JPS63148559A - Manufacture of bromine absorbing electrode - Google Patents
Manufacture of bromine absorbing electrodeInfo
- Publication number
- JPS63148559A JPS63148559A JP61292602A JP29260286A JPS63148559A JP S63148559 A JPS63148559 A JP S63148559A JP 61292602 A JP61292602 A JP 61292602A JP 29260286 A JP29260286 A JP 29260286A JP S63148559 A JPS63148559 A JP S63148559A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- bromine
- ion exchange
- powder
- parts
- 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
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 title claims abstract description 31
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 title claims abstract description 31
- 229910052794 bromium Inorganic materials 0.000 title claims abstract description 31
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 239000000843 powder Substances 0.000 claims abstract description 27
- 229920000642 polymer Polymers 0.000 claims abstract description 18
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000006229 carbon black Substances 0.000 claims abstract description 10
- 239000011149 active material Substances 0.000 claims abstract description 9
- 238000004898 kneading Methods 0.000 claims abstract description 8
- 239000004698 Polyethylene Substances 0.000 claims abstract description 6
- 238000005341 cation exchange Methods 0.000 claims abstract description 6
- -1 polyethylene Polymers 0.000 claims abstract description 6
- 229920000573 polyethylene Polymers 0.000 claims abstract description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 5
- 150000002500 ions Chemical class 0.000 claims abstract description 5
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 5
- 239000000284 extract Substances 0.000 claims description 15
- 150000001875 compounds Chemical class 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 9
- 239000011159 matrix material Substances 0.000 claims description 4
- 229910052736 halogen Inorganic materials 0.000 claims description 3
- 229920005992 thermoplastic resin Polymers 0.000 claims description 3
- 125000000542 sulfonic acid group Chemical group 0.000 claims description 2
- 238000005342 ion exchange Methods 0.000 abstract description 16
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 abstract description 11
- 239000003456 ion exchange resin Substances 0.000 abstract description 11
- 229920003303 ion-exchange polymer Polymers 0.000 abstract description 11
- 239000000463 material Substances 0.000 abstract description 8
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 abstract description 5
- 239000004372 Polyvinyl alcohol Substances 0.000 abstract description 5
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 abstract description 5
- 229920002451 polyvinyl alcohol Polymers 0.000 abstract description 5
- 150000001768 cations Chemical class 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 abstract description 2
- 239000003792 electrolyte Substances 0.000 description 18
- ZRXYMHTYEQQBLN-UHFFFAOYSA-N [Br].[Zn] Chemical compound [Br].[Zn] ZRXYMHTYEQQBLN-UHFFFAOYSA-N 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 229910052799 carbon Inorganic materials 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 230000000717 retained effect Effects 0.000 description 4
- 230000004913 activation Effects 0.000 description 3
- 239000008151 electrolyte solution Substances 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 2
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000008139 complexing agent Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- VNDYJBBGRKZCSX-UHFFFAOYSA-L zinc bromide Chemical compound Br[Zn]Br VNDYJBBGRKZCSX-UHFFFAOYSA-L 0.000 description 2
- 241000282320 Panthera leo Species 0.000 description 1
- 239000004962 Polyamide-imide Substances 0.000 description 1
- 239000004642 Polyimide Substances 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000005219 brazing Methods 0.000 description 1
- 238000003490 calendering Methods 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 210000000416 exudates and transudate Anatomy 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920002312 polyamide-imide Polymers 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229940102001 zinc bromide Drugs 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
-
- 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
Abstract
Description
【発明の詳細な説明】
A、a業上の利用分野
この発明は、金属−ハロゲン電池の電極に関し、とくに
亜鉛−臭素電池における臭素活物質を吸収して保持可能
な電極に関するものである。DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application This invention relates to an electrode for a metal-halogen battery, and more particularly to an electrode capable of absorbing and retaining a bromine active material in a zinc-bromine battery.
