JPH0119628B2 - - Google Patents
Info
- Publication number
- JPH0119628B2 JPH0119628B2 JP57044476A JP4447682A JPH0119628B2 JP H0119628 B2 JPH0119628 B2 JP H0119628B2 JP 57044476 A JP57044476 A JP 57044476A JP 4447682 A JP4447682 A JP 4447682A JP H0119628 B2 JPH0119628 B2 JP H0119628B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- air
- iron phthalocyanine
- present
- cobalt vanadate
- 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
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
- H01M4/90—Selection of catalytic material
-
- 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)
- Inert Electrodes (AREA)
Description
【発明の詳細な説明】
本発明は、分極が小さく、大電流の取得を可能
にする燃料電池または空気電池用の電極、さらに
詳細には、燃料電池または空気電池の空気極また
は酸素極において、該電極が触媒として鉄フタロ
シアニンとコバルトバナデートCO2V2O7の両物
質を含有する新規な上記電極に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides an electrode for a fuel cell or an air cell that has small polarization and can obtain a large current, and more specifically, an air electrode or an oxygen electrode for a fuel cell or an air cell. The present invention relates to the above novel electrode, wherein the electrode contains both iron phthalocyanine and cobalt vanadate CO 2 V 2 O 7 as catalysts.
従来、燃料電池、空気電池用の空気極または酸
素極に用いる触媒については、種々の提案がなさ
れている。 Conventionally, various proposals have been made regarding catalysts used in air electrodes or oxygen electrodes for fuel cells and air cells.
すなわち、燃料電池用の空気極触媒又は酸素極
触媒としては、銅、銀、金、白金、パラジウム等
の金属類、タングステンプロンズ、鉄又は銅フタ
ロシニアン、活性炭及びリチウムをドープした酸
化ニツケル等が知られ、又、空気電池用の空気極
触媒としては、白金、パラジウム、ルチニウム及
び銀等の貴金属類、銀と水銀及びルチニウムと金
等の合金類、マンガン及びオスミウム等の遷移金
属の酸化物類及びNiFe2O4、CoFe2O4、NiCr2O4
及びCoAl2O4等のスピネル酸化物類が知られてい
る。 That is, as air electrode catalysts or oxygen electrode catalysts for fuel cells, metals such as copper, silver, gold, platinum, and palladium, tungsten bronze, iron or copper phthalocyanine, activated carbon, and nickel oxide doped with lithium are known. In addition, as air electrode catalysts for air batteries, noble metals such as platinum, palladium, rutinium and silver, alloys of silver and mercury and rutinium and gold, oxides of transition metals such as manganese and osmium, and NiFe2O4 , CoFe2O4 , NiCr2O4 _
Spinel oxides such as CoAl 2 O 4 and CoAl 2 O 4 are known.
しかしながら、従来技術におけるこれらの触媒
のうち、貴金属類は高価なため経済的でなく、そ
れ以外のものは安価であるが、これを触媒として
用いた空気極又は酸素極はその分極が貴金属より
大きく、又、大電流密度領域におけるかなりの電
位抵下が避けられない等、その電極特性が十分に
良好でなく、ひいては、このような電極を組み込
んだ燃料電池及び空気電池において、大電流が取
得できないという欠点があつた。 However, among these catalysts in the prior art, noble metals are expensive and therefore uneconomical, while others are inexpensive, but the air electrode or oxygen electrode using these as catalysts has a polarization greater than that of noble metals. In addition, the electrode characteristics are not sufficiently good, such as a considerable potential drop in the high current density region being unavoidable, and as a result, large currents cannot be obtained in fuel cells and air cells incorporating such electrodes. There was a drawback.
本発明はこのような現状に鑑みてなされたもの
であり、その目的は、分極が小さく、大電流密度
領域においても電位低下が殆んど起こらず、大電
流の取得が可能である高エネルギー密度の燃料電
池、空気電池用電極を提供することである。 The present invention has been made in view of the current situation, and its purpose is to provide a high energy density device with small polarization, almost no potential drop even in a high current density region, and a high current that can be obtained. The present invention provides electrodes for fuel cells and air cells.
本発明につき概説すれば、本発明の燃料電池及
び空気電池用電極は、正極が触媒として鉄フタロ
シアニン及びコバルトバナデートを含有すること
を特徴とするものである。 To summarize the present invention, the electrode for fuel cells and air cells of the present invention is characterized in that the positive electrode contains iron phthalocyanine and cobalt vanadate as a catalyst.
