JPH02103861A - Method for manufacturing electrodes for molten carbonate fuel cells - Google Patents
Method for manufacturing electrodes for molten carbonate fuel cellsInfo
- Publication number
- JPH02103861A JPH02103861A JP63253894A JP25389488A JPH02103861A JP H02103861 A JPH02103861 A JP H02103861A JP 63253894 A JP63253894 A JP 63253894A JP 25389488 A JP25389488 A JP 25389488A JP H02103861 A JPH02103861 A JP H02103861A
- Authority
- JP
- Japan
- Prior art keywords
- nickel
- chromium
- particles
- anode
- powder
- 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.)
- Granted
Links
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
- H01M4/88—Processes of manufacture
-
- 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
- H01M8/14—Fuel cells with fused electrolytes
- H01M2008/147—Fuel cells with molten carbonates
-
- 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
- H01M4/88—Processes of manufacture
- H01M4/8878—Treatment steps after deposition of the catalytic active composition or after shaping of the electrode being free-standing body
- H01M4/8882—Heat treatment, e.g. drying, baking
- H01M4/8885—Sintering or firing
-
- 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
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- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inert Electrodes (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、溶融炭酸塩型燃料電池用のアノードの製造法
に係り、特にニッケル・クロム合金製のアノードの製造
法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for manufacturing an anode for a molten carbonate fuel cell, and in particular to a method for manufacturing an anode made of a nickel-chromium alloy.
従来から、浴融炭酸塩型燃料電池は、化学反応のエネル
ギを電気エネルギに変換するものとして知られており、
溶融炭酸塩の電解質をはさんで、カソードとアノードを
配置し、カソード側には酸化剤ガスを、アノード側には
燃料ガスを供給する構成になっている。Traditionally, bath-fused carbonate fuel cells have been known to convert the energy of chemical reactions into electrical energy.
A cathode and an anode are arranged with a molten carbonate electrolyte sandwiched between them, and an oxidant gas is supplied to the cathode side, and a fuel gas is supplied to the anode side.
電極部でガスと炭酸塩の反応を効率よく行わせるために
、電極は多孔質構造であることが必要とされ、今までは
、主にニッケル粉末の焼結体が使用されている。In order for the reaction between gas and carbonate to occur efficiently in the electrode portion, the electrode needs to have a porous structure, and up to now, sintered bodies of nickel powder have been mainly used.
この場合、酸化剤ガス側のカソードは電池運転中に酸化
雰囲気によ、!7衣而に酸化物層を形成するので、ニッ
ケル粒子のシンクリングは進行しない。ところが、燃料
ガス側のアノードは電池運転中に水素を含む還元雰囲気
によシ、ニッケル粒子の表面が金属状態を維持している
。このため、600〜700℃の電池作動温度において
電極はシンクリングし易く、シンクリングが進行すると
当初の気孔率が低下する。さらに、電極には常に、電池
として組み込んだ際の締めつけ圧力が付加されており、
これが原因でアノードはクリープ変形を起こし、当初の
気孔率が低下する。このようなアノードの気孔率低下は
電池性能の劣化をもたらすことになる。In this case, the cathode on the oxidizing gas side is exposed to the oxidizing atmosphere during battery operation! 7. Since an oxide layer is formed on the coating, sinkling of the nickel particles does not proceed. However, during battery operation, the anode on the fuel gas side is exposed to a reducing atmosphere containing hydrogen, and the surface of the nickel particles maintains a metallic state. Therefore, the electrode tends to sink at a battery operating temperature of 600 to 700°C, and as sinkling progresses, the initial porosity decreases. Furthermore, the electrodes are always subject to clamping pressure when assembled into a battery.
This causes the anode to undergo creep deformation, reducing its initial porosity. Such a decrease in the porosity of the anode results in deterioration of battery performance.
これらを防止する方法として、アノードには、ニッケル
に第二元素を添加した素材を用いる方法が広く行われて
おシ、特にクロムの添加は有効であることが知られてい
る。As a method for preventing these, a method of using a material in which a second element is added to nickel is widely used for the anode, and it is known that addition of chromium is particularly effective.