B9発明の概要
この発明は、高分子化合物(熱可塑性樹脂)をマトリッ
クスとする電極において、上記の高分子化合物に、陽イ
オン交換基をもつイオン交換体とカーボンブラックと油
出物と親、水性付与剤を添加混練して多孔質電極を形成
し、この電極に活物質である臭素を保持する吸収能を高
めた臭素吸収電極の製造方法を提供するものである。B9 Summary of the Invention This invention provides an electrode having a polymer compound (thermoplastic resin) as a matrix, in which the above-mentioned polymer compound is combined with an ion exchanger having a cation exchange group, carbon black, an oil exudate, and a hydrophilic, aqueous polymer. The present invention provides a method for manufacturing a bromine-absorbing electrode in which a porous electrode is formed by adding and kneading an imparting agent, and the electrode has enhanced absorption capacity for retaining bromine as an active material.
C9従来の技術
近年、新型電池を用いた各種応用が検討されている。例
えば、電力貯蔵、電気自動車用電池への応用が活発であ
る。C9 Prior Art In recent years, various applications using new types of batteries have been studied. For example, it is actively being applied to power storage and electric vehicle batteries.
新型電池の中でも、金属−ハロゲン電池が注目されてお
り、その中でも亜鉛−臭素電池は、安価であり、構造が
簡単でコンパクトになる点に注目されて開発が進められ
ている。亜鉛−臭素電池は1800年代から提案されて
いるが、正極活物質の臭素が液体であるため、析出した
後、電解液中に一部溶解し、自己放電を生じたり、酸化
力が強いため、構成材料に限界がある等問題をかかえて
いた。しかし最近、臭素と結合してオイル状になる錯化
剤が開発され、本電池の実用性が大きく高まった。この
錯化剤と臭素分子が結合して生ずるオイル状の臭素コン
プレックスは充電時に電極表面、あるいは電解液中で生
成され、電解液から分離される。そこで、本電池の基本
構造は第1図で示す様なポンプを用いて電解液を循環さ
せ、生成された臭素コンプレックスをタンク底に貯蔵し
、放電時に電解液と一緒に循環させる、いわゆる電解液
種環形亜鉛−臭素電池が現状の方式である。Among new types of batteries, metal-halogen batteries are attracting attention, and among them, zinc-bromine batteries are being developed because they are inexpensive, have a simple structure, and are compact. Zinc-bromine batteries have been proposed since the 1800s, but since the positive electrode active material bromine is a liquid, after it precipitates, it partially dissolves in the electrolyte, causing self-discharge, and has strong oxidizing power. There were some problems, such as limitations on the materials used to construct it. However, recently, a complexing agent that combines with bromine to form an oil has been developed, greatly increasing the practicality of this battery. An oil-like bromine complex produced by the combination of this complexing agent and bromine molecules is generated on the electrode surface or in the electrolyte during charging, and is separated from the electrolyte. Therefore, the basic structure of this battery is to circulate the electrolyte using a pump as shown in Figure 1, store the generated bromine complex at the bottom of the tank, and circulate it together with the electrolyte during discharge. Seed ring zinc-bromine batteries are the current method.
なお、第1図は電解液種環形亜鉛−臭素電池の構成説明
図である。図において、1は電池の単セルを示す電池反
応槽、2は正極室、3は負極室、4はセパレータとして
の膜、5は正極、6は負極、7は正極電解液、8は負極
電解液、9は正極電解液用のタンク、10は負極電解液
用のタンク、11及び12は電解液循環用のポンプ、1
3及び13aは電解液循環用の配管系、14は上記の臭
素錯化物(コンプレックス)である。なお、配管系13
及び13aの脇に示した矢印は電解液の流れ方向を示す
ものである。Note that FIG. 1 is an explanatory diagram of the structure of a ring-type zinc-bromine battery using an electrolytic solution. In the figure, 1 is a battery reaction tank showing a single cell of the battery, 2 is a positive electrode chamber, 3 is a negative electrode chamber, 4 is a membrane as a separator, 5 is a positive electrode, 6 is a negative electrode, 7 is a positive electrode electrolyte, and 8 is a negative electrode electrolyte. 9 is a tank for positive electrode electrolyte, 10 is a tank for negative electrode electrolyte, 11 and 12 are pumps for electrolyte circulation, 1
3 and 13a are piping systems for electrolyte circulation, and 14 is the above-mentioned bromine complex. In addition, piping system 13
The arrows shown beside 13a and 13a indicate the flow direction of the electrolytic solution.
