JPH03220713A - Manufacture of electric double layer capacitor - Google Patents
Manufacture of electric double layer capacitorInfo
- Publication number
- JPH03220713A JPH03220713A JP2014793A JP1479390A JPH03220713A JP H03220713 A JPH03220713 A JP H03220713A JP 2014793 A JP2014793 A JP 2014793A JP 1479390 A JP1479390 A JP 1479390A JP H03220713 A JPH03220713 A JP H03220713A
- Authority
- JP
- Japan
- Prior art keywords
- double layer
- electric double
- resin
- capacitance
- layer capacitor
- 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.)
- Pending
Links
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)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は電気二重層コンデンサの製造方法に関し、特に
電気二重層コンデンサ用電極材料である活性炭の製造に
特徴を有する電気二重層コンデンサの製造方法に関する
ものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for manufacturing an electric double layer capacitor, and particularly to a method for manufacturing an electric double layer capacitor, which is characterized in manufacturing activated carbon, which is an electrode material for an electric double layer capacitor. It is related to.
[従来の技術およびその課題]
電気二重層コンデンサの基本構成(以下、基本素子と称
す〉は、第2図に示すように、活性炭層1と集電体2を
単位分極性電極とし、一対の分極性電極の間に電解質溶
液を含浸し、電子絶縁性でかつイオン透過性の多孔性セ
パレータ3で電子的短絡を防止したものである。なお、
4は絶縁性ガスケットである。電気二重層コンデンサは
、基本素子の使用最高電圧が電解質溶液の電気分解電圧
以下であるため、使用電圧に応じて1枚以上積層した構
造となっている。[Prior art and its problems] The basic configuration of an electric double layer capacitor (hereinafter referred to as the basic element) consists of an activated carbon layer 1 and a current collector 2 as unit polarizable electrodes, and a pair of An electrolyte solution is impregnated between the polarizable electrodes, and electronic short circuits are prevented by a porous separator 3 that is electronically insulating and ion permeable.
4 is an insulating gasket. Electric double layer capacitors have a structure in which one or more capacitors are laminated depending on the voltage used, since the maximum operating voltage of the basic element is lower than the electrolytic voltage of the electrolyte solution.
ところで、電気二重層コンデンサは、小型で大容量のコ
ンデンサとして、マイコン、メモリ等のバックアップや
、瞬時に大電流を供給できる補助電源などに広く用いら
れており、マイコン等を組み込んだ装置やシステムの小
型・軽量化に伴い、そこに用いられる電気二重層コンデ
ンサも小型のものが強く望まれている。この電気二重層
コンデンサの小型化を実現するためには、単位体積当た
りの電気二重層容量を増加させることが非常に重要とな
っている。By the way, electric double layer capacitors are small, large-capacity capacitors that are widely used for backup of microcomputers, memories, etc., and for auxiliary power supplies that can instantaneously supply large currents. As devices become smaller and lighter, there is a strong desire for smaller electric double layer capacitors to be used there. In order to realize miniaturization of this electric double layer capacitor, it is very important to increase the electric double layer capacitance per unit volume.
従来、電気二重層コンデンサに使用されていた活性炭は
、吸着用または触媒用に開発されたものを転用していた
。そのため電気二重層コンデンサの分極性電極に適した
材料設計がされておらず、どの活性炭を用いても静電容
量2等価点列抵抗などのコンデンサ特性にそれほど変化
がなかった。Conventionally, the activated carbon used in electric double layer capacitors was originally developed for adsorption or catalyst use. For this reason, materials have not been designed that are suitable for the polarizable electrodes of electric double layer capacitors, and no matter which activated carbon is used, capacitor characteristics such as capacitance two-equivalent dot series resistance do not change much.
また、現在まで分極性電極の形態などに関する提案は多
くなされているが、電気二重層コンデンサに適した活性
炭の製造条件に関してはそれほど多くなく、かつ十分に
満足できるものではなかつた。Furthermore, although many proposals regarding the form of polarizable electrodes have been made up to now, there have not been many proposals regarding the manufacturing conditions for activated carbon suitable for electric double layer capacitors, and none have been fully satisfactory.
本発明は以上述べたにうな従来の課題を解決するために
なされたもので、分極性電極の単位体積当たりの電気二
重層容量が大きな小型・大容量の電気二重層コンデンサ
の製造方法を提供することにある。The present invention has been made to solve the above-mentioned conventional problems, and provides a method for manufacturing a small and large-capacity electric double layer capacitor with a large electric double layer capacitance per unit volume of polarizable electrodes. There is a particular thing.
