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JPH0121592B2 - - Google Patents
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JPH0121592B2 - - Google Patents

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Publication number
JPH0121592B2
JPH0121592B2 JP57012561A JP1256182A JPH0121592B2 JP H0121592 B2 JPH0121592 B2 JP H0121592B2 JP 57012561 A JP57012561 A JP 57012561A JP 1256182 A JP1256182 A JP 1256182A JP H0121592 B2 JPH0121592 B2 JP H0121592B2
Authority
JP
Japan
Prior art keywords
present
amorphous alloy
alloy
atomic
electrode
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
Application number
JP57012561A
Other languages
Japanese (ja)
Other versions
JPS58131656A (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.)
Tosoh Corp
Original Assignee
Tosoh Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tosoh Corp filed Critical Tosoh Corp
Priority to JP57012561A priority Critical patent/JPS58131656A/en
Publication of JPS58131656A publication Critical patent/JPS58131656A/en
Publication of JPH0121592B2 publication Critical patent/JPH0121592B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/92Metals of platinum group
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M2004/8678Inert electrodes with catalytic activity, e.g. for fuel cells characterised by the polarity
    • H01M2004/8684Negative electrodes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inert Electrodes (AREA)

Description

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

本発明は、例えばメチルアルコール、ホルムア
ルデヒド、蟻酸などメタノール系燃料を用いる燃
料電池の燃料極材料として好適な表面を活性化し
た非晶質合金に関するものである。 従来、メタノール系燃料電池の電極として白金
黒などが利用されているが、使用中に活動度の低
下が大きいなどの欠点がある。 通常、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急冷凝固させると、固体状態
でも液体に類似した結晶構造をもたない非晶構造
が得られ、このような合金を非晶質合金という。
この非晶質合金は、従来の実用金属に比べ、著し
く高い強度を保有し、かつ、組成に応じて種々の
特性を示す。 また、Znなどを金属の表面層に拡散浸透させ、
次いでこれを浸出させその金属のもつ特殊な性質
を助長させる処理を表面活性化処理という。本発
明者らは、このような非晶質合金を燃料電池の燃
料極として用いると、電力を有効かつ安定して取
り出しうることを見出し、本発明を達成したもの
である。 本発明は例えば、メチルアルコール、ホルムア
ルデヒド、蟻酸などのメタノール系燃料を用いる
燃料電池の燃料極として用いると効果的に電力を
取り出せるなど、燃料電池用燃料極として優れた
性能を備えた非晶質合金を堤供することを目的と
するものである。 本発明は下記2発明からなる。 1 P、SiおよびBのいずれか1種あるいは2種
以上4−35原子%を含み残部パラジウムからな
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 2 P、SiおよびBのいずれか1種あるいは2種
以上4−35原子%含みかつ (1) Ni、Ru、RhおよびIrの1種あるいは2種
以上65%以下 (2) Fe、Co、PtおよびSnの1種あるいは2種
以上40原子%以下 (3) Ti、Zr、Cu、AuおよびAgのいずれか1
種または2種以上25原子%以下 の群のうちから選ばれた1群または2群以上を
合計量で65原子%以下含有し、実質的残部とし
て15原子%以上Pdを含み、全体を100原子%と
す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 本発明において、前記組成の溶融合金を超急冷
凝固して得た非晶質合金は、前記各元素が均一に
固溶した単相合金である。元来、金属電極に特定
の化学反応に対する選択的活動度を付与するため
には、有効元素を必要量含む作る必要がある。し
かし結晶質金属においては、多種多量の合金元素
を添加すると、しばしば、化学的性質の異なる多
相構造となり、またこのために機械的強度を得難
いことが多い。これに対し、本発明の非晶質合金
は、液体状態から超急冷によつて作製される非晶
質構造であるため、常に均一な単相固溶体とな
り、優れた機械的性質ならびに耐食性を有すると
共に安定かつ均一な電極特性を示す。 さらに、燃料電池の燃料極としての活動度を高
めるために、合金表面層にZnなどを拡散浸透さ
せ次いでこれをアルカリ溶液に浸透させるなど表
面活性化処理を施す必要がある。結晶質金属で
は、Znなどの拡散浸透が主として結晶粒界でお
こるため、その後Znなどを浸出させると金属表
面から結晶粒が脱落し、金属が脆化するのみで、
表面活性化が有効でない場合が多い。これに対し
本発明の非晶質合金は、結晶質でないため、当然
ながら結晶粒界が存在せず結晶粒界にZnなどが
優先的に拡散浸透することによる脆化はおこらな
いのみならず、本質的にZnなどの拡散速度が速
いため、比較的低温の処理であつても、Znなど
が合金の表面層全体に拡散浸透し、次いでこれを
浸出させることによつて表面を十分に活性化させ
ることができる。 これが、本発明の表面を活性化した非晶質合金
がメタノール系燃料電池の燃料極材料として優れ
た特性を保有する理由である。 なお、Znなどの拡散浸透は、例えばZn粉末中
で合金を熱処理するとか、合金に亜鉛メツキを施
したのち真空熱処理を行うなどによつて実現す
る。この場合、熱処理温度が高く非晶質合金が結
晶化することは表面を活性化するためには特に支
障がない。但し、結晶化が進行すると合金が脆化
する場合があるので、結晶化の進行を避けること
が望ましい。 次に、本発明の非晶質合金の製造方法を説明す
る。 本発明の成分組成を有する合金溶場を溶融状態
から約104℃/秒以上の冷却速度で超急冷するこ
とにより非晶質合金を製造することができる。冷
却速度が約104℃/秒より遅いと完全に非晶質化
することはできない。したがつて、このような超
急冷を実現できれば、どのような装置であつても
本発明の非晶質合金を製造することが原理的に可
能である。一例として、本発明の非晶質合金を作
製する装置を図1に示す。図において2は下方先
端に垂直にノズル3を有する石英管で、この石英
管2の上端に設けられている送入口1より原料4
ならびに原料の酸化を防止する不活性ガスを送入
