Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0358149B2 - - Google Patents
[go: Go Back, main page]

JPH0358149B2 - - Google Patents

Info

Publication number
JPH0358149B2
JPH0358149B2 JP58223261A JP22326183A JPH0358149B2 JP H0358149 B2 JPH0358149 B2 JP H0358149B2 JP 58223261 A JP58223261 A JP 58223261A JP 22326183 A JP22326183 A JP 22326183A JP H0358149 B2 JPH0358149 B2 JP H0358149B2
Authority
JP
Japan
Prior art keywords
electrode
carbon
electrodes
plastic
conductive sheet
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
JP58223261A
Other languages
Japanese (ja)
Other versions
JPS60117559A (en
Inventor
Akihiko Hirota
Eiichi Fujii
Toshinori Fujii
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 JP58223261A priority Critical patent/JPS60117559A/en
Publication of JPS60117559A publication Critical patent/JPS60117559A/en
Publication of JPH0358149B2 publication Critical patent/JPH0358149B2/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)
  • Hybrid Cells (AREA)

Description

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

〔発明の技術分野〕 本発明は、臭素−亜鉛電池において使用するカ
ーボンプラスチツク電極に係り、高温処理したカ
ーボン繊維から成る導電性シートを従来のカーボ
ンプラスチツク部材の表面にバツキング(裏う
ち)処理を行うことによつて、電気化学的反応の
効率向上とその効率を安定して維持することので
きるカーボンプラスチツク電極に関するものであ
る。 〔従来技術〕 臭素−亜鉛系の二次電池において従来から用い
られている電極を材料面から大別すると、金属を
使用した金属電極、炭素自体を利用した炭素電極
及びプラスチツクに導電性材料(例えは、カーボ
ン、銀など)を混練して導電性を付与させたプラ
スチツク電極がある。 このうち、金属電極においては、電池を充電す
る際に発生する臭素分子の腐食作用を考慮すると
その材質は例えば白金などの貴金属に限定され
る。これら貴金属は、一般に電気抵抗が非常に小
さく電池の電圧効率も良好であるし、放電時にお
ける放電時間も長くなりかつクーロン効率も優れ
ているという利点を有しているが、最大の欠点は
その価格が高く結局実用には不向きである。 また、炭素電極は、金属電極に次いで電気抵抗
が低いものではあるが、機械的強度が弱く特に衝
撃によるクラツク発生のおそれが充分に高くその
信頼性に問題がある。加うるに炭素電極は、一般
的に多孔性であるため電去自体に隔離板の機能を
もたせるバイボーラ型直列積層電池システムには
その使用ができないという欠点を有するものであ
る。 最後にプラスチツク電極は、機械的強度につい
ては充分満足できるがその電気抵抗が高く、また
クーロン効率にいおいても活物質との反応性が小
さく、その結果低効率に甘んじなければならない
という問題点が残つている。 以上のように各材質にはそれぞれ経済性、寿
命、効率などにおいて一長一短があり、臭素−亜
鉛系二次電池に安心して使用できる電極材料は未
だに見出されていない。 本願発明者等は先に以上の問題点を解決する電
極として特開昭57−197772号にて、導電極プラス
チツク部材表面に接着剤層を介しあるいは介さな
いままで炭素繊維からなり、フエルト、ニツトま
たはクロス形態中から選ばれた導電性シートの層
を形成してなるプラスチツク電極を提案した。然
しながら未だ不充分である。 〔発明の目的〕 本発明はこのような情況の中で高効率長寿命、
廉価な電極材料を得るために種々検討を加え、電
池の電圧効率、クーロン効率を比較的容易に向上
させることが可能な電極を得ることを目的とする
ものである。 〔発明の概要〕 本発明は、前述の研究に更に改良を加え得られ
たもので上記炭素繊維からないフエルト、ニツト
またはクロス形態中から選ばれた導電性シートを
導電性プラスチツク部材表面にバツキングする前
に高温処理を行なうことも特徴とするカーボンプ
ラスチツク電極にある。 電極基体を構成する導電性のプラスチツク部材
のペースポリマーは、遊離臭素ないしはイオン状
態の臭素と長時間接触していても変質の起りにく
いものという条件を満足させる必要からポリオレ
フインが使用される。 導電性プラスチツク部材(CP)は、例えば高
密度ポリエチレン100重量部にカーボンブラツク
50重量部を混練してプレス成形などにより作るこ
とができる。 更に本発明における導電性シートの高温処理の
方法は上記フエルト、ニツト、クロスなどの形態
を保つている炭素繊維から成るシートを、微量酸
素雰囲気中で、一般には電気炉中にて1000〜2000
℃、10分〜2時間加熱するものである。 高温処理した導電性シートを従来の導電性プラ
スチツク部材(CP)の表面に従来法でバツキン
グして得られる電極(HT.CC−CP電極という。)
はどの形態の導電性シートを用いたものでも従来
の高温処理しない導電性シートをバツキングした
電極(CC−CP電極)に比べて特性が向上してい
る。処理面、即ちHT.CC−CP電極の比抵抗(p)を
測定すると従来のCC−CP電極に比較して低下し
ており、これは高温処理によつて炭素繊維が黒鉛
化することによりシートの導電性が増加しHT.
CC−CP電極の低比抵抗化に寄与するものであ
る。熱処理時間、及び温度でカーボンプラスチツ
ク電極の特性は異なるが、これは、高温処理によ
る炭素繊維の黒鉛化の度合によるものである。 高温処理した導電性シート(HT.CC)の層を
導電性プラスチツク部材(CP)上に形成するに
は、加熱圧着によつて行なう。この圧着作業は、
プラスチツク電極部材が、加熱によつて充分軟化
が進んだときに行うが、HT.CCの層をプラスチ
ツク部材表面上に設けることにより副次的効果と
して電極表面の保護効果を発揮しながら表面活性
化層を形成する。 使用するHT.CCは多孔質の炭素繊維からなる
ものを用いると更に導電性シートがバツキングさ
れた電極(HT.CC−CP電極)の比抵抗を低下で
きる。シートのもつ気孔率、厚み、目付等の限定
はないがその厚みはバイポーラ、ポーラ型を問わ
ず直列接続(積層)して電圧を高くする際大きく
ならないようにCPの厚みの1/2〜3/2程度が望ま
しく高温処理における処理温度及び時間は1500℃
前後で約1時間が後述する実施例2より経済的で
ありこれらHT.CC−CP電極によつて構成された
Zn−Br2電池の放電特性は従来処理CP電極で構
成されたZn−Br2電池のそれよりも電圧効率は高
く、従つてエネルギー効率は向上している。 次に高温処理される炭素繊維から成るHT.CC
の形態についてはクロス形態またはニツト形態が
更に気孔率が大きい多孔質のものを高温処理して
得られたHT.CCを用いて成る電極(HT.CC−CP
電極)は従来以上の特性向上を示すことが後述す
る実施例によつて確認された。 以下実施例によつて本発明の構成・効果をより
具体的に説明する。 〔発明の実施例〕 実施例 1 クロス形態の導電性シートを電気炉で微量酸素
雰囲気で1000℃、1400℃、1600℃、2000℃で何れ
も30分間高温処理を行なつた。一方従来の高温処
理しないクロス形態の導電性シートと前記4種類
の高温処理導電性シートをCPに熱圧着する。得
られた電極():CC−CP電極:HT1000CC−
CP電極、:HT1400CC−CP電極、:
HT1600CC−CP電極、:HT2000CC−CP電極と
してこれらを臭素側電極として、亜鉛側電極には
従来のプラスチツク電極(CP電極)を使用し、
陽極と陰極間の極間距離2mm、隔膜として旭化成
(株)製RAS0.6を用い臭素−亜鉛電池を構成し、電
解液濃度3mol/のZnBr2+Br2、20mA/cm2
電流密度により室温(25℃)で放電を行い、その
際のAg−AgCl電極に対比させて得た電極電位(V)
を求めた結果第1図が得られた。第1図に示す如
く、高温処理無しのCC−CP電極に比して高温処
理のHT.CC−CP電極は放電特性に於て優れて居
り、また処理温度が高い程特性も向上している。
然しまたその特性の向上度合いは1500〜1600℃以
上ではゆるやかな上昇にとどまる。 実施例 2 実施例1と同様の雰囲気中で、但し高温処理温
度のみを1600℃一定として、処理時間を10分
()30分()1時間()1時間30分()
2時間()に変化せしめ作製したHT.CCをCP
にバツキングして得たHT.CC−CP電極を実施例
1と同様の臭素−亜鉛電池にて同様の条件で放電
試験を行い、Ag−AgCl電極に対比して得た電極
電位(V)を求めた結果第2図が得られた。第2図に
示す如く、1600℃高温処理で1時間以上処理した
ものは殆んど同じ様に優れた特性を示している。 実施例 3 1500℃にて、1時間高温処理した導電性シート
をCPにバツキングしたカーボンプラスチツク電
極(A)(HT.CC−CP電極)を陽極とし、陰極にカ
ーボンプラスチツク電極(CP電極)を使用した
Zn−Br2電池と比較のため陽極に従来のCC−CP
電極(B)及び未処理CP電極(C)をまた陰極には何れ
もCP電極を夫々用いたZn−Br2電池の特性試験
を陽極と陰極間の極間距離を2mm隔膜旭化成(株)製
RAS0.6、20mA/cm2定電流充、放電(充電3時
間、放電0Vカツトオフ)の作動条件にて行なつ
た。その結果を第1表に示す。
[Technical Field of the Invention] The present invention relates to a carbon plastic electrode used in a bromine-zinc battery, in which a conductive sheet made of high temperature treated carbon fiber is back-treated on the surface of a conventional carbon plastic member. In particular, the present invention relates to a carbon plastic electrode capable of improving the efficiency of electrochemical reactions and stably maintaining the efficiency. [Prior art] The electrodes conventionally used in bromine-zinc secondary batteries can be broadly classified from the material standpoint: metal electrodes using metal, carbon electrodes using carbon itself, and conductive materials such as plastics. There are plastic electrodes made by kneading carbon, silver, etc.) to give them conductivity. Among these, the material of the metal electrode is limited to noble metals such as platinum, considering the corrosive effect of bromine molecules generated when charging the battery. These precious metals generally have the advantage of having very low electrical resistance, good battery voltage efficiency, long discharging time, and excellent coulombic efficiency, but their biggest drawback is their It is expensive and ultimately unsuitable for practical use. Furthermore, although carbon electrodes have the lowest electrical resistance next to metal electrodes, they have low mechanical strength and are particularly susceptible to cracking due to impact, which poses a problem in their reliability. In addition, carbon electrodes have the disadvantage that, because they are generally porous, they cannot be used in bibolar series stacked battery systems in which the electrode itself functions as a separator. Finally, although plastic electrodes have sufficient mechanical strength, their electrical resistance is high, and their coulombic efficiency is low in reactivity with the active material, resulting in the problem of having to settle for low efficiency. remains. As described above, each material has its advantages and disadvantages in terms of economy, lifespan, efficiency, etc., and an electrode material that can be safely used in bromine-zinc secondary batteries has not yet been found. The inventors of the present application previously proposed in Japanese Patent Laid-Open No. 57-197772 an electrode to solve the above problems, in which a conductive electrode was made of carbon fiber with or without an adhesive layer on the surface of the plastic member, and was made of felt or knit. We also proposed a plastic electrode formed by forming a layer of conductive sheets selected from cross-type or cross-type conductive sheets. However, it is still insufficient. [Object of the Invention] Under these circumstances, the present invention provides high efficiency, long life,
