JPS6314860B2 - - Google Patents
Info
- Publication number
- JPS6314860B2 JPS6314860B2 JP58200301A JP20030183A JPS6314860B2 JP S6314860 B2 JPS6314860 B2 JP S6314860B2 JP 58200301 A JP58200301 A JP 58200301A JP 20030183 A JP20030183 A JP 20030183A JP S6314860 B2 JPS6314860 B2 JP S6314860B2
- Authority
- JP
- Japan
- Prior art keywords
- electrolyte
- conductive
- polarizable electrode
- electrode
- electric double
- 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
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- 239000003990 capacitor Substances 0.000 claims description 28
- 239000003792 electrolyte Substances 0.000 claims description 24
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 11
- 239000010936 titanium Substances 0.000 claims description 11
- 229910052719 titanium Inorganic materials 0.000 claims description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 229910052782 aluminium Inorganic materials 0.000 claims description 9
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 8
- 238000007750 plasma spraying Methods 0.000 claims description 4
- 239000004744 fabric Substances 0.000 claims description 2
- 238000005507 spraying Methods 0.000 claims description 2
- 239000000835 fiber Substances 0.000 claims 1
- 238000007751 thermal spraying Methods 0.000 claims 1
- 238000007740 vapor deposition Methods 0.000 claims 1
- 238000000354 decomposition reaction Methods 0.000 description 11
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 239000011255 nonaqueous electrolyte Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000008151 electrolyte solution Substances 0.000 description 4
- 230000010287 polarization Effects 0.000 description 4
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 2
- 229910000906 Bronze Inorganic materials 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000010974 bronze Substances 0.000 description 2
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- MHCFAGZWMAWTNR-UHFFFAOYSA-M lithium perchlorate Chemical compound [Li+].[O-]Cl(=O)(=O)=O MHCFAGZWMAWTNR-UHFFFAOYSA-M 0.000 description 2
- 229910001486 lithium perchlorate Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- -1 polytetrafluoroethylene Polymers 0.000 description 2
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 2
