JPH0512425B2 - - Google Patents

Info

Publication number
JPH0512425B2
JPH0512425B2 JP61154570A JP15457086A JPH0512425B2 JP H0512425 B2 JPH0512425 B2 JP H0512425B2 JP 61154570 A JP61154570 A JP 61154570A JP 15457086 A JP15457086 A JP 15457086A JP H0512425 B2 JPH0512425 B2 JP H0512425B2
Authority
JP
Japan
Prior art keywords
atomic
alloy
amorphous
alloys
methanol
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 - Lifetime
Application number
JP61154570A
Other languages
Japanese (ja)
Other versions
JPS6311647A (en
Inventor
Koji Hashimoto
Asahi Kawashima
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yanmar Co Ltd
Original Assignee
Yanmar Diesel Engine Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yanmar Diesel Engine Co Ltd filed Critical Yanmar Diesel Engine Co Ltd
Priority to JP61154570A priority Critical patent/JPS6311647A/en
Publication of JPS6311647A publication Critical patent/JPS6311647A/en
Publication of JPH0512425B2 publication Critical patent/JPH0512425B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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  • Inert Electrodes (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

産業上の利用分野 本発明は、例えば、メタノール、ホルムアルデ
ヒド、ギ酸等のメタノール系燃料を用いる燃料電
池のための燃料極として好適であつて、少なくと
も一部、非晶質相を含むと共に、表面活性化処理
を施してなる電極活性が高く、且つ、耐食性にす
ぐれる低廉な非晶質合金に関する。 従来の技術 従来、メタノール系燃料電池用電極として、白
金微粉末を金網や多孔質炭素板上に塗布してなる
ものが知られているが、高価な白金を多量に用い
るために、高価とならざるを得ず、また、使用中
に活性の低下が大きい等の問題を有する。 他方、近年、非晶質合金は注目を集めている。
従来より知られている通常の合金は、固体状態で
は結晶化しているが、合金組成を限定して、溶融
状態から超急冷して凝固させる等、固体形成の過
程においいて原子配列に長周期的規則性をもたせ
ない方法を適用することによつて、結晶構造をも
つことになしに、液体に類似した非晶質構造を有
することとなる。このような合金は、非晶質合金
と称されており、多くは、過飽和固溶体の均一な
単相合金であつて、従来の通常の実用金属に比べ
て著しく高い強度を有し、且つ、組成に応じて異
常に高い耐食性をはじめ、種々の特異な特性を示
す。また、組成が合金全体を非晶質相とし得ない
場合であつても、通常の非晶質合金の製造法を適
用して製造した合金は、固溶限が拡大した過飽和
固溶体であつて、非晶質合金に準じたすぐれた特
性を有している。 本発明者らは、既に、このような非晶質合金の
すぐれた特性を活用して、パラジウムを主成分と
する非晶質合金に表面活性化処理を施してなるメ
タノール系燃料電池燃料極用表面活性化非晶質合
金を得ているが(特願昭57−12561号)、尚高価で
ある。 更に、本発明者らは、水溶液を電解して、酸素
及び塩素を発生させる電極を得るために、非晶質
合金を用いる研究を行なつて、電極活性を担う白
金族元素を少量しか含まない非晶質合金或いは過
飽和固溶体合金であつても、これらの合金が白金
族金属が均一に分散した合金であることを活用し
て、白金族金属以外の合金元素を合金表面から選
択溶解させる腐食溶液に浸漬する表面活性化処理
によつて、溶液電解用高活性電極を得ることがで
きることを見出している(特願昭60−169764号、
特願昭60−169765号、特願昭60−169766号及び特
願昭60−169767号)。 発明が解決しようとする問題点 そこで、本発明者らは、高価な白金の使用量を
低減しながら、メタノール系燃料の電気化学的酸
化に対して高い電極触媒活性を有すると共に、電
解条件下に高い耐食性を有するメタノール系燃料
電池電極用非晶質合金を得ることを目的として、
本発明を発明するに至つたものである。 問題点を解決するための手段 そして、本発明の発明者らは、上述した非晶質
合金の特性を活用して、燃料電池用燃料極を得る
べく鋭意研究した結果、原理的には、 (a) Ni及びCoより選ばれる少なくとも1種と、 (b) Ti及びZrより選ばれる少なくとも一種及
び/又はNb及びTaより選ばれる少なくとも一
種、とからなる非晶質合金、又は一部、非晶質
相を含む過飽和固溶体合金にメタノールの電解
酸化に活性なPtを添加し、更に、必要に応じ
てPtの作用を助ける種々の元素を添加してな
る合金に前記した表面活性化処理を施すことに
よつて、白金黒よりも高活性であつて、硫酸酸
性メタノール燃料溶液中で高い耐食性を備えた
低廉な燃料電池用燃料極を得ることができるこ
とを見出した。 すなわち、本発明のメタノール系燃料電池電極
用表面活性化非晶質合金の第1は、pt0.5〜20原
子%、Ti及びZrの1種又は2種20〜80原子%、
残部実質的にNi及びCoの1種又は2種10原子%
以上からなる。 第2は、Pt0.5〜20原子%、Ti及びZrの1種又
は2種20〜80原子%、Ru,Rh,Pd,Ir,Tl,
Si,Ge,Sn,Pb及びBiよりなる群から選ばれる
1種又は2種以上10原子%以下(但し、Pt10原
子%以下のときは、原子%でPtと同量以下)、残
部実質的にNi及びCoの1種又は2種10原子%以
上からなる。 第3は、Pt0.5〜20原子%、Nb及びTaの1種
又は2種20〜70原子%、残部実質的にNi及びCo
の1種又は2種からなる。 第4は、pt0.5〜20原子%、Nb及びTaの1種
又は2種20〜70原子%、Ru,Rh,Pd,Ir,Tl,
Si,Ge,Sn,Pb及びBiよりなる群から選ばれる
1種又は2種以上10原子%以下(但し、Pt10原
子%以下のときは、原子%でPtと同量以下)、残
部実質的にNi及びCoの1種又は2種10原子%以
上からなる。 第5は、Pt0.5〜20原子%、Nb及びTaの1種
又は2種70原子%以下とTi及びZrの1種又は2
種との合計量20〜80原子%(上記Nb及びTaの1
種又は2種の量を含む。)、残部実質的にNi及び
Coの1種又は2種10原子%以上からなる。 第6は、Pt0.5〜20原子%、Nb及びTaの1種
又は2種70原子%以下とTi及びZrの1種又は2
種との合計量20〜80原子%(上記Nb及びTaの1
種又は2種の量を含む。)、Ru,Rh,Pd,Ir,
Tl,Si,Ge,Sn,Pb及びBiよりなる群から選ば
れる1種又は2種以上10原子%以下(但し、
Pt10原子%以下のときは、原子%でPtと同量以
下)、残部実質的にNi及びCoの1種又は2種10原
子%以上からなる。第1表に、これら第1ないし
第6の発明の構成元素及び含有率を示す。 上記した組成の合金を溶融超急冷凝固させ、或
いは平均組成が上記と同じ混合物をターゲツトと
してスパツターデポジシヨンを行なう等、非晶質
合金を製造する従来より知られている種々の方法
Industrial Application Field The present invention is suitable as a fuel electrode for a fuel cell using methanol fuel such as methanol, formaldehyde, formic acid, etc., which contains at least a portion of an amorphous phase, and which has a surface active surface. The present invention relates to an inexpensive amorphous alloy that has been subjected to chemical treatment and has high electrode activity and excellent corrosion resistance. Conventional technology Electrodes for methanol-based fuel cells have been known in which fine platinum powder is coated on a wire mesh or porous carbon plate, but since a large amount of expensive platinum is used, it is not expensive. Unavoidably, there are also problems such as a large decrease in activity during use. On the other hand, amorphous alloys have been attracting attention in recent years.
Conventionally known conventional alloys are crystallized in the solid state, but in the process of solid formation, the atomic arrangement has a long periodicity, such as by limiting the alloy composition and solidifying it by ultra-rapid cooling from the molten state. By applying a method that does not provide regularity, an amorphous structure similar to a liquid can be obtained without having a crystalline structure. Such alloys are called amorphous alloys, and most of them are homogeneous single-phase alloys of supersaturated solid solutions, and have significantly higher strength than conventional ordinary practical metals, and have a composition of It exhibits various unique properties, including abnormally high corrosion resistance depending on the situation. Furthermore, even if the composition does not allow