The purpose of this study is to conduct various studies to obtain inexpensive electrode materials, and to obtain electrodes that can relatively easily improve the voltage efficiency and Coulombic efficiency of a battery. [Summary of the Invention] The present invention was obtained by further improving the above-mentioned research, and includes backing a conductive sheet selected from the above-mentioned felt, knit, or cloth forms not made of carbon fibers on the surface of a conductive plastic member. The carbon plastic electrode is characterized by being subjected to high-temperature treatment beforehand. Polyolefin is used as the paste polymer of the conductive plastic member constituting the electrode base because it is required to be resistant to deterioration even when in contact with free bromine or ionic bromine for a long time. The conductive plastic member (CP) is made of, for example, 100 parts by weight of high-density polyethylene and carbon black.
It can be made by kneading 50 parts by weight and press molding. Furthermore, the method of high-temperature treatment of a conductive sheet in the present invention involves heating a sheet made of carbon fiber in the form of felt, knit, cloth, etc. in a trace oxygen atmosphere, generally in an electric furnace, to a temperature of 1000 to 2000 ml.
℃ for 10 minutes to 2 hours. An electrode obtained by backing a high-temperature-treated conductive sheet onto the surface of a conventional conductive plastic member (CP) using a conventional method (referred to as HT.CC-CP electrode).
No matter which form of conductive sheet is used, the characteristics are improved compared to conventional electrodes (CC-CP electrodes) that are backed by conductive sheets that are not subjected to high-temperature treatment. When measuring the specific resistance (p) of the treated surface, that is, the HT.CC-CP electrode, it was lower than that of the conventional CC-CP electrode, and this is because the carbon fiber graphitizes due to the high temperature treatment. The conductivity of HT increases.
This contributes to lowering the specific resistance of the CC-CP electrode. The characteristics of carbon plastic electrodes vary depending on the heat treatment time and temperature, and this is due to the degree of graphitization of the carbon fibers due to the high temperature treatment. The layer of high temperature treated conductive sheet (HT.CC) is formed on the conductive plastic component (CP) by thermocompression bonding. This crimping work is
This is done when the plastic electrode member has sufficiently softened due to heating, but by providing a layer of HT.CC on the surface of the plastic member, the surface is activated while exerting a secondary effect of protecting the electrode surface. form a layer. If the HT.CC used is one made of porous carbon fiber, the specific resistance of the electrode backed with a conductive sheet (HT.CC-CP electrode) can be further reduced. There are no restrictions on the porosity, thickness, or basis weight of the sheet, but the thickness should be 1/2 to 3 of the CP thickness, regardless of bipolar or polar type, to avoid increasing the voltage when connected in series (laminated) to increase the voltage. /2 is desirable, and the treatment temperature and time in high temperature treatment is 1500℃.
It took about 1 hour before and after, and it was more economical than Example 2, which will be described later, and was constructed with these HT.CC-CP electrodes.
The discharge characteristics of Zn-Br 2 cells are more voltage efficient and therefore more energy efficient than those of Zn-Br 2 cells constructed with conventionally treated CP electrodes. HT.CC made of carbon fiber which is then treated at high temperature
Regarding the morphology of HT.CC, the cross morphology or nitrite morphology is an electrode made using HT.CC obtained by high-temperature treatment of a porous material with a higher porosity (HT.CC-CP).
It was confirmed by the Examples described later that the electrode) exhibited improved characteristics over conventional electrodes. The configuration and effects of the present invention will be explained in more detail below using Examples. [Examples of the Invention] Example 1 A cross-shaped conductive sheet was subjected to high-temperature treatment in an electric furnace in a trace oxygen atmosphere at 1000°C, 1400°C, 1600°C, and 2000°C for 30 minutes each. On the other hand, a conventional cross-shaped conductive sheet that is not subjected to high temperature treatment and the four types of high temperature treated conductive sheets are thermocompression bonded to the CP. Obtained electrode (): CC−CP electrode: HT 1000 CC−
CP electrode: HT 1400 CC−CP electrode:
HT 1600 CC-CP electrode, :HT 2000 CC-CP electrode These are used as the bromine side electrode, and a conventional plastic electrode (CP electrode) is used as the zinc side electrode.
Distance between the anode and cathode is 2mm, and Asahi Kasei is used as the diaphragm.
A bromine-zinc battery was constructed using RAS0.6 manufactured by Co., Ltd., and discharged at room temperature (25°C) with an electrolyte concentration of 3 mol/ZnBr 2 +Br 2 and a current density of 20 mA/cm 2 . -Electrode potential (V) compared to AgCl electrode
As a result, Figure 1 was obtained. As shown in Figure 1, the high temperature treated HT.CC-CP electrode has better discharge characteristics than the non-high temperature treated CC-CP electrode, and the higher the treatment temperature, the better the characteristics. .
However, the degree of improvement in the properties is only gradual at temperatures above 1500 to 1600°C. Example 2 In the same atmosphere as in Example 1, only the high temperature treatment temperature was kept constant at 1600°C, and the treatment time was 10 minutes () 30 minutes () 1 hour () 1 hour 30 minutes ()
CP the HT.CC prepared after changing for 2 hours ()
A discharge test was performed on the HT.CC-CP electrode obtained by bombarding the HT. As a result, Figure 2 was obtained. As shown in FIG. 2, those treated at a high temperature of 1600° C. for more than 1 hour show almost the same excellent properties. Example 3 A carbon plastic electrode (A) (HT.CC-CP electrode) in which a conductive sheet that has been subjected to high temperature treatment for 1 hour at 1500°C is backed with CP is used as an anode, and a carbon plastic electrode (CP electrode) is used as a cathode. did
For comparison with Zn-Br 2 batteries, conventional CC-CP was used as the anode.
Characteristic tests were carried out on Zn-Br 2 batteries using the electrode (B), the untreated CP electrode (C), and the CP electrode as the cathode.
The operation was carried out under the following operating conditions: RAS 0.6, 20 mA/cm 2 constant current charging and discharging (charging for 3 hours, discharge cutoff at 0 V). The results are shown in Table 1.