そして、この種のアノードを製造する場合、第1の方法
として、ニッケルと第二元素の合金粉末を作製し、この
粉末を成形、焼結する方法がある。しかし、一般にこれ
らの合金粉末は、アトマイズ法によって製造されるので
、粒子が球状になシ、焼結した際に多孔度の高いものが
得られない。また、通常使用されている電極素材用ニッ
ケル粉末はカーボニル法によって製造されるため、平均
粒径数μm以下のものが容易に得られるのに対して、ア
トマイズ法では数10μm以上の粗粒子が大部分を占め
、数μm以下の粉末を得るには歩留まりが悪かった。When manufacturing this type of anode, the first method is to prepare an alloy powder of nickel and a second element, mold this powder, and sinter it. However, since these alloy powders are generally manufactured by an atomization method, the particles are not spherical, and when sintered, it is difficult to obtain particles with high porosity. In addition, since the commonly used nickel powder for electrode materials is produced by the carbonyl method, it is easy to obtain particles with an average particle size of several micrometers or less, whereas with the atomization method, coarse particles with an average particle size of several tens of micrometers or more are produced. The yield was poor to obtain powder of several micrometers or less.
第2の方法として、発泡ニッケルやニッケル粉末焼結体
などの多孔体を予め作製し、これに第二元素を金属塩な
どの形で含浸した後、化学的に還元熱処理する方法があ
るが、製造工程が複雑であるとともに、第二元素を多量
に添加する場合には多数回にわたる含浸処理が必要であ
や、工業上の効率が悪い。The second method is to prepare a porous body such as nickel foam or sintered nickel powder in advance, impregnate it with a second element in the form of a metal salt, and then chemically treat it with reduction heat. The manufacturing process is complicated, and when a large amount of the second element is added, multiple impregnation treatments are required, resulting in poor industrial efficiency.
第3の方法として、基材ニッケル粉末と第二元素の粉末
とを混合し、これを成形、焼結する方法がアシ、前記二
種の方法に比べて、最も単純で容易である。しかし、本
方法では第二元素成分の偏析が避けられず、第二元素を
含有しない部分を生じる可能性があるとともに、偏析に
よって、焼結時に局部的な合金化反応がすすみ、焼結反
応に伴う収縮が不均一になり、割れや変形を起こす場合
があった。また、たとえ、構造的欠陥が生じなかったと
しても、第二元素の偏析を少なくするには高温で長時間
の熱処理が必要とされ、この場合には焼結体の多孔度が
低下することになり好ましくない。As a third method, the method of mixing the base nickel powder and the powder of the second element, molding and sintering this is the simplest and easiest method compared to the above two methods. However, in this method, segregation of the second element component is unavoidable, and there is a possibility that some parts do not contain the second element, and due to segregation, local alloying reaction progresses during sintering, and the sintering reaction The accompanying shrinkage became uneven, sometimes resulting in cracks and deformation. Furthermore, even if no structural defects occur, long-term heat treatment at high temperatures is required to reduce the segregation of the second element, and in this case, the porosity of the sintered body may decrease. I don't like it.
前記したように、従来法において今だ種々の問題があり
満足すべき方法はなかった。As mentioned above, conventional methods still have various problems and no satisfactory method has been found.
本発明は、従来法の問題点を解決し、ニッケル・クロム
合金製アノードを簡易な方法で得ることを目的とする。The present invention aims to solve the problems of the conventional method and to obtain a nickel-chromium alloy anode by a simple method.
本発明者らは、前記の目的を達成するために鋭意検討の
結果、ニッケル・クロム合金製アノードの製造において
、第二元素たるクロムを純金属の形で、しかも蒸発法に
よって作製したクロム超微粒子の形で用いることによっ
て、偏析することがなく、均一に分散したアノードを製
造し得ることを見出し本発明を完成した。In order to achieve the above object, the inventors of the present invention have made extensive studies and found that in the production of nickel-chromium alloy anodes, ultrafine chromium particles are produced using chromium, which is the second element, in the form of a pure metal and by an evaporation method. The present invention was completed based on the discovery that by using the above-mentioned anode, it is possible to produce a uniformly dispersed anode without segregation.
すなわち、本発明は、溶融炭酸塩型燃料電池用ニッケル
・クロム合金製アノードを製造する方法において、ニッ
ケル粉末と蒸発法で製造されたクロム超微粒子とを混合
し、成形、焼結することを特徴とするニッケル・クロム
合金製アノードの製造法に関する。That is, the present invention is characterized in that, in a method for manufacturing a nickel-chromium alloy anode for a molten carbonate fuel cell, nickel powder and ultrafine chromium particles manufactured by an evaporation method are mixed, molded, and sintered. This invention relates to a method for manufacturing a nickel-chromium alloy anode.
次に本発明を更に詳しく説明する。Next, the present invention will be explained in more detail.
