 V was applied to perform ion bomber ring. Then, using chromium for the electrodes, nitrogen gas was flown into the chamber so as to have a pressure of 0.5 Pa, an arc was generated at the electrodes and the chamber wall surface at a voltage of 200 V and a current of 80 A, and the sample plate was rotated while nitriding Chrome 5μ
m coated (hereinafter referred to as "CrN coating material").
【0033】同上の装置を用い、同上のステンレス板を
イオンボンバーリングの後、アルゴンガス雰囲気中で金
属クロムを2μmコーティングし、その後、窒素雰囲気
として窒化クロム層を3μm形成した(以下、「Cr/Cr
N皮膜材」という)。Using the same apparatus as above, the above stainless steel plate was subjected to ion bombarding, followed by coating with metallic chromium of 2 μm in an argon gas atmosphere, and then forming a chromium nitride layer of 3 μm in a nitrogen atmosphere (hereinafter referred to as “Cr / Cr
N film material ").
【0034】マグネトロンスパッタリング装置を用い、
同上のステンレス板をイオンボンバーリングの後、タン
グステンターゲットを使用してアルゴンとアセチレン混
合ガス中で、金属タングステンが炭化タングステン中に
分散した皮膜を形成した(以下、「W-DLC皮膜材」とい
う)。Using a magnetron sputtering device,
After ion bombarding the stainless steel plate described above, a tungsten target was used to form a film in which metallic tungsten was dispersed in tungsten carbide in a mixed gas of argon and acetylene (hereinafter referred to as "W-DLC film material"). .
【0035】(2)特性の評価
上記のCrN皮膜材、Cr/CrN皮膜材およびW-DLC皮膜材に
ついて、導電性および耐食性の評価を以下のように行っ
た。(2) Evaluation of characteristics The above-mentioned CrN coating material, Cr / CrN coating material and W-DLC coating material were evaluated for conductivity and corrosion resistance as follows.
【0036】導電性は、接触電気抵抗測定器〔(株)山
崎精機研究所製山崎式SQメーター〕により、皮膜の接触
電気抵抗を測定して評価した。試料表面に、黒鉛電極を
接圧20Kg/cm2で接触させ、10mm走査させたとき
の接触電気抵抗を測定した。その結果、CrN皮膜材0.
355Ω、Cr/CrN皮膜材0.285Ω、W-DLC皮膜材
0.593Ωであり、これらは無垢のステンレス13
4.66Ωに比較して十分小さく、純金0.158Ωに
近い値となっている。The electrical conductivity was evaluated by measuring the contact electric resistance of the film with a contact electric resistance measuring device [Yamazaki SQ meter manufactured by Yamazaki Seiki Laboratory Co., Ltd.]. A graphite electrode was brought into contact with the surface of the sample at a contact pressure of 20 kg / cm 2 , and the contact electric resistance when scanning for 10 mm was measured. As a result, the CrN coating material 0.
355Ω, Cr / CrN coating material 0.285Ω, W-DLC coating material 0.593Ω, these are pure stainless steel 13
The value is sufficiently smaller than 4.66Ω and is a value close to 0.158Ω of pure gold.
【0037】耐食性は、80℃の5%硫酸中に148時
間浸漬し、皮膜面の溶出量を測定して評価した。溶出量
は、CrN皮膜材が0.25mg/m2/h、Cr/CrN皮膜材が
0.22mg/m2/h、W-DLC皮膜材が0.38mg/m2/h、
と僅かな値である。The corrosion resistance was evaluated by immersing it in 5% sulfuric acid at 80 ° C. for 148 hours and measuring the amount of elution on the coating surface. Elution amount, CrN coating material is 0.25mg / m 2 / h, Cr / CrN coating material is 0.22mg / m 2 / h, W -DLC film material is 0.38mg / m 2 / h,
And a small value.
【0038】次に、上記3種類の皮膜形成ステンレス板
を用いて溝状の構造にプレス加工を施した後、単セル燃
料電池にセパレータとして組み入れ、発電試験を行っ
た。高分子電解質膜と電極を一体化したものを本セパレ
ータで挟み、両端に酸化ガスおよび水素ガスを供給した
ところ、初期電圧0.7Vが得られた。さらに、500
時間連続運転を行った後も、いずれも約0.67Vの出
力が得られた。これは僅か5%の電圧降下に過ぎないも
のである。Next, after pressing the groove-shaped structure using the above-mentioned three types of film-formed stainless steel plates, it was incorporated into a single cell fuel cell as a separator and a power generation test was conducted. When the polymer electrolyte membrane and the electrode integrated with each other were sandwiched between the separators and an oxidizing gas and a hydrogen gas were supplied to both ends, an initial voltage of 0.7 V was obtained. In addition, 500
An output of about 0.67 V was obtained in each case even after continuous operation for an hour. This is a voltage drop of only 5%.
【0039】[0039]
【発明の効果】 上述のように構成した本発明によれ
ば、次のような顕著な効果が得られる。According to the present invention configured as described above, the following remarkable effects can be obtained.
【0040】請求項1に記載の発明によれば、固体高分
子電解質型燃料電池用セパレータを、耐全面腐食係数G
I=[Cr%]+3.6[Ni%]+4.7[Mo%]+1
1.5[Cu%]が90以上であるステンレス鋼の表面
に、導電性化合物を被覆したもので構成することから、
被覆部分には、皮膜と下地金属の間に不動態皮膜が存在
しない結果、良好な導電性が担保される一方、耐食性に
ついても、被覆部分は、皮膜自身の耐食性によって高い
耐食性が担保され、非被覆部分(ピンホールなどの欠陥
部のある部分)は、下地である高耐食性ステンレス鋼自
体の不動態皮膜により担保され、これによって、従来に
ない高耐食性および良導電性を併有した固体高分子電解
質型燃料電池用セパレータを提供することができる。According to the invention described in claim 1, the solid polymer electrolyte fuel cell separator is provided with a general corrosion resistance G
I = [Cr%] + 3.6 [Ni%] + 4.7 [Mo%] + 1
Since the surface of stainless steel having 1.5 [Cu%] of 90 or more is coated with a conductive compound,
As a result of the absence of a passivation film between the film and the underlying metal in the coated part, good conductivity is assured, while also in terms of corrosion resistance, the coated part has a high corrosion resistance due to the corrosion resistance of the film itself. The coated part (the part with defects such as pinholes) is secured by the passivation film of the high corrosion-resistant stainless steel itself, which is the base, and as a result, it is a solid polymer with both high corrosion resistance and good conductivity that have never been seen before. It is possible to provide a separator for an electrolyte fuel cell.
【0041】加えて、そもそもステンレス鋼製セパレー
タであるため、材質上、従来の黒鉛製セパレータのよう
な脆さがなく、耐衝撃性を必要とされる自動車用燃料電
池などにも広く使用することができる。さらに、流路用
の溝加工などのために切削加工を施す必要がなく、プレ
ス加工により簡単に且つ安価に成形することができ、そ
の結果、低コストの燃料電池を提供することができ、し
かも、体積効率が良好なために、コンパクト化も図るこ
とができる。In addition, since it is a stainless steel separator in the first place, it does not have the brittleness of conventional graphite separators due to its material, and can be widely used for fuel cells for automobiles that require impact resistance. You can Further, it is not necessary to perform cutting work for groove processing for the flow path, and it can be easily and inexpensively formed by press work, and as a result, a low cost fuel cell can be provided, and Since the volume efficiency is good, it can be made compact.
【0042】請求項2および3に記載の発明によれば、
それぞれステンレス鋼の表面に被覆する導電性化合物を
金属窒化物と金属分散ダイヤモンドライクカーボンにす
ることにより、被覆部分について、より効果的に高い耐
食性を確保すると共に良好な導電性を確保することがで
きる。According to the invention described in claims 2 and 3,
By using a metal nitride and a metal-dispersed diamond-like carbon as the conductive compound that coats the surface of each stainless steel, it is possible to more effectively secure high corrosion resistance and good conductivity for the coated portion. .
【0043】請求項4に記載の発明によれば、上述した
耐全面腐食係数が90以上の高耐食性ステンレス鋼表面
に、イオンボンバーリングを前処理として行い、次い
で、イオンプレーティング加工によって導電性化合物を
コーティングする構成とすることにより、ステンレス鋼
の表面に存在する不動態皮膜を予め除去し、皮膜と下地
金属との密着性を向上させて、高耐食性および良導電性
を併有した皮膜をステンレス鋼表面に効果的に形成する
ことができる。According to the fourth aspect of the present invention, the surface of the high corrosion resistant stainless steel having the above general corrosion resistance of 90 or more is subjected to ion bomber ring pretreatment, and then ion plating is performed to form a conductive compound. By coating the stainless steel, the passivation film existing on the surface of the stainless steel is removed in advance, the adhesion between the film and the underlying metal is improved, and a film having both high corrosion resistance and good conductivity is formed on the stainless steel. It can be effectively formed on the steel surface.
【図1】 各種成分組成を有したステンレス鋼における
所定条件下の耐全面腐食係数と腐食減量との関係を示す
図表である。FIG. 1 is a chart showing a relationship between a general corrosion resistance coefficient and a corrosion weight loss under a predetermined condition in stainless steel having various component compositions.
Claims (4)
%]+4.7[Mo%]+11.5[Cu%]の耐全面腐食
係数が90以上であるステンレス鋼の表面に、導電性化
合物を被覆してなることを特徴とする、固体高分子電解
質型燃料電池用セパレータ。1. When expressed in mass%, [Cr%] + 3.6 [Ni
%] + 4.7 [Mo%] + 11.5 [Cu%] stainless steel having a general corrosion resistance of 90 or more, which is obtained by coating a conductive compound on the surface of the solid polymer electrolyte. Type fuel cell separator.
とを特徴とする、請求項1に記載の固体高分子電解質型
燃料電池用セパレータ。2. The solid polymer electrolyte fuel cell separator according to claim 1, wherein the conductive compound is a metal nitride.
ドライクカーボンであることを特徴とする、請求項1に
記載の固体高分子電解質型燃料電池用セパレータ。3. The solid polymer electrolyte fuel cell separator according to claim 1, wherein the conductive compound is metal-dispersed diamond-like carbon.
テンレス鋼の表面にイオンボンバーリングを前処理とし
て行い、次いで、イオンプレーティング加工によって前
記導電性化合物をコーティングしてなることを特徴とす
る、請求項1、2又は3に記載の固体高分子電解質型燃
料電池用セパレータの製造方法。4. The stainless steel is used as a base metal, the surface of the stainless steel is subjected to ion bombarding as a pretreatment, and then the conductive compound is coated by ion plating. The method for producing the solid polymer electrolyte fuel cell separator according to claim 1, 2, or 3.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001312581A JP3498077B2 (en) | 2001-10-10 | 2001-10-10 | Solid polymer electrolyte fuel cell separator |
| PCT/JP2002/007480 WO2003034525A1 (en) | 2001-10-10 | 2002-07-24 | Solid polymer electrolyte type fuel cell-use separator and production method therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001312581A JP3498077B2 (en) | 2001-10-10 | 2001-10-10 | Solid polymer electrolyte fuel cell separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2003123781A true JP2003123781A (en) | 2003-04-25 |
| JP3498077B2 JP3498077B2 (en) | 2004-02-16 |
Family
ID=19131215
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001312581A Expired - Lifetime JP3498077B2 (en) | 2001-10-10 | 2001-10-10 | Solid polymer electrolyte fuel cell separator |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP3498077B2 (en) |
| WO (1) | WO2003034525A1 (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003083980A1 (en) * | 2002-03-29 | 2003-10-09 | Honda Giken Kogyo Kabushiki Kaisha | Metal separator for fuel cell and manufacturing method thereof |
| EP1575109A1 (en) * | 2004-03-11 | 2005-09-14 | Nissan Motor Co., Ltd. | Fuel cell separator, fuel cell stack, fuel cell vehicle, and method of manufacturing fuel cell separator |
| WO2005124913A1 (en) * | 2004-06-22 | 2005-12-29 | Honda Motor Co., Ltd. | Method for manufacturing separator for fuel cell |
| WO2008114561A1 (en) | 2007-02-22 | 2008-09-25 | Toyota Jidosha Kabushiki Kaisha | Fuel cell separator, fuel cell separator manufacturing method and fuel cell |
| JP2010287542A (en) * | 2009-06-15 | 2010-12-24 | Nissan Motor Co Ltd | Conductive member, method for producing the same, fuel cell separator using the same, and polymer electrolyte fuel cell |
| US7960071B2 (en) | 2004-03-23 | 2011-06-14 | Korea Institute Of Science And Technology | Separator for fuel cell using a metal plate coated with titanium nitride, method for manufacturing the same, and polymer electrolyte membrane fuel cell comprising the separator |
| CN102201582A (en) * | 2010-03-22 | 2011-09-28 | 现代Hysco株式会社 | Metal separator for fuel cell and method of manufacturing the same |
| JP2018514647A (en) * | 2015-03-20 | 2018-06-07 | アペラン | Metal strip or sheet with chromium nitride coating, bipolar plate and associated manufacturing method |
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| KR101015899B1 (en) | 2004-12-22 | 2011-02-23 | 삼성에스디아이 주식회사 | Metal Separators for Fuel Cells |
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|---|---|---|---|---|
| JPS5919327A (en) * | 1982-07-23 | 1984-01-31 | Citizen Watch Co Ltd | Surface processing method by ion bombarding |
| JP3904696B2 (en) * | 1997-11-11 | 2007-04-11 | 日新製鋼株式会社 | Low temperature fuel cell separator and method for producing the same |
| JP3908359B2 (en) * | 1997-10-21 | 2007-04-25 | 日新製鋼株式会社 | Low temperature fuel cell separator |
| JP2000164228A (en) * | 1998-11-25 | 2000-06-16 | Toshiba Corp | Solid polymer electrolyte fuel cell separator and method for producing the same |
| JP2000353531A (en) | 1999-06-08 | 2000-12-19 | Sumitomo Electric Ind Ltd | Separator for polymer electrolyte fuel cell and method for producing the same |
| JP2001093538A (en) * | 1999-09-27 | 2001-04-06 | Nisshin Steel Co Ltd | Stainless steel low temperature fuel cell separator |
| JP2001236967A (en) * | 2000-02-25 | 2001-08-31 | Sumitomo Electric Ind Ltd | Solid polymer electrolyte fuel cell separator |
| JP4604302B2 (en) * | 2000-02-28 | 2011-01-05 | パナソニック株式会社 | Polymer electrolyte fuel cell |
-
2001
- 2001-10-10 JP JP2001312581A patent/JP3498077B2/en not_active Expired - Lifetime
-
2002
- 2002-07-24 WO PCT/JP2002/007480 patent/WO2003034525A1/en not_active Ceased
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| WO2003083980A1 (en) * | 2002-03-29 | 2003-10-09 | Honda Giken Kogyo Kabushiki Kaisha | Metal separator for fuel cell and manufacturing method thereof |
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Also Published As
| Publication number | Publication date |
|---|---|
| WO2003034525A1 (en) | 2003-04-24 |
| JP3498077B2 (en) | 2004-02-16 |
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