【表】 上表に示される如く、プラスチツク電極(HT.
CC−CP)Aは他のB(CC−CP電極)、C(CP電
極に比して特に電圧効率の点に於て増加した値を
示しており、従つてエネルギー効率が向上してい
る。 実施例 4 クロス形態の多孔質炭素繊維から成る導電性シ
ート(P.CC)を電気炉にて1500℃微量酸素濃度
の不活性雰囲気中で30分間加熱する。得られた高
温処理多孔質導電性シートを導電性プラスチツク
部材に該部材に枠部を成形する時に同時に熱圧着
する。こうして得られたクロス形態の高温処理多
孔質導電性シート、バツキングカーボンプラスチ
ツク電極(以下HT.P.CC−CP電極)は、クロス
の厚み、目付及び空孔量から気孔率を計算すると
12.8%となつた。次に上記HT.P.CC−CP電極と
従来のクロス形態で高温処理してない多孔質導電
性シート、バツキングカーボンプラスチツク電極
(以下P.CC.−CP電極、気孔率12.8%)及び未処
理のカーボンプラスチツク電極(CP電極)の放
電電位特性試験を電解液濃度3mol/のZnBr2
+Br2、40mA/cm2の電流密度で25℃で放電試験
を行い、実施例1の同様に電極電位(V)を求め、第
3図の如き結果を得た。第3図に於て曲線は
HT.P.CC−CP電極、曲線はP.CC.−CP電極、
曲線はCP電極を用いた場合の特性曲線であり、
気孔率が等しいに拘わらずHT.P.CC−CPは従来
のP.CC.−CPに比して特に低Br2濃度域で高い放
電電位を保持することが明らかである。更に上記
3種の電極の特性値を第2表に示す。
[Table] As shown in the table above, plastic electrodes (HT.
CC-CP) A shows an increased value especially in terms of voltage efficiency compared to the other B (CC-CP electrode) and C(CP electrode), and therefore the energy efficiency is improved. Example 4 A conductive sheet (P.CC) made of cross-shaped porous carbon fibers is heated in an electric furnace at 1500°C in an inert atmosphere with a trace oxygen concentration for 30 minutes.The resulting high-temperature-treated porous conductive sheet The sheet is thermocompression bonded to a conductive plastic member at the same time as the frame is formed on the member.The cross-shaped high temperature treated porous conductive sheet thus obtained is called a backing carbon plastic electrode (hereinafter referred to as HT.P.CC-CP). (electrode), the porosity is calculated from the thickness of the cloth, the basis weight, and the amount of pores.
It became 12.8%. Next, the above HT.P.CC-CP electrode, a conventional cross-form porous conductive sheet that has not been subjected to high temperature treatment, a backing carbon plastic electrode (hereinafter referred to as P.CC.-CP electrode, porosity 12.8%) and an untreated A discharge potential characteristic test of treated carbon plastic electrodes (CP electrodes) was carried out using ZnBr 2 with an electrolyte concentration of 3 mol/ZnBr 2.
A discharge test was conducted at 25° C. with +Br 2 and a current density of 40 mA/cm 2 , and the electrode potential (V) was determined in the same manner as in Example 1, and the results shown in FIG. 3 were obtained. In Figure 3, the curve is
HT.P.CC-CP electrode, the curve is P.CC.-CP electrode,
The curve is a characteristic curve when using a CP electrode,
It is clear that despite the same porosity, HT.P.CC-CP maintains a higher discharge potential than conventional P.CC.-CP, especially in the low Br 2 concentration range. Furthermore, the characteristic values of the above three types of electrodes are shown in Table 2.