- 230000002829 reductive effect Effects 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- WGHUNMFFLAMBJD-UHFFFAOYSA-M tetraethylazanium;perchlorate Chemical compound [O-]Cl(=O)(=O)=O.CC[N+](CC)(CC)CC WGHUNMFFLAMBJD-UHFFFAOYSA-M 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000006399 behavior Effects 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 230000015654 memory Effects 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000005486 organic electrolyte Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000007650 screen-printing Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- Y02E60/13—Energy storage using capacitors
Landscapes
- Electric Double-Layer Capacitors Or The Like (AREA)
Description
産業上の利用分野
本発明は小型大容量の湿式タイプの電気二重層
キヤパシタに関するものである。
従来例の構成とその問題点
従来、この種の電気二重層キヤパシタは第1図
に示すように、分極性電極体1に導電性電極2を
形成し、これをセパレータ3を介して積層し電解
液を注入することにより構成されている。
また、第2図に示すように分極性電極1とし
て、活性炭粉末に、黒鉛,カーボンブラツク,ポ
リ4弗化エチレン,ポリビニルピロリドン等を加
えてできたペーストを使用し、導電性電極2とし
て、金属の薄板,ネツトまたはパンチングメタル
を使用し、この表面に分極性電極材料を成形プレ
スするか、またはゴム状のものを圧延ローラにか
け分極性電極体と導電性電極を形成している。そ
して、セパレータ3を介して一対の導電性電極を
有する分極性電極体を巻取り、電解液を注入した
ものである。
第1図に示した構成の具体例を第3図に示す。
分極性電極体1として活性炭繊維布を用い、また
導電性電極2としてアルミニウム,チタン等の金
属層,または導電性樹脂層を形成した構成を有す
る。これらをセパレータ3を介して重ね合わせ、
電解液を注入した後ガスケツト4で正,負極を絶
縁した状態でコイン型ケース5で封口ケーシング
する。ここで、金属の導電性電極は、プラズマ溶
射法,アーク溶射法により、また導電性樹脂層は
主にカーボンを導電性粒子とした導電性樹脂をス
クリーン印刷法やスプレイ法,デイツプ法のいず
れかにより形成されている。導電性樹脂を用いた
場合は、金属層を用いた場合より、内部インピー
ダンスが大きくなり、強放電の用途には適さない
キヤパシタとなる。
次に、従来の構成法では問題となるキヤパシタ
の耐電圧について述べる。耐電圧は使用する導電
性電極および電解液に大きく依存する。そこで(1)
水系電解液,(2)非水系電解液を用いた場合の耐電
圧について述べる。
(1) 水系電解液を用いた場合
水系電解液は、非水系電解液に比べ2桁導電率
が高く強放電に適したキヤパシタが得られる。し
かしながら、酸または塩基の水溶液では電解質の
種類に関係せず分解電圧がほとんど一定の値約
1.7Vを示す。例えば1N.25℃で、H2SO4;1.67V,
HaOH;1.69Vとなる。すなわち、この電圧でア
ノードで酸素,カソードで水素の発生が始まる。
しかし、1気圧におけるこの反応の理論的な酸
素,水素の両電極の可逆電位差は約1.23Vで1.7V
の値はこれよりはるかに大きく分極している。実
際には、1.7V付近の分解電圧に近づくにつれ残
余電流がしだいに大きくなり、1.23V以下にキヤ
パシタの印加電圧を制御しないと、漏えい電流が
大きくなり、信頼性を始めとするキヤパシタ特性
が著しく低下する。このように水系電解液を用い
るかぎり、1.23V以上の耐電圧を有し、しかも信
頼性の高いキヤパシタを得ることは不可能であ
る。
(2) 非水系電解液を用いた場合
プロピレンカーボネート,γ―ブチロラクト
ン,N―N―ジメチルホルムアミド,アセトニト
リル等の溶媒に、過塩素酸リチウム,過塩素酸テ
トラエチルアンモニウム等の溶質を溶解させた有
機電解液は水系の電解液より導電率は低いが耐電
圧が高くなることが広く知られている。ここで耐
電圧は、アノードでは、電解液の酸化分解,アノ
ード電極の溶解で規制される一方、カソードでは
電解液,またはカソード電極の還元分解により規
制される。
アノード側の導電性電極にステンレススチール
やアルミニウムを用いた場合、アノード分極する
と不動体化せず溶解し、この溶解による電流が流
れ始める電位は、上記有機溶媒を用いた電解質中
での活性炭電極のアノード酸化あるいは電解質の
分解電位よりも低いため、ステンレススチールま
たはアルミニウムを集電体とした場合には陽極電
位がこれらの溶解電位で制限され、分極性電極と
電解液で決定される電気化学的に安定な電位領域
を有効に使用することができない。
さらにカソード側導電性電極としてチタンを使
用した場合、チタン中の酸化チタンが次式のよう
な反応によりチタンブロンズとなる。
TiO2+H++e→HTiO2
この反応によりカソード分極で電流が流れ始
め、キヤパシタの漏れ電流となる。このように本
キヤパシタは使用する電解液と導電性電極によ
り、耐電圧が大きく左右されることがわかる。さ
らに現在、電気二重層キヤパシタはメモリ素子の
バツクアツプ電源として使用されており、多くの
メモリは5.5V作動するため、水系電解液を使用
した場合、7〜8層もの単セルを積層,非水電解