することができる。前記試料4を加熱するため石
英管2の周囲に加熱炉5を設ける。ノズル3の垂
直下方に、高速回転ロール7を設け、これをモー
ター6によつて回転させる。非晶質合金の作製に
は、所定の組成の原料4を石英管2内で不活性ガ
ス雰囲気下で、加熱炉5によつて加熱溶融し、こ
の溶湯をモーター6によつて1000〜10000r.p.mで
高速回転しているロール7の外周面上に、加圧不
活性ガスによつて噴射させると、例えば厚さ0.1
mm、幅10mm、長さ数m程度の長い薄板として、本
発明の非晶質合金を得ることができる。 上記方法により作製した本発明の非晶質合金
は、ビツカース硬さが約400〜600、引つ張り強さ
が約120〜200Kg/mm2の範囲にあり、また、完全密
着曲げや冷間圧延(50%以上)が可能な非晶質合
金特有の優れた機械的性質を保有している。 次に本発明合金の詳細を説明する。 燃料電池の燃料極の具備すべき条件は、燃料の
電気化学的な酸化反応に対する電極触媒能が高く
かつ長時間にわたつて安定であること、この電極
反応条件で、高耐食性と十分な機械的強度を保有
することである。合金が非晶質構造を有すること
は、複雑な組成の合金を単相固溶体として作製す
ることを可能にすると共に、表面活性化を容易に
するため、高くかつ安定な電極触媒能と高耐食性
ならびに優れた機械的性質を兼ね備えるために必
須である。 この非晶質合金に対して、本発明の目的である
安定で高い電極触媒能と高耐食性ならびに優れた
機械的性質を併せて備えた合金は、本発明記載の
成分組成であることを見出した。その例を表1に
まとめて示す。 本発明の表面を活性化した非晶質合金は、表面
を活性化したパラジウムよりメタノール系燃料電
池の燃料極としてはるかに電極触媒能が高く、白
金黒より優れた電極触媒能をもつものが多い。ま
た、白金黒などの電極触媒能は使用時間と共にか
なり低下するのに対し、本発明の表面を活性化し
た非晶質合金の電極触煤能は長時間使用してもほ
とんど変化せず、きわめて安定である。 したがつて、本発明の表面を活性化した非晶質
合金はメタノール系燃料電池の燃料極として優れ
た特性を具備している。 次に本発明における成分組成を限定する理由を
述べる。 P、SiおよびBは非晶質構造を得るために必要
な元素である。しかし、P、SiおよびBの1種ま
たは2種以上の合計が4原子%未満ならびに35原
子%を越えると非晶質構造を得ることが困難にな
る。したがつてP、SiおよびBの1種または2種
以上の合計は、4−35原子%の範囲にすることが
必要であり、なかでも16−25原子%の時に非晶質
構造が容易に得られる。Pdは本発明の非晶質合
金の基本金属であり、非晶質化およびメタノール
系燃料の電気化学的酸化反応に有効な元素であ
る。したがつて、本発明の第2項において15原子
%以上Pdを含むことが必要である。 Ni、Ru、RhおよびIrは、非晶質化を容易にす
ると共に適量添加すると電極触媒能を高める有効
な元素であるが、多量添加すると返つて電極触媒
能を低下させる。したがつて本発明の第2項にお
いてNi、Ru、RhおよびIrの1種または2種以上
の合計を65原子%以下にとどめる必要がある。 PtおよびSnは共に電極触媒能を高める元素で
あるが、多量添加すると非晶質合金の結晶化温度
が低下するため、表面活性化処理の際脆化しやす
くなる。したがつて、本発明の第2項において、
PtおよびSnのいずれか1種または2種の合計を
40原子%以下にとどめる必要がある。Feおよび
Coは共に非晶質化を促進する有効な元素である。
しかし多量添加は電極触媒能を低下させるため、
本発明の第2項においてFeおよびCoの1種また
は2種の合計を40原子%以下にとどめる必要があ
る。 Ti、Zr、Cu、AuおよびAgはいずれも酸およ
びアルカリ溶液中における非晶質合金の耐食性を
改善する有効な元素であるが、多量添加すると、
電極触媒能が低下するため、本発明の第2項にお
いて、Ti、Zr、Cu、AuおよびAgの1種または
2種以上の合計を25原子%以下にとどめる必要が
ある。 この他、C、N、O、Al、S、Geなどの元素
は、いずれも非晶質構造を安定化するものであつ
て、5%未満の添加は、本発明の目的に何ら支障
をきたさない。 次に本発明を実施例により更に説明する。 実施例 1 所定の組成の原料合金を前述の方法で加熱溶解
後超急冷して厚さ0.02−0.05mm、幅1〜5mm、長
さ約10mの非晶質合金薄板を得た。これら非晶質
合金薄板より、所定の長さを切り出し、これに
400g/ZnSO4・7H2Oと70g/Na2SO4から
なる30℃の水溶液中20mA/cm2の一定電流密度で
Znメツキを施した。次いでこれらを200−300℃
で30分間真空熱処理して、Znを拡散浸透させた
後80℃の6MKOH水溶液中でZnを浸出させ、試
料電極を得た。このようにして作られた試料電極
を用い、種々の濃度のメチルアルコールを含む
1MKOH水溶液中で45mV/minの電位送引速度
の動電位法によりアノード分極曲線を求めた。1
例として表2に1MCH3OHを含む30℃の
1MKOH溶液中1mA/cm2の電流密度を示す電位
を動電位分極曲線から求めてまとめて記した。電
位はいずれも負の値であるが、絶対値の大きなも
の程熱料電池として大きな電圧が得られ有効であ
る。 本発明の表面を活性化した非晶質合金は、同じ
条件で表面を活性化したPdよりはるかに活性で
ある。また白金黒と比較しても本発明の大半の合
金は電極触煤能が高い。残りのものも白金黒と同
程度あるいはやや劣る電極触媒能を有する。更に
本発明の表面を活性化した非晶質合金はメチルア
ルコールの酸化反応中きわめて安定であつて、例
えば1MCH3OHを含む30℃の1MKOH水溶液中
において50mA/cm2の電流密度で10時間メチルア
ルコールを酸化してもほとんど電極電位に変動が
ない。これに対し、白金黒や表面を活性化したパ
ラジウムは同じ電流密度で10時間メチルアルコー
ルを酸化し続けると、それぞれ0.063Vおよび
0.050V電位の絶対値が低下し、それだけ燃料電
池の電圧が低下することになる。 実施例 2 実施例1と同様にして作製した試料電極を用
い、1MHCOONaを含む30℃の1MKOH溶液中で
動電位アノード分極曲線を側定した。これら動電
位分極曲線より求めた1mA/cm2の電流密度を示
す電位を表3にまとめた。表3の電位がいずれも
表2と比べて負の大きな値であるのはHCOONa
の酸化の平衡電位がCH3OHより負なためであ
る。 本発明の表面を活性化した非晶質合金は
HCOONaの酸化に対して同じ条件で表面を活性
化したPdよりはるかに高い電極触煤能をもち、
また白金黒と比較しても電極触媒能は優れている
か同等のものである。 実施例 3 実施例1と同様にして作製した試料電極を用
い、1MHCHOを含む30℃の1MKOH水溶液中で
動電位アノード分極曲線を測定した。これら動電
位分極曲線より求めた1mA/cm2の電流密度を示
す電位を表4にまとめた。表4の電位が表2およ
び表3に比べていずれも負の大きな値であるのは
HCHOの酸化の平衡電位がCH3OHおよび
HCOONaより負なためである。 本発明の表面を活性化した非晶質合金は
HCHOの酸化に対して同じ条件で表面を活性化
したPdよりはるかに高い電極触媒能をもつ。ま
た白金黒よりも優れたものが大半であつて残りも
白金黒に必敵する電極触媒能をもつている。
The present invention relates to a surface-activated amorphous alloy suitable as a fuel electrode material for fuel cells using methanol-based fuels such as methyl alcohol, formaldehyde, and formic acid. Conventionally, platinum black and the like have been used as electrodes in methanol-based fuel cells, but they have drawbacks such as a large decrease in activity during use. Usually, alloys are crystallized in the solid state, but