【表】 第2表に示す如くHT.P.CC−CP電極は従来の
P.CC.−CP電極に比して特に比抵抗値が小さいこ
とが明らかである。 実施例 5 気孔率(P)の夫々6.0%、13.2%、19.2%と異なる
3種のクロス形態の導電性シートCC6.0、CC13.2
CC19.2(サフイツクスの数値はP%を示す)を選
び、これらを電気炉で実施例4と同様の雰囲気で
1100℃、30分間加熱して高温処理を行なつた。そ
の後実施例4で示したのと同様の方法で導電性プ
ラスチツク部材にヒートプレスして高温処理多孔
質導電性シートバツキングCP電極(3種を夫々
HT.P.CC6.0−CP、電極HT.P.CC13.7−CP電極、
及びHT.P.CC19.2−CP電極という。)を得た。次
にこれらを夫々セルに組み従来方法で放電時の電
極電位を測定した。尚電解液には3mol/の
ZnBr2+Br2液を用い対極には未処理のCP電極を
使用した。得られた40mA/cm2放電での放電電位
曲線から電解液Br2濃度0.4〜1.0mol/における
平均放電電位(V40)を求めた。その結果を第3
表に示す。
[Table] As shown in Table 2, the HT.P.CC-CP electrode is
It is clear that the specific resistance value is particularly small compared to the P.CC.-CP electrode. Example 5 Three types of cross-shaped conductive sheets CC 6.0 , CC 13.2 , with different porosity (P) of 6.0%, 13.2%, and 19.2 %, respectively.
CC 19.2 (the number of saphix indicates P%) was selected and heated in an electric furnace in the same atmosphere as in Example 4.
High temperature treatment was carried out by heating at 1100°C for 30 minutes. Thereafter, a conductive plastic member was heat-pressed in the same manner as shown in Example 4 to form high-temperature-treated porous conductive sheet backing CP electrodes (three types of
HT.P.CC 6.0 −CP, electrode HT.P.CC 13.7 −CP electrode,
and HT.P.CC 19.2 −CP electrode. ) was obtained. Next, each of these was assembled into a cell and the electrode potential during discharge was measured using a conventional method. In addition, the electrolyte contains 3 mol/
A ZnBr 2 +Br 2 solution was used, and an untreated CP electrode was used as the counter electrode. The average discharge potential (V 40 ) at an electrolytic solution Br 2 concentration of 0.4 to 1.0 mol/was determined from the obtained discharge potential curve at 40 mA/cm 2 discharge. The result is the third
Shown in the table.

