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JPH027144B2 - - Google Patents
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JPH027144B2 - - Google Patents

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Publication number
JPH027144B2
JPH027144B2 JP56005088A JP508881A JPH027144B2 JP H027144 B2 JPH027144 B2 JP H027144B2 JP 56005088 A JP56005088 A JP 56005088A JP 508881 A JP508881 A JP 508881A JP H027144 B2 JPH027144 B2 JP H027144B2
Authority
JP
Japan
Prior art keywords
electrode
weight
carbon black
added
metal oxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP56005088A
Other languages
Japanese (ja)
Other versions
JPS57119462A (en
Inventor
Toshinori Fujii
Eiichi Fujii
Toshihiko Ochiai
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.)
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Electric Manufacturing Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Electric Manufacturing Co Ltd
Priority to JP56005088A priority Critical patent/JPS57119462A/en
Publication of JPS57119462A publication Critical patent/JPS57119462A/en
Publication of JPH027144B2 publication Critical patent/JPH027144B2/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
    • H01M4/96Carbon-based 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
    • Y02E60/10Energy storage using batteries
    • 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)
  • 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]

[産業上の利用分野] 本発明は、金属−臭素二次電池に用いられる平
板状の枠付き電極に関するものである。 第1図は、本発明の電極が適用される金属−臭
素電池の一例を示す構成図である。ここでは充電
時の状態を示す。電解槽1は、その中央にこの電
解槽1を仕切るイオン交換膜4を有しており、一
方の側に正極5が、他方の側に負極6がそれぞれ
配置されている。正極5の周囲には正極液貯蔵槽
9からポンプ11によつて正極電解液(MBr2
Br2)2が供給され、また負極6の周囲には、負
極液貯蔵槽10からポンプ12によつて負極電解
液(MBr2)3が提供されている。 このような構成の金属−臭素電池の電極として
は、従来は正極材料として臭素の腐食性の面から
耐食性の高い金属材料を中心に使用されており、
Pt電極やRuO2電極が主となつていた。しかしな
がら、これらの金属材料が高価なために、安価な
エネルギー貯蔵手段を提供することを目的とする
本電池系の電極には不適当である。 一方、これらの電極材料に代り、安価なカーボ
ン電極も提案されているが、機械的強度に難点が
あると同時に消耗するため長寿命電池の電極とし
ては不適当である。これらの問題点を改善し、さ
らに軽量で量産性に優れている等の点からポリオ
レフイン系プラスチツクにカーボンブラツク等の
導電性物質を添加混練し成形したカーボンプラス
チツク電極が使用されている。 ところで、金属−臭素二次電池は、電極とセパ
レータを交互に重ね合せてボルトで締付ける等し
て一体化した積層電池として実用されている。こ
の場合にも電極としてカーボンプラスチツク電極
が用いられ、電極は、電極部分の周囲に、絶縁性
の枠部分をヒートプレスあるいはインジエクシヨ
ンモールド法等により形成されて成る。しかし、
電極部分が不均一に熱収縮し、電極全体にそりを
生じたり、電極部分と枠部分の接合部に割れを生
じたりするという問題があつた。このようなそり
のある電極を用いて積層電池を構成すると、そり
の部分に締付のための応力が加わつてひび割れが
生じたり、そのために十分な締付け力が加えられ
ないということが起こり、電解液を循環させた際
に電解液が外部に漏れてしまうという問題が生じ
ていた。 この発明は、かかる点に鑑みてなされたもので
あり、そりやたわみがなく、かつ電気抵抗や機械
強度についても実用に適した特性を有する平板状
の枠付きカーボンプラスチツク電極を提供するこ
とを目的とするものである。 本発明においては、ポリエチレン、ポリプロピ
レン及びエチレン−プロピレン共重合体の1種か
ら成るポリオレフイン系プラスチツク35〜77wt
%、カーボンブラツク20〜45wt%及び酸化珪素、
アルミナから選ばれた少なくとも1つの金属酸化
物粉末3〜20wt%を、加熱加圧下で混練成形し
てなる平板状の電極部分と、該電極部分の全周に
形成された前記ポリオレフイン系プラスチツクと
同一のプラスチツクからなる枠部分とを備えた電
極によつて、上記の目的を達成している。 ここで、本発明において用いるカーボンブラツ
クは、アセチレンブラツク等の電気抵抗の低いカ
ーボンブラツクが望ましく、具体的には
Conductexsc(商品名:コロンビヤ・カーボンブ
ラツク社製)、Vulcan XC−72(商品名:キヤボ
ツト社製)、電化ブラツク(商品名:電気化学工
業(株)製)等が好適である。 また、本発明で用いられる金属酸化物は、添加
によつて本来電極として必要な機械強度や電気抵
抗等の特性に悪影響を与えず、かつ電解液に対す
る耐食性にも優れているものが選択される。この
金属酸化物を添加することにより、電極部分の熱
膨張率が低下し、電極部分の周囲に枠部分を形成
する際の加熱工程における電極の変形を防止する
ことができる。具体的には、SiO2、Al2O3等の金
属酸化物が挙げられる。 次に、上記の素材を用いて電極としてのシート
を製造する方法を説明する。先づ、ベースとなる
プラスチツク粉体とカーボンブラツク及び金属酸
化物粉末の所定量を秤量し、ニーダにて加熱混練
する。この場合のニーダは通常の加圧ニーダが最
適であるが、混練前に混合機により充分混合させ
ることが加圧ニーダによる加熱、混練時間を短時
間に抑え併も均一に混練するために好ましい。こ
こで、混練時間を短時間にすることは、ベースと
なつているプラスチツクの変質を防止するために
も有効な手段である。 本発明における電極部分の抵抗値は、基本的に
はポリオレフイン系プラスチツクへのカーボンブ
ラツクの添加量に依存する。第4図に示されるよ
うに、添加量を増加するにつれて電気抵抗が減少
し、45(重量)%では0.1Ω・cmと低い値になる。
しかし、45(重量)%を越えて添加しても減少割
合は緩慢になり、添加量を増した割には抵抗値が
低下せず、むしろ機械的強度が低下して、プラス
チツク本来の特質が消失してしまう。また混練時
間も長くなり均一な組成の電極を作製することが
難しいために、カーボンブラツク粒子とプラスチ
ツクの界面を通しても電気液が電極内に浸透する
危険がある。また、20%(重量)%未満では、第
4図に示されるように、電気抵抗抵抗が急激に上
昇してしまう。 以上の観点から本発明ではカーボンブラツクの
添加量は電極部分を構成する混練物全体の20〜45
(重量)%としている(詳細後述)。 又、本発明における金属酸化物の添加量は電極
として求められる機械的強度及び電気抵抗(基本
的にはカーボンブラツクの添加量で決るが、カー
ボンブラツク量がほぼ同じであつても金属酸化物
の添加によつて抵抗値は上昇する)の確保と熱変
形防止の両面から電極部分を構成する混練物全体
の3〜20(重量)%としている(詳細後述)。 以下に、本発明を実施例によつて更に詳細に説
明する。 高密度ポリエチレン74.1重量%、カーボンブラ
ツク22.2重量%(高密度ポリエチレン100gに対
して30g)、SiO23.7重量%(高密度ポリエチレン
100gに対して5g)を秤量し、混合機で約10分
間混合した後、あらかじめ180〜200℃に加熱した
加圧ニーダで約5分間混練し、高密度ポリエチレ
ン中にカーボンブラツク及びSiO2とが均一に混
練された状態の塊を得、次で上記の塊をヒートロ
ーラーのロールのギヤツプを調整することにより
任意の厚みのシート状の電極部分を製造した。さ
らに、このシート状電極と金属ネツトを重ね、ヒ
ートローラーに通すことにより層中間に金属ネツ