本発明では、第二元素なるクロムを純金属の形で添加す
るが、その特徴は第二元素に蒸発法によって作製したク
ロム超微粒子を用いるところにある。ところで、蒸発法
は材料の固体を加熱して蒸気にし、それを冷媒中で冷却
して超微粒子に凝結させるもので、クロムの場合は平均
粒径線50OAのものが得られる。ここで得られる金属
超微粒子自体は、粒径が非常に小さいので、単独では焼
結用素材に適さないが、第二元素添加用物質としてはそ
の効果を発揮する。In the present invention, chromium, which is the second element, is added in the form of a pure metal, and its feature is that ultrafine chromium particles produced by an evaporation method are used as the second element. By the way, the evaporation method heats the solid material to vaporize it, cools it in a refrigerant, and condenses it into ultrafine particles.In the case of chromium, particles with an average particle diameter of 50 OA are obtained. The ultrafine metal particles obtained here have a very small particle size, so they are not suitable as a sintering material alone, but they are effective as a material for adding a second element.
すなわち、得られたクロム超微粒子は粒径が基材ニッケ
ル粉末より2桁小さいので、ニッケル粉体間に均一に分
散することが容易であり、大きく偏析することはない。That is, since the obtained ultrafine chromium particles have a particle size two orders of magnitude smaller than the base nickel powder, they can easily be uniformly dispersed between the nickel powders and do not segregate to a large extent.
また、該超微粒子は焼結熱処理時に容易にニッケル中に
拡散し、添加量の殆んどがニッケルと合金化するので、
所望の合金組成に相当する量を添加するだけでよい。In addition, the ultrafine particles easily diffuse into nickel during sintering heat treatment, and most of the added amount is alloyed with nickel.
It is sufficient to add only an amount corresponding to the desired alloy composition.
また、本発明の場合は、純金属単体を第二元素添加物と
して用いているにもかかわらず、分散の効果は金属塩な
どと同等であり、しかも、−度の焼結処理で所望の第二
元素成分を含有する合金焼結体を得ることができる。In addition, in the case of the present invention, although a pure metal element is used as the second element additive, the dispersion effect is equivalent to that of metal salts, and moreover, the desired dispersion effect can be achieved by -degree sintering treatment. An alloy sintered body containing two element components can be obtained.
また、更に拡散を良くするためには、原料の段階で基材
ニッケル粉末とクロム超微粒子を所定量だけ秤量した後
混合し、電極製造時の焼結温度より低い温度で予備的に
熱処理することによって、よりよくニッケル中にクロム
を拡散させることが可能である。この予備熱処理後の粉
末を原料にして焼結体を作製すれば、焼結体中のクロム
の分布はさらに均一化される利点がある。In order to further improve the diffusion, it is necessary to weigh and mix a predetermined amount of base nickel powder and chromium ultrafine particles at the raw material stage, and then preliminarily heat-treat the mixture at a temperature lower than the sintering temperature during electrode manufacturing. It is possible to better diffuse chromium into nickel. If a sintered body is produced using the powder after this preliminary heat treatment as a raw material, there is an advantage that the distribution of chromium in the sintered body can be made more uniform.
焼結反応の主な駆動力は粉体粒子の表面エネルギである
。このエネルギを減少させるように物質移動が起こ勺、
粉体粒子の表面積が減少するように焼結がすすむ。本発
明では焼結すべき素材が2種類の金属粉末の混合物であ
り、前記物質移動にともなって、2棟の金属の合金化が
進行する。すなわち、基材ニッケル粉末は相互の融着に
よって多孔体の物理的性状を決定する多孔体構造を形成
するが、その際に各部に分散したクロム超微粒子と合金
化する。この場合、クロム超微粒子の代わりに、ミクロ
ンオーダのクロム粉末を用いた場合でも同様の反応は起
こるが、超微粒子の場合の方が粒子の表面エネルギが大
きく、またニッケル粉末間への分散性もよいので、焼結
反応がすすみやすい。The main driving force for the sintering reaction is the surface energy of the powder particles. Mass transfer occurs to reduce this energy,
Sintering proceeds such that the surface area of the powder particles is reduced. In the present invention, the material to be sintered is a mixture of two types of metal powders, and as the material transfers, alloying of the two metals progresses. That is, the base nickel powder forms a porous body structure that determines the physical properties of the porous body by mutual fusion, and at that time, it is alloyed with the ultrafine chromium particles dispersed in various parts. In this case, a similar reaction occurs even if micron-order chromium powder is used instead of ultrafine chromium particles, but ultrafine particles have a higher particle surface energy and are less dispersible among nickel powders. The sintering reaction progresses easily.