When the alloy composition is limited and the alloy is rapidly solidified, an amorphous structure similar to that of a liquid without a crystalline structure is obtained even in the solid state, and such an alloy is called an amorphous alloy.
This amorphous alloy has significantly higher strength than conventional practical metals, and exhibits various properties depending on its composition. In addition, by diffusing and penetrating Zn etc. into the surface layer of the metal,
The process of leaching out this material and promoting the special properties of the metal is called surface activation treatment. The present inventors have discovered that when such an amorphous alloy is used as a fuel electrode of a fuel cell, electric power can be extracted effectively and stably, and the present invention has been achieved. The present invention provides an amorphous alloy that has excellent performance as a fuel electrode for fuel cells, such as being able to effectively extract electric power when used as a fuel electrode for fuel cells that use methanol-based fuels such as methyl alcohol, formaldehyde, and formic acid. The purpose is to provide. The present invention consists of the following two inventions. 1 A surface-activated amorphous alloy for methanol fuel cell fuel electrodes containing 4-35 atomic % of any one or more of P, Si and B, with the balance being palladium 2 Any 1 of P, Si and B (1) One or more of Ni, Ru, Rh, and Ir at 65% or less (2) One or more of Fe, Co, Pt, and Sn40 Atomic % or less (3) Any one of Ti, Zr, Cu, Au, and Ag
Contains 65 at% or less in total of one or more groups selected from species or groups of two or more and up to 25 at%, and contains Pd as the substantial balance of at least 15 at%, with a total of 100 atoms Surface-activated amorphous alloy for methanol-based fuel cell fuel electrodes In the present invention, the amorphous alloy obtained by ultra-rapidly solidifying the molten alloy having the above composition is a monomer in which each of the above elements is uniformly dissolved in solid solution. It is a phase alloy. Originally, in order to impart selective activity to a specific chemical reaction to a metal electrode, it is necessary to make it contain a necessary amount of effective elements. However, in crystalline metals, when a large amount of various alloying elements are added, a multiphase structure with different chemical properties is often formed, and for this reason, it is often difficult to obtain mechanical strength. In contrast, the amorphous alloy of the present invention has an amorphous structure created by ultra-rapid cooling from a liquid state, so it is always a uniform single-phase solid solution, and has excellent mechanical properties and corrosion resistance. Shows stable and uniform electrode characteristics. Furthermore, in order to increase the activity as a fuel electrode of a fuel cell, it is necessary to perform a surface activation treatment such as diffusing and permeating Zn into the alloy surface layer and then permeating this into an alkaline solution. In crystalline metals, diffusion and infiltration of Zn and other substances mainly occurs at grain boundaries, so if Zn and other substances are subsequently leached, the crystal grains will fall off from the metal surface and the metal will become brittle.