ト層を持つシート状の電極部分を作製しても良
い。この際のヒートローラの温度は上記混練物の
場合170〜180℃の範囲が適当であつた。 第1表は上記実施例と同様の方法によつて組成
を変えて製造した電極部分のカーボンブラツク及
び金属酸化物の配合量を示したものであり、第2
表は作製したシート状の電極部分の特性を示すも
のである。なお、第1表における配合量はプラス
チツク100gに対する重量(g)であり、厚みは
すべて1mmである。
[Industrial Application Field] The present invention relates to a flat plate-shaped framed electrode used in a metal-bromine secondary battery. FIG. 1 is a block diagram showing an example of a metal-bromine battery to which the electrode of the present invention is applied. Here, the state during charging is shown. The electrolytic cell 1 has an ion exchange membrane 4 partitioning the electrolytic cell 1 at its center, and a positive electrode 5 is placed on one side and a negative electrode 6 is placed on the other side. Around the positive electrode 5, a positive electrode electrolyte (MBr 2 +
Br 2 ) 2 is supplied, and a negative electrode electrolyte (MBr 2 ) 3 is provided around the negative electrode 6 from a negative electrode storage tank 10 by a pump 12 . Conventionally, the electrodes of metal-bromine batteries with such a configuration have mainly been made of metal materials with high corrosion resistance due to the corrosive nature of bromine as the positive electrode material.
The main electrodes were Pt electrodes and RuO2 electrodes. However, the high cost of these metal materials makes them unsuitable for electrodes in the present battery system, which is intended to provide an inexpensive means of energy storage. On the other hand, inexpensive carbon electrodes have been proposed as an alternative to these electrode materials, but they are not suitable as electrodes for long-life batteries because they have drawbacks in mechanical strength and are subject to wear. In order to improve these problems and to be lightweight and suitable for mass production, carbon plastic electrodes are used, which are made by kneading and kneading conductive substances such as carbon black into polyolefin plastics. By the way, a metal-bromine secondary battery is put into practical use as a stacked battery in which electrodes and separators are stacked alternately and integrated by tightening with bolts or the like. In this case as well, a carbon plastic electrode is used as the electrode, and the electrode is formed by forming an insulating frame part around the electrode part by heat pressing, injection molding, or the like. but,
There have been problems in that the electrode portion thermally shrinks unevenly, causing warpage in the entire electrode and cracking at the joint between the electrode portion and the frame portion. If a stacked battery is constructed using such warped electrodes, stress for tightening will be applied to the warped portions, which may cause cracks or cause insufficient tightening force to be applied. There has been a problem in that the electrolyte leaks to the outside when the solution is circulated. The present invention has been made in view of the above, and an object of the present invention is to provide a flat framed carbon plastic electrode that is free from warping and bending and has properties suitable for practical use in terms of electrical resistance and mechanical strength. That is. In the present invention, 35 to 77wt of polyolefin plastic made of one of polyethylene, polypropylene, and ethylene-propylene copolymer
%, carbon black 20-45wt% and silicon oxide,
The flat electrode part is formed by kneading and molding 3 to 20 wt% of at least one metal oxide powder selected from alumina under heat and pressure, and the polyolefin plastic formed around the entire circumference of the electrode part is the same. The above object is achieved by an electrode having a frame part made of plastic. Here, the carbon black used in the present invention is preferably a carbon black with low electrical resistance such as acetylene black, and specifically,