これまで燃料電池及び空気電池用の空気極又は
酸素極に触媒として鉄フタロシアニン及びコバル
トバナデートの両物質を共に用いた例はない。本
発明によれば、電極に鉄フタロシアニン及びコバ
ルトバナデート両物質を含有させる新規な構成に
より、後述するように各々単独に用いるよりも分
極を小さくし、かつ、大電流の取得を可能にする
という優れた複合効果が得られる。 Until now, there has been no example of using both iron phthalocyanine and cobalt vanadate as catalysts in air electrodes or oxygen electrodes for fuel cells and air cells. According to the present invention, a novel configuration in which the electrode contains both iron phthalocyanine and cobalt vanadate makes it possible to reduce polarization and obtain a large current compared to when each is used alone, as described below. Excellent combined effects can be obtained.
本発明を更に詳しく説明する。 The present invention will be explained in more detail.
燃料電池は、負極活物質として水素ガス等を使
用し、電解質としてKOH、NaOH等のアルカリ
電解質、NaCl、KCl等の中性電解質、リン酸等
の酸性電解質を使用して構成され、また、空気電
池は負極活物質として亜鉛、アルミニウム、マグ
ネシウム、白金またはこれらの合金等を使用し、
電解質として上記と同じものを使用して構成され
る。 A fuel cell is constructed by using hydrogen gas as a negative electrode active material, alkaline electrolytes such as KOH and NaOH, neutral electrolytes such as NaCl and KCl, and acidic electrolytes such as phosphoric acid as electrolytes. Batteries use zinc, aluminum, magnesium, platinum, or alloys of these as negative electrode active materials,
It is constructed using the same electrolyte as above.
本発明における電極は、上述の燃料電池ないし
空気電池の正極として用いられるが、上記正極材
料は、炭素粉末、活性炭、グラフアイト、または
アセチレンブラツク等の炭素物質とテフロン等の
溌水剤等との混合粉体から成り、本発明によれ
ば、これに鉄フタロシアニン及びコバルトバナデ
ートの混合物質を触媒として混合等の手段により
担持する。 The electrode of the present invention is used as a positive electrode of the above-mentioned fuel cell or air cell, and the above-mentioned positive electrode material is a combination of a carbon material such as carbon powder, activated carbon, graphite, or acetylene black, and a water repellent agent such as Teflon. It consists of a mixed powder, and according to the present invention, a mixed substance of iron phthalocyanine and cobalt vanadate is supported thereon as a catalyst by means such as mixing.
正極電極は、上記炭素物質、溌水剤及び鉄フタ
ロシアニン及びコバルトバナデートから成る混合
粉体をニツケル、銀等の金属網と共に成形圧着
し、これを加熱焼成して作製することができる。 The positive electrode can be produced by molding and pressing a mixed powder consisting of the carbon material, water repellent, iron phthalocyanine, and cobalt vanadate together with a metal mesh of nickel, silver, etc., and then heating and baking the mixture.
本発明における上記鉄フタロシアニン及びコバ
ルトバナデート混合体が複合触媒として有効であ
る理由は、正極の電極反応のうち最も効率のよい
4電子反応(O2+2H2O+4l-→40H-)を選択し
得る鉄フタロシアニンと、4電子反応の選択性が
低い場合(O2+H2O+2l-→HO2 --+OH-、
HO2 -→1/202+OH-の2電子反応が優勢とな
る)においても生成する中間体(酸性電解質使用
の場合:H2O2、アルカリ電解質使用の場合:
HO2 -)の分解速度を大きくするコバルトバナデ
ートを共に担持することにより、どのような反応
プロセスをとろうとも電極反応を十分円滑に進め
るに足る電子の供給が容易であるためと考えられ
る。特に測定の結果では、中間体の分解速度は、
白金黒とほぼ同程度であり、鉄フタロシアニン単
独の場合の2倍に達している。 The reason why the above-mentioned mixture of iron phthalocyanine and cobalt vanadate in the present invention is effective as a composite catalyst is that the most efficient four-electron reaction (O 2 + 2H 2 O + 4l - → 40H - ) can be selected among the positive electrode reactions. When the selectivity of the four-electron reaction with iron phthalocyanine is low (O 2 +H 2 O+2l - →HO 2 -- +OH - ,
HO 2 - → 1/20 2 +OH - two - electron reaction is predominant) .