Surface activation is often not effective. On the other hand, since the amorphous alloy of the present invention is not crystalline, it naturally does not have grain boundaries and does not suffer from embrittlement due to preferential diffusion and penetration of Zn and the like into the grain boundaries. Due to the inherently fast diffusion rate of Zn, etc., Zn can diffuse into the entire surface layer of the alloy, and then be leached out, thereby sufficiently activating the surface, even during relatively low-temperature processing. can be done. This is the reason why the surface-activated amorphous alloy of the present invention has excellent properties as a fuel electrode material for methanol fuel cells. Incidentally, the diffusion and penetration of Zn and the like can be achieved, for example, by heat treating the alloy in Zn powder, or by performing vacuum heat treatment after galvanizing the alloy. In this case, the fact that the heat treatment temperature is high and the amorphous alloy crystallizes does not pose any particular problem in activating the surface. However, since the progress of crystallization may cause the alloy to become brittle, it is desirable to avoid the progress of crystallization. Next, a method for manufacturing the amorphous alloy of the present invention will be explained. An amorphous alloy can be produced by ultra-quenching an alloy melt field having the composition of the present invention from a molten state at a cooling rate of about 10 4 C/sec or more. If the cooling rate is slower than about 10 4 C/sec, complete amorphization cannot be achieved. Therefore, if such ultra-rapid cooling can be achieved, it is theoretically possible to produce the amorphous alloy of the present invention using any type of equipment. As an example, an apparatus for producing the amorphous alloy of the present invention is shown in FIG. In the figure, reference numeral 2 denotes a quartz tube with a nozzle 3 vertically disposed at its lower end.
Additionally, an inert gas can be introduced to prevent oxidation of the raw material. A heating furnace 5 is provided around the quartz tube 2 to heat the sample 4. A high speed rotating roll 7 is provided vertically below the nozzle 3 and is rotated by a motor 6. To produce an amorphous alloy, a raw material 4 of a predetermined composition is heated and melted in a heating furnace 5 in an inert gas atmosphere in a quartz tube 2, and the molten metal is heated by a motor 6 for 1000 to 10000 r. When the pressurized inert gas is injected onto the outer peripheral surface of the roll 7 which is rotating at high speed at pm, for example, a thickness of 0.1
The amorphous alloy of the present invention can be obtained as a long thin plate with a width of 10 mm, a width of 10 mm, and a length of several meters. The amorphous alloy of the present invention produced by the above method has a Vickers hardness of about 400 to 600 and a tensile strength of about 120 to 200 Kg/mm 2 , and can be fully contact bent or cold rolled. (more than 50%) Possesses excellent mechanical properties unique to amorphous alloys. Next, details of the alloy of the present invention will be explained. The conditions that the fuel electrode of a fuel cell must have are that it has a high electrode catalytic ability for the electrochemical oxidation reaction of the fuel and is stable for a long time.Under these electrode reaction conditions, it must have high corrosion resistance and sufficient mechanical strength. It is about having strength. The amorphous structure of the alloy makes it possible to prepare alloys with complex compositions as single-phase solid solutions, and also facilitates surface activation, resulting in high and stable electrocatalytic ability, high corrosion resistance, and This is essential in order to have excellent mechanical properties. For this amorphous alloy, it has been found that an alloy that has the objective of the