Conductexsc (trade name: manufactured by Columbia Carbon Black Co., Ltd.), Vulcan XC-72 (trade name: manufactured by Kabot Corporation), Denka Black (trade name: manufactured by Denki Kagaku Kogyo Co., Ltd.), etc. are suitable. Furthermore, the metal oxide used in the present invention is selected so that its addition does not adversely affect properties such as mechanical strength and electrical resistance that are originally required for an electrode, and also has excellent corrosion resistance against electrolytes. . By adding this metal oxide, the coefficient of thermal expansion of the electrode portion is reduced, and deformation of the electrode during the heating step when forming a frame portion around the electrode portion can be prevented. Specifically, metal oxides such as SiO 2 and Al 2 O 3 can be mentioned. Next, a method of manufacturing a sheet as an electrode using the above material will be explained. First, predetermined amounts of base plastic powder, carbon black, and metal oxide powder are weighed and heated and kneaded in a kneader. In this case, an ordinary pressure kneader is most suitable, but it is preferable to thoroughly mix the ingredients with a mixer before kneading, in order to keep the heating and kneading time by the pressure kneader short and to ensure uniform kneading. Here, shortening the kneading time is an effective means to prevent deterioration of the base plastic. The resistance value of the electrode portion in the present invention basically depends on the amount of carbon black added to the polyolefin plastic. As shown in FIG. 4, the electrical resistance decreases as the amount added increases, and at 45% (by weight) it reaches a low value of 0.1 Ω·cm.
However, even if more than 45% (by weight) is added, the rate of decrease becomes slow, and the resistance value does not decrease even though the amount added is increased.In fact, the mechanical strength decreases, and the original characteristics of the plastic are lost. It disappears. Furthermore, since the kneading time is long and it is difficult to produce an electrode with a uniform composition, there is a risk that the electric liquid will penetrate into the electrode even through the interface between the carbon black particles and the plastic. On the other hand, if it is less than 20% (by weight), the electrical resistance will increase rapidly as shown in FIG. From the above viewpoint, in the present invention, the amount of carbon black added is 20 to 45% of the total kneaded material constituting the electrode part.
(weight)% (details will be described later). In addition, the amount of metal oxide added in the present invention is determined by the mechanical strength and electrical resistance required for the electrode (basically determined by the amount of carbon black added, but even if the amount of carbon black is approximately the same, the amount of metal oxide The amount is set at 3 to 20% (by weight) of the entire kneaded material constituting the electrode portion, both to ensure that the resistance value increases with addition (the resistance value increases with addition) and to prevent thermal deformation (details will be described later). Hereinafter, the present invention will be explained in more detail with reference to Examples. 74.1% by weight of high-density polyethylene, 22.2% by weight of carbon black (30g per 100g of high-density polyethylene), 3.7% by weight of SiO 2 (high-density polyethylene
5g for 100g), mixed for about 10 minutes in a mixer, and then kneaded for about 5 minutes in a pressure kneader preheated to 180-200℃ to form carbon black and SiO 2 in high-density polyethylene. A homogeneously kneaded lump was obtained, and then a sheet-like electrode portion of an arbitrary thickness was manufactured from the above lump by adjusting the roll gap of a heat roller. Furthermore, a sheet-like electrode portion having a metal net layer between the layers may be produced by overlapping this sheet-like electrode and a metal net and passing it through a heat roller. In the case of the above-mentioned kneaded product, the appropriate temperature of the heat roller at this time was in the range of 170 to 180°C. Table 1 shows the blending amounts of carbon black and metal oxides in electrode parts manufactured with different compositions by the same method as in the above examples.
The table shows the characteristics of the produced sheet-like electrode portion. The amounts in Table 1 are weights (g) per 100 g of plastic, and the thicknesses are all 1 mm.