【表】 第3表の結果から高温処理して得られたHT.P.
CC−CP電極は凡て従来のP.CC.−CP電極に比べ
て夫々特性値が向上していることが判る。 実施例 6 実施例4で述べた高温処理多孔質導電性シート
バツキングカーボンプラスチツク電極(HT.P.
CC−CP電極)、多孔質導電性シートバツキング
カーボンプラスチツク電極(P.CC.−CP電極)を
夫々陽極(臭素極)に使用し、陰極に未処理カー
ボンプラスチツク電極隔膜に実施例1と同じ
RAS0.6を用い極間離約2mm充放電電流密度20m
A/cm2で3時間充電し、放電は0Vでカツトした
場合の電圧効率(Veff%)クーロン効率(Ceff
%)及びエネルギー効率(Eeff%)の特性を第4
表に示す。
[Table] From the results in Table 3, HT.P obtained by high temperature treatment.
It can be seen that all the CC-CP electrodes have improved characteristic values compared to the conventional P.CC.-CP electrode. Example 6 The high temperature treated porous conductive sheet-backed carbon plastic electrode (HT.P.
CC-CP electrode) and a porous conductive sheet-backed carbon plastic electrode (P.CC.-CP electrode) were used as the anode (bromine electrode), respectively, and an untreated carbon plastic electrode diaphragm was used as the cathode as in Example 1.
Using RAS0.6, the electrode spacing is approximately 2mm, and the charging and discharging current density is 20m.
Voltage efficiency (Veff%) and coulombic efficiency (Ceff
%) and energy efficiency (Eeff%)
Shown in the table.