present invention of stable and high electrocatalytic ability, high corrosion resistance, and excellent mechanical properties has the composition described in the present invention. . Examples are summarized in Table 1. The surface-activated amorphous alloy of the present invention has much higher electrocatalytic ability as a fuel electrode for methanol fuel cells than surface-activated palladium, and many have better electrocatalytic ability than platinum black. . Furthermore, while the electrocatalytic ability of materials such as platinum black deteriorates considerably over time, the electrocatalytic ability of the surface-activated amorphous alloy of the present invention hardly changes even after long-term use, and is extremely It is stable. Therefore, the surface-activated amorphous alloy of the present invention has excellent properties as a fuel electrode for methanol fuel cells. Next, the reason for limiting the component composition in the present invention will be described. P, Si and B are elements necessary to obtain an amorphous structure. However, if the total content of one or more of P, Si and B is less than 4 at % or more than 35 at %, it becomes difficult to obtain an amorphous structure. Therefore, the total amount of one or more of P, Si, and B must be in the range of 4-35 at%, and in particular, an amorphous structure is easily formed when the content is 16-25 at%. can get. Pd is the basic metal of the amorphous alloy of the present invention, and is an effective element for amorphization and electrochemical oxidation reaction of methanol fuel. Therefore, in the second aspect of the present invention, it is necessary to contain Pd in an amount of 15 atomic % or more. Ni, Ru, Rh, and Ir are effective elements that facilitate amorphization and increase the electrocatalytic ability when added in appropriate amounts; however, when added in large amounts, they reduce the electrocatalytic ability. Therefore, in the second aspect of the present invention, it is necessary to keep the total amount of one or more of Ni, Ru, Rh, and Ir to 65 atomic % or less. Both Pt and Sn are elements that enhance the electrode catalytic ability, but when added in large amounts, the crystallization temperature of the amorphous alloy decreases, making it more likely to become brittle during surface activation treatment. Therefore, in Section 2 of the present invention,
The sum of one or two of Pt and Sn
It is necessary to keep it below 40 atomic percent. Fe and
Both Co and Co are effective elements that promote amorphization.
However, adding a large amount will reduce the electrode catalytic ability.
In item 2 of the present invention, the total content of one or both of Fe and Co must be kept at 40 atomic % or less. Ti, Zr, Cu, Au and Ag are all effective elements for improving the corrosion resistance of amorphous alloys in acid and alkaline solutions, but when added in large amounts,
Since the electrode catalytic ability decreases, in the second aspect of the present invention, it is necessary to keep the total amount of one or more of Ti, Zr, Cu, Au, and Ag at 25 atomic % or less. In addition, elements such as C, N, O, Al, S, and Ge all stabilize the amorphous structure, and adding less than 5% will not impede the purpose of the present invention. do not have. Next, the present invention will be further explained by examples. Example 1 A raw material alloy having a predetermined composition was heated and melted using the method described above, and then ultra-quenched to obtain an amorphous alloy thin plate having a thickness of 0.02-0.05 mm, a width of 1-5 mm, and a length of about 10 m. Cut out a predetermined length from these amorphous alloy thin plates, and