本発明の方法は、燃料電池用電極のような合金多孔体の
製造法として特に効果がある。すなわち、単にち密質の
合金焼結体を製造する場合には焼結温度を高くしたシ、
成形あるいは焼結時の加圧力付加によって粒子同志を密
着したシして、ニッケルとクロムを容易に合金化できる
が多孔質焼結体を製造する場合には、高い焼結温度や加
圧力の付加は多孔度を低下させるので好ましくない。と
ころが本発明に依れば多孔度を低下させることなくニッ
ケルとクロムラ合金化することができるのである。The method of the present invention is particularly effective as a method for producing porous alloy bodies such as electrodes for fuel cells. In other words, when simply producing a dense alloy sintered body, the sintering temperature must be increased,
Nickel and chromium can be easily alloyed by applying pressure during molding or sintering to bring the particles into close contact with each other, but when producing porous sintered bodies, it is necessary to apply high sintering temperatures and pressure. is undesirable because it reduces porosity. However, according to the present invention, nickel and chrome alloy can be formed without reducing the porosity.
以下に実施例にもとづき本発明を説明するが、本発明は
これらの実施例に限定されるものではない。The present invention will be explained below based on Examples, but the present invention is not limited to these Examples.
実施例1
基材として平均粒径2.2〜2.8μmのニッケル粉末
(lNC0製Type255) を90f1第二元素
添加物として、ガス中蒸発法によって作製された平均粒
径500Aのクロム超微粒子(真空冶金製)を1021
有機質バインダとしてポリビニルブチラール’i8 F
、可塑剤としてヒドロキシプルメチルセルロース’e2
F、溶剤としてエタノールとトリクレンの重量比1対1
の混合溶液を802、それぞれ秤量しこれらをボールミ
ル中で100時間混練してスラリを作製した。Example 1 Ultrafine chromium particles (with an average particle size of 500 A) produced by evaporation in gas using nickel powder (Type 255 manufactured by INC0) with an average particle size of 2.2 to 2.8 μm as a base material and a 90f1 second element additive ( (manufactured by vacuum metallurgy) 1021
Polyvinyl butyral 'i8 F as an organic binder
, hydroxypurmethylcellulose 'e2 as plasticizer
F, 1:1 weight ratio of ethanol and trichlene as solvents
A slurry was prepared by weighing 802 pieces of mixed solutions and kneading them in a ball mill for 100 hours.
このスラリ全ドクターブレード装置により、補強材のニ
ッケル金網(線径o、2■、20メツシユ〕上に塗布し
て薄板に成形した。乾燥後の成形体を真空中で950℃
に1時間加熱保持して焼結し、厚さα81+1111で
90■角のアノードを得た。この電極から約1fの試験
片を採取し、補強材を含んだ状態での多孔度を測定した
ところ、64%の値を示した。This slurry was coated onto a reinforcing nickel wire mesh (wire diameter o, 2 mm, 20 mesh) using a full doctor blade device and formed into a thin plate.The formed product after drying was heated to 950°C in a vacuum.
The anode was heated and held for 1 hour for sintering to obtain a 90 square anode with a thickness α81+1111. A test piece of about 1 f was taken from this electrode and its porosity including the reinforcing material was measured, and it showed a value of 64%.
実施例2
実施例1に用いたと同じニッケル粉末、クロム超微粒子
をそれぞれ合計重量の90重量%、10重量%になるよ
うに秤量した。粉体総重量00重量部として50重量部
にあたるエタノールと上記2柚の金属粉体とをボールミ
ル中で100時間混合した。混合後のスラリを乾燥した
後、アルミナルツボに入れ、予備熱処理として真空中、
650℃で4時間加熱保持し、ニッケル中へクロムを拡
散させた。予備熱処理後の粉末を乳鉢で粉砕した後、3
5メツシ二のふるいで粗粒をと勺除いた。Example 2 The same nickel powder and ultrafine chromium particles used in Example 1 were weighed so that their total weight was 90% by weight and 10% by weight, respectively. Ethanol corresponding to 50 parts by weight based on the total powder weight of 00 parts by weight and the above two yuzu metal powders were mixed in a ball mill for 100 hours. After drying the mixed slurry, it is placed in an aluminium crucible and subjected to preliminary heat treatment in a vacuum.