液を使用した場合でも3層単セルを直列につなが
なければ耐電圧が得られない。したがつて直列に
積層した場合の合成容量は、水系電解液の場合で
単セルの1/7〜1/8にも低下,非水系電解液の場合
でも単セルの1/3にも低下してしまい、いかに高
耐圧のキヤパシタを得ることが有利であるかがわ
かる。以上記載したように従来の導電性電極構成
では、最高の使用耐圧を単セル当たり、2.3V以
上に上げることが困難である。
発明の目的
本発明は、従来の電気二重層キヤパシタの導電
性電極構成を改良することにより、高耐圧の電気
二重層キヤパシタを得ることを目的とするもので
ある。
発明の構成
この目的を達成するために本発明は、アノード
側分極性電極体の片面にチタンからなる導電性電
極を形成するとともに、カソード側分極性電極体
の片面にアルミニウムから導電性電極を形成し、
この導電性電極を形成したアノード側およびカソ
ード側分極性電極体をセパレータを介して相対向
させ電解液を注入して構成したものである。
実施例の説明
具体的実施例を述べる前に電気二重層キヤパシ
タの耐電圧について説明する。
理想的な、キヤパシタの耐圧は、キヤパシタを
アノード分極,カソード分極した時の分極性電
極,導電性電極の分解電位が電解液の分解電位よ
りも大きく、分解電流が、電解液の酸化,還元に
よる分解により規制されるものである。したがつ
て、第4図に示すi―E曲線のように、分極性電
極,導電性電極の分解電位6が電解液の分解電位
7より大きければ良いことになる。
また、このキヤパシタの構成材料のアノード分
極,カソード分極を行つた場合の電流,電位曲線
(i―E曲線)は、通常の3極法により、対向極
に銀,照合電極にカーボンを用いた実験により求
めた。
(実施例 1)
分極性電極に比表面積が2000m2/gの活性炭繊
維を用い、アノード側分極性電極体8の片面にプ
ラズマ溶射法によりチタンの導電性電極9を形成
し、カソード側分極性電極体10の片面にプラズ
マ溶射法によりアルミニウムの導電性電極11を
形成し、電子的な短絡を防止するためポリプロピ
レン製のセパレータ12を介して重ね合わせ、過
塩素酸テトラエチルアンモニウムをプロピレンカ
ーボネートに溶解させた溶液を電解液Aとして注
入した後、第5図に示すようなコイン型のケース
5に封入してケーシングする。ここで、本実施例
の分極性電極,導電性電極の電気化学的挙動を調
べた。用いた電解液はいずれもAである。
第6図に3極法によるカーボンのi―E曲線を
示す。アノード,カソード分極により流れる電流
13,14は電解液の分解に起因するものと考え
られ、中間領域での電流15は、電気二重層への
充電電流である。
また、第7図に同様なチタンのi―E曲線を、
第8図にアルミニウムのi―E曲線を示す。第7
図よりチタンはカソード分極でチタンブロンズを
生成するので、カソード分極した場合、この反応
による電流が流れる。第8図よりアルミニウムは
アノード分極で溶解するため、アノード分極で大
きな耐圧を期待できないことがわかる。
実施例1では、アノード導電性電極にチタンを
カソード導電性電極にアルミニウムを使用してい
るため、約2.9の耐圧が得られる。
分極性電極を直径15mmの円にした時のキヤパシ
タ諸特性を第1表に示す。従来のものに比べ耐圧
が2.3Vから2.9Vと向上する。
INDUSTRIAL APPLICATION FIELD The present invention relates to a small-sized, large-capacity, wet-type electric double layer capacitor. Conventional Structure and Problems Conventionally, this type of electric double layer capacitor, as shown in FIG. It is constructed by injecting liquid. Further, as shown in FIG. 2, a paste made by adding graphite, carbon black, polytetrafluoroethylene, polyvinylpyrrolidone, etc. to activated carbon powder is used as the polarizable electrode 1, and a metal paste is used as the conductive electrode 2. A polarizable electrode material is formed and pressed onto the surface of a thin plate, net, or punched metal, or a rubber-like material is applied to a rolling roller to form a polarizable electrode body and a conductive electrode. Then, a polarizable electrode body having a pair of conductive electrodes is wound up with a separator 3 interposed therebetween, and an electrolyte is injected therein. A specific example of the configuration shown in FIG. 1 is shown in FIG.