[課題を解決するための手段]
本発明は、活性炭および電解質溶液の混合物と集電体と
で分極性電極を形成し、セパレータを介して対向させた
一対の前記分極性電極を積層してなる電気二重層コンデ
ンサの製造方法において、活性炭は、熱硬化性樹脂を5
00〜700°Cの温度で炭化させて製造することを特
徴とする電気二重層コンデンサの製造方法である。[Means for Solving the Problems] The present invention comprises forming a polarizable electrode with a mixture of activated carbon and an electrolyte solution and a current collector, and stacking a pair of the polarizable electrodes facing each other with a separator interposed therebetween. In the method for manufacturing electric double layer capacitors, activated carbon is made of thermosetting resin.
This is a method for manufacturing an electric double layer capacitor, which is characterized by carbonizing the capacitor at a temperature of 00 to 700°C.
[作用]
熱硬化性樹脂を炭化していくと、樹脂から炭素前駆体に
変化する変曲点が400’Cと500’Cの間に存在し
、このため等価直列抵抗の値は400 ’Cと500°
Cの間に大ぎな差がでる。一方、炭化温度を−Lげて炭
素化を進めると、重量減少・収縮が起こるが、650
’C付近までは重量減少の影響が大きいために、650
’C付近で炭化物の表面積が最大となる。そして650
℃以上では、炭化物の収縮による影響が大きいため、漸
次気孔が消滅する。この気孔が賦活時の反応に重要な役
割を果たしているものと考えられる。従って、静電容量
が明らかに大きく等価直列抵抗の値が問題のない炭化湿
度の領域は、500℃以上、700℃以下であるといえ
る。[Function] When the thermosetting resin is carbonized, there is an inflection point between 400'C and 500'C where the resin changes to a carbon precursor, so the value of the equivalent series resistance is 400'C. and 500°
There is a big difference between C. On the other hand, if carbonization is promoted by lowering the carbonization temperature by -L, weight loss and shrinkage occur, but 650
Up to around 'C, the effect of weight loss is large, so 650
The surface area of carbides is maximum near 'C. and 650
At temperatures above 0.degree. C., the pores gradually disappear due to the large effect of shrinkage of carbides. It is thought that these pores play an important role in the reaction during activation. Therefore, it can be said that the range of carbonization humidity where the capacitance is clearly large and the value of equivalent series resistance is not a problem is 500° C. or higher and 700° C. or lower.
[実施例] 次に、本発明の実施例について説明する。[Example] Next, examples of the present invention will be described.
実施例1〜3、比較例1〜5
原材料に熱硬化性樹脂であるフェノール樹脂を使用した
。この樹脂20gをアルミナのセックに入れ、窒素雰囲
気において管状型電気炉により、第1表に示すように4
00〜1400’Cで炭化した。Examples 1 to 3, Comparative Examples 1 to 5 Phenol resin, which is a thermosetting resin, was used as a raw material. 20g of this resin was placed in an alumina SEC and heated in a tubular electric furnace in a nitrogen atmosphere to produce 4
Carbonized at 00-1400'C.
炭化時間は2時間で、昇温速度は1時間当たり100℃
である。得られた炭化物を遊星ボールミルで粉砕後、こ
の炭素粉末をアルミナのセックに入れ、管状型電気炉で
賦活を行った。賦活温度は900℃であり、昇温速度は
1時間当たり200″Gである。賦活方法は、水蒸気に
よるガス賦活法であり、所定の温度に到達後、窒素ガス
をキャリヤガスとして、露点温度が室温であるような水
蒸気を炉内に導入した。賦活時間は4時間である。Carbonization time is 2 hours, temperature increase rate is 100℃ per hour
It is. After the obtained carbide was pulverized in a planetary ball mill, the carbon powder was placed in an alumina SEC and activated in a tubular electric furnace. The activation temperature is 900°C, and the heating rate is 200''G per hour.The activation method is a gas activation method using water vapor, and after reaching a predetermined temperature, nitrogen gas is used as a carrier gas to raise the dew point temperature. Steam was introduced into the furnace at room temperature.The activation time was 4 hours.
上記試料を後述する基本素子の活性炭として用いて、電
気二重層コンデンサを製造した。An electric double layer capacitor was manufactured using the above sample as activated carbon for a basic element to be described later.
