JPH01227360A - Manufacture of fuel cell catalyst - Google Patents
Manufacture of fuel cell catalystInfo
- Publication number
- JPH01227360A JPH01227360A JP63053091A JP5309188A JPH01227360A JP H01227360 A JPH01227360 A JP H01227360A JP 63053091 A JP63053091 A JP 63053091A JP 5309188 A JP5309188 A JP 5309188A JP H01227360 A JPH01227360 A JP H01227360A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- chloroplatinic acid
- acid
- fine particles
- particles
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 52
- 239000000446 fuel Substances 0.000 title claims description 6
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000002253 acid Substances 0.000 claims abstract description 21
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 17
- 239000000203 mixture Substances 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 7
- 239000010419 fine particle Substances 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 abstract description 11
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 abstract description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 abstract description 4
- 239000006229 carbon black Substances 0.000 abstract description 4
- 230000007774 longterm Effects 0.000 abstract description 4
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 abstract description 3
- 235000019253 formic acid Nutrition 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 abstract description 2
- 239000000243 solution Substances 0.000 abstract description 2
- 239000000969 carrier Substances 0.000 abstract 3
- 239000006185 dispersion Substances 0.000 abstract 2
- 239000012670 alkaline solution Substances 0.000 abstract 1
- 230000036962 time dependent Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 5
- 229910000510 noble metal Inorganic materials 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 238000005275 alloying Methods 0.000 description 4
- 229910001260 Pt alloy Inorganic materials 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000006230 acetylene black Substances 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003487 electrochemical reaction Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- -1 polytetrafluoroethylene Polymers 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 239000010970 precious metal Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 229910001111 Fine metal Inorganic materials 0.000 description 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 150000003057 platinum Chemical class 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000001132 ultrasonic dispersion Methods 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/92—Metals of platinum group
- H01M4/925—Metals of platinum group supported on carriers, e.g. powder carriers
- H01M4/926—Metals of platinum group supported on carriers, e.g. powder carriers on carbon or graphite
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/92—Metals of platinum group
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Catalysts (AREA)
- Inert Electrodes (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明はリン酸型の燃料電池電極触媒の製造方法に係
り、特に触媒上に微細な白金微粒子を均一に担持させる
方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for manufacturing a phosphoric acid type fuel cell electrode catalyst, and particularly to a method for uniformly supporting fine platinum particles on a catalyst.
燃料電池は燃料のもつ化学エネルギを直接電気エネルギ
に変換する装置であり、その構成は電解液層 (図示せ
ず)をはさんで第2図に示すようなカーボンからなる電
極基材24の上に電極触媒層25を付着させた電極26
を対向して配置し、外部のガス供給系より前記各t8i
へ燃料ガスおよび酸化剤ガスを供給し、各電極の触媒微
粒子27の上で酸化剤ガスと燃料ガスを個別に電気化学
的に反応させ、その結果として系外に電気エネルギをと
り出す発電装置である。A fuel cell is a device that directly converts the chemical energy of fuel into electrical energy, and its structure consists of an electrode base material 24 made of carbon, as shown in Figure 2, with an electrolyte layer (not shown) in between. An electrode 26 to which an electrode catalyst layer 25 is attached
are arranged facing each other, and each t8i is supplied from an external gas supply system.
A power generation device that supplies fuel gas and oxidizing gas to the catalytic converter, causes the oxidizing gas and fuel gas to react electrochemically on the catalyst fine particles 27 of each electrode, and extracts electrical energy from the system as a result. be.
触媒微粒子27としてはカーボンブラックなどの触媒単
体22の上に白金などの貴金属微粒子21を担持したも
のが用いられ、この触媒微粒子27がポリテトラフロロ
エチレン (PTFE)からなるフッ素樹脂の微粒子2
3によって結着されて電極触媒層25が形成される。The fine catalyst particles 27 are made by supporting fine metal particles 21 such as platinum on a single catalyst 22 such as carbon black, and these fine catalyst particles 27 are fine particles 2 of a fluororesin made of polytetrafluoroethylene (PTFE).
3 to form an electrode catalyst layer 25.