It has a structure in which an activated carbon fiber cloth is used as the polarizable electrode body 1, and a metal layer of aluminum, titanium, etc., or a conductive resin layer is formed as the conductive electrode 2. These are superimposed via a separator 3,
After injecting the electrolyte, the positive and negative electrodes are insulated with a gasket 4, and then sealed with a coin-shaped case 5. Here, the metal conductive electrode is formed by a plasma spraying method or an arc spraying method, and the conductive resin layer is formed by a screen printing method, a spray method, or a dip method. It is formed by When a conductive resin is used, the internal impedance becomes larger than when a metal layer is used, resulting in a capacitor that is not suitable for strong discharge applications. Next, we will discuss the withstand voltage of the capacitor, which is a problem with conventional construction methods. The withstand voltage largely depends on the conductive electrode and electrolyte used. Therefore (1)
We will discuss the withstand voltage when using an aqueous electrolyte and (2) a non-aqueous electrolyte. (1) When using an aqueous electrolyte Aqueous electrolytes have two orders of magnitude higher conductivity than non-aqueous electrolytes and can provide capacitors suitable for strong discharge. However, in aqueous solutions of acids or bases, the decomposition voltage remains almost constant regardless of the type of electrolyte.
Indicates 1.7V. For example, 1N.25℃, H 2 SO 4 ; 1.67V,
HaOH: 1.69V. That is, at this voltage, oxygen begins to be generated at the anode and hydrogen begins to be generated at the cathode.
However, the theoretical reversible potential difference between the oxygen and hydrogen electrodes for this reaction at 1 atm is approximately 1.23V and 1.7V.
The value of is much more polarized than this. In reality, the residual current gradually increases as it approaches the decomposition voltage of around 1.7V, and unless the voltage applied to the capacitor is controlled below 1.23V, the leakage current will increase and the capacitor characteristics, including reliability, will significantly deteriorate. descend. As long as an aqueous electrolyte is used in this way, it is impossible to obtain a highly reliable capacitor that has a withstand voltage of 1.23 V or more. (2) When using a nonaqueous electrolyte Organic electrolysis in which a solute such as lithium perchlorate or tetraethylammonium perchlorate is dissolved in a solvent such as propylene carbonate, γ-butyrolactone, N-N-dimethylformamide, or acetonitrile. It is widely known that the electrolyte has a lower electrical conductivity than an aqueous electrolyte, but has a higher withstand voltage. Here, the withstand voltage is regulated at the anode by oxidative decomposition of the electrolyte and dissolution of the anode electrode, while at the cathode it is regulated by the reductive decomposition of the electrolyte or the cathode electrode. When stainless steel or aluminum is used for the conductive electrode on the anode side, when the anode is polarized, it does not become passivated but dissolves, and the potential at which a current begins to flow due to this dissolution is the same as that of the activated carbon electrode in the electrolyte using the above organic solvent. Since it is lower than the anodic oxidation or electrolyte decomposition potential, when stainless steel or aluminum is used as the current collector, the anodic potential is limited by these dissolution potentials, and the electrochemical potential determined by the polarizable electrode and electrolyte is The stable potential region cannot be used effectively. Furthermore, when titanium is used as the cathode side conductive electrode, titanium oxide in titanium becomes titanium bronze through a reaction as shown in the following formula. TiO 2 +H + +e→HTiO 2 Due to this reaction, current begins to flow due to cathode polarization, resulting in leakage current of the capacitor. Thus, it can be seen that the withstand voltage of this capacitor is greatly influenced by the electrolyte and conductive electrode used. Furthermore, electric double layer capacitors are currently used as backup power sources for memory devices, and since many memories operate at 5.5V, when using an aqueous electrolyte, seven or eight layers of single cells are stacked