実施例4
原材料として熱硬化性樹脂であるフェノール樹脂の繊維
を使用した。このフェノール樹脂繊維20gをアルミナ
のせツタに入れ、窒素雰囲気に弓
おいて管状型電気炉により600’Cで炭化した。炭化
時間は2時間で、昇温速度は1時間当たり100°Cで
ある。得られた炭素繊維をそのままアルミナのセックに
入れ、管状型電気炉で賦活を行った。Example 4 Fibers of phenolic resin, which is a thermosetting resin, were used as a raw material. 20 g of this phenolic resin fiber was placed in an alumina pot, placed in a nitrogen atmosphere, and carbonized at 600'C in a tubular electric furnace. The carbonization time was 2 hours, and the temperature increase rate was 100°C per hour. The obtained carbon fibers were directly placed in an alumina SEC and activated in a tubular electric furnace.
賦活工程は実施例1と同様である。The activation process is the same as in Example 1.
上記試料を後述する基本素子の活性炭として用いて、電
気二重層コンデンサを製造した。An electric double layer capacitor was manufactured using the above sample as activated carbon for a basic element to be described later.
実施例5
原材料として実施例1で使用したものと同じフェノール
系の熱硬化性樹脂を使用した。この樹脂を比重1.8の
塩化亜鉛溶液に浸漬し、乾燥後、管状型電気炉において
薬品賦活を行った。樹脂に対する塩化亜鉛の重量比は1
.65である。賦活温度は600°Cで、昇温速度は1
時間当たりioo’cである。また、賦活時間は4時間
とした。得られた活性炭を洗浄・乾燥後、後述する基本
素子の活性炭として用いて、電気二重層コンデンサを製
造した。Example 5 The same phenolic thermosetting resin used in Example 1 was used as a raw material. This resin was immersed in a zinc chloride solution with a specific gravity of 1.8, and after drying, chemical activation was performed in a tubular electric furnace. The weight ratio of zinc chloride to resin is 1
.. It is 65. The activation temperature is 600°C, and the heating rate is 1
ioo'c per hour. Moreover, the activation time was 4 hours. After washing and drying the obtained activated carbon, an electric double layer capacitor was manufactured by using it as activated carbon for a basic element to be described later.
比較例6
原材料として熱可塑性樹脂であるポリ塩化ビ二ルを使用
した。原材料以外の活性炭製造条件は、実施例1と同じ
である。Comparative Example 6 Polyvinyl chloride, which is a thermoplastic resin, was used as a raw material. The activated carbon production conditions other than the raw materials were the same as in Example 1.
上記試料を後述する基本素子の活性炭として用いて、電
気二重層コンデンサを製造した。An electric double layer capacitor was manufactured using the above sample as activated carbon for a basic element to be described later.
上述した実施例および比較例の電気二重層コンデンサの
製造方法は、以下のとおりである。The method for manufacturing the electric double layer capacitors of the above-mentioned Examples and Comparative Examples is as follows.
第2図において、集電体2としては膜厚200IIIn
で直径8.2 mmの未加硫の導電性ブチルゴムを用い
た。また、絶縁性ガスケット4としては膜厚500jJ
、直径8.2mmで、同心円状に3.8mmの孔を開け
た未加硫のブチルゴムを用いた。多孔性セパレータ3に
はポリエチレン製の膜厚100胸で直径6、Ommのも
のを使用した。In FIG. 2, the current collector 2 has a film thickness of 200IIIn.
An unvulcanized conductive butyl rubber having a diameter of 8.2 mm was used. In addition, the film thickness of the insulating gasket 4 is 500JJ.
, unvulcanized butyl rubber with a diameter of 8.2 mm and concentric holes of 3.8 mm was used. The porous separator 3 was made of polyethylene and had a thickness of 100mm and a diameter of 60mm.
実施例4以外は、集電体2と絶縁性ガスケット4を圧着
して形成された凹部に、各実施例および比較例で得られ
た活性炭と電解質溶液とを混合したペーストを充填する
ことにより、単位分極性電極を得た。実施例4は、集電
体2と絶縁性ガスケット4を圧着して形成された凹部に
、実施例より得られた活性炭布を直径3.8mmの円状
に打ち抜き、電解質溶液を含浸させたものを充填するこ
とにより、単位分極性電極を得た。電解質溶液には、4
0重量%の硫酸水溶液を用いた。この単位分極性電極の
一対をペーストが相対する方向で多孔性セパレータ3を
介して圧着し、7に’j/Cm2の圧力を加えた状態で
120℃の温度に3時間放置することで、集電体2と絶
縁性ガスケット4および絶縁性ガスケット4間を加硫接
着し、電気二重層コンデンサの基本素子8を得た。この
基本素子8を第3図に示すように6枚積層し、金属ケー
ス5と絶縁ケース6でかしめ封口して、電極7a、7b
で外部に端子を取り出すことにより、動作電圧5Vの電
気二重層コンデンサを製造した。In all cases other than Example 4, the recesses formed by crimping the current collector 2 and the insulating gasket 4 were filled with a paste containing a mixture of activated carbon and electrolyte solution obtained in each Example and Comparative Example. A unit polarizable electrode was obtained. In Example 4, the activated carbon cloth obtained in Example was punched into a circular shape with a diameter of 3.8 mm and impregnated with an electrolyte solution in the recess formed by pressing the current collector 2 and the insulating gasket 4 together. A unit polarizable electrode was obtained by filling the solution with . The electrolyte solution contains 4
A 0% by weight aqueous sulfuric acid solution was used. A pair of unit polarizable electrodes is crimped with the paste facing each other through a porous separator 3, and a pressure of 'j/Cm2 is applied to 7, and the mixture is left at a temperature of 120°C for 3 hours. The electric body 2, the insulating gasket 4, and the insulating gasket 4 were bonded together by vulcanization to obtain a basic element 8 of an electric double layer capacitor. Six basic elements 8 are laminated as shown in FIG.
By taking out the terminals to the outside, an electric double layer capacitor with an operating voltage of 5V was manufactured.
各実施例および比較例で製造した電気二重層コンデンサ
について、コンデンサ特性である静電容量と等価直列抵
抗を測定した。静電容量の測定は、コンデンサに直列に
1にΩの抵抗を挿入し、5■の定電圧を印加した時の時
定数より算出した。Capacitance and equivalent series resistance, which are capacitor characteristics, were measured for the electric double layer capacitors manufactured in each Example and Comparative Example. The capacitance was measured by inserting a 1Ω resistor in series with the capacitor and calculating from the time constant when a constant voltage of 5Ω was applied.
また、等価直列抵抗は、電気二重層コンデンサに1 k
Hz・ 10 mAの定電流を流し、電気二重層コンデ
ンサの両端の電圧を測定することにより求めた。Also, the equivalent series resistance is 1 k for the electric double layer capacitor.
It was determined by flowing a constant current of Hz/10 mA and measuring the voltage across the electric double layer capacitor.
第1表に各実施例および比較例で得られた電気二重層コ
ンデンサの特性を示す。また、第1図に炭化温度と静電
容量の関係を示す。第1図中の番号は、第1表の試料番
号に対応するものである。Table 1 shows the characteristics of the electric double layer capacitors obtained in each example and comparative example. Further, FIG. 1 shows the relationship between carbonization temperature and capacitance. The numbers in FIG. 1 correspond to the sample numbers in Table 1.
第1図から明らかなように、炭化温度が低いほど静電容
量が大きくなっているが、等価直列抵抗の値は400℃
と500℃の間に大きな差があることがわかる。本発明
者らの研究・調査によれば、樹脂を炭化していくと樹脂
から炭素前駆体に変化する変曲点が400℃と500℃
の間に存在する。そして、炭化温度を上げ炭素化を進め
ると重量減少・収縮が起こるが、650℃付近までは重
量減少の影響が大きいために、E)50℃付近で炭化物
の表面積が最大となる。そして650℃以上では、炭化
物の収縮による影響が大きいため、漸次気孔が消滅する
。この気孔が賦活時の反応に重要な役割を果たしている
ものと考えられる。従って、静電容量が明らかに大きく
等価直列抵抗の値が問題のない炭化温度の領域は、50
0℃以上、700’l下であるといえる。As is clear from Figure 1, the lower the carbonization temperature, the larger the capacitance, but the value of the equivalent series resistance is 400°C.
It can be seen that there is a large difference between 500℃ and 500℃. According to the research and investigation conducted by the present inventors, when resin is carbonized, the inflection point at which the resin changes into a carbon precursor is 400°C and 500°C.
exists between. Then, when the carbonization temperature is increased and carbonization is progressed, weight loss and shrinkage occur, but the effect of weight loss is large up to around 650°C, so E) The surface area of the carbide reaches its maximum at around 50°C. At temperatures above 650° C., the pores gradually disappear due to the large effect of shrinkage of the carbide. It is thought that these pores play an important role in the reaction during activation. Therefore, the carbonization temperature range where the capacitance is clearly large and the value of equivalent series resistance is not a problem is 50
It can be said that the temperature is above 0°C and below 700'l.
実施例4および5でも、実施例2と比較して静電容量は
ほぼ同じ値になった。この結果より、樹脂の形態や賦活
方法に比べ、炭化の条件が電気二重層コンデンサの性能
に多大な影響を与えるものであるといえる。In Examples 4 and 5, the capacitances were also approximately the same as in Example 2. From this result, it can be said that the carbonization conditions have a greater influence on the performance of electric double layer capacitors than the form of the resin or the activation method.
比較例6は、熱硬化性樹脂と比較してコンデンサ特性に
それほど効果がみられなかった。これは、樹脂の炭素化
過程において流動性があるために、炭化後の気孔が少な
いことによるものと思われる。Comparative Example 6 did not show much effect on capacitor properties compared to thermosetting resin. This is thought to be because the resin has fluidity during the carbonization process, so there are fewer pores after carbonization.
(以下余白)
弔
1
表
]
[発明の効果]
以上説明したように、本発明の方法によれば、小型で大
容量の電気二重層コンデンサを得ることができる。(The following is a margin) Condolences 1 Table] [Effects of the Invention] As explained above, according to the method of the present invention, it is possible to obtain a small-sized, large-capacity electric double layer capacitor.
第1図は樹脂の炭化温度と電気二重層コンデンサの静電
容量との関係を示す特性図、第2図は電気二重層コンデ
ンサの基本素子の断面図、第3図は本発明の一実施例に
よって得られる電気二重層コンデンサの断面図である。Fig. 1 is a characteristic diagram showing the relationship between the carbonization temperature of the resin and the capacitance of the electric double layer capacitor, Fig. 2 is a sectional view of the basic element of the electric double layer capacitor, and Fig. 3 is an embodiment of the present invention. FIG. 2 is a cross-sectional view of an electric double layer capacitor obtained by the method.
Claims (1)
分極性電極を形成し、セパレータを介して対向させた一
対の前記分極性電極を積層してなる電気二重層コンデン
サの製造方法において、活性炭は、熱硬化性樹脂を50
0〜700℃の温度で炭化させて製造することを特徴と
する電気二重層コンデンサの製造方法。(1) A method for manufacturing an electric double layer capacitor in which a polarizable electrode is formed with a mixture of activated carbon and an electrolyte solution and a current collector, and a pair of the polarizable electrodes are laminated to face each other with a separator in between. 50% thermosetting resin
A method for manufacturing an electric double layer capacitor, which comprises carbonizing the capacitor at a temperature of 0 to 700°C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2014793A JPH03220713A (en) | 1990-01-26 | 1990-01-26 | Manufacture of electric double layer capacitor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2014793A JPH03220713A (en) | 1990-01-26 | 1990-01-26 | Manufacture of electric double layer capacitor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03220713A true JPH03220713A (en) | 1991-09-27 |
Family
ID=11870933
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2014793A Pending JPH03220713A (en) | 1990-01-26 | 1990-01-26 | Manufacture of electric double layer capacitor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03220713A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5603867A (en) * | 1994-09-09 | 1997-02-18 | Nippon Sanso Corporation | Method of production for active carbon electrode for use as electrical double layer condenser and active carbon electrode obtained thereby |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6027113A (en) * | 1983-07-22 | 1985-02-12 | 松下電器産業株式会社 | Electric double layer capacitor |
| JPS60201612A (en) * | 1984-03-27 | 1985-10-12 | 古河電気工業株式会社 | Polarized electrode for capacitor |
| JPS6446913A (en) * | 1987-08-17 | 1989-02-21 | Kanebo Ltd | Electric double layer capacitor |
| JPH02297915A (en) * | 1989-05-11 | 1990-12-10 | Mitsui Petrochem Ind Ltd | Electric double layer capacitor |
-
1990
- 1990-01-26 JP JP2014793A patent/JPH03220713A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6027113A (en) * | 1983-07-22 | 1985-02-12 | 松下電器産業株式会社 | Electric double layer capacitor |
| JPS60201612A (en) * | 1984-03-27 | 1985-10-12 | 古河電気工業株式会社 | Polarized electrode for capacitor |
| JPS6446913A (en) * | 1987-08-17 | 1989-02-21 | Kanebo Ltd | Electric double layer capacitor |
| JPH02297915A (en) * | 1989-05-11 | 1990-12-10 | Mitsui Petrochem Ind Ltd | Electric double layer capacitor |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5603867A (en) * | 1994-09-09 | 1997-02-18 | Nippon Sanso Corporation | Method of production for active carbon electrode for use as electrical double layer condenser and active carbon electrode obtained thereby |
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