The mixture was heated and maintained at 650°C for 4 hours to diffuse chromium into the nickel. After crushing the powder after preliminary heat treatment in a mortar,
5. Use a second sieve to remove coarse particles.
このようにして作製した予備熱処理後の粉末1001に
、実施例1と同種、同量の有機バインダ、0]′塑剤、
溶剤を加え、実施例1と同じ条件で、混合、成形した。The powder 1001 after the preliminary heat treatment prepared in this way was added with the same type and amount of organic binder as in Example 1, 0]' plasticizer,
A solvent was added, and the mixture was mixed and molded under the same conditions as in Example 1.
乾燥後の成形体を真空中で1020℃に1時間加熱保持
して焼結し、実施例1と同様形状のアノードを得た。ま
た、実施例1と同様にして多孔度を測定したところ、6
5%の多孔度を示した。The dried molded body was heated and held at 1020° C. for 1 hour in a vacuum to sinter it to obtain an anode having the same shape as in Example 1. In addition, when the porosity was measured in the same manner as in Example 1, it was found that 6
It showed a porosity of 5%.
比較例
基材として、実施例で用いたと同じニッケル粉末90t
1第二元素添加物として粉砕法によって作製した平均粒
径2μmのカロム粉末(淵用金属事務所製)102、実
施例と同種、同量の有機バインダ、可塑剤、溶剤とを実
施例と同じ条件で混合、成形した。As a comparative example base material, 90t of the same nickel powder as used in the example was used.
1 Carom powder (manufactured by Fuchiyo Metal Office) 102 with an average particle size of 2 μm prepared by a pulverization method as a second element additive, the same type and the same amount of organic binder, plasticizer, and solvent as in the example. It was mixed and molded under certain conditions.
乾燥後の成形体を真空中で1080℃に1時間加熱保持
して焼結し、実施例と同様形状のアノードを得た。また
、実施例と同様にして多孔度を測定したところ、59%
の多孔度を示した。The dried molded body was heated and held at 1080° C. for 1 hour in a vacuum to sinter it to obtain an anode having the same shape as in the example. In addition, when the porosity was measured in the same manner as in the example, it was found to be 59%.
showed a porosity of
2と
〔実施例1および比較例の比較〕
Δ
第1−イ図、第2−イ図及び第3−イ図は、それぞれ実
施例1および2と比較例についての0カ
電極の人工破壊面の粒子構造を示す走査電子顕微鏡写真
であり、また、第1−口、ノ・図、第2−ロ、ハ図、第
3−口、71図は、それぞれEPMA(X線マイクロア
ナライザー)による当該部分のニッケルとクロムの特性
X線写真を示す。2 and [Comparison of Example 1 and Comparative Example] Δ Fig. 1-A, Fig. 2-A, and Fig. 3-A are the artificial fracture surfaces of the 0-electrode for Examples 1 and 2 and Comparative Example, respectively. These are scanning electron micrographs showing the particle structures of A characteristic X-ray photograph of nickel and chromium of the part is shown.
これらの図面から分かるように、比較例1には約20μ
mのクロムの偏析部が見られるのに対して、実施例1お
よび2ではクロムは若干の偏析は見られるものの概ね均
一に分布している。As can be seen from these drawings, Comparative Example 1 has approximately 20μ
In contrast, in Examples 1 and 2, chromium is generally uniformly distributed, although some segregation is observed.
また実施例1よりも実施例2の方がクロムの偏析は少な
い。Further, the segregation of chromium is smaller in Example 2 than in Example 1.
前記各図面に示した各電極の人工破壊面のうち、クロム
の偏析がなく、均一に分布していると思われる部分につ
いて、EPMAによるクロムの定量分析を行った。結果
を表1に示す。なお、表中には、参考として前出の焼結
温度および多孔度もあわせて記した。Of the artificially fractured surfaces of each electrode shown in the drawings, a quantitative analysis of chromium was performed using EPMA on a portion where chromium was thought to be uniformly distributed without segregation. The results are shown in Table 1. In addition, the above-mentioned sintering temperature and porosity are also listed in the table for reference.
表
実施例2、実施例1、比較例の順にクロム濃度は高く、
実施例2の場合は添加量の90%に相当するクロム濃度
を示した。The chromium concentration is higher in the order of Example 2, Example 1, and Comparative Example,
In the case of Example 2, the chromium concentration was equivalent to 90% of the added amount.