上記のような亜鉛−臭素電池はよく知られており、また
すでに実用化されているので、その動作原理などの詳細
説明は割愛する。Since the zinc-bromine battery described above is well known and has already been put into practical use, a detailed explanation of its operating principle will be omitted.
D5発明が解決しようとする問題点
°上記のような亜鉛、臭素電池の正極は過去に数多く検
討され、現在では、カーボンプラスチック電極が主流で
ある。これは、ポリオレフィン系の樹脂に導電性を付与
するためカーボン粉末を添加し、混練、成型したもめで
ある。この電極表面に活性化処理を施し充電時における
臭素発生(酸化反応)を容易にし、また放電時に於ては
臭素活物質との反応面積の増大及び還元反応を容易にし
ている。この様な活性化処理面で充電時に発生した臭素
は直ちに電解液中に穆動し、電解液と共に循環する。こ
れより電極及び電極表面の活性処理面は発生した臭素を
保持する機能を兼ね備えていない事になる。しかし、こ
の保持機能は従来の活性化処理面に掻くわずかに存在し
ている。これは、通常の活性化処理によって、カーボン
ブラック粉末あるいは活性炭粉末が若干の吸着機能をも
っているため、これにより発生する臭素分子が電極表面
上にわずかながら保持される事による。例えばカーボン
プラスチック電極表面に熱圧着した活性炭繊維(東洋紡
製CF−303)においては電流密度20 mA/cm
2で3 mol/Ilの臭化亜鉛溶液で充電した場合約
1時間、つまり20 mAh/cm2までは電解液は無
色透明で臭素が電解液中へ析出せず保持されるが、それ
以上になると、電解液が赤褐色化して、臭素保持が不可
能になることを示す。この程度の保持力だと電池容量と
しても少なく、電気自動車や、電力貯蔵用電池としての
電極としては不十分である。従ってとくに、電気自動車
のようなコンパクトで高性能を要求される電池において
も、ポンプや配管やタンク等を使用しなければならず大
きなネックとなる問題点である。D5 Problems to be Solved by the Invention Many positive electrodes for zinc and bromine batteries as described above have been studied in the past, and carbon plastic electrodes are currently the mainstream. This is a product made by adding carbon powder to polyolefin resin to give it electrical conductivity, kneading and molding it. This electrode surface is subjected to activation treatment to facilitate bromine generation (oxidation reaction) during charging, and to increase the reaction area with the bromine active material and facilitate reduction reaction during discharging. Bromine generated during charging during such activation treatment immediately migrates into the electrolyte and circulates together with the electrolyte. This means that the electrode and the active treatment surface on the electrode surface do not have the function of retaining the generated bromine. However, this retention function exists only slightly on conventional activated surfaces. This is because the carbon black powder or activated carbon powder has a slight adsorption function due to the normal activation treatment, so that a small amount of the bromine molecules generated thereby are retained on the electrode surface. For example, in the case of activated carbon fiber (CF-303 manufactured by Toyobo Co., Ltd.) bonded by thermocompression to the surface of a carbon plastic electrode, the current density is 20 mA/cm.
When charging with a 3 mol/Il zinc bromide solution at 2, the electrolyte is colorless and transparent for about 1 hour, that is, up to 20 mAh/cm2, and bromine is retained without being precipitated into the electrolyte. , indicating that the electrolyte becomes reddish-brown and bromine retention becomes impossible. With this level of holding power, the battery capacity is also small, making it insufficient as an electrode for electric vehicles or power storage batteries. Therefore, even in batteries that are required to be compact and have high performance, such as those used in electric vehicles, pumps, piping, tanks, etc. must be used, which is a major problem.