together, and non-aqueous electrolyte Even if liquid is used, withstand voltage cannot be obtained unless three-layer single cells are connected in series. Therefore, when stacked in series, the combined capacity is reduced to 1/7 to 1/8 of a single cell in the case of an aqueous electrolyte, and 1/3 of a single cell in the case of a non-aqueous electrolyte. This shows how advantageous it is to obtain a capacitor with high withstand voltage. As described above, with the conventional conductive electrode configuration, it is difficult to increase the maximum usable breakdown voltage to 2.3 V or more per single cell. OBJECT OF THE INVENTION The object of the present invention is to obtain an electric double layer capacitor with high withstand voltage by improving the conductive electrode structure of a conventional electric double layer capacitor. Structure of the Invention In order to achieve this object, the present invention forms a conductive electrode made of titanium on one side of an anode-side polarizable electrode body, and forms a conductive electrode made of aluminum on one side of a cathode-side polarizable electrode body. death,
The anode-side and cathode-side polarizable electrode bodies on which the conductive electrodes are formed are opposed to each other with a separator interposed therebetween, and an electrolytic solution is injected thereinto. Description of Examples Before describing specific examples, the withstand voltage of an electric double layer capacitor will be explained. The ideal breakdown voltage of a capacitor is that when the capacitor is polarized as an anode or a cathode, the decomposition potential of the polarizable electrode and conductive electrode is greater than the decomposition potential of the electrolyte, and the decomposition current is caused by oxidation and reduction of the electrolyte. It is regulated by decomposition. Therefore, as shown in the iE curve shown in FIG. 4, it is sufficient that the decomposition potential 6 of the polarizable electrode and the conductive electrode is greater than the decomposition potential 7 of the electrolytic solution. In addition, the current and potential curves (i-E curves) when the constituent materials of this capacitor are polarized anode and cathode are obtained using the usual three-electrode method using silver for the opposing electrode and carbon for the reference electrode. It was calculated by (Example 1) Activated carbon fibers with a specific surface area of 2000 m 2 /g were used for the polarizable electrode, and a titanium conductive electrode 9 was formed on one side of the anode-side polarizable electrode body 8 by plasma spraying, and the cathode-side polarizability An aluminum conductive electrode 11 is formed on one side of the electrode body 10 by plasma spraying, and is overlapped with a polypropylene separator 12 interposed therebetween to prevent electronic short circuits, and tetraethylammonium perchlorate is dissolved in propylene carbonate. After injecting the solution as electrolyte A, it is enclosed in a coin-shaped case 5 as shown in FIG. 5 and cased. Here, the electrochemical behavior of the polarizable electrode and conductive electrode of this example was investigated. The electrolyte solution used was A in all cases. FIG. 6 shows the iE curve of carbon obtained by the three-electrode method. Currents 13 and 14 flowing due to anode and cathode polarization are considered to be caused by decomposition of the electrolyte, and current 15 in the intermediate region is a charging current to the electric double layer. In addition, a similar iE curve of titanium is shown in Figure 7.
Figure 8 shows the iE curve of aluminum. 7th
As shown in the figure, titanium produces titanium bronze when cathodically polarized, so when cathodically polarized, a current flows due to this reaction. From FIG. 8, it can be seen that since aluminum is dissolved by anode polarization, a large withstand voltage cannot be expected by anodic polarization. In Example 1, since titanium is used for the anode conductive electrode and aluminum is used for the cathode conductive electrode, a breakdown voltage of about 2.9 is obtained. Table 1 shows the various characteristics of the capacitor when the polarizable electrode is a circle with a diameter of 15 mm. Compared to the conventional model, the withstand voltage is improved from 2.3V to 2.9V.