This is thought to be because by supporting cobalt vanadate, which increases the decomposition rate of HO 2 - ), it is easy to supply enough electrons to make the electrode reaction proceed smoothly no matter what reaction process is used. In particular, the results of the measurements show that the decomposition rate of the intermediate is
It is almost the same as platinum black, and twice as much as iron phthalocyanine alone.
鉄フタロシアニンとコバルトバナデートの混合
比は好ましくは鉄フタロシアニン1に対しコバル
トバナデート0.1〜9である。0.1未満であると鉄
フタロシアニン単独の効果と同様となり、一方9
を超えるとコバルトバナデート単独の効果同様と
なつて、いずれも混合する利点が失なわれるおそ
れがあるからである。 The mixing ratio of iron phthalocyanine and cobalt vanadate is preferably 1 part iron phthalocyanine to 0.1 to 9 parts cobalt vanadate. If it is less than 0.1, the effect will be similar to that of iron phthalocyanine alone, while 9
This is because if it exceeds the above, the effect will be similar to that of cobalt vanadate alone, and the advantage of mixing both may be lost.
次に、本発明における正極の構造を図面により
説明する。すなわち、第1図は本発明における正
極(空気極)の構造の一具体例を示した断面概略
図を示し、1は電極材料層、2はニツケル製網を
示す。 Next, the structure of the positive electrode in the present invention will be explained with reference to the drawings. That is, FIG. 1 shows a schematic cross-sectional view showing a specific example of the structure of the positive electrode (air electrode) according to the present invention, in which 1 shows an electrode material layer and 2 shows a nickel mesh.
この空気極を電池に組み込むに当つては、電極
材料層1が電解質に、ニツケル製網がガスに接す
るように向きを定める。この結果、電極材料層1
中に電解質、ガス及び電極粉体の三相界面が形成
される。なお、ニツケル製網2は、電極材料層1
の支持体及び集電体として設けられる。なお、こ
の際、電極の寿命を延ばすために、ガス側に接す
る金属網の外側に、第2の電極材料層をサンドイ
ツチ型に設けてもよく、この場合、第2の電極材
料層は、電解質側に設けた第1の電極材料層より
溌水剤の混合割合を多くして溌水性を高め、か
つ、多孔性を大にする。 When this air electrode is assembled into a battery, it is oriented so that the electrode material layer 1 is in contact with the electrolyte and the nickel mesh is in contact with the gas. As a result, electrode material layer 1
A three-phase interface of electrolyte, gas and electrode powder is formed therein. Note that the nickel net 2 has an electrode material layer 1
It is provided as a support and a current collector. In this case, in order to extend the life of the electrode, a second electrode material layer may be provided in a sanderch type on the outside of the metal mesh in contact with the gas side. In this case, the second electrode material layer The mixing ratio of the water repellent agent is higher than that of the first electrode material layer provided on the side to increase water repellency and increase porosity.
次に、本発明を実施例によつて説明するが、本
発明はこれにより何ら限定されるものではない。
なお、実施例における電極電位の電流依存性の測
定は20〜25℃の室温中で行なつた。 Next, the present invention will be explained with reference to Examples, but the present invention is not limited thereto in any way.
In addition, the measurement of the current dependence of the electrode potential in the Examples was carried out at room temperature of 20 to 25°C.
実施例 1
炭素粉末(200メツシユ通過)4g、アセチレン
ブラツク4g、鉄フタロシアニンとコバルトバナ
デートの触媒混合物0.2gとテフロンエマルジヨン
(テフロン60%含有)3.3gをよく混合し、ロール
でシート状にする。シートを30分間程度空気中で
乾燥させた後、片側にニツケル製網(50メツシ
ユ)を置き、250℃の温度、100Kg/cm2の圧で30分
間ホツトプレスする。空気中で冷却し、直径30mm
の円形に切り出して空気極(正極)を作製した。
なおコバルトバナデートはCoOとV2O5の所定量
(2:1)を690℃、24時間の焼成を空気中で行な
つて得た。電解質としてIN KOHを使用し、亜
鉛を負極として空気電池を構成し、空気中で空気
極の電極電位(E、対飽和カロメル電極)の電流
密度依存性を調べた。結果を第2図に示す。すな
わち、第2図は、本実施例における空気極の電流
密度と電極電圧との関係を示したグラフであり、
Aは本実施例のうち、混合触媒重量の割合が鉄フ
タロシアニン1:1コバルトバナデートの場合、
Bは本実施例のうち混合触媒の重量割合が鉄フタ
ロシアニン4:1コバルトバナデートの場合、C
は本実施例のうち割合が鉄フタロシアニン1:4
コバルトバナデートの場合、D、Eは併せて行な
つた従来既知の触媒を用いた空気極の場合であ
り、Dは鉄フタロシアニン、Eは銀触媒を用いた
場合である。Example 1 4 g of carbon powder (passed through 200 meshes), 4 g of acetylene black, 0.2 g of a catalyst mixture of iron phthalocyanine and cobalt vanadate, and 3.3 g of Teflon emulsion (containing 60% Teflon) were mixed well and formed into a sheet using a roll. . After the sheet is dried in the air for about 30 minutes, a nickel mesh (50 mesh) is placed on one side and hot pressed at a temperature of 250°C and a pressure of 100 kg/cm 2 for 30 minutes. Cooled in air, diameter 30mm
An air electrode (positive electrode) was prepared by cutting out a circular shape.
Cobalt vanadate was obtained by calcining a predetermined amount (2:1) of CoO and V 2 O 5 at 690° C. for 24 hours in air. An air battery was constructed using IN KOH as the electrolyte and zinc as the negative electrode, and the dependence of the electrode potential (E, vs. saturated calomel electrode) of the air electrode in air on current density was investigated. The results are shown in Figure 2. That is, FIG. 2 is a graph showing the relationship between the current density of the air electrode and the electrode voltage in this example,
In this example, A is when the weight ratio of the mixed catalyst is iron phthalocyanine 1:1 cobalt vanadate,
In this example, B is C when the weight ratio of the mixed catalyst is iron phthalocyanine 4:1 cobalt vanadate.
In this example, the ratio is iron phthalocyanine 1:4.
In the case of cobalt vanadate, D and E are the air electrodes using a conventionally known catalyst, D is the case where iron phthalocyanine is used, and E is the case where a silver catalyst is used.
第2図によると、鉄フタロシアニンとコバルト
バナデートが1:1の重量比で混合担持された場
合、平衡電位が+0.014V(対SCE≪飽和カロメル
電極≫)、100mA/cm2のとき−0.61(対SCE)、一
方、鉄フタロシアニンとコバルトバナデートが
4:1の重量比で混合担持された場合には平衝電
位が+0.024V(対SCE)、100mA/cm2のとき−
0.061V(対SCE)となる。 According to Figure 2, when iron phthalocyanine and cobalt vanadate are mixed and supported at a weight ratio of 1:1, the equilibrium potential is +0.014V (vs. SCE <<saturated calomel electrode>>) and -0.61 at 100mA/ cm2 . (vs. SCE), On the other hand, when iron phthalocyanine and cobalt vanadate are mixed and supported at a weight ratio of 4:1, the equilibrium potential is +0.024 V (vs. SCE), and - at 100 mA/cm 2
It becomes 0.061V (vs. SCE).
第2図から明らかなように、鉄フタロシアニン
や銀を用いた従来の場合に比し、鉄フタロシアニ
ンとコバルトバナデートを混合して用いた本発明
の場合には、平衡電位が高く、分極が小さく、か
つ大電流密度領域でも電位の大幅な低下が見られ
ず安定している。 As is clear from Figure 2, compared to the conventional case using iron phthalocyanine and silver, the equilibrium potential is higher and the polarization is smaller in the case of the present invention using a mixture of iron phthalocyanine and cobalt vanadate. , and is stable with no significant drop in potential even in the high current density region.
以上説明したように、鉄フタロシアニンとコバ
ルトバナデートの両物質を触媒として混合担持し
た本発明における正極(空気極または酸素極)
は、分極が小さく、かつ、大電流密度領域におい
ても電位低下が殆んど起こらず、この点、従来の
ものに比し優れた効果を発揮するものである。従
つて、この電極を正極として組み込んだ燃料電池
及び空気電池は、大電流の取得ができ、また、よ
り一層の高エネルギー密度化が可能であり、従来
品に比し極めて高い実用価値を期待することがで
きる。 As explained above, the positive electrode (air electrode or oxygen electrode) in the present invention supports a mixture of iron phthalocyanine and cobalt vanadate as catalysts.
The polarization is small, and there is almost no potential drop even in the high current density region, and in this respect, it exhibits superior effects compared to conventional ones. Therefore, fuel cells and air cells incorporating this electrode as a positive electrode can obtain large currents and have even higher energy density, and are expected to have extremely high practical value compared to conventional products. be able to.
第1図は本発明における正極(空気極)の構造
の一具体例を示した断面概略図、第2図はそれぞ
れ本発明の実施例の空気極の電流密度と電極電位
の関係を示したグラフである。
1……電極材料層、2……ニツケル製網。
FIG. 1 is a cross-sectional schematic diagram showing a specific example of the structure of the positive electrode (air electrode) according to the present invention, and FIG. 2 is a graph showing the relationship between current density and electrode potential of the air electrode of the embodiment of the present invention. It is. 1... Electrode material layer, 2... Nickel net.
Claims (1)
合金属酸化物であるコバルトバナデートを触媒と
して含有することを特徴とする燃料電池、空気電
池用電極。1. An electrode for a fuel cell or an air cell, which contains iron phthalocyanine, which is a transition metal complex, and cobalt vanadate, which is a composite metal oxide, as a catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57044476A JPS58163174A (en) | 1982-03-23 | 1982-03-23 | Electrode for fuel cell and air battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57044476A JPS58163174A (en) | 1982-03-23 | 1982-03-23 | Electrode for fuel cell and air battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58163174A JPS58163174A (en) | 1983-09-27 |
| JPH0119628B2 true JPH0119628B2 (en) | 1989-04-12 |
Family
ID=12692575
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57044476A Granted JPS58163174A (en) | 1982-03-23 | 1982-03-23 | Electrode for fuel cell and air battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58163174A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013016474A (en) * | 2011-06-06 | 2013-01-24 | Sumitomo Chemical Co Ltd | Positive electrode catalyst for air secondary battery and air secondary battery |
| JP6026793B2 (en) * | 2011-11-17 | 2016-11-16 | 株式会社日本触媒 | Electrode catalyst and method for producing the same |
| JP6713258B2 (en) * | 2015-08-06 | 2020-06-24 | 株式会社日本触媒 | Air electrode catalyst |
-
1982
- 1982-03-23 JP JP57044476A patent/JPS58163174A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58163174A (en) | 1983-09-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0667041B1 (en) | Bifunctional airelectrode | |
| US5069988A (en) | Metal and metal oxide catalyzed electrodes for electrochemical cells, and methods of making same | |
| US4132619A (en) | Electrocatalyst | |
| JPH11126616A (en) | Electrodes for co-resistant platinum zinc fuel cells | |
| JP4568124B2 (en) | Air electrode and air secondary battery using the air electrode | |
| JPS618851A (en) | Fuel battery and electrolyte catalyst therefor | |
| US6428931B1 (en) | Methods for making oxygen reduction catalyst using micelle encapsulation and metal-air electrode including said catalyst | |
| US3453149A (en) | Fluorocarbon matrix membrane containing free acid and method of fabricating | |
| JP3586883B2 (en) | Catalyst for oxygen reduction electrode | |
| US3753782A (en) | Electrode for electrochemical reduction of oxygen and process for its production | |
| WO1999035701A1 (en) | Zinc based electrochemical cell | |
| US3357863A (en) | Rhodium catalyst and fuel cell | |
| JPH04348B2 (en) | ||
| JP4937527B2 (en) | Platinum catalyst for fuel cell and fuel cell including the same | |
| JPH0677460B2 (en) | Method for producing positive electrode for fuel cell / air cell | |
| JPS6319981B2 (en) | ||
| CN118198385A (en) | Oxygen electrocatalytic material and preparation and application thereof | |
| Dong et al. | An air–metal hydride battery using MmNi3. 6Mn0. 4Al0. 3Co0. 7 in the anode and a perovskite in the cathode | |
| Gamburzev et al. | Development of a novel metal hydride–air secondary battery | |
| US3429750A (en) | Process for preparing an improved platinum electrode | |
| US3709834A (en) | Method of making a uranium containing catalyst for a metal electrode | |
| WO1991020102A1 (en) | Metal and metal oxide catalyzed electrodes for electrochemical cells, and methods of making same | |
| JPH04345B2 (en) | ||
| JPS58163174A (en) | Electrode for fuel cell and air battery | |
| Abrashev et al. | Optimization of the bi-functional oxygen electrode (BOE) structure for application in a Zn-air accumulator |