電極触媒層25の内部においては触媒微粒子27の表面
において電解液であるリン酸と反応ガスが接触して3相
界面が形成され、燃料ガスの酸化または酸化剤ガスの還
元といった電気化学的反応がおこる。この電気化学的反
応が効率良く進むためには、3相界面が多く存在するこ
とが必要で、そのためには触媒微粒子27は良く分散し
てその表面積が大きくなければならないし、さらに触媒
微粒子27において触媒担体22上の青金m徽粒子21
の結晶子径が小さくかつ均一に担持されていることが必
要である。Inside the electrode catalyst layer 25, phosphoric acid, which is an electrolytic solution, and the reactive gas contact each other on the surface of the catalyst fine particles 27 to form a three-phase interface, and an electrochemical reaction such as oxidation of the fuel gas or reduction of the oxidant gas occurs. It happens. In order for this electrochemical reaction to proceed efficiently, it is necessary that many three-phase interfaces exist, and for this purpose, the catalyst fine particles 27 must be well dispersed and have a large surface area. Blue gold particles 21 on catalyst carrier 22
It is necessary that the crystallite size of the crystallites is small and that the crystallites are uniformly supported.
従来貴金属微粒子21を触媒担体22上に担持させる方
法として酸などにより前処理した触媒担体22を水に分
散させてから塩化白金酸を添加しアルカリを添加撹拌し
その後還元剤を用いて塩化白金酸を還元し貴金属微粒子
21を担持していた。Conventionally, as a method for supporting noble metal fine particles 21 on a catalyst carrier 22, the catalyst carrier 22 pretreated with an acid or the like is dispersed in water, chloroplatinic acid is added thereto, an alkali is added and stirred, and then chloroplatinic acid is added using a reducing agent. was reduced to support noble metal fine particles 21.
しかしこのような方法では貴金属微粒子21を高分散化
することができず、白金合金の微粒子を得るために合金
成分を添加して合金化させたとき白金合金からなる貴金
属微粒子の結晶子径が40〜70人となり合金化前の結
晶子径の25〜30人に比して大きくなる。また触媒担
体22に担持される白金合金の貴金属微粒子に偏在が観
測され、高電位下において長時間電池を運転したとき触
媒微粒子の溶出とかシンタリングがおこり、電池の寿命
が短いという問題点があった。However, with this method, it is not possible to highly disperse the noble metal fine particles 21, and when alloying components are added to obtain platinum alloy fine particles, the crystallite diameter of the noble metal fine particles made of platinum alloy is 40. The crystallite diameter is ~70, which is larger than the crystallite diameter of 25 to 30 before alloying. In addition, maldistribution of precious metal fine particles of platinum alloy supported on the catalyst carrier 22 has been observed, and when the battery is operated for a long time under high potential, elution and sintering of the catalyst fine particles occur, resulting in a short battery life. Ta.
この発明は上述の点に鑑みてなされその目的は触媒担体
と塩化白金酸とが相互によく混合分散するようにして、
触媒担体上に高分散化した貴金属微粒子が均一に担持さ
れた燃料電池用触媒の製造方法を提供することにある。This invention was made in view of the above points, and its purpose is to mix and disperse the catalyst carrier and chloroplatinic acid well with each other.
An object of the present invention is to provide a method for producing a fuel cell catalyst in which highly dispersed noble metal fine particles are uniformly supported on a catalyst carrier.
上記の目的はこの発明によれば、水と触媒担体22と塩
化白金酸の混合物に超音波を印加して触媒担体と塩化白
金酸をよく混合分散させたのち還元剤を用いて触媒担体
22上に白金微粒子21を担持させることによって達成
される。According to the present invention, the above object is achieved by applying ultrasonic waves to a mixture of water, catalyst carrier 22 and chloroplatinic acid to thoroughly mix and disperse the catalyst carrier and chloroplatinic acid, and then applying a reducing agent to the catalyst carrier 22. This is achieved by supporting platinum fine particles 21 on the metal.
触媒担体としてはカーボンブラック等が用いられる。こ
のカーボンブラックは酸処理をして分散性を高めておく
ことができる。還元剤により塩化白金酸が還元され、白
金の微粒子が触媒担体上に担持される。Carbon black or the like is used as the catalyst carrier. This carbon black can be treated with an acid to improve its dispersibility. The chloroplatinic acid is reduced by the reducing agent, and fine particles of platinum are supported on the catalyst carrier.
超音波を水と触媒担体と塩化白金酸の混合体に印加する
と触媒担体と塩化白金酸のそれぞれがよ(分散する。混
合の均一性も向上する。When ultrasonic waves are applied to a mixture of water, catalyst carrier, and chloroplatinic acid, the catalyst carrier and chloroplatinic acid are each dispersed. The uniformity of the mixture is also improved.