E0問題点を解決するための手段
この発明は以上の問題点を解決するためになされたもの
で、電極の母体である高分子化合物に、陽イオン交換性
をもつイオン交換体とカーボンブラックなどの導電物の
ほか、抽出物と親水性付与剤を添加混練して電極を形成
したもので、充電特電極表面で発生した臭素活物質が電
極に保持されるとともに、放電時にはこれを活物質とし
て利用し得るような臭素保持力を飛躍的に高めた臭素吸
叡電極の製造方法であり、上記のような応用分野に十分
使用できるものである。Means for Solving the E0 Problem This invention was made to solve the above problems, and includes an ion exchanger having cation exchange properties and carbon black etc. in the polymer compound that is the base material of the electrode. Electrodes are formed by adding and kneading extracts and hydrophilic agents in addition to conductive materials.The bromine active material generated on the surface of the special charging electrode is retained in the electrode, and is used as an active material during discharge. This is a method for producing a bromine-absorbing electrode that has dramatically increased bromine retention, and can be fully used in the above-mentioned application fields.
F0作用
この発明において、イオン交換性を付与するために用い
たイオン交換樹脂は、スルホン酸基(−SO3−H”)
をもつポリビニルアルコールの陽イオン交換体であり、
このポリビニルアルコール粉末と、導電性を与えるカー
ボンブラックの粉末を混合し、電極母体をなす高分子化
合物である熱可塑性樹脂すなわちポリエチレン粉末と混
練してシート化したプラスチック電極は実験の結果臭素
をよく吸収する特性を有することが判明している。F0 effect In this invention, the ion exchange resin used to impart ion exchange properties has a sulfonic acid group (-SO3-H")
It is a cation exchanger of polyvinyl alcohol with
Experiments have shown that this plastic electrode is made by mixing this polyvinyl alcohol powder with carbon black powder, which provides conductivity, and kneading it with a thermoplastic resin (polyethylene powder), which is a polymeric compound that forms the electrode base, to form a sheet that absorbs bromine well. It has been found that it has the following properties.
とくに、本電池の正極面上で充電時に発生する臭素分子
(s rz)を電極中に存在する陽イオン交換樹脂微粉
末が直ちにトラップし、電解液中に溶比させないことが
確認されている。In particular, it has been confirmed that the cation exchange resin fine powder present in the electrode immediately traps bromine molecules (s rz) generated on the positive electrode surface of the battery during charging, and does not dissolve them into the electrolyte.
しかし、より詳細な化学的根拠は不明であるが、この陽
イオン交換微粉末が、臭素を吸収すると赤色化する事が
観察された。また、この微粉末を含む上記の電極に臭素
を含ませ、あるいは後述する電池の充放電過程の中で、
充電後この電極を取り出し、約60〜80℃程度に加熱
すると、電極表面から臭素が放出される様子が顕微鏡下
で観察されている。However, although the detailed chemical basis is unknown, it was observed that this cation exchange fine powder turned red when absorbing bromine. In addition, by impregnating the above-mentioned electrode containing this fine powder with bromine, or during the charging and discharging process of the battery described below,
After charging, the electrode is taken out and heated to about 60 to 80°C, and the release of bromine from the electrode surface is observed under a microscope.
以上のほか、本発明で用いた添加物のうち、抽出物には
ジオクチルフタレートを用いるが、これはシート成形後
に溶剤で抽出除去し、電極の多孔化を行なうものである
。さらに、シリカ又はアルミナ粉末は母体である高分子
化合物とイオン交換性粉末とが均一に抽出物に濡れるよ
うに親水性を付与するものである。In addition to the above, among the additives used in the present invention, dioctyl phthalate is used as an extract, which is extracted and removed with a solvent after sheet forming to make the electrode porous. Furthermore, the silica or alumina powder imparts hydrophilicity so that the parent polymer compound and the ion exchange powder are uniformly wetted by the extract.
G0発明の実施例
はじめに、本発明による電極用シートであるカーボンプ
ラスチック電極の製法と材料など予備実験で得た条件に
ついて説明する。G0 Example of the Invention First, the conditions obtained in preliminary experiments, such as the manufacturing method and materials of the carbon plastic electrode, which is the electrode sheet according to the present invention, will be explained.