【表】 第4表に明らかな如く陽極としてHT.P.CC−
CP電極を使用した電池は特に電圧効率が向上し
その結果エネルギー効率が増加した。 実施例 7 ニツト形態多孔質導電性シートを電気炉にて
1100℃微量酸素濃度の不活性雰囲気中、30分間加
熱する。得られた高温処理ニツト形態の多孔質導
電性シートを、カーボンプラスチツク部材に該部
材に枠付を行なう時に熱圧着する。尚カーボンプ
ラスチツク(CP)電極は例えば密度0.94g/cm3
以上の高密度ポリエチレン100重量部にカーボン
ブラツク(表面積1000m2/g、平均粒子径30n
m)50重量部を混練して加熱プレス成形などによ
り薄板状の電極を作る。斯くして成形されたニツ
ト形態の高温処理多孔質導電性シートバツキング
CP電極(以下HT.N.P.CC−CP電極と云う)と
従来のニツト形態の導電性シートバツキングCP
電極(以下N.P.CC−CP電極という)かついずれ
も気孔率P:14.1%タイプのものを夫々その特性
を比較し第5表が得られた。
[Table] As shown in Table 4, HT.P.CC− as an anode
Batteries using CP electrodes had particularly improved voltage efficiency and, as a result, increased energy efficiency. Example 7 A porous conductive sheet in the form of a nitrate was prepared in an electric furnace.
Heat at 1100℃ for 30 minutes in an inert atmosphere with trace oxygen concentration. The obtained porous conductive sheet in the form of a high-temperature treated knit is thermocompression bonded to a carbon plastic member when the member is framed. Carbon plastic (CP) electrodes have a density of 0.94g/ cm3 , for example.
Carbon black (surface area 1000m 2 /g, average particle size 30n) is added to 100 parts by weight of high-density polyethylene
m) Knead 50 parts by weight and make a thin plate electrode by hot press molding. High-temperature-treated porous conductive sheet backing in the form of a knit formed in this way
CP electrode (hereinafter referred to as HT.NPCC-CP electrode) and conventional knitted conductive sheet backing CP
Table 5 was obtained by comparing the characteristics of electrodes (hereinafter referred to as NPCC-CP electrodes) with a porosity P of 14.1%.

【表】 第5表に明らかな如くHT.N.P.CC−CP電極は
比表面積が殆んど変化してないにもかかわらず全
体の比抵抗が下り電位特性(平均電位)が向上し
ている。 実施例 8 実施例7で得られたHT.N.P.CC−CP()及
びN.P.CC−CP()を臭素極として電解液とし
て3mol/のZnBr2+Br2、40mA/cm2の電流密
度で25℃で放電を行い電極電位(V)を求め第4図の
如き結果を得た。HT.N.P.CC−CP電極がこの電
流密度においても特性向上は明らかである。 実施例 9 実施例7と同じく気孔率Pが異なるニツト形態
多孔質導電性シート、A(P=0%)、B(P=
14.1%)及びC(P=16.0%)の3種類を選び
夫々電気炉で実施例7の雰囲気で1000℃、40分加
熱し高温処理を行なつた。その後、高温処理した
AB及びCを夫々従来方法でCPに熱圧着して表面
処理電極を作製した。これをA−HT.CC−CP電
極、B−HT.CC−CP電極、C−HT.CC−CP電
極とする。これらについて20mA/cm2定電流放電
での電解液中Br2濃度0.4〜1.0mol/範囲の平均
放電電位V20を従来の高温処理していないものと
比較し第6表が得られた。
[Table] As is clear from Table 5, although the specific surface area of the HT.NPCC-CP electrode has hardly changed, the overall resistivity has decreased and the potential characteristics (average potential) have improved. Example 8 HT.NPCC-CP() and NPCC-CP() obtained in Example 7 were used as a bromine electrode, and 3 mol/ZnBr 2 +Br 2 was used as the electrolyte, and discharged at 25°C at a current density of 40 mA/cm 2 The electrode potential (V) was determined and the results shown in Figure 4 were obtained. It is clear that the characteristics of the HT.NPCC-CP electrode are improved even at this current density. Example 9 Nit-form porous conductive sheets with different porosity P as in Example 7, A (P=0%), B (P=
Three types, 14.1%) and C (P=16.0%), were selected and subjected to high-temperature treatment by heating each in an electric furnace at 1000° C. for 40 minutes in the atmosphere of Example 7. Then, it was treated at high temperature
Surface-treated electrodes were fabricated by thermocompression bonding AB and C to CP using conventional methods. These are designated as the A-HT.CC-CP electrode, the B-HT.CC-CP electrode, and the C-HT.CC-CP electrode. For these, the average discharge potential V 20 at a constant current discharge of 20 mA/cm 2 at a Br 2 concentration in the electrolyte in the range of 0.4 to 1.0 mol/was compared with that of a conventional one not subjected to high temperature treatment, and Table 6 was obtained.