次にこの発明の実施例を図面に基づいて説明する。アセ
チレンブラック900gに10重量%の硝酸水溶液40
1を添加し、これを攪拌しながら約55℃まで昇温し、
約2時間攪拌を続けた0次にこれを濾過しケーキのpH
が7になるまで充分に水洗した。Next, embodiments of the present invention will be described based on the drawings. Acetylene black 900g and 10% by weight nitric acid aqueous solution 40g
1 was added, and the temperature was raised to about 55°C while stirring,
After stirring for about 2 hours, the cake was filtered and the pH of the cake was determined.
It was thoroughly washed with water until the temperature reached 7.
このケーキを超音波を用いた407の水に充分分散させ
た。その後金属として100gの白金を含存する塩化白
金酸の水溶液IO1を添加して白金塩とアセチレンプラ
ッタが充分に接触するように約30分間攪拌を続けた。This cake was thoroughly dispersed in 407 water using ultrasound. Thereafter, an aqueous solution IO1 of chloroplatinic acid containing 100 g of platinum as a metal was added, and stirring was continued for about 30 minutes so that the platinum salt and the acetylene platter were brought into sufficient contact.
さらにこのあと超音波を30分印加する。このあとに0
.1M炭酸ナトリウム水溶液19.5 ffiを加えさ
らに30分間攪拌を続けた。Furthermore, after this, ultrasonic waves are applied for 30 minutes. After this 0
.. 19.5 ffi of a 1M aqueous sodium carbonate solution was added, and stirring was continued for an additional 30 minutes.
以上の工程が終わってから、系の温度を約2時間かげて
55℃に上昇させた。昇温後30重量%の過酸化水素水
1.07Nを加え5分間攪拌した0次に0.1M蟻酸水
溶液20.5 jlを約5時間かけて攪拌しながら添加
する。この際塩化白金酸が蟻酸により還元されて白金の
超微粒子がアセチレンブラックの表面に析出する0反応
が完了してからケーキを濾別し、塩素イオンが検出され
なくなるまで充分に洗浄した。得られたケーキを粉砕し
温度50℃において真空乾燥して触媒を得た。得られた
触媒を分析した結果、白金担持量は10.2%、平均結
晶子径は25〜30人、白金の比表面積は約172 m
”/g−ptであった。この触媒の熱的安定性を評価
するためこの触媒を窒素雰囲気中で約2時間部度900
℃で熱処理した。熱処理後の平均結晶子径は約40人で
あり白金担持触媒としても、白金と第2あるいは第3成
分の合金担持触媒の出発物質としても充分な物性を有し
ていることがわかった0例えば鉄を合金化させたあとの
資金IE!粒子の結晶子径は35人となる。After the above steps were completed, the temperature of the system was raised to 55° C. for about 2 hours. After raising the temperature, 1.07N of 30% by weight hydrogen peroxide solution was added and stirred for 5 minutes. Next, 20.5 liters of 0.1M formic acid aqueous solution was added over about 5 hours with stirring. At this time, after the zero reaction in which chloroplatinic acid was reduced by formic acid and ultrafine platinum particles were precipitated on the surface of acetylene black was completed, the cake was filtered and thoroughly washed until no chlorine ions were detected. The resulting cake was crushed and dried under vacuum at a temperature of 50°C to obtain a catalyst. As a result of analyzing the obtained catalyst, the amount of supported platinum was 10.2%, the average crystallite diameter was 25 to 30 crystallites, and the specific surface area of platinum was approximately 172 m
”/g-pt. To evaluate the thermal stability of this catalyst, it was heated at 900° C. for about 2 hours in a nitrogen atmosphere.
Heat treated at ℃. The average crystallite diameter after heat treatment was approximately 40, and it was found that it has sufficient physical properties as a platinum-supported catalyst and as a starting material for an alloy-supported catalyst of platinum and a second or third component. Fund IE after alloying iron! The crystallite size of the particles is 35 particles.
このようにして調製された触媒微粒子を用いて電極触媒
層を作製して電池の寿命特性を調べた。An electrode catalyst layer was prepared using the catalyst fine particles thus prepared, and the life characteristics of the battery were investigated.
電池の運転条件は温度200℃、電流密度200請^/
−9動作圧力4kg/−である。結果が第1図に示され
る。第1図において曲線11は超音波分散をしない従来
法の触媒の寿命特性で曲線12がこの発明の実施例に係
る触媒の寿命特性である。この発明に係る触媒を用いた
電池は長期信頬性にすぐれている。The battery operating conditions are a temperature of 200℃ and a current density of 200℃.
-9 operating pressure is 4 kg/-. The results are shown in FIG. In FIG. 1, curve 11 is the life characteristic of the conventional catalyst without ultrasonic dispersion, and curve 12 is the life characteristic of the catalyst according to the embodiment of the present invention. A battery using the catalyst according to the present invention has excellent long-term reliability.