the entire alloy to be in an amorphous phase, the alloy produced by applying a normal amorphous alloy production method is a supersaturated solid solution with an expanded solid solubility limit. It has excellent properties similar to those of amorphous alloys. The present inventors have already taken advantage of the excellent properties of such amorphous alloys to create a fuel electrode for methanol fuel cells, which is made by surface-activating an amorphous alloy mainly composed of palladium. A surface-activated amorphous alloy has been obtained (Japanese Patent Application No. 12561/1983), but it is still expensive. Furthermore, in order to obtain an electrode that generates oxygen and chlorine by electrolyzing an aqueous solution, the present inventors conducted research using an amorphous alloy, and found that it contains only a small amount of platinum group elements responsible for electrode activity. A corrosive solution that selectively dissolves alloying elements other than platinum group metals from the alloy surface, taking advantage of the fact that these alloys are alloys in which platinum group metals are uniformly dispersed, even if they are amorphous alloys or supersaturated solid solution alloys. It has been discovered that a highly active electrode for solution electrolysis can be obtained by surface activation treatment by immersion in water (Japanese Patent Application No. 60-169764,
(Japanese Patent Application No. 60-169765, Japanese Patent Application No. 169766, and Japanese Patent Application No. 169767). Problems to be Solved by the Invention Therefore, the present inventors have developed a method that has high electrocatalytic activity for electrochemical oxidation of methanol-based fuels while reducing the amount of expensive platinum used, and which can be used under electrolytic conditions. With the aim of obtaining an amorphous alloy for methanol fuel cell electrodes with high corrosion resistance,
This led to the invention of the present invention. Means for Solving the Problems The inventors of the present invention have conducted intensive research to obtain a fuel electrode for fuel cells by utilizing the characteristics of the amorphous alloy described above, and as a result, in principle, ( a) an amorphous alloy consisting of at least one selected from Ni and Co; (b) at least one selected from Ti and Zr and/or at least one selected from Nb and Ta; Adding Pt, which is active in the electrolytic oxidation of methanol, to a supersaturated solid solution alloy containing a solid phase, and further adding various elements that assist the action of Pt as necessary, and subjecting the alloy to the above-mentioned surface activation treatment. It has been found that it is possible to obtain an inexpensive fuel electrode for fuel cells that has higher activity than platinum black and has high corrosion resistance in a sulfuric acid acidic methanol fuel solution. That is, the first surface-activated amorphous alloy for methanol-based fuel cell electrodes of the present invention contains 0.5 to 20 atomic % of pt, 20 to 80 atomic % of one or both of Ti and Zr,
The remainder is essentially 10 atom% of one or both of Ni and Co.
It consists of the above. The second is 0.5 to 20 at% of Pt, 20 to 80 at% of one or both of Ti and Zr, Ru, Rh, Pd, Ir, Tl,
One or more selected from the group consisting of Si, Ge, Sn, Pb and Bi, up to 10 atomic % (however, when Pt is 10 atomic % or less, the atomic % is the same amount or less as Pt), and the remainder is substantially Consists of 10 atomic % or more of one or both of Ni and Co. The third is 0.5 to 20 at% of Pt, 20 to 70 at% of one or both of Nb and Ta, and the balance is essentially Ni and Co.
Consisting of one or two types. The fourth is pt0.5-20 at%, 20-70 at% of one or both of Nb and Ta, Ru, Rh, Pd, Ir, Tl,
One or more selected from the group consisting of Si, Ge, Sn, Pb and Bi, up to 10 atomic % (however, when Pt is 10 atomic % or less, the atomic % is the same amount or less as Pt), and the remainder is substantially Consists of 10 atomic % or more of one or both of Ni and Co. Fifth, 0.5 to 20 at% of Pt, 70 at% or less of one or two of Nb and Ta, and one or two of Ti and Zr.
20 to 80 atomic% in total with seeds (1% of the above Nb and Ta)
Contains a quantity of a species or two species. ), the remainder substantially Ni and
Consists of 10 atomic % or more of one or two types of Co. The sixth is 0.5 to 20 at% of Pt, 70 at% or less of one or two of Nb and Ta, and one or two of Ti and Zr.
20 to 80 atomic% in total with seeds (1% of the above Nb and Ta)
Contains a quantity of a species or two species. ), Ru, Rh, Pd, Ir,
One or more selected from the group consisting of Tl, Si, Ge, Sn, Pb, and Bi and up to 10 atomic % (however,
When the amount of Pt is 10 atomic % or less, the amount in atomic % is the same as that of Pt), and the remainder substantially consists of 10 atomic % or more of one or both of Ni and Co. Table 1 shows the constituent elements and content rates of these first to sixth inventions. Various conventionally known methods for manufacturing amorphous alloys include melting and ultra-rapidly solidifying an alloy having the above composition, or performing sputter deposition using a mixture having the same average composition as above as a target.