本シートは高分子化合物と、導電性付与用にカーボンブ
ラックと、イオン交換性付与にイオン交換樹脂粉末とさ
らに多孔性付与のための形成物質つまり抽出物と、親木
性を増すための無機塩を混練し、成形後に上記多孔質形
成物質をシート中より除去し、イオン交換性を供与した
多孔質導電シートを製造した。This sheet contains a polymer compound, carbon black to impart conductivity, ion exchange resin powder to impart ion exchange properties, a forming substance or extract to impart porosity, and an inorganic salt to increase wood affinity. After kneading and molding, the porous forming substance was removed from the sheet to produce a porous conductive sheet having ion exchange properties.
成形方法は、一般的なカレンダーロール、コンプレッシ
ョン法、インジェクション法、押出機による成形法が用
いられる。高分子化合物としては、ポリオレフィン系、
ポリアミド系、ポリイミド系がある。一般的で安価とい
う意味ではポリオレフィン系が良い。特に本目的の電池
に使用する場合に於ては、耐薬品性も要求されるため、
ポリエチレンが最良である。またシートに多孔性を与え
る抽出物としては、親油性のものは、石油オイル、ジオ
クチルフタレートがあり、親水性のものは、ポリビニル
アルコールや無機塩としては、塩化カリウム、塩化ナト
リウム、シリカ、アルミナ粉末が一般的である。As the molding method, a general calender roll method, compression method, injection method, or molding method using an extruder is used. Examples of polymer compounds include polyolefins,
There are polyamide and polyimide types. Polyolefins are good because they are common and inexpensive. Especially when used in batteries for this purpose, chemical resistance is also required.
Polyethylene is best. Lipophilic extracts that give porosity to the sheet include petroleum oil and dioctyl phthalate, hydrophilic extracts such as polyvinyl alcohol, and inorganic salts such as potassium chloride, sodium chloride, silica, and alumina powder. is common.
また、イオン交換性粉末としては、高分子母体としてス
チレンとジビニルベンゼンとの共重合体が一般的である
。最近ポリビニルアルコールを高分子母体としたイオン
交換樹脂もある。Further, as an ion exchange powder, a copolymer of styrene and divinylbenzene is generally used as a polymer base. Recently, there are also ion exchange resins that use polyvinyl alcohol as a polymer matrix.
そこで、本電極の基シートである高分子化合物100重
量部に対して、イオン交換体粉末は10〜90重量部が
シートの強度から好ましい。Therefore, from the viewpoint of the strength of the sheet, it is preferable that the ion exchanger powder be used in an amount of 10 to 90 parts by weight based on 100 parts by weight of the polymer compound that is the base sheet of the present electrode.
ただし、本電極にイオン交換能力をさらに高めたい場合
は90重量部以上でもよいし、該能力が低くてもよい場
合には、10重量部以下でもよい。However, if it is desired to further increase the ion exchange ability of the electrode, the amount may be 90 parts by weight or more, and if the ability is acceptable to be low, the amount may be 10 parts by weight or less.
一般にイオン交換樹脂のイオン交換能力を判定すル場合
に“イオン交換容量”が使われている。本電極のイオン
交換容量を増加させて、本シートの臭素吸収能力を高め
るためには、イオン交換樹脂粉末の添加量を増大させれ
ばよい。Generally, "ion exchange capacity" is used to judge the ion exchange ability of an ion exchange resin. In order to increase the ion exchange capacity of this electrode and the bromine absorption capacity of this sheet, it is sufficient to increase the amount of ion exchange resin powder added.
また、抽出物の量は20〜50重量部であることが好ま
しい。そして、この抽出物量は高分子物質とイオン交換
性粉末とが均一に抽出物に濡れることが好ましい。また
、この添、加量によって多孔部分の量を調節することが
できる。多孔部分を増加させようとすれば、抽出物の添
加量を増加させればよいが、150重量部以上では、シ
ートの機J的強度が低下するし、20重量部以下である
と、上記構成原料を均一に濡らすのに不足することがわ
かフた。Moreover, it is preferable that the amount of extract is 20 to 50 parts by weight. It is preferable that the amount of the extract is such that the polymer substance and the ion exchange powder are uniformly wetted with the extract. Further, the amount of porous portion can be adjusted by this addition. If you want to increase the porous area, you can increase the amount of extract added, but if it is more than 150 parts by weight, the mechanical strength of the sheet will decrease, and if it is less than 20 parts by weight, the above structure It was found that it was insufficient to wet the raw materials uniformly.