この理由は超音波のエネルギにより触媒担体と塩化白金
酸とが良く混合分散するため、還元により発生する白金
微粒子の分散性が向上するためである。The reason for this is that the catalyst carrier and chloroplatinic acid are mixed and dispersed well by the ultrasonic energy, so that the dispersibility of the platinum fine particles generated by reduction is improved.
この発明によれば、水と触媒担体と塩化白金酸の混合物
に超音波を印加して触媒担体と塩化白金酸をよく混合分
散させたのち還元剤を用いて触媒担体上に白金微粒子を
担持させるので触媒担体上に担持される白金微粒子の結
晶子径は小さいうえ、その分布も均一でありそのために
電池の電極として使用される際に貴金属微粒子のシンタ
リングが少な(電池の長期信鯨性が増す、また白金微粒
子の高分散性のためにこれを合金化する際に合金微粒子
の結晶子径を小さくかつ均一に分布させることができ、
電池運転における経時的な出力電圧減少が低減される。According to this invention, ultrasonic waves are applied to a mixture of water, a catalyst carrier, and chloroplatinic acid to thoroughly mix and disperse the catalyst carrier and chloroplatinic acid, and then platinum fine particles are supported on the catalyst carrier using a reducing agent. Therefore, the crystallite size of the platinum fine particles supported on the catalyst carrier is small and their distribution is uniform, so when used as a battery electrode, there is little sintering of the precious metal fine particles (the long-term stability of the battery is reduced). In addition, due to the high dispersibility of platinum fine particles, when alloying them, the crystallite size of the alloy fine particles can be small and uniformly distributed.
Decrease in output voltage over time during battery operation is reduced.
第1図はこの発明の実施例に係る触媒の寿命特性を従来
の触媒と対比した線図、第2図は電池の電極を示す模式
断面図である。FIG. 1 is a diagram comparing the life characteristics of a catalyst according to an embodiment of the present invention with that of a conventional catalyst, and FIG. 2 is a schematic cross-sectional view showing an electrode of a battery.
Claims (1)
して触媒担体と塩化白金酸をよく混合分散させたのち還
元剤を用いて触媒担体上に白金微粒子を担持させること
を特徴とする燃料電池用触媒の製造方法。1) The method is characterized by applying ultrasonic waves to a mixture of water, catalyst carrier, and chloroplatinic acid to mix and disperse the catalyst carrier and chloroplatinic acid well, and then using a reducing agent to support platinum fine particles on the catalyst carrier. A method for producing a fuel cell catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63053091A JPH01227360A (en) | 1988-03-07 | 1988-03-07 | Manufacture of fuel cell catalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63053091A JPH01227360A (en) | 1988-03-07 | 1988-03-07 | Manufacture of fuel cell catalyst |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01227360A true JPH01227360A (en) | 1989-09-11 |
Family
ID=12933113
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63053091A Pending JPH01227360A (en) | 1988-03-07 | 1988-03-07 | Manufacture of fuel cell catalyst |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01227360A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH08162133A (en) * | 1994-12-05 | 1996-06-21 | Agency Of Ind Science & Technol | Manufacture of platinum catalyst |
WO2015020079A1 (en) * | 2013-08-09 | 2015-02-12 | 日産自動車株式会社 | Catalyst particles, and electrocatalyst, electrolyte membrane-electrode assembly, and fuel cell using such catalyst particles |
-
1988
- 1988-03-07 JP JP63053091A patent/JPH01227360A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH08162133A (en) * | 1994-12-05 | 1996-06-21 | Agency Of Ind Science & Technol | Manufacture of platinum catalyst |
WO2015020079A1 (en) * | 2013-08-09 | 2015-02-12 | 日産自動車株式会社 | Catalyst particles, and electrocatalyst, electrolyte membrane-electrode assembly, and fuel cell using such catalyst particles |
JPWO2015020079A1 (en) * | 2013-08-09 | 2017-03-02 | 日産自動車株式会社 | Catalyst particles and electrode catalyst, electrolyte membrane-electrode assembly and fuel cell using the same |
US10014532B2 (en) | 2013-08-09 | 2018-07-03 | Nissan Motor Co., Ltd. | Catalyst particle, and electrode catalyst, electrolyte membrane-electrode assembly, and fuel cell using the same |
US10847811B2 (en) | 2013-08-09 | 2020-11-24 | Nissan Motor Co., Ltd. | Catalyst particle, and electrode catalyst, electrolyte membrane-electrode assembly, and fuel cell using the same |
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