【表】 によつて得られる非晶質合金は、前記元素が均一
に固溶した単相合金である。また、同様に、少な
くとも一部、非晶質相を含む過飽和固溶体合金
も、前記元素の分布が極めて均一な合金である。
元来、特定の電気化学反応に対する選択的電極触
媒活性とその反応条件に耐える高耐食性を備えた
合金を得るには、有効な元素を所定量添加するこ
とが必要である。しかし、通常の方法によつて製
造される結晶質合金の場合は、多種多量の元素を
添加すると、しばしば化学的性質の異なる多相構
造を形成する結果、期待する電極活性が得られな
いのみならず、耐食性や機械的強度も劣る。これ
に対して、本発明の非晶質合金、又は少なくとも
一部、非晶質相を含む過飽和固溶体合金は、構成
元素が局在することを許さない非晶質合金製造に
よつて製造されるために、組成の均一性が極めて
高く、必要な電極触媒活性及び耐食性を備えてい
る。 次に、本発明の合金において、化学成分を限定
する理由について説明する。 Ptは、メタノール系燃料電池の電気化学的酸
化活性を担う必須元素であつて、0.5原子%未満
では十分な活性が得られず、一方、20原子%を越
えて添加しても、電極活性の向上が著しくなく、
且つ、電極を高価にする。従つて、本発明におい
ては、Ptは0.5〜20原子%の範囲とする。 Ti,Zr,Nb及びTaよりなる群から選ばれる
いずれか1種又は2種以上の元素は、Ni及びCo
の1種又は2種と共存するとき、これに前述した
種々の非晶質合金の製造法を適用することによつ
て、非晶質合金を得ることができる。 Ni及びCoの1種又は2種10原子%以上と共存
する元素がTi及びZrの1種又は2種である場合
(前記第1及び第2の合金)は、Ti及びZrの1種
又は2種が20〜80原子%のとき、非晶質構造を容
易に得ることができる。同様に、Ni及びCoの1
種又は2種と共存する元素がNb及びTaの1種又
は2種である場合(前記第3及び第4の合金)
は、Nb及びTaの1種又は2種が20〜70原子%の
とき、非晶質構造を容易に得ることができる。 Ti及びZrの1種又は2種と、Nb及びTaの1
種又は2種とが共にNi及びCoの1種又は2種10
原子%以上と共存する場合(前記第5及び第6の
合金)は、Nb及びTaの1種又は2種を70原子%
とTi及びZrの1種又は2種との合計量(上記Nb
及びTaの1種又は2種の量を含む。)を20〜80原
子%とするとき、非晶質構造を容易に得ることが
できる。 本発明においては、合金は、Ni及びCoの1種
又は2種10原子%以上と、Ti及びZrの1種又は
2種及びNb及びTaの1種又は2種と共に、Ru,
Rh,Pd,Ir,Tl,Si,Ge,Sn,Pb及びBiより
なる群から選ばれる少なくとも1種を含むことが
できる。(前記第2,4及び6の合金)。 Ru,Rh,Pd,Ir,Tl,Si,Ge,Sn,Pb及び
Biは、Ptの効果を助けて活性を向上させるが、
多量の添加は有効ではない。従つて、本発明にお
いては、これらの元素の1種又は2種以上の添加
量は総量にて10原子%以下とし、特に、Pt量が
10原子%以下のときは、原子%でPt量と同量以
下とすることが必要である。 Ni及びCoの1種又は2種は、前述したように、
Ti,Zr,Nb及びTaの1種又は2種以上と共存
下に非晶質構造を形成させるための元素である。
Ni及びCoをPtにて置換することも、非晶質構造
の形成には有効ではあるが、しかし、Ni及びCo
の全量をPtにて置換するときは、非晶質構造の
形成が困難となる。従つて、本発明においては、
Ni及びCoの1種又は2種の添加量は、10原子%
以上とすることが必要である。 本発明による合金は、V,Mo及びWの1種又
は2種以上を3原子%以下の範囲で含んでいて
も、また、Cr及びFeの1種又は2種を10原子%
以下の範囲で含んでいても、メタノール燃料電池
用電極としての機能に何ら支障を与えない。 B,C,P等の半金属元素は、従来、非晶質構
造の形成に有効であることが知られているが、本
発明においては、これらの元素を多量に添加する
ときは、電極活性が低下する。しかし、これらの
元素も、その添加量が7原子%程度までであれ
ば、非晶質構造の形成に有効である一方、電極活
性に有害な影響を与えないので、本発明において
は、上記半金属元素は、7原子%までの添加は許
容される。 次に、燃料電池電極として十分な触媒活性を有
するためには、電気化学的に有効な表面を増大さ
せると共に、電極反応の活性点として作用する
Ptを合金表面に集めることが必要である。この
ために、本発明においては、非晶質合金又は少な
くとも非晶質相を一部含む過飽和固溶体合金をフ
ツ酸に浸漬する表面活性化処理を施す。フツ酸の
濃度及び温度は、対象とする非晶質合金や、少な
くとも非晶質相を一部含む過飽和固溶体合金の組
成に応じて、適宜に選ばれる。 本発明の非晶質合金又は少なくとも非晶質相を
一部含む過飽和固溶体合金をフツ酸に浸漬する
と、このような合金は均一性が高いために、均一
に分布したPt或いはその他の白金族元素上で盛
んに水素が発生し、この結果、白金族元素よりも
卑であるNi,Co,Ti,Zr,Nb,Ta等の元素が
選択的に合金表面から溶解し、合金表面が微細化
して、黒色を帯びると共に、電極活性を担うPt
とこれを助ける他の白金族元素をはじめとする元
素が合金表面に濃縮される。従つて、表面活性化
処理は、表面が黒色を帯びた時点をもつて終了と
すればよい。 尚、通常の方法によつて製造された結晶質合金
の場合は、その平均組成が本発明で規定する組成
と同じであつても、多相構造を有して、合金元素
が局在化しているために、上記表面活性化処理を
施しても、水素の発生が観測されず、また、Ni,
Co,Ti,Zr,Nb,Ta等の元素の選択溶解も起
こり難いために、表面の活性が向上しない。更
に、通常の方法によつて製造された不均一な結晶
質合金は、耐食性が低いために、メタノール系燃
料を含む酸に耐えない。 しかしながら、本発明による非晶質合金又は少
なくとも一部、非晶質相を含む過飽和固溶体合金
は、成分元素が均一に分布しているために、上記
表面活性化処理によつて、フツ酸中にNi,Co,
Ti,Zr,Nb,Ta等の元素が均一に溶解し、有
効表面積が著しく増大すると共に、電極活性を担
うPt及びPtの作用を助ける元素が表面に濃縮さ
れ、十分に活性化することができる。このように
して、本発明による合金は、メタノール系燃料電
池用電極として電極活性及び耐食性に著しくすぐ
れるのである。 本発明による非晶質合金及び少なくとも一部非
晶質相を含む過飽和固溶体合金は、溶体合金を超
急冷凝固させて、非晶質合金を製造するために広
く用いられている種々の方法によつて製造するこ
とができる。 本発明の非晶質合金及び少なくとも一部非晶質
相を含む過飽和固溶体合金を製造するための装置
の一例を第1図に示す。 この装置は、破線で示す真空容器内に置かれて
いる。垂直な石英管2の下端にノズル3が取り付
けられており、高速回転せしめられるロール7が
上記ノズルの下方に配設されている。このロール
は、モーター6によつて駆動される。また、石英
管の周囲には、原料合金4を加熱溶融するための
ヒーター5が配設されており、石英管の上端に
は、原料合金4と溶融した原料合金を吹き出すた
めの不活性ガスの入口1が設けられている。 この装置によつて本発明の非晶質合金又は少な
くとも一部非晶質相を含む過飽和固溶体合金を製
造するには、先ず、装置内を10-5Torr程度に減
圧し、次いで、アルゴンのような不活性ガスを1
気圧程度まで装置内に導入する。この不活性ガス
雰囲気で石英管中の所定の組成の原料合金をヒー
ターにて加熱溶融させる。この加熱溶融した合金
を0.4〜2Kg/cm2程度の不活性ガスによつてノズ
ルからジエツトとして吹き出し、1000〜
10000rpm程度で高速回転しているロールの外表
面に衝突させると、溶融合金の熱はロールによつ
て急速に奪われて、リボン状の非晶質合金又は少
なくとも一部非晶質相を含む過飽和固溶体合金を
得ることができる。このようにして得られる合金
は、例えば、その厚さ0.005〜0.1mm、幅0.5〜10
mm、長さ数mm乃至数十mである。 実施例 以下に本発明を実施例に基づいて説明する。 実施例 1 市販金属を所定の割合で混合し、Ar雰囲気の
高周波炉で加熱溶融し、原料合金とした。また
Ti,Zr,Nb及びTaのうち、Nb,Taを含まない
合金は、アルゴンアーク溶融して原料合金とし
た。これらの原料合金を第1図に示した装置を用
い、再溶融急冷することによつて、非晶質合金及
び非晶質相を一部含む過飽和固溶体合金を製造し
た。これらの合金の化学組成を第1表に示す。非
晶質相の形成は、X線回折により確認し、多くの
合金は非晶質合金特有のハローパターンを示し
た。しかし、なかにはハローパターンに結晶相に
基づく鋭い回折線が重畳しており、非晶質相と結
晶相の混合構造であるが、非晶質相が存在するこ
とから、これらの合金は過飽和固溶体であること
が判明した。 これらの合金はメタノール系燃料を電気化学的
に酸化する硫酸酸性環境で、十分な耐食性をもつ
ことを確認するため、これらの合金をシクロヘキ
サン中、SiC紙1000番まで研磨した後、0.5M硫酸
溶液中及び0.5M H2SO4−1MCH3OH溶液中でア
ノード分極曲線を測定した。一例を第2図に示
す。0.5M硫酸中で観測される負の電位領域の電
流は、水素発生に費やされた負の電流を符号に変
えて記したものである。0.5MH2SO4中では、広
い電位領域にわたり10-2Am-2以上の電流が観測
されず、この合金が極めて耐食性の高い合金であ
ることを示している。尚、1.1V(SCE)付近から
認められる電流の上昇は、酸素発生に基づくもの
である。 0.5M H2SO4−1M CH3OH溶液中では、0.4V
(SCE)付近から10-2Am-2の桁のアノード電流が
認められる。これはメタノールの酸化のための電
流である。しかし、この桁のメタノール酸化電流
では、活性が低すぎて、電極材料としては使うこ
とができない。 電極活性を向上させるために、市販46%HF溶
液に数分浸漬する表面活性化処理を行なつた。
尚、Ti,Zr,Nb,Taのうち、Nb,Taを含まな
い合金の場合、46%HF溶液では活性化に要する
時間が短く、制御が困難であつたので、4.6%HF
溶液に数分浸漬することによつて、表面活性化処
理を行なつた。 0.5M H2SO4−1M CH3OH溶液中で測定した
表面活性化非晶質合金のアノード分極曲線を白金
黒のアノード分極曲線と比較して第3図に示す。
本発明の非晶質合金は、白金黒よりメタノールの
酸化に対して高活性であるため、白金黒より低い
電位からメタノールの酸化のための電流が観測さ
れ、また同一電位では、本発明の非晶質合金が比
較例の白金黒より低い電位からメタノールの酸化
のための高い電流密度を示している。 第3表に、表面活性化非晶質合金及び非晶質相
を一部含む過飽和固溶体合金について、0.5MH2
SO4−1M CH3OH溶液中で定電位分極を行なつ
た際に観測された電流密度を白金黒及び平滑白金
で観測された電流密度と比較して示す。いずれの
合金の電流も白金黒より大きいか、又はほぼ同等
の大きさである。従つて、表面活性化処理を施し
たこれらの合金は、白金含量が極めて低いにもか
かわらず、メタノールの電気化学的酸化に対して
白金黒と同様、或いは一層すぐれた電極触媒活性
を備えている。 実施例 2 実施例1と同様にして製造した非晶質合金及び
一部非晶質相を含む過飽和固溶体合金に実施例1
に記したように表面活性化処理を施し、ホルムア
ルデビドの電気化学的酸化に対する触媒活性を調
べた。 第4表に、表面活性化非晶質合金及び非晶質相
を一部含む過飽和固溶体合金について、0.5MH2
SO4−1M HCHO溶液中で定電位分極を行つた際
に観測された電流密度を白金黒及び平滑白金で観
測された電流密度と比較して示す。いずれの合金
の電流密度も白金黒より大きい。従つて、表面活
性化処理を施したこれらの合金は、白金含量が極
めて低いにもかかわらず、ホルムアルデビドの電
気化学的酸化に対して白金黒よりすぐれた電極触
媒活性を備えている。 実施例 3 実施例1と同様にして製造した非晶質合金及び