【表】【table】

【表】【table】

【表】 第1表に示された配合量を重量%に換算すると
電極A〜Kの組成は以下のようになる。 電極A プラスチツク 75.2重量% カーボンブラツク 24.8重量% 電極B、D、F プラスチツク 72.5重量% カーボンブラツク 23.9重量% 金属酸化物粉末 3.6重量% 電極C、E、G プラスチツク 69.9重量% カーボンブラツク 23.1重量% 金属酸化物粉末 7.0重量% 電極H プラスチツク 78.7重量% カーボンブラツク 17.3重量% 金属酸化物粉末 4.0重量% 電極I プラスチツク 75.8重量% カーボンブラツク 16.7重量% 金属酸化物粉末 7.5重量% 電極J プラスチツク 48.8重量% カーボンブラツク 48.8重量% 金属酸化物粉末 2.4重量% 電極K プラスチツク 47.6重量% カーボンブラツク 47.6重量% 金属酸化物粉末 4.8重量% 第6図は、第1表、第2表をグラフ化したもの
で、金属酸化物の添加量(重量%)と電極の電気
抵抗(Ω・cm)および引張強度(Kg/cm2)の関係
を示したものである。図中、、はそれぞれ金
属酸化物を添加しない場合の引張強度と電気抵抗
を、、はそれぞ金属酸化物としてSiO2を添
加した場合の引張強度と電気抵抗を、、はそ
れぞれ金属酸化物としてAl2O3を添加した場合の
引張強度と電気抵抗を、、はカーボンブラツ
クを20wt%未満としてSiO2を添加した場合の引
張強度と電気抵抗を、、はカーボンブラツク
を45wt%以上としてSiO2を添加した場合の引張
強度と電気抵抗を示すものである。 また、第5図は金属酸化物の添加量と熱膨張低
下率%(金属酸化物を添加しない場合を基準とし
た熱膨張率の低下の割合)の関係を示したグラフ
である。 第6図に示されるように、カーボンブラツクの
添加量が20wt%未満では、引張強度は20wt%以
上のものに比べて同程度か若干高いものの(と
、を比較)、電気抵抗値は金属酸化物の添加
量が僅かであつても20wt%以上のものに比べて
かなり高くなつてしまう。(と、を比較)。 一方、カーボンブラツクを45wt%を越えて添
加すると、電気抵抗値は低くなるものの(と
、を比較)、引張強度は金属酸化物をほとん
ど添加しなくとも45wt%以下の場合に比べて大
幅に低下してしまう(と、を比較)。 これらのことから、電気抵抗値と機械強度の両
方の点で実用に適した電極とするには、カーボン
ブラツクの添加量を20〜45wt%とすべきことが
明らかである。 また、金属酸化物の添加量については、第5図
及び第6図のグラフから明らかなように、添加量
が3重量%未満では引張強度が高く電気抵抗も低
いが(カーボンブラツクは20〜45wt%の場合)、
電極部分の熱膨張率の低下は僅かである。即ち、
3重量%未満の添加では枠部分を形成する際の熱
変形を効果的に防止することができない。 一方、金属酸化物を20重量%を越えて添加する
と、電極部分の熱膨張率は大きく低下するが、引
張強度が減少し電気抵抗も上昇してしまう。引張
強度が低下すると、積層電池を構成するために積
層した電極とセパレータをボルト締めする際に電
極が破損してしまい、電極としての機能と果たし
えなくなる。 以上のことから、本発明では金属酸化物の添加
量を3〜20重量%としている。 即ち、カーボンブラツクの添加量を20〜45wt
%、金属酸化物の添加量を3〜20重量%とするこ
とによつて、電極として実用に適する機械強度と
電気抵抗を確保しながら、第5図に示されるよう
に熱膨張率を5〜20%低下させることができる。 次に、上述したシート状の電極部分A(比較
例:プラスチツク75.2重量%、カーボンブラツク
24.8重量%、金属酸化物添加せず)及びB(実施
例:プラスチツク72.5重量%、カーボンブラツク
23.9重量%、金属酸化物粉末3.6重量%)を各10
枚ずつ作製してそれぞれ周囲に枠部分を形成し、
定盤上に枠付き電極を載置してそりの高さhを測
定した。この結果を第3表に示す。なお、積層電
池を構成する場合、電極とセパレータの距離が例
えば1.6mmであるとすると、電極のそりの許容範
囲は0.6mm未満(セパレータまでの距離のほぼ40
%未満)である。
[Table] When the compounding amounts shown in Table 1 are converted to weight percent, the compositions of electrodes A to K are as follows. Electrode A Plastic 75.2% by weight Carbon black 24.8% by weight Electrodes B, D, F Plastic 72.5% by weight Carbon black 23.9% by weight Metal oxide powder 3.6% by weight Electrodes C, E, G Plastic 69.9% by weight Carbon black 23.1% by weight Metal oxide Material powder 7.0% by weight Electrode H Plastic 78.7% by weight Carbon black 17.3% by weight Metal oxide powder 4.0% by weight Electrode I Plastic 75.8% by weight Carbon black 16.7% by weight Metal oxide powder 7.5% by weight Electrode J Plastic 48.8% by weight Carbon black 48.8 Weight% Metal oxide powder 2.4% by weight Electrode K Plastic 47.6% by weight Carbon black 47.6% by weight Metal oxide powder 4.8% by weight Figure 6 is a graph of Tables 1 and 2. The graph shows the relationship between the amount added (wt%) and the electrical resistance (Ω·cm) and tensile strength (Kg/cm 2 ) of the electrode. In the figure, , are the tensile strength and electrical resistance when no metal oxide is added, , are the tensile strength and electrical resistance when SiO 2 is added as a metal oxide, respectively, and , are the tensile strength and electrical resistance when SiO 2 is added as a metal oxide, respectively. The tensile strength and electrical resistance when Al 2 O 3 is added are the tensile strength and electrical resistance when carbon black is less than 20 wt% and SiO 2 is added, , is the