【表】
(実施例 2)
実施例1とまつたく同様な分極性電極と導電性
電極を用い、第2図に示した構造のキヤパシタを
作成した。本実施例でのキヤパシタ特性を第2表
に示す。第2表からも本構造のキヤパシタは従来
のものより大きな耐圧を示すことがわかる。
用いた分極性電極は10cm×5cmの大きさのもの
である。[Table] (Example 2) Using polarizable electrodes and conductive electrodes that were exactly the same as in Example 1, a capacitor having the structure shown in FIG. 2 was created. Table 2 shows the capacitor characteristics in this example. It can also be seen from Table 2 that the capacitor of this structure exhibits a higher withstand voltage than the conventional capacitor. The polarizable electrode used had a size of 10 cm x 5 cm.
【表】
(実施例 3)
実施例1,2と同様な分極性電極と導電性電極
を用い、第3表に示す溶媒と電解質の組み合わせ
による電解液を使用した場合における耐電圧を測
定し、第3表の右欄に示した。第3表より、有機
電解液を用いたキヤパシタは2.8〜3.0Vの耐圧を
示すことがわかる。[Table] (Example 3) Using the same polarizable electrodes and conductive electrodes as in Examples 1 and 2, the withstand voltage was measured when an electrolytic solution with the combination of solvent and electrolyte shown in Table 3 was used. It is shown in the right column of Table 3. From Table 3, it can be seen that the capacitor using the organic electrolyte exhibits a withstand voltage of 2.8 to 3.0V.
【表】【table】
【表】
〓α:過塩素酸リチウム 〓
[Table] 〓α: Lithium perchlorate 〓
Claims (1)
なる導電性電極を形成するとともに、カソード側
分極性電極体の片面にアルミニウムからなる導電
性電極を形成し、このアノード側およびカソード
側分極性電極体をセパレータを介して相対向させ
電解液を注入して構成した電気二重層キヤパシ
タ。 2 分極性電極体の片面に形成された導電性電極
が導電性ケースと接触することを特徴とする特許
請求の範囲第1項記載の電気二重層キヤパシタ。 3 導電性電極がプラズマ溶射,アーク溶射等の
溶射法、または蒸着法のいずれかにより、分極性
電極体上に形成されたことを特徴とする特許請求
の範囲第1項記載の電気二重層キヤパシタ。 4 分極性電極体に、繊維布状,紙状,フエルト
状,あるいは多孔体状の活性炭を用いることを特
徴とする特許請求の範囲第1項記載の電気二重層
キヤパシタ。[Claims] 1. A conductive electrode made of titanium is formed on one side of the polarizable electrode body on the anode side, and a conductive electrode made of aluminum is formed on one side of the polarizable electrode body on the cathode side. An electric double layer capacitor constructed by placing cathode-side polarizable electrode bodies facing each other with a separator in between and injecting an electrolyte. 2. The electric double layer capacitor according to claim 1, wherein the conductive electrode formed on one side of the polarizable electrode body is in contact with the conductive case. 3. The electric double layer capacitor according to claim 1, wherein the conductive electrode is formed on the polarizable electrode body by either a thermal spraying method such as plasma spraying or arc spraying, or a vapor deposition method. . 4. The electric double layer capacitor according to claim 1, wherein activated carbon in the form of fiber cloth, paper, felt, or porous body is used for the polarizable electrode body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58200301A JPS6092605A (en) | 1983-10-26 | 1983-10-26 | electric double layer capacitor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58200301A JPS6092605A (en) | 1983-10-26 | 1983-10-26 | electric double layer capacitor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6092605A JPS6092605A (en) | 1985-05-24 |
| JPS6314860B2 true JPS6314860B2 (en) | 1988-04-01 |
Family
ID=16422035
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58200301A Granted JPS6092605A (en) | 1983-10-26 | 1983-10-26 | electric double layer capacitor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6092605A (en) |
-
1983
- 1983-10-26 JP JP58200301A patent/JPS6092605A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6092605A (en) | 1985-05-24 |
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