比較例1の場合にはクロムとニッケルの合金化を促進す
るために、焼結温度を3例中最も高くしたが、クロム濃
度は最も低かった。また、焼結温度が高いために、多孔
度は60%以下と最も低かった。In the case of Comparative Example 1, the sintering temperature was the highest among the three examples in order to promote alloying of chromium and nickel, but the chromium concentration was the lowest. Furthermore, due to the high sintering temperature, the porosity was the lowest at 60% or less.
以上述べた如く、本発明によればニッケル・クロム合金
多孔体からなる溶融炭酸塩型燃料電池用アノードを容易
に製造することができる。As described above, according to the present invention, an anode for a molten carbonate fuel cell made of a porous nickel-chromium alloy can be easily manufactured.
また、本発明の方法は、ニッケル・クロム合金以外の合
金の多孔体の製造にも応用が可能である。Furthermore, the method of the present invention can be applied to the production of porous bodies made of alloys other than nickel-chromium alloys.
本発明のニッケル・クロム合金製アノードの製造法によ
れば、ニッケル粉末中にクロム超微粒子が均一に分散し
偏析することがなく、また、その製造工程も、ニッケル
粉末単独で焼結する場合と同様の工程で、任意組成のニ
ッケル・クロム合金多孔体を容易に製造できる。According to the method for manufacturing a nickel-chromium alloy anode of the present invention, ultrafine chromium particles are uniformly dispersed in nickel powder without segregation, and the manufacturing process is also different from sintering nickel powder alone. A nickel-chromium alloy porous body of any composition can be easily manufactured using a similar process.
第1−イ図、第2−イ図及び第5−イ図は、それぞれ、
実施例1.2及び比較例の電極の人工破壊面における粒
子構造を示す電子顕微鋼写真であり、第1−口図、第2
−口図及び第5−口図は、それぞれのイ図部分のN1の
特性X線写真であり、また、第1−ノ・図、第2−ノ・
図及び第5−ハ図は、それぞれイ図部分のCrの特性X
線写真である。Figure 1-A, Figure 2-A, and Figure 5-A are, respectively,
These are electron micrographs showing the particle structures on the artificially fractured surfaces of the electrodes of Example 1.2 and Comparative Example.
The -mouth view and the 5th -mouth view are N1 characteristic X-ray photographs of the respective A view portions, and the 1st-No. view and the 2nd-No.
Figure 5-C shows the characteristic X of Cr in the part shown in Figure A, respectively.
It is a line photograph.
Claims (1)
ノードを製造する方法において、ニッケル粉末と蒸発法
で製造されたクロム超微粒子とを混合し、成形、焼結す
ることを特徴とするニッケル・クロム合金製アノードの
製造法。 2、前記ニッケル粉末とクロム超微粒子との混合物を、
電極の焼結温度より低い温度で熱処理した後、成形、焼
結することを特徴とする請求項1記載のニッケル・クロ
ム合金製アノードの製造法。[Claims] 1. A method for producing a nickel-chromium alloy anode for a molten carbonate fuel cell, which includes mixing nickel powder and ultrafine chromium particles produced by an evaporation method, and then molding and sintering the mixture. A method for producing a nickel-chromium alloy anode characterized by: 2. The mixture of the nickel powder and ultrafine chromium particles,
2. The method for producing a nickel-chromium alloy anode according to claim 1, wherein the anode is heat-treated at a temperature lower than the sintering temperature of the electrode, and then shaped and sintered.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63253894A JPH02103861A (en) | 1988-10-11 | 1988-10-11 | Method for manufacturing electrodes for molten carbonate fuel cells |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63253894A JPH02103861A (en) | 1988-10-11 | 1988-10-11 | Method for manufacturing electrodes for molten carbonate fuel cells |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02103861A true JPH02103861A (en) | 1990-04-16 |
| JPH0565990B2 JPH0565990B2 (en) | 1993-09-20 |
Family
ID=17257577
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63253894A Granted JPH02103861A (en) | 1988-10-11 | 1988-10-11 | Method for manufacturing electrodes for molten carbonate fuel cells |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02103861A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008166286A (en) * | 2006-12-29 | 2008-07-17 | Doosan Heavy Industries & Construction Co Ltd | Method for manufacturing electrolyte impregnated electrode of molten carbonate fuel cell using wet method |
-
1988
- 1988-10-11 JP JP63253894A patent/JPH02103861A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008166286A (en) * | 2006-12-29 | 2008-07-17 | Doosan Heavy Industries & Construction Co Ltd | Method for manufacturing electrolyte impregnated electrode of molten carbonate fuel cell using wet method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0565990B2 (en) | 1993-09-20 |
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