このほか、導電性付与のためのカーボンブラッりについ
ては、導電性を上げる場合は添加量を増大させればよい
が、通常は30〜90重量部の範囲で添加される。また
、上記のイオン交換樹脂粉末で若干の親水性をもってい
るが、さらに親水性を増大するために、無機物のシリカ
(Si O2)又はアルミナ(Aj220.)の粉末を
30〜50重量部で添加すればよいことがわかった。In addition, regarding carbon brazing for imparting conductivity, the amount added may be increased to increase conductivity, but it is usually added in a range of 30 to 90 parts by weight. In addition, although the above ion exchange resin powder has some hydrophilicity, in order to further increase the hydrophilicity, 30 to 50 parts by weight of inorganic silica (SiO2) or alumina (Aj220.) powder may be added. It turned out to be a good thing.
実施例:
上記のような予備実験の結果にもとづいて、イオン交換
性をもつ多孔質の臭素吸収電極を作製した。すなわち、
密度が0.96g/c+n3、MFR(フローインデッ
クス) 0.80g/l 0m1nのポリエチレン10
0重量部に対し、イオン交換樹脂粉末にチビKK製、イ
オン交換容量3.6meq/gのもの)とカーボンブラ
ック(ライオンアクゾKK製、商標:ケッチェンEC)
をそれぞれ50重量部添加し、さらにシリカ粉末50重
量部を加えて均一に乾燥混合した。この混合物に、ポリ
エチレン100重量部に対して、抽出物としてのジオク
チルフタレートを100重量部の重量混合比率で、バン
バリーミキサ−やニーダ−などにより混練した。この混
練物をカレンダ成形によって厚さ1 mmのシートに成
形した。この成形シートを有機溶媒トリクロルエチレン
によって上記抽出物ジオクチルフタレートを抽出し、多
孔化した電極シートを形成した。Example: Based on the results of the preliminary experiments as described above, a porous bromine absorption electrode with ion exchange properties was produced. That is,
Polyethylene 10 with density 0.96g/c+n3, MFR (flow index) 0.80g/l 0mln
0 parts by weight, ion exchange resin powder manufactured by Chibi KK, ion exchange capacity 3.6 meq/g) and carbon black (manufactured by Lion Akzo KK, trademark: Ketjen EC)
50 parts by weight of each were added, and further 50 parts by weight of silica powder were added and uniformly mixed by drying. This mixture was kneaded with a Banbury mixer, a kneader, etc. at a mixing ratio of 100 parts by weight of dioctyl phthalate as an extract to 100 parts by weight of polyethylene. This kneaded material was formed into a sheet with a thickness of 1 mm by calendering. The above-mentioned extract dioctyl phthalate was extracted from this molded sheet using an organic solvent trichlorethylene to form a porous electrode sheet.
上記のようにして得たイオン交換性多孔質シートの比表
面積は600II12/gで、イオン交換容量は1、O
meq/gである。また、この電極シートの電気抵抗値
は1 mm厚のシートで0.370Ωであった。また、
このシートの臭素の吸収能力を調べた所、1 cmx
1 cmx 1 mm厚のもので、約0.5gの臭素の
吸収を確認した。The specific surface area of the ion-exchangeable porous sheet obtained as described above is 600II12/g, the ion-exchange capacity is 1, O
meq/g. Further, the electrical resistance value of this electrode sheet was 0.370Ω for a 1 mm thick sheet. Also,
When I investigated the bromine absorption capacity of this sheet, it was found that 1 cmx
It was confirmed that about 0.5 g of bromine was absorbed by a 1 cm x 1 mm thick piece.