一部非晶質相を含む過飽和固溶体合金に実施例1
に記したように表面活性化処理を施し、ギ酸の電
気化学的酸化に対する触媒活性を調べた。 第5表に、表面活性化非晶質合金及び非晶質相
を一部含む過飽和固溶体合金について、0.5MH2
SO4−1M HCOOH溶液中で定電位分極を行なつ
た際に観測された電流密度を白金黒及び平滑白金
で観測された電流密度と比較して示す。いずれの
合金の電流密度も白金黒より大きい。従つて、表
面活性化処理を施したこれらの合金は、白金含量
が極めて低いにもかかわらず、ギ酸の電気化学的
酸化に対して白金黒よりすぐれた電極触媒性を備
えている。
The amorphous alloy obtained by [Table] is a single-phase alloy in which the above elements are uniformly dissolved in solid solution. Similarly, a supersaturated solid solution alloy containing at least a portion of an amorphous phase is also an alloy in which the distribution of the above elements is extremely uniform.
Originally, in order to obtain an alloy with selective electrocatalytic activity for a specific electrochemical reaction and high corrosion resistance that can withstand the reaction conditions, it is necessary to add a certain amount of effective elements. However, in the case of crystalline alloys manufactured by conventional methods, when a large number of different elements are added, a multiphase structure with different chemical properties is often formed, and the expected electrode activity may not be obtained. Moreover, its corrosion resistance and mechanical strength are also inferior. In contrast, the amorphous alloy of the present invention, or the supersaturated solid solution alloy containing at least a portion of the amorphous phase, is produced by amorphous alloy production that does not allow the constituent elements to localize. Therefore, it has extremely high compositional uniformity and has the necessary electrocatalytic activity and corrosion resistance. Next, the reason for limiting the chemical components in the alloy of the present invention will be explained. Pt is an essential element responsible for the electrochemical oxidation activity of methanol fuel cells, and if it is less than 0.5 atom%, sufficient activity cannot be obtained, whereas if it is added in excess of 20 atom%, the electrode activity is There is no significant improvement,
Moreover, the electrodes become expensive. Therefore, in the present invention, Pt is contained in a range of 0.5 to 20 atomic %. Any one or more elements selected from the group consisting of Ti, Zr, Nb and Ta are Ni and Co.
When coexisting with one or both of these, an amorphous alloy can be obtained by applying the various amorphous alloy manufacturing methods described above to this. When the element coexisting with 10 atomic % or more of one or two of Ni and Co is one or two of Ti and Zr (the first and second alloys), one or two of Ti and Zr An amorphous structure can be easily obtained when the species is 20-80 at%. Similarly, 1 of Ni and Co
When the element coexisting with the species or two species is one or two of Nb and Ta (the third and fourth alloys)
When one or both of Nb and Ta are present in an amount of 20 to 70 atomic %, an amorphous structure can be easily obtained. One or two of Ti and Zr and one of Nb and Ta
The species or two species are both Ni and Co10
When Nb and Ta coexist at 70 atomic % or more (in the fifth and sixth alloys), one or both of Nb and Ta are present at 70 atomic %.
and one or two of Ti and Zr (the above Nb
and Ta. ) is 20 to 80 atomic %, an amorphous structure can be easily obtained. In the present invention, the alloy contains 10 atomic % or more of one or two of Ni and Co, one or two of Ti and Zr, and one or two of Nb and Ta, as well as Ru,
It can contain at least one member selected from the group consisting of Rh, Pd, Ir, Tl, Si, Ge, Sn, Pb, and Bi. (The second, fourth and sixth alloys). Ru, Rh, Pd, Ir, Tl, Si, Ge, Sn, Pb and
Bi helps the effect of Pt and improves its activity, but
Addition of large amounts is not effective. Therefore, in the present invention, the total amount of one or more of these elements added is 10 atomic % or less, and in particular, if the amount of Pt is
When it is 10 atomic % or less, it is necessary that the atomic % is equal to or less than the amount of Pt. As mentioned above, one or both of Ni and Co are
It is an element for forming an amorphous structure in coexistence with one or more of Ti, Zr, Nb, and Ta.
Although replacing Ni and Co with Pt is also effective for forming an amorphous structure,
When the entire amount of is replaced with Pt, it becomes difficult to form an amorphous structure. Therefore, in the present invention,
The amount of one or both of Ni and Co added is 10 atomic%
It is necessary to do the above. Even if the alloy according to the present invention contains one or more of V, Mo, and W in an amount of 3 atomic % or less, it also contains one or more of Cr and Fe in an amount of 10 atomic %.
Even if it is contained within the following range, it will not impede the function as an electrode for methanol fuel cells. Metalloid elements such as B, C, and P are conventionally known to be effective in forming an amorphous structure, but in the present invention, when adding a large amount of these elements, the electrode activity decreases. However, these elements are effective in forming an amorphous structure when added in amounts up to about 7 atomic percent, but do not have a detrimental effect on electrode activity. Addition of up to 7 atomic % of metal elements is permitted. Next, in order to have sufficient catalytic activity as a fuel cell electrode, it is necessary to increase the electrochemically effective surface and act as an active site for electrode reactions.