tensile strength and electrical resistance when SiO 2 is added when carbon black is 45 wt% or more. This shows the tensile strength and electrical resistance when . Further, FIG. 5 is a graph showing the relationship between the amount of metal oxide added and the thermal expansion reduction rate % (rate of reduction in thermal expansion coefficient based on the case where no metal oxide is added). As shown in Figure 6, when the amount of carbon black added is less than 20wt%, the tensile strength is the same or slightly higher than that of 20wt% or more (compared with), but the electrical resistance value is lower than that of metal oxidation. Even if the amount of added substance is small, it will be considerably higher than that of 20wt% or more. (compare and). On the other hand, when more than 45wt% of carbon black is added, although the electrical resistance value becomes lower (compare and), the tensile strength is significantly lower than when it is less than 45wt% even if almost no metal oxide is added. (compare). From these facts, it is clear that in order to obtain an electrode suitable for practical use in terms of both electrical resistance and mechanical strength, the amount of carbon black added should be 20 to 45 wt%. Regarding the amount of metal oxide added, as is clear from the graphs in Figures 5 and 6, if the amount added is less than 3% by weight, the tensile strength is high and the electrical resistance is low (carbon black is 20 to 45wt%). %in the case of),
The decrease in the coefficient of thermal expansion of the electrode portion is slight. That is,
If less than 3% by weight is added, thermal deformation during the formation of the frame portion cannot be effectively prevented. On the other hand, if more than 20% by weight of metal oxide is added, the coefficient of thermal expansion of the electrode portion will be greatly reduced, but the tensile strength will also decrease and the electrical resistance will increase. If the tensile strength decreases, the electrodes will be damaged when bolting the stacked electrodes and separators together to form a stacked battery, and the electrodes will no longer function as electrodes. From the above, in the present invention, the amount of metal oxide added is set at 3 to 20% by weight. In other words, the amount of carbon black added is 20 to 45wt.
%, and by adjusting the amount of metal oxide added from 3 to 20% by weight, the coefficient of thermal expansion can be increased from 5 to 5%, as shown in Figure 5, while ensuring mechanical strength and electrical resistance suitable for practical use as an electrode. Can be reduced by 20%. Next, the above-mentioned sheet-like electrode part A (comparative example: plastic 75.2% by weight, carbon black
24.8% by weight, no metal oxide added) and B (Example: Plastic 72.5% by weight, carbon black)
23.9 wt%, metal oxide powder 3.6 wt%) each 10
Create one sheet at a time and form a frame around each.
A framed electrode was placed on a surface plate and the height h of the warp was measured. The results are shown in Table 3. In addition, when configuring a stacked battery, if the distance between the electrode and the separator is, for example, 1.6 mm, the allowable range for electrode warpage is less than 0.6 mm (approximately 40 mm of the distance to the separator).
(less than %).

【表】 第3表に示された測定結果から明らかなよう
に、本発明による電極は枠形成のための加熱工程
における変形が大幅に改善されている。 次に、亜鉛−臭素二次電池で使用されるZnBr2
に4mol/lのKClを添加した溶液で第1表に示
す各電極の分極特性を測定した結果を第2図、第
3図に示す。第2図は電極の負極分極曲線であ
り、第3図は電極の正極分極曲線である。 第2図および第3図の結果から、本発明の電極
は高電流密度領域まで電圧が平坦であることが分
り、本電池系においてZn過電圧、臭素過電圧の
面からも十分有利な特性である。 以上のように本発明においては、電極部分に金
属酸化物粉末を添加して組成を特性のものとした
ことにより、電極として実用に適する電気抵抗や
機械強度を確保しながら電極部分の熱膨張率を低
下させている。このため、電極部分の周囲に枠部
分を形成する際の加熱工程において電極全体にそ
りやたわみが生じたり、電極部分と枠部分の接合
部に割れが発生したりするのを防止することがで
きる。 従つて、本発明による電極を用いれば、電極を
積層して枠部分と電極部分で電解槽を形成する場
合に、電解槽を気密に保つことができ、電解液が
漏れるのを防止することができる。 また、電極とセパレータを交互に重ね合せ、ボ
ルトなどで締付けて一体化して積層電池を構成す
る場合、電極にそり等の変形が生じていないの
で、締付け圧によつて電極にひび割れが生じたり
積層電池が変形したりすることがない。
[Table] As is clear from the measurement results shown in Table 3, the electrode according to the present invention has significantly improved deformation during the heating process for forming the frame. Next, ZnBr 2 used in zinc-bromine secondary batteries
Figures 2 and 3 show the results of measuring the polarization characteristics of each electrode shown in Table 1 using a solution in which 4 mol/l of KCl was added. FIG. 2 is a negative polarization curve of the electrode, and FIG. 3 is a positive polarization curve of the electrode. From the results shown in FIGS. 2 and 3, it can be seen that the electrode of the present invention has a flat voltage up to a high current density region, which is a sufficiently advantageous characteristic in terms of Zn overvoltage and bromine overvoltage in this battery system. As described above, in the present invention, by adding metal oxide powder to the electrode part to make the composition specific, the thermal expansion coefficient of the electrode part is ensured while ensuring electrical resistance and mechanical strength suitable for practical use as an electrode. is decreasing. Therefore, it is possible to prevent the entire electrode from warping or bending during the heating process when forming the frame around the electrode, and from cracking at the joint between the electrode and the frame. . Therefore, if the electrode according to the present invention is used, when the electrodes are stacked to form an electrolytic cell with the frame part and the electrode part, the electrolytic cell can be kept airtight and leakage of the electrolyte can be prevented. can. In addition, when forming a laminated battery by stacking electrodes and separators alternately and tightening them with bolts etc., the electrodes do not warp or otherwise deform, so the clamping pressure may cause cracks in the electrodes or the stacking The battery will not be deformed.