At a constant current density of 20 mA/cm 2 in an aqueous solution of 400 g/ZnSO 4 7H 2 O and 70 g/Na 2 SO 4 at 30°C.
Zn plating was applied. Then heat these to 200-300℃
After vacuum heat treatment for 30 minutes to diffuse and infiltrate Zn, Zn was leached in a 6M KOH aqueous solution at 80°C to obtain a sample electrode. Using sample electrodes made in this way, samples containing various concentrations of methyl alcohol were used.
The anodic polarization curve was determined by potentiodynamic method at a potential transfer rate of 45 mV/min in a 1M KOH aqueous solution. 1
As an example, Table 2 shows the temperature at 30℃ containing 1MCH 3 OH.
Potentials indicating a current density of 1 mA/cm 2 in a 1M KOH solution were determined from potentiodynamic polarization curves and are summarized. All of the potentials have negative values, but the larger the absolute value, the more effective the potential is as a result of being able to obtain a larger voltage as a heating cell. The surface-activated amorphous alloy of the present invention is much more active than surface-activated Pd under the same conditions. Moreover, most of the alloys of the present invention have high electrode soot contact ability even when compared to platinum black. The remaining ones also have electrocatalytic abilities comparable to or slightly inferior to platinum black. Furthermore, the surface-activated amorphous alloy of the present invention is extremely stable during the oxidation reaction of methyl alcohol. There is almost no change in electrode potential even when alcohol is oxidized. On the other hand, when platinum black and surface-activated palladium continue to oxidize methyl alcohol at the same current density for 10 hours, the voltage is 0.063V and
The absolute value of the 0.050V potential decreases, and the voltage of the fuel cell decreases accordingly. Example 2 Using a sample electrode prepared in the same manner as in Example 1, a potentiodynamic anodic polarization curve was determined in a 1M KOH solution containing 1MHCOONa at 30°C. Potentials representing a current density of 1 mA/cm 2 determined from these potentiodynamic polarization curves are summarized in Table 3. The reason why the potentials in Table 3 are all negative values compared to Table 2 is HCOONa.
This is because the equilibrium potential for oxidation of CH 3 OH is more negative than that of CH 3 OH. The surface activated amorphous alloy of the present invention is
It has a much higher electrode soot ability than Pd whose surface has been activated under the same conditions for the oxidation of HCOONa.
Moreover, when compared with platinum black, the electrode catalytic ability is superior or equivalent. Example 3 Using a sample electrode prepared in the same manner as in Example 1, a potentiodynamic anodic polarization curve was measured in a 1M KOH aqueous solution containing 1MHCHO at 30°C. Table 4 summarizes the potentials representing a current density of 1 mA/cm 2 determined from these potentiodynamic polarization curves. The reason why the potentials in Table 4 are all negative values compared to Tables 2 and 3 is that
The equilibrium potential for oxidation of HCHO is CH 3 OH and
This is because it is more negative than HCOONa. The surface activated amorphous alloy of the present invention is
It has a much higher electrocatalytic ability for the oxidation of HCHO than Pd whose surface is activated under the same conditions. Most of them are superior to platinum black, and the rest have electrocatalytic ability that rivals platinum black.