H1発明の効果
この発明は以上説明したとおり、亜鉛−臭素電池などで
使用される正極用のカーボンプラスチック電極として、
高分子化合物の母体に、イオン交換樹脂と抽出物および
カーボンブラックを混練し、これに抽出物除去の処理を
行なうことによって、イオン交換性をもつ多孔質電極を
構成したので、臭素吸収能の高い電極を得ることができ
た。H1 Effects of the invention As explained above, this invention can be used as a carbon plastic electrode for positive electrodes used in zinc-bromine batteries, etc.
A porous electrode with ion-exchange properties was constructed by kneading ion-exchange resin, extracts, and carbon black into a matrix of polymeric compounds, and then treating this to remove the extracts. I was able to obtain the electrode.
このため、電池の運転における充電時に正極表面に発生
する臭素活物質を電極内に吸収保持し、放電時にこれを
活物質として利用できるので、電解液のタンクおよび配
管系と切り放して電池を使用できるため電気自動車への
搭載容積を小きくすることができる。For this reason, the bromine active material generated on the surface of the positive electrode during charging during battery operation can be absorbed and retained within the electrode and used as an active material during discharge, allowing the battery to be used separately from the electrolyte tank and piping system. Therefore, the mounting volume on an electric vehicle can be reduced.
第1図は電解液種環形亜鉛−臭素電池の動作原理説明図
である。FIG. 1 is an explanatory diagram of the operating principle of an annular zinc-bromine battery using an electrolytic solution.
Claims (4)
の電極において、上記高分子化合物100重量部に対し
、陽イオン交換基をもつイオン交換体粉末を10〜90
重量部、抽出物を20〜150重量部、カーボンブラッ
クを30〜90重量部及び親水性付与剤粉末を30〜5
0重量部を添加して混練成形したのち多孔質処理してな
り、該多孔質電極が臭素活物質の吸収能を備えたことを
特徴とする臭素吸収電極の製造方法。(1) In an electrode for a metal-halogen battery using a polymer compound as a matrix, 10 to 90 parts of ion exchanger powder having a cation exchange group is added to 100 parts by weight of the polymer compound.
parts by weight, 20 to 150 parts by weight of extract, 30 to 90 parts by weight of carbon black, and 30 to 5 parts by weight of hydrophilicity imparting agent powder.
1. A method for producing a bromine-absorbing electrode, which comprises adding 0 parts by weight of the bromine-absorbing electrode, kneading and forming the bromine-absorbing electrode, and then subjecting the porous electrode to a porous treatment so that the porous electrode has the ability to absorb a bromine active material.
である特許請求の範囲第1項記載の電極の製造方法。(2) The method for manufacturing an electrode according to claim 1, wherein the polymer compound is polyethylene, which is a thermoplastic resin.
求の範囲第1項記載の電極の製造方法。(3) The method for producing an electrode according to claim 1, wherein the cation exchange group is a sulfonic acid group.
ずれかの粉末である特許請求の範囲第1項記載の電極の
製造方法。(4) The method for manufacturing an electrode according to claim 1, wherein the hydrophilicity imparting agent powder is either silica or alumina powder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61292602A JPS63148559A (en) | 1986-12-10 | 1986-12-10 | Manufacture of bromine absorbing electrode |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61292602A JPS63148559A (en) | 1986-12-10 | 1986-12-10 | Manufacture of bromine absorbing electrode |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63148559A true JPS63148559A (en) | 1988-06-21 |
JPH0559551B2 JPH0559551B2 (en) | 1993-08-31 |
Family
ID=17783912
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61292602A Granted JPS63148559A (en) | 1986-12-10 | 1986-12-10 | Manufacture of bromine absorbing electrode |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63148559A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4823072B2 (en) * | 2004-11-09 | 2011-11-24 | 株式会社ミツバ | Wiper blade |
US9707932B2 (en) | 2014-03-12 | 2017-07-18 | Kbws Corporation | Wiper blade |
-
1986
- 1986-12-10 JP JP61292602A patent/JPS63148559A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4823072B2 (en) * | 2004-11-09 | 2011-11-24 | 株式会社ミツバ | Wiper blade |
US9707932B2 (en) | 2014-03-12 | 2017-07-18 | Kbws Corporation | Wiper blade |
Also Published As
Publication number | Publication date |
---|---|
JPH0559551B2 (en) | 1993-08-31 |
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