It is necessary to collect Pt on the alloy surface. For this purpose, in the present invention, an amorphous alloy or a supersaturated solid solution alloy containing at least a portion of an amorphous phase is subjected to a surface activation treatment by immersing it in hydrofluoric acid. The concentration and temperature of hydrofluoric acid are appropriately selected depending on the composition of the target amorphous alloy or the supersaturated solid solution alloy containing at least a portion of the amorphous phase. When an amorphous alloy of the present invention or a supersaturated solid solution alloy containing at least a portion of an amorphous phase is immersed in hydrofluoric acid, such alloys have a high degree of homogeneity, resulting in a uniform distribution of Pt or other platinum group elements. As a result, elements such as Ni, Co, Ti, Zr, Nb, and Ta, which are more base than platinum group elements, are selectively dissolved from the alloy surface, and the alloy surface becomes finer. , Pt has a black color and is responsible for electrode activity.
And supporting elements, including other platinum group elements, are concentrated on the alloy surface. Therefore, the surface activation treatment may be completed when the surface becomes blackish. In addition, in the case of a crystalline alloy manufactured by a normal method, even if its average composition is the same as the composition specified in the present invention, it has a multiphase structure and the alloying elements are localized. Therefore, even if the above surface activation treatment is performed, hydrogen generation is not observed.
Selective dissolution of elements such as Co, Ti, Zr, Nb, and Ta is also difficult to occur, so surface activity is not improved. Additionally, heterogeneous crystalline alloys produced by conventional methods do not withstand acids, including methanol-based fuels, due to their low corrosion resistance. However, since the amorphous alloy according to the present invention or the supersaturated solid solution alloy containing at least a portion of the amorphous phase has a uniform distribution of component elements, it can be dissolved in hydrofluoric acid by the above surface activation treatment. Ni, Co,
Elements such as Ti, Zr, Nb, Ta, etc. are uniformly dissolved, and the effective surface area is significantly increased. Pt, which is responsible for electrode activity, and elements that help Pt are concentrated on the surface, allowing for sufficient activation. . In this way, the alloy according to the present invention exhibits outstanding electrode activity and corrosion resistance as an electrode for methanol fuel cells. Amorphous alloys and supersaturated solid solution alloys containing at least a partially amorphous phase according to the present invention can be prepared by ultra-rapid solidification of solution alloys by various methods widely used to produce amorphous alloys. It can be manufactured by An example of an apparatus for producing an amorphous alloy of the present invention and a supersaturated solid solution alloy containing at least a portion of an amorphous phase is shown in FIG. The device is placed in a vacuum vessel, indicated by dashed lines. A nozzle 3 is attached to the lower end of a vertical quartz tube 2, and a roll 7 rotated at high speed is disposed below the nozzle. This roll is driven by a motor 6. Further, a heater 5 for heating and melting the raw material alloy 4 is arranged around the quartz tube, and at the upper end of the quartz tube, an inert gas is provided for blowing out the raw material alloy 4 and the molten raw material alloy. An entrance 1 is provided. In order to produce the amorphous alloy of the present invention or a supersaturated solid solution alloy containing at least a portion of an amorphous phase using this apparatus, first, the pressure inside the apparatus is reduced to about 10 -5 Torr, and then the pressure is 1 inert gas
Introduce it into the device to about atmospheric pressure. In this inert gas atmosphere, the raw material alloy of a predetermined composition in the quartz tube is heated and melted using a heater. This heated and molten alloy is blown out as a jet from a nozzle with an inert gas of about 0.4 to 2 kg/ cm2 , and
When the molten alloy collides with the outer surface of a roll rotating at a high speed of about 10,000 rpm, the heat of the molten alloy is rapidly removed by the roll, resulting in a ribbon-shaped amorphous alloy or a supersaturated alloy containing at least a portion of the amorphous phase. A solid solution alloy can be obtained. The alloy thus obtained has a thickness of, for example, 0.005 to 0.1 mm and a width of 0.5 to 10 mm.
mm, and the length is several mm to several tens of meters. Examples The present invention will be described below based on examples. Example 1 Commercially available metals were mixed at a predetermined ratio and heated and melted in a high frequency furnace in an Ar atmosphere to obtain a raw material alloy. Also
Among Ti, Zr, Nb, and Ta, alloys not containing Nb and Ta were melted in an argon arc to obtain raw material alloys. These raw material alloys were remelted and rapidly cooled using the apparatus shown in FIG. 1 to produce an amorphous alloy and a supersaturated solid solution alloy partially containing an amorphous phase. The chemical compositions of these alloys are shown in Table 1. The formation of an amorphous phase was confirmed by X-ray diffraction, and many alloys showed a halo pattern characteristic of amorphous alloys. However, in some halo patterns, sharp diffraction lines based on the crystalline phase are superimposed, indicating a mixed structure of amorphous and crystalline phases, but since the amorphous phase exists, these alloys are not supersaturated solid solutions. It turns out that there is something. To confirm that these alloys have sufficient corrosion resistance in a sulfuric acid acidic environment that electrochemically oxidizes methanol-based fuel, these alloys were polished in cyclohexane to No. 1000 SiC paper and then polished in a 0.5M sulfuric acid solution. The anodic polarization curves were measured in medium and 0.5MH2SO4-1MCH3OH solutions . An example is shown in FIG. The current in the negative potential region observed in 0.5M sulfuric acid is the negative current consumed for hydrogen generation with its sign changed. In 0.5MH 2 SO 4 , no current of 10 −2 Am −2 or more was observed over a wide potential range, indicating that this alloy has extremely high corrosion resistance. Note that the increase in current observed from around 1.1V (SCE) is based on oxygen generation. 0.4V in 0.5MH 2 SO 4 −1M CH 3 OH solution
An anode current on the order of 10 -2 Am -2 is observed from around (SCE). This is the current for methanol oxidation. However, at methanol oxidation currents of this order, the activity is too low and it cannot be used as an electrode material. In order to improve the electrode activity, a surface activation treatment was performed by immersing the electrode in a commercially available 46% HF solution for several minutes.
In addition, in the case of alloys that do not contain Nb or Ta among Ti, Zr, Nb, and Ta, the time required for activation with 46% HF solution was short and control was difficult, so 4.6% HF solution was used.
Surface activation treatment was performed by immersing it in a solution for several minutes. The anodic polarization curve of the surface activated amorphous alloy measured in a 0.5MH 2 SO 4 -1M CH 3 OH solution is shown in FIG. 3 in comparison with the anodic polarization curve of platinum black.
Since the amorphous alloy of the present invention has higher activity for methanol oxidation than platinum black, a current for methanol oxidation is observed from a lower potential than platinum black, and at the same potential, the non-crystalline alloy of the present invention The crystalline alloy exhibits higher current densities for methanol oxidation from lower potentials than the comparative platinum black. Table 3 shows 0.5MH 2 for surface activated amorphous alloys and supersaturated solid solution alloys containing some amorphous phase.
The current density observed during potentiostatic polarization in SO 4 -1M CH 3 OH solution is shown in comparison with the current density observed in platinum black and smooth platinum. The current for both alloys is greater than or approximately the same magnitude as platinum black. Therefore, these surface-activated alloys have similar or better electrocatalytic activity than platinum black for the electrochemical oxidation of methanol, despite their extremely low platinum content. . Example 2 Example 1 was applied to an amorphous alloy produced in the same manner as in Example 1 and a supersaturated solid solution alloy containing a partially amorphous phase.
The surface activation treatment was performed as described in , and the catalytic activity for electrochemical oxidation of formaldebide was investigated. Table 4 shows 0.5MH 2 for surface activated amorphous alloys and supersaturated solid solution alloys containing some amorphous phase.
The current density observed during potentiostatic polarization in SO 4 -1M HCHO solution is shown in comparison with the current density observed in platinum black and smooth platinum. The current density of both alloys is higher than that of platinum black. These surface-activated alloys therefore have better electrocatalytic activity than platinum black for the electrochemical oxidation of formaldebide, despite their extremely low platinum content. Example 3 Example 1 was applied to an amorphous alloy produced in the same manner as in Example 1 and a supersaturated solid solution alloy containing a partially amorphous phase.
Surface activation treatment was performed as described in , and the catalytic activity for electrochemical oxidation of formic acid was investigated. Table 5 shows 0.5MH 2 for surface-activated amorphous alloys and supersaturated solid solution alloys containing some amorphous phase.
The current density observed during potentiostatic polarization in SO 4 -1M HCOOH solution is shown in comparison with the current density observed in platinum black and smooth platinum. The current density of both alloys is higher than that of platinum black. These surface-activated alloys therefore have better electrocatalytic properties than platinum black for the electrochemical oxidation of formic acid, despite their extremely low platinum content.

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】 発明の効果 以上に詳述したように、本発明のメタノール系
燃料電池用表面活性化処理非晶質合金は、高価な
白金の添加量が極めて低いにもかかわらず、メタ
ノール系燃料電池の電気化学的酸化に対して極め
て高い電極触媒活性を有すると共に、電解条件下
で高耐食性を有する。 しかも、本発明によるこのような合金は、既に
広く知られている非晶質合金の製造の技術のいず
れによつても製造することができるので、何ら特
殊な装置を必要としない。
[Table] Effects of the Invention As detailed above, the surface-activated amorphous alloy for methanol fuel cells of the present invention can be used in methanol fuel cells even though the amount of expensive platinum added is extremely low. It has extremely high electrocatalytic activity for electrochemical oxidation of , and has high corrosion resistance under electrolytic conditions. Moreover, such an alloy according to the present invention can be manufactured by any of the already widely known techniques for manufacturing amorphous alloys, and therefore does not require any special equipment.

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

第1図は本発明の合金を製造するための装置の
一例を示す断面図、第2図は0.5M H2SO4及び
0.5M H2SO4−1M CH3OH中において測定した
非晶質Ni−40Nb−3Pt合金の分極曲線、第3図
は表面活性化処理を施した非晶質Ni−40Nb−
2.7Pt−0.3Ru合金及び比較のための白金黒を試料
としてそれぞれ用いて、0.5M H2SO4−1MCH3
OH中において測定した分極曲線である。
Figure 1 is a cross-sectional view showing an example of an apparatus for producing the alloy of the present invention, and Figure 2 is a cross- sectional view showing an example of an apparatus for producing the alloy of the present invention.
Polarization curve of amorphous Ni−40Nb−3Pt alloy measured in 0.5MH 2 SO 4 −1M CH 3 OH, Figure 3 shows amorphous Ni−40Nb− subjected to surface activation treatment.
Using 2.7Pt−0.3Ru alloy and platinum black for comparison as samples, 0.5MH 2 SO 4 −1MCH 3
This is a polarization curve measured in OH.

Claims (1)

【特許請求の範囲】 1 Pt0.5〜20原子%、Ti及びZrの1種又は2種
20〜80原子%、残部実質的にNi及びCoの1種又
は2種10原子%以上からなることを特徴とするメ
タノール系燃料電池電極用表面活性化非晶質合
金。 2 Pt0.5〜20原子%、Ti及びZrの1種又は2種
20〜80原子%、Ru,Rh,Pd,Ir,Tl,Si,Ge,
Sn,Pb及びBiよりなる群から選ばれる1種又は
2種以上10原子%以下(但し、Pt10原子%以下
のときは、原子%でPtと同量以下)、残部実質的
にNi及びCoの1種又は2種10原子%以上からな
ることを特徴とするメタノール系燃料電池電極用
表面活性化非晶質合金。 3 Pt0.5〜20原子%、Nb及びTaの1種又は2
種20〜70原子%、残部実質的にNi及びCoの1種
又は2種からなることを特徴とするメタノール系
燃料電池電極用表面活性化非晶質合金。 4 Pt0.5〜20原子%、Nb及びTaの1種又は2
種20〜70原子%、Ru,Rh,Pd,Ir,Tl,Si,
Ge,Sn,Pb及びBiよりなる群から選ばれる1種
又は2種以上10原子%以下(但し、Pt10原子%
以下のときは、原子%でPtと同量以下)、残部実
質的にNi及びCoの1種又は2種10原子%以上か
らなることを特徴とするメタノール系燃料電池電
極用表面活性化非晶質合金。 5 Pt0.5〜20原子%、Nb及びTaの1種又は2
種70原子%以下とTi及びZr1種又は2種との合計
量20〜80原子%(上記Nb及びTaの1種又は2種
の量を含む。)、残部実質的にNi及びCoの1種又
は2種10原子%以上からなることを特徴とするメ
タノール系燃料電池電極用表面活性化非晶質合
金。 6 Pt0.5〜20原子%、Nb及びTaの1種又は2
種70原子%以下とTi及びZrの1種又は2種との
合計量20〜80原子%(上記Nb及びTaの1種又は
2種の量を含む。)、Ru,Rh,Pd,Ir,Tl,Si,
Ge,Sn,Pb及びBiよりなる群から選ばれる1種
又は2種以上10原子%以下(但し、Pt10原子%
以下のときは、原子%でPtと同量以下)、残部実
質的にNi及びCoの1種又は2種10原子%以上か
らなることを特徴とするメタノール系燃料電池電
極用表面活性化非晶質合金。
[Claims] 1. 0.5 to 20 atomic % of Pt, one or two of Ti and Zr.
1. A surface-activated amorphous alloy for methanol-based fuel cell electrodes, characterized in that it comprises 20 to 80 atomic %, and the remainder substantially 10 atomic % or more of one or both of Ni and Co. 2 Pt0.5-20 at%, one or two of Ti and Zr
20-80 atomic%, Ru, Rh, Pd, Ir, Tl, Si, Ge,
One or more selected from the group consisting of Sn, Pb and Bi, up to 10 atomic % (however, when Pt is 10 atomic % or less, the atomic % is the same amount or less as Pt), and the remainder is substantially Ni and Co. A surface-activated amorphous alloy for a methanol-based fuel cell electrode, characterized by comprising 10 atomic % or more of one or two types. 3 Pt0.5-20 atomic%, one or two of Nb and Ta
1. A surface-activated amorphous alloy for methanol-based fuel cell electrodes, characterized in that the surface-activated amorphous alloy is comprised of 20 to 70 atomic % of seeds, and the remainder substantially of one or both of Ni and Co. 4 Pt0.5-20 atomic%, one or two of Nb and Ta
Species 20-70 atomic%, Ru, Rh, Pd, Ir, Tl, Si,
One or more selected from the group consisting of Ge, Sn, Pb and Bi, up to 10 atomic % (However, Pt10 atomic %
In the following cases, the surface-activated amorphous material for methanol-based fuel cell electrodes is characterized in that the remainder consists essentially of at least 10 at % of one or both of Ni and Co. quality alloy. 5 Pt0.5-20 atomic%, one or two of Nb and Ta
A total amount of 70 at % or less of species and one or two types of Ti and Zr is 20 to 80 at % (including the amount of one or two of the above Nb and Ta), the balance is substantially one of Ni and Co or a surface-activated amorphous alloy for methanol-based fuel cell electrodes, characterized by comprising 10 atomic % or more of two types. 6 Pt0.5 to 20 atomic%, one or two of Nb and Ta
A total amount of 70 at % or less of species and one or two of Ti and Zr (including the amount of one or two of the above Nb and Ta), Ru, Rh, Pd, Ir, Tl, Si,
One or more selected from the group consisting of Ge, Sn, Pb and Bi, up to 10 atomic % (However, Pt10 atomic %
In the following cases, the surface-activated amorphous material for methanol-based fuel cell electrodes is characterized in that the remainder consists essentially of at least 10 at % of one or both of Ni and Co. quality alloy.
JP61154570A 1986-06-30 1986-06-30 Surface activated amorphous alloy for methanol fuel cell electrode Granted JPS6311647A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61154570A JPS6311647A (en) 1986-06-30 1986-06-30 Surface activated amorphous alloy for methanol fuel cell electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61154570A JPS6311647A (en) 1986-06-30 1986-06-30 Surface activated amorphous alloy for methanol fuel cell electrode

Publications (2)

Publication Number Publication Date
JPS6311647A JPS6311647A (en) 1988-01-19
JPH0512425B2 true JPH0512425B2 (en) 1993-02-18

Family

ID=15587120

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61154570A Granted JPS6311647A (en) 1986-06-30 1986-06-30 Surface activated amorphous alloy for methanol fuel cell electrode

Country Status (1)

Country Link
JP (1) JPS6311647A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
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JP2012517341A (en) * 2009-02-11 2012-08-02 ジョンソン、マッセイ、パブリック、リミテッド、カンパニー Three-way platinum alloy catalyst

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Publication number Priority date Publication date Assignee Title
JP5305699B2 (en) * 2007-03-19 2013-10-02 株式会社東芝 Catalyst, catalyst manufacturing method, membrane electrode assembly, and fuel cell
JP5314910B2 (en) * 2008-03-26 2013-10-16 株式会社東芝 Methanol oxidation catalyst and method for producing the same
JP6741545B2 (en) * 2016-10-10 2020-08-19 田中貴金属工業株式会社 Catalyst for polymer electrolyte fuel cell and method for producing the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012517341A (en) * 2009-02-11 2012-08-02 ジョンソン、マッセイ、パブリック、リミテッド、カンパニー Three-way platinum alloy catalyst

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