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of drawings]

図1は本発明非晶質合金を製造する装置の一例
を示す概略図である。 1……原料送入口、2……石英管、3……ノズ
ル部、4……原料、5……加熱炉、6……モータ
ー、7……高速回転ロール。
FIG. 1 is a schematic diagram showing an example of an apparatus for producing the amorphous alloy of the present invention. 1... Raw material inlet, 2... Quartz tube, 3... Nozzle section, 4... Raw material, 5... Heating furnace, 6... Motor, 7... High speed rotating roll.

Claims (1)

【特許請求の範囲】 1 P、SiおよびBのいずれか1種あるいは2種
以上4−35原子%を含み残部パラジウムからなる
メタノール系燃料電池燃料極用表面活性化非晶質
合金。 2 P、SiおよびBのいずれか1種あるいは2種
以上4−35原子%を含みかつ (1) Ni、Ru、RhおよびIrの1種あるいは2種以
上65原子%以下 (2) Fe、Co、PtおよびSnの1種あるいは2種以
上40原子%以下 (3) Ti、Zr、Cu、AuおよびAgのいずれか1種
または2種以上25原子%以下 の群のうちから選ばれた1群または2群以上を合
計量で65原子%以上含有し、実質的残部として15
原子%以上Pdを含み、全体を100原子%とするメ
タノール系燃料電池燃料極用表面活性化非晶質合
金。
[Scope of Claims] 1. A surface-activated amorphous alloy for a fuel electrode of a methanol-based fuel cell, comprising 4 to 35 atomic % of one or more of P, Si, and B, and the balance being palladium. 2 Contains 4-35 atomic % of one or more of P, Si, and B, and (1) 65 atomic % or less of one or more of Ni, Ru, Rh, and Ir (2) Fe, Co , one or more of Pt and Sn, or more than 40 atomic % (3) One group selected from the group consisting of one or more of Ti, Zr, Cu, Au, and Ag, or more than 25 atomic % of Ti, Zr, Cu, Au, and Ag or contains two or more groups in a total amount of 65 at% or more, with the substantial balance being 15
A surface-activated amorphous alloy for methanol-based fuel cell fuel electrodes containing Pd at % or more, with a total content of 100 atomic%.
JP57012561A 1982-01-30 1982-01-30 Surface activated amorphous alloy for fuel electrode of methanol system fuel cell Granted JPS58131656A (en)

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JP57012561A JPS58131656A (en) 1982-01-30 1982-01-30 Surface activated amorphous alloy for fuel electrode of methanol system fuel cell

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JP57012561A JPS58131656A (en) 1982-01-30 1982-01-30 Surface activated amorphous alloy for fuel electrode of methanol system fuel cell

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JPS58131656A JPS58131656A (en) 1983-08-05
JPH0121592B2 true JPH0121592B2 (en) 1989-04-21

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JP (1) JPS58131656A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0713897B2 (en) * 1985-03-30 1995-02-15 株式会社リケン Surface activated amorphous alloy for fuel cell electrodes
TWI301001B (en) * 2004-05-25 2008-09-11 Lg Chemical Ltd Ruthenium-rhodium alloy electrode catalyst and fuel cell comprising the same

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