【表】 第6表からも明らかな様に気孔率の大きいもの
程、高温処理された電極も特性が良好となつてい
る。 実施例 10 実施例9で得られたC−HT.CC−CP電極と従
来のC−CC−CP電極を夫々Zn−Br2電池の陽極
(臭素極)とし、陰極(亜鉛極)には未処理CP電
極、陽極室と陰極室間の隔膜に実施例1にて用い
たと同様のRAS0.6を用い、電池及び電池を
組立て極間距離2mm、充放電電流密度20mA/cm3
で3時間充電し、放電は0Vカツトオフした時の
電池特性(電圧効率Veff%、クーロン効率Ceff
%、及びエネルギー効率Eeff%)の比較を行なつ
た。その結果は次の第7表に示す通りである。
[Table] As is clear from Table 6, the higher the porosity, the better the characteristics of the electrode treated at high temperature. Example 10 The C-HT.CC-CP electrode obtained in Example 9 and the conventional C-CC-CP electrode were respectively used as the anode (bromine electrode) of a Zn-Br 2 battery, and the negative electrode (zinc electrode) was Using the same RAS0.6 as used in Example 1 for the treated CP electrode and the diaphragm between the anode chamber and the cathode chamber, the battery was assembled with a distance between electrodes of 2 mm and a charge/discharge current density of 20 mA/cm 3
Battery characteristics (voltage efficiency Veff%, coulombic efficiency Ceff
%, and energy efficiency Eeff%). The results are shown in Table 7 below.

〔発明の効果〕〔Effect of the invention〕

Zn−Br2電池陽極用電極である炭素繊維から成
る導電性シートバツキングCP電極においてバツ
キング材料である導電性シート殊に微細の孔を形
成させた多孔質導電性シートをバツキングする前
に電気炉にて1000〜2000℃、10分〜2時間高温処
理し、然る後にバツキングして得られる高温処理
導電性シートバツキングCP電極(HT.CC−CP
電極)は高温処理による炭素繊維の黒鉛化のため
にシートの導電性が増し、従つてこれを用いて成
る電極自体の放電電位特性が未処理CC−CP電極
に比して向上し、このHT.CC−CP電極を陽極と
するZn−Br2電池は従来のCC−CP電極を陽極と
する電池に比べて電圧効率が増加し従つてエネル
ギー効率が向上した。上記の特性はクロスまたは
ニツト形態の多孔質導電性シートを高温処理した
場合も同様である。またシートの空孔量によつて
多孔質導電性シートバツキングCP電極は気孔率
が異なり、従つて表面積の大小によつて電位特性
も異なるが、その種々の気孔率をもつシートを高
温処理してバツキングした電極は、夫夫高温処理
しないものより特性が向上した。 叙上の如く本発明によるカーボンプラスチツク
電極はZn−Br2電池の陽極として適用した場合、
従来材料による電極を用いた場合に比べて電池の
電圧効率、クーロン効率、エネルギー効率を格段
と向上せしむる効果を有するものである。
Electroconductive sheet made of carbon fiber which is an electrode for Zn-Br 2 battery Anode The conductive sheet which is the backing material in the CP electrode, especially the porous conductive sheet with fine pores formed therein, is heated in an electric furnace before backing. A high-temperature-treated conductive sheet-backed CP electrode (HT.CC-CP
The conductivity of the sheet increases due to the graphitization of carbon fibers caused by high-temperature treatment, and therefore the discharge potential characteristics of the electrode itself are improved compared to untreated CC-CP electrodes. .The Zn-Br 2 battery with the CC-CP electrode as the anode has increased voltage efficiency and therefore energy efficiency compared to the conventional battery with the CC-CP electrode as the anode. The above characteristics are the same when the porous conductive sheet in the form of cloth or knit is subjected to high temperature treatment. In addition, the porosity of porous conductive sheet backing CP electrodes differs depending on the amount of pores in the sheet, and therefore the potential characteristics also differ depending on the surface area. The properties of the electrodes that were exposed to heat were improved compared to those that were not subjected to high-temperature treatment. As mentioned above, when the carbon plastic electrode according to the present invention is applied as an anode of a Zn-Br 2 battery,
This has the effect of significantly improving the voltage efficiency, Coulomb efficiency, and energy efficiency of the battery compared to when electrodes made of conventional materials are used.