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

第1図は金属−臭素二次電池の構成図であり、
第2図及び第3図は本発明の実施例の電極の分極
特性を示すグラフであつて、第2図は負極分極曲
線、第3図は正極分極曲線を示す。また、第4図
はカーボンブラツクの添加量と電気抵抗の関係を
示すグラフ、第5図は金属酸化物の添加量と熱膨
張低下率の関係を示すグラフ、第6図は金属酸化
物の添加量と電気抵抗及び引張強度の関係を示す
グラフである。
Figure 1 is a block diagram of a metal-bromine secondary battery.
FIGS. 2 and 3 are graphs showing the polarization characteristics of electrodes according to examples of the present invention, with FIG. 2 showing a negative polarization curve and FIG. 3 showing a positive polarization curve. Also, Figure 4 is a graph showing the relationship between the amount of carbon black added and electrical resistance, Figure 5 is a graph showing the relationship between the amount of metal oxide added and the coefficient of thermal expansion reduction, and Figure 6 is the graph showing the relationship between the amount of metal oxide added and the reduction in thermal expansion. It is a graph showing the relationship between the amount, electrical resistance, and tensile strength.

Claims (1)

【特許請求の範囲】 1 電極部分と絶縁性の枠部分とが一体に形成さ
れてなる金属−臭素電池の電極において、 ポリエチレン、ポリプロピレン及びエチレン−
プロピレン共重合体の1種から成るポリオレフイ
ン系プラスチツク35〜77wt%、カーボンブラツ
ク20〜45wt%、および酸化珪素、アルミナから
選ばれた少なくとも1つの金属酸化物粉末3〜
20wt%を、加熱加圧下で混練成形してなる平板
状の電極部分と、 該電極部分の全周に一体に形成された前記ポリ
オレフイン系プラスチツクと同一のプラスチツク
からなる枠部分とを備えたことを特徴とする金属
−臭素電池の電極。
[Claims] 1. An electrode for a metal-bromine battery in which an electrode portion and an insulating frame portion are integrally formed, comprising: polyethylene, polypropylene, and ethylene.
35 to 77 wt% of polyolefin plastic made of one type of propylene copolymer, 20 to 45 wt% of carbon black, and 3 to 30% of at least one metal oxide powder selected from silicon oxide and alumina.
20 wt% is kneaded and molded under heat and pressure to form a flat plate-shaped electrode part, and a frame part made of the same polyolefin plastic as the polyolefin plastic integrally formed around the entire circumference of the electrode part. Features of metal-bromine battery electrodes.
JP56005088A 1981-01-19 1981-01-19 Electrode for metal-bromine battery and its manufacture Granted JPS57119462A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56005088A JPS57119462A (en) 1981-01-19 1981-01-19 Electrode for metal-bromine battery and its manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56005088A JPS57119462A (en) 1981-01-19 1981-01-19 Electrode for metal-bromine battery and its manufacture

Publications (2)

Publication Number Publication Date
JPS57119462A JPS57119462A (en) 1982-07-24
JPH027144B2 true JPH027144B2 (en) 1990-02-15

Family

ID=11601633

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56005088A Granted JPS57119462A (en) 1981-01-19 1981-01-19 Electrode for metal-bromine battery and its manufacture

Country Status (1)

Country Link
JP (1) JPS57119462A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5996663A (en) * 1982-11-24 1984-06-04 Meidensha Electric Mfg Co Ltd Conductive plastic electrode for bromine zinc battery
JPS59215667A (en) * 1983-05-24 1984-12-05 Meidensha Electric Mfg Co Ltd Electrode of zinc-bromine cell
JPS59215670A (en) * 1983-05-24 1984-12-05 Meidensha Electric Mfg Co Ltd Electrode of zinc-bromine cell

Also Published As

Publication number Publication date
JPS57119462A (en) 1982-07-24

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