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

第1図〜第4図は本発明の効果を示すための
Br2濃度−電極電位のグラフである。
Figures 1 to 4 are for showing the effects of the present invention.
It is a graph of Br 2 concentration vs. electrode potential.

Claims (1)

【特許請求の範囲】 1 導電性プラスチツク部材の表面に、高温処理
した炭素繊維から成るシートをバツキングして成
ることを特徴とするカーボンプラスチツク電極。 2 前記炭素繊維から成るシートが、フエルト、
ニツトまたはクロス形態から成りこの中から選ば
れた導電性シートを使用することを特徴とする特
許請求の範囲第1項記載のカーボンプラスチツク
電極。 3 前記炭素繊維から成るシートを微量酸素濃度
の不活性雰囲気中にて温度1000〜2000℃、10分〜
2時間加熱高温処理することを特徴とする特許請
求の範囲第1項記載のカーボンプラスチツク電
極。 4 前記シートが多孔質炭素繊維から成ることを
特徴とする特許請求の範囲第1項及び第2項記載
のカーボンプラスチツク電極。
[Scope of Claims] 1. A carbon plastic electrode characterized in that it is made by backing a sheet made of high temperature treated carbon fiber on the surface of a conductive plastic member. 2 The sheet made of carbon fiber is felt,
2. A carbon plastic electrode according to claim 1, characterized in that a conductive sheet selected from the above is used. 3. The sheet made of the carbon fiber is heated in an inert atmosphere with a trace oxygen concentration at a temperature of 1000 to 2000°C for 10 minutes.
The carbon plastic electrode according to claim 1, characterized in that it is heated at high temperature for 2 hours. 4. The carbon plastic electrode according to claims 1 and 2, wherein the sheet is made of porous carbon fiber.
JP58223261A 1983-11-29 1983-11-29 Carbon plastic electrode Granted JPS60117559A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58223261A JPS60117559A (en) 1983-11-29 1983-11-29 Carbon plastic electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58223261A JPS60117559A (en) 1983-11-29 1983-11-29 Carbon plastic electrode

Publications (2)

Publication Number Publication Date
JPS60117559A JPS60117559A (en) 1985-06-25
JPH0358149B2 true JPH0358149B2 (en) 1991-09-04

Family

ID=16795329

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58223261A Granted JPS60117559A (en) 1983-11-29 1983-11-29 Carbon plastic electrode

Country Status (1)

Country Link
JP (1) JPS60117559A (en)

Also Published As

Publication number Publication date
JPS60117559A (en) 1985-06-25

Similar Documents

Publication Publication Date Title
US4925752A (en) Solid state electrochemical cell having porous cathode current collector
US5604660A (en) Electrochemical cell having solid polymer electrolyte and asymmetric inorganic electrodes
CA1278032C (en) Cathodic electrode
US4714665A (en) Secondary battery
US3749608A (en) Primary electrochemical energy cell
US4731310A (en) Cathodic electrode
EP0228573B1 (en) A surface treated electrode and a zinc-halogen secondary battery incorporating the same
US3770507A (en) Electrochemical battery employing bonded lead dioxide electrode and fluoroboric acid electrolyte
US3023262A (en) Battery electrode
TW202424273A (en) Copper foil
KR102853164B1 (en) Method for preparing the anode and secondary battery with enhanced high speed performance comprising the same
JPH0358149B2 (en)
EP0112068A1 (en) Electrically conductive plastic electrode having a porous surface
KR102436817B1 (en) Method for manufacturing stretchable lithium metal electrode with high-elongation and low resistance and lithium metal electrode manufactured thereby
RU2098892C1 (en) Combined electrode for alkali storage battery
EP4625531A1 (en) Bipolar current collector for zinc bromine static battery apparatus and method of preparation thereof
JP2732442B2 (en) Manufacturing method of solid state secondary battery
JPH0329130B2 (en)
JPH0445937B2 (en)
KR20250177171A (en) Lithium metal anode for a lithium secondary battery and a method of making the same
JP2007149533A (en) Electrode, and electrochemical cell using it
JPH044700B2 (en)
JP2680578B2 (en) Solid electrolyte battery
JPS62128451A (en) Vitreous carbon composite electrode
JPH0414467B2 (en)

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees