JPH0722295A - Production of electric double layer capacitor - Google Patents

Production of electric double layer capacitor

Info

Publication number
JPH0722295A
JPH0722295A JP5147388A JP14738893A JPH0722295A JP H0722295 A JPH0722295 A JP H0722295A JP 5147388 A JP5147388 A JP 5147388A JP 14738893 A JP14738893 A JP 14738893A JP H0722295 A JPH0722295 A JP H0722295A
Authority
JP
Japan
Prior art keywords
double layer
electric double
layer capacitor
negative electrode
positive electrode
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
Application number
JP5147388A
Other languages
Japanese (ja)
Inventor
Kazuo Takada
和夫 高田
Kohei Yamamoto
浩平 山本
Masanori Nakanishi
正典 中西
Mitsuhiro Nakamura
光宏 中村
Tatsuya Yamazaki
龍也 山崎
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.)
FDK Corp
Original Assignee
FDK Corp
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 FDK Corp filed Critical FDK Corp
Priority to JP5147388A priority Critical patent/JPH0722295A/en
Publication of JPH0722295A publication Critical patent/JPH0722295A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • Y02E60/13Energy storage using capacitors

Landscapes

  • Electric Double-Layer Capacitors Or The Like (AREA)

Abstract

PURPOSE:To provide an electric double layer capacitor in which the inner pressure rise and swelling of case due to generation of gas after completion of product is prevented while preventing the capacitance from lowering due to increase of inner resistance by removing the moisture thoroughly from a polarizing electrode prior to sealing of the case. CONSTITUTION:Before an electric double layer capacitor cell is sealed, a positive pole can 1 and a negative pole can 4, each formed with a polarizing electrode 2 therein, are impregnated with an organic electrolyte, i.e., 1M(Et)4NBF4/PC, and opposed to each other through a separator 5. A voltage of 2.0V is then applied between the positive and negative cans 1, 4 from a constant voltage source 7 thus subjecting the residual moisture to electrolysis.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、電気二重層コンデンサ
の製造方法に係わり、特に有機電解液を使用する電気二
重層コンデンサの製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing an electric double layer capacitor, and more particularly to a method for manufacturing an electric double layer capacitor using an organic electrolyte.

【0002】[0002]

【従来の技術】電気二重層コンデンサの代表的な例であ
るコイン形電気二重層コンデンサの製造手順は、概略次
の通りである。まず、活性炭粉末、結着剤等からなる粉
末合剤を偏平円板状のペレットに形成して、一方の電極
端子を構成する偏平容器状の金属製ケース内と他方の電
極端子を構成する金属製カバー内とにそれぞれ配置し
て、有機電解液を含浸させる。次いで、前記金属製カバ
ーを封口ガスケットを介して前記金属製ケースに嵌合さ
せてセパレータを挟んで両ペレットを対峙させ、前記金
属製ケースを金属製カバーにカシメ付けることで完成す
る。
2. Description of the Related Art The procedure for manufacturing a coin type electric double layer capacitor, which is a typical example of an electric double layer capacitor, is roughly as follows. First, a powder mixture made of activated carbon powder, a binder, etc. is formed into flat disk-shaped pellets, and a metal forming a flat container-shaped metal case that constitutes one electrode terminal and a metal that constitutes the other electrode terminal The cover is placed inside the cover and impregnated with the organic electrolyte. Then, the metal cover is fitted into the metal case via a sealing gasket, the separator is sandwiched between the two pellets to face each other, and the metal case is caulked to the metal cover.

【0003】このようなコイン形電気二重層コンデンサ
の製造工程にあっては、金属製ケースに金属製カバーを
カシメ付けて封口する前のいずれかの工程で、有機電解
液を除く各部材を加熱して水分を除去することが一般に
行われている。これは、封口されたケース内に水分が残
っていると、水の分解電圧以上の電圧が印加された場合
に水素ガス及び酸素ガスが発生してケース及びカバーが
膨張するために、ケース及びカバーと電極合剤との接触
状態が悪くなり、内部抵抗が上昇して静電容量が低下す
るという問題が生じるのを防止するためである。
In the manufacturing process of such a coin-type electric double layer capacitor, each member except the organic electrolytic solution is heated in any process before the metal cover is caulked and sealed in the metal case. It is common practice to remove water by doing so. This is because if moisture remains in the sealed case, hydrogen gas and oxygen gas are generated when the voltage higher than the decomposition voltage of water is applied, and the case and cover expand. This is to prevent the problem that the contact state between the electrode mixture and the electrode mixture deteriorates, the internal resistance increases, and the electrostatic capacitance decreases.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、このよ
うな加熱によって水分を除去する方法にあっては、特に
活性炭粉末のように多数の微小孔を有する多孔性物質に
ついて、その微小孔に捕捉されている水分を完全に除去
することは困難であり、前記のケース内の水分残留によ
る静電容量低下という問題を完全に防ぐことができなか
った。
However, in such a method of removing water by heating, a porous substance having a large number of fine pores such as activated carbon powder is trapped in the fine pores. It is difficult to completely remove the water contained therein, and it has not been possible to completely prevent the problem of capacitance reduction due to water remaining in the case.

【0005】本発明は以上の問題点を解決するためにな
されたもので、その目的は、分極性電極中に含まれる水
分をケースの封口前に予め完全に除去することにより、
製品完成後のガス発生に伴う内圧上昇とそれによるケー
スの膨張、及び内部抵抗の上昇による静電容量の低下を
防止することができる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 problems, and an object thereof is to completely remove water contained in a polarizable electrode in advance before sealing the case.
An object of the present invention is to provide a method for manufacturing an electric double layer capacitor which can prevent an increase in internal pressure due to gas generation after product completion, expansion of the case due to it, and a decrease in electrostatic capacitance due to increase in internal resistance.

【0006】[0006]

【課題を解決するための手段】前記目的を達成するため
に、本発明は、活性炭粉末を含む粉末合剤を所定の形状
に成形して得られる電極に有機電解液を含浸させてなる
正極と負極とをセパレータを介して対峙させ、偏平容器
状の金属製ケース及び金属製カバーに収装してなる電気
二重層コンデンサの製造方法において、前記有機電解液
含浸後で前記金属製ケースと金属製カバーとの封口前
に、前記正極と負極との間に所定の電圧を印加して、該
正極及び負極中に含有される水分を電気分解させて除去
することを特徴とする。
To achieve the above object, the present invention provides a positive electrode obtained by impregnating an electrode obtained by molding a powder mixture containing activated carbon powder into a predetermined shape with an organic electrolytic solution. In a method of manufacturing an electric double layer capacitor, which comprises a negative electrode and a negative electrode that face each other through a separator, and is housed in a flat container-shaped metal case and a metal cover, the metal case and the metal case after being impregnated with the organic electrolytic solution. Before sealing with the cover, a predetermined voltage is applied between the positive electrode and the negative electrode to electrolyze and remove water contained in the positive electrode and the negative electrode.

【0007】ここで、前記電気分解は、前記電極に前記
有機電解液を含浸させてから所定時間経過した後に行う
ことが好ましい。
Here, it is preferable that the electrolysis is carried out after a predetermined time has elapsed since the electrodes were impregnated with the organic electrolytic solution.

【0008】さらに、前記有機電解液の含浸は、45〜
70℃の雰囲気温度で行うことが好ましい。
Further, the impregnation with the organic electrolyte is 45 to
It is preferable to carry out at an ambient temperature of 70 ° C.

【0009】さらにまた、前記電気分解の際に前記正極
と負極との間に印加される電圧は、1.8〜2.3V の
範囲に設定されることが好ましい。
Furthermore, the voltage applied between the positive electrode and the negative electrode during the electrolysis is preferably set in the range of 1.8 to 2.3V.

【0010】[0010]

【作用】以上の構成を有する本発明によれば、電気二重
層コンデンサの封口前に、コンデンサの正極と負極との
間に所定の電圧を印加して、該正極及び負極中に含有さ
れる水分を電気分解させて除去するので、従来のような
各部材の加熱による高温乾燥では除去することができな
かった微量な水分も除去することができる。
According to the present invention having the above-described structure, a predetermined voltage is applied between the positive electrode and the negative electrode of the electric double layer capacitor before sealing the electric double layer capacitor so that the moisture contained in the positive electrode and the negative electrode is increased. Since it is electrolyzed and removed, it is possible to remove even a small amount of water that could not be removed by high temperature drying by heating each member as in the related art.

【0011】有機電解液を電極に含浸させてから所定の
時間経過した後に電圧を印加すれば、電極に十分電解液
が含浸された状態で電圧が印加されるので、より完全に
水分の除去を行うことができる。
If a voltage is applied after a predetermined time has passed since the electrode was impregnated with the organic electrolytic solution, the voltage is applied while the electrode is sufficiently impregnated with the electrolytic solution, so that the water content can be more completely removed. It can be carried out.

【0012】また、有機電解液の含浸を45〜70℃の
雰囲気温度で行えば、有機電解液の粘度が低下して含浸
速度が向上するので、作業工程時間が短縮される。
Further, if the impregnation of the organic electrolytic solution is carried out at an ambient temperature of 45 to 70 ° C., the viscosity of the organic electrolytic solution is lowered and the impregnation speed is improved, so that the working process time is shortened.

【0013】さらに、正極と負極との間に印加する電圧
を1.8〜2.3V の範囲とすれば、有機電解液に影響
を与えることなく水分の電気分解のみを行うことができ
る。
Further, when the voltage applied between the positive electrode and the negative electrode is in the range of 1.8 to 2.3 V, only the electrolysis of water can be performed without affecting the organic electrolytic solution.

【0014】[0014]

【実施例】以下、本発明の一実施例につき添付図面を参
照して詳細に説明する。図1はコイン形電気二重層コン
デンサの組立完了状態での断面図である。偏平容器状の
金属製ケースである正極缶1の内底面と、それに対応す
る金属製カバーである負極缶4の内底面とには、それぞ
れステンレス等の金属ネットで形成された集電体3が、
予めスポット溶接等によって固設されている。分極性電
極2は、それぞれ77wt%の活性炭と20wt%のアセチ
レンブラックと3wt%のテフロン結着剤とからなる粉末
合剤を正極缶1及び負極缶4の中に入れ、ペレット状に
缶内成形したものである。分極性電極2が形成された正
極缶1と負極缶4とは、200℃で8時間加熱して、予
め大部分の水分を除去した後、露点が−50℃以下のド
ライボックス中に移して、次の予備電解処理を行った。
An embodiment of the present invention will be described in detail below with reference to the accompanying drawings. FIG. 1 is a cross-sectional view of a coin type electric double layer capacitor in an assembled state. On the inner bottom surface of the positive electrode can 1 which is a flat container-shaped metal case and on the inner bottom surface of the corresponding negative electrode can 4 which is a metal cover, there are collectors 3 each formed of a metal net such as stainless steel. ,
It is fixed in advance by spot welding or the like. For the polarizable electrode 2, a powder mixture comprising 77 wt% of activated carbon, 20 wt% of acetylene black and 3 wt% of Teflon binder was placed in the positive electrode can 1 and the negative electrode can 4 and molded into a can. It was done. The positive electrode can 1 and the negative electrode can 4 on which the polarizable electrode 2 is formed are heated at 200 ° C. for 8 hours to remove most of water in advance, and then transferred to a dry box having a dew point of −50 ° C. or lower. The following preliminary electrolytic treatment was performed.

【0015】すなわち、前記分極性電極2が缶内成形さ
れた正極缶1と負極缶4とにそれぞれ有機電解液として
1M(Et)4 NBF4 /PCを含浸し、図2に示すよ
うに、セパレータ5を介して対峙させ、正負極間に定電
圧電源7によって2.0V の電圧を印加した。
That is, the positive electrode can 1 and the negative electrode can 4 in which the polarizable electrode 2 was molded in the can were impregnated with 1M (Et) 4 NBF 4 / PC as an organic electrolyte, respectively, and as shown in FIG. A voltage of 2.0 V was applied between the positive and negative electrodes by a constant voltage power supply 7 with the separator 5 facing each other.

【0016】前記のように、正極缶1と負極缶4との間
に与えた電圧は、水の分解電圧よりも大きいので、正極
缶1及び負極缶4の分極性電極2では、それぞれ次のよ
うな反応が進行する。
As described above, since the voltage applied between the positive electrode can 1 and the negative electrode can 4 is higher than the decomposition voltage of water, the polarizable electrodes 2 of the positive electrode can 1 and the negative electrode can 4 respectively have the following characteristics. Such a reaction proceeds.

【0017】 正極缶1での反応:4OH- →2H2 O+O2 ↑+4e- … (1) 負極缶4での反応:2H+ +2e- →H2 ↑ … (2) したがって、反応式(1),(2) より、全体の反応は、 4H+ +4OH- →2H2 O+2H2 ↑+O2 ↑ すなわち 2H2 O→2H2 ↑+O2 ↑ となって、分極性電極2中の活性炭に含有されている水
分は、水素ガスと酸素ガスとに分解されて除去される。
Reaction in positive electrode can 1: 4OH → 2H 2 O + O 2 ↑ + 4e (1) Reaction in negative electrode can: 2H + + 2e → H 2 ↑ (2) Therefore, reaction formula (1) , (2), the whole reaction becomes 4H + + 4OH → 2H 2 O + 2H 2 ↑ + O 2 ↑, that is, 2H 2 O → 2H 2 ↑ + O 2 ↑, and is contained in the activated carbon in the polarizable electrode 2. The water content is decomposed into hydrogen gas and oxygen gas and removed.

【0018】また、有機電解液の含浸を行う際の雰囲気
温度としては、45℃から70℃が望ましい。これは、
雰囲気温度が45℃に達しない条件の下では、分極性電
極2に完全に有機電解液が含浸されるまでに長時間を要
するためであり、また、雰囲気温度が70℃を超えてい
る場合には、有機電解液の揮発による静電容量の減少が
生じたり、取扱いが煩雑になるといった問題が生じると
ともに、60℃程度以上に雰囲気温度を上げても含浸速
度の向上が余り認められないためである。
The ambient temperature when impregnating the organic electrolyte is preferably 45 ° C to 70 ° C. this is,
This is because it takes a long time until the polarizable electrode 2 is completely impregnated with the organic electrolyte under the condition that the ambient temperature does not reach 45 ° C. Further, when the ambient temperature exceeds 70 ° C. The problem is that the volatilization of the organic electrolyte causes a decrease in capacitance and the handling becomes complicated, and even if the ambient temperature is raised to about 60 ° C. or more, the impregnation speed is not improved so much. is there.

【0019】以上のように、分極性電極2に有機電解液
を含浸させて電気分解によって水分を除去した後、正極
缶1を負極缶4にカシメ付ければ、本発明のコイン形電
気二重層コンデンサが完成する。
As described above, after the polarizable electrode 2 is impregnated with the organic electrolytic solution to remove water by electrolysis, the positive electrode can 1 is caulked to the negative electrode can 4, and then the coin type electric double layer capacitor of the present invention. Is completed.

【0020】次に、本発明の予備電解処理を行わずに製
造された従来のコイン形電気二重層コンデンサと、前記
本実施例の製造方法にあって、含浸時の雰囲気温度、及
び含浸後予備電解処理を開始するまでの有機電解液への
浸漬時間を変化させて製造した同コンデンサとの性能を
比較した。それぞれのコンデンサの製造上の仕様を表1
に示す。
Next, in the conventional coin-type electric double layer capacitor manufactured without performing the pre-electrolysis treatment of the present invention, and the manufacturing method of this embodiment, the ambient temperature at the time of impregnation and the pre-impregnation preliminary The performance was compared with the capacitor manufactured by changing the immersion time in the organic electrolytic solution until the electrolytic treatment was started. Table 1 shows the manufacturing specifications of each capacitor.
Shown in.

【0021】[0021]

【表1】 まず、それぞれのコイン形電気二重層コンデンサについ
て、2V の電圧を連続して印加した場合の内部抵抗変化
率とセルの厚さの変化率とを測定したところ、図3、図
4に示す結果を得た。これらの図から明らかなように、
予備電解処理による水分除去を行わない従来品では、電
圧印加直後からセルの厚さが急激に増大し、最終的に電
圧印加前に比べてほぼ8%程度厚くなっている。そし
て、それに伴って内部抵抗も急速に増大しており、初期
値の1.5倍程度となった。このことから、セル内部に
おいて残留水分に起因するガス発生が起こり、内圧上昇
が生じていることが推定される。
[Table 1] First, for each coin type electric double layer capacitor, the rate of change in internal resistance and the rate of change in cell thickness when a voltage of 2 V was continuously applied were measured, and the results shown in FIGS. 3 and 4 were obtained. Obtained. As you can see from these figures,
In the conventional product in which the water content is not removed by the preliminary electrolytic treatment, the cell thickness rapidly increases immediately after the voltage is applied, and finally becomes about 8% thicker than before the voltage is applied. Along with that, the internal resistance also increased rapidly, becoming about 1.5 times the initial value. From this, it is presumed that gas generation due to residual moisture occurs inside the cell, causing an increase in internal pressure.

【0022】一方、室温で有機電解液を含浸させて予備
電解処理を実施したグループの本発明品1及び2にあっ
ては、セルの厚さ変化率、内部抵抗の変化率とも従来品
と比較して大幅に抑制されている。特に、電解液に含浸
後予備電解処理を開始するまでに1日放置して電解液を
より十分に含浸させた本発明品2では、本発明品1より
も性能改善効果が高い。
On the other hand, in the products 1 and 2 of the present invention of the group in which the organic electrolytic solution was impregnated at room temperature and the preliminary electrolysis treatment was performed, the cell thickness change rate and the internal resistance change rate were both compared with the conventional product. And is greatly suppressed. In particular, the product 2 of the present invention, which was left for 1 day after impregnation in the electrolytic solution and more fully impregnated with the electrolytic solution before starting the preliminary electrolysis treatment, has a higher performance improving effect than the product 1 of the present invention.

【0023】さらに、60℃で有機電解液を含浸させて
予備電解処理を実施したグループの本発明品3及び4に
あっては、セルの厚さ、内部抵抗のいずれについてもほ
とんど変化が認められなかった。これは、有機電解液の
含浸時の温度を上げたことによって有機電解液の粘度が
低下し、電極合剤へ含浸し易くなったためと考えられ
る。
Furthermore, in the products 3 and 4 of the present invention of the group impregnated with the organic electrolytic solution at 60 ° C. and subjected to the pre-electrolytic treatment, almost no change was observed in both the cell thickness and the internal resistance. There wasn't. It is considered that this is because the viscosity of the organic electrolytic solution was lowered by increasing the temperature during the impregnation of the organic electrolytic solution, and the electrode mixture was easily impregnated.

【0024】[0024]

【発明の効果】以上実施例によって詳細に説明したよう
に、本発明に係る電気二重層コンデンサの製造方法によ
れば、有機電解液含浸後で電気二重層コンデンサの封口
前に、コンデンサの正極と負極との間に所定の電圧を印
加して、該正極及び負極中に含有される水分を電気分解
させて除去するので、従来のような各部材の加熱による
高温乾燥のみでは除去することができなかった微量な水
分も除去することができ、使用時のセル内でのガス発生
に起因するセルの膨張やそれに伴う内部抵抗の増大を防
ぐことができる。
As described above in detail with reference to the embodiments, according to the method for manufacturing an electric double layer capacitor of the present invention, the positive electrode of the capacitor is formed after the impregnation of the organic electrolytic solution and before the sealing of the electric double layer capacitor. Since a predetermined voltage is applied between the negative electrode and the positive electrode and the negative electrode, the water contained in the negative electrode is electrolyzed and removed, so that it can be removed only by high temperature drying by heating each member as in the conventional case. It is possible to remove a small amount of water that has not been present, and it is possible to prevent expansion of the cell and increase in internal resistance due to expansion of the cell due to gas generation in the cell during use.

【0025】また、有機電解液を電極に含浸させてから
所定の時間経過した後に電圧を印加すれば、電極に十分
電解液が含浸された状態で電圧が印加されるので、水分
の除去をより完全に行うことができる。
If a voltage is applied after a predetermined time has passed since the electrode was impregnated with the organic electrolytic solution, the voltage is applied while the electrode is sufficiently impregnated with the electrolytic solution. It can be done completely.

【0026】さらに、有機電解液の含浸を45〜70℃
の雰囲気温度で行えば、有機電解液の粘度が低下して含
浸速度が向上するので、作業工程時間が短縮される。
Further, the impregnation with the organic electrolytic solution is carried out at 45 to 70 ° C.
If the ambient temperature is used, the viscosity of the organic electrolytic solution is lowered and the impregnation rate is improved, so that the working process time is shortened.

【0027】さらにまた、正極と負極との間に印加する
電圧を1.8〜2.3V の範囲とすれば、有機電解液に
影響を与えることなく水分の電気分解のみを行うことが
できる等の種々優れた効果を奏するものである。
Furthermore, if the voltage applied between the positive electrode and the negative electrode is in the range of 1.8 to 2.3 V, only the electrolysis of water can be carried out without affecting the organic electrolytic solution. It has various excellent effects.

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

【図1】コイン形電気二重層コンデンサの断面図であ
る。
FIG. 1 is a cross-sectional view of a coin type electric double layer capacitor.

【図2】本発明の方法に係るコイン形電気二重層コンデ
ンサの予備電解処理工程を示す説明図である。
FIG. 2 is an explanatory view showing a preliminary electrolytic treatment step of the coin-type electric double layer capacitor according to the method of the present invention.

【図3】電気二重層コンデンサのセルへの電圧印加時間
とセルの厚さ変化率との関係を示すグラフである。
FIG. 3 is a graph showing the relationship between the voltage application time to the cell of the electric double layer capacitor and the cell thickness change rate.

【図4】電気二重層コンデンサのセルへの電圧印加時間
と内部抵抗変化率との関係を示すグラフである。
FIG. 4 is a graph showing a relationship between a voltage application time to a cell of an electric double layer capacitor and an internal resistance change rate.

【符号の説明】[Explanation of symbols]

1 正極缶 2 分極性電極 3 集電体 4 負極缶 5 セパレータ 6 封口ガスケット 7 定電圧電源 1 positive electrode can 2 polarizable electrode 3 current collector 4 negative electrode can 5 separator 6 sealing gasket 7 constant voltage power supply

フロントページの続き (72)発明者 中村 光宏 東京都港区新橋5丁目36番11号 富士電気 化学株式会社内 (72)発明者 山崎 龍也 東京都港区新橋5丁目36番11号 富士電気 化学株式会社内Front page continuation (72) Inventor Mitsuhiro Nakamura 5-36-11 Shimbashi, Minato-ku, Tokyo Fuji Electric Chemical Co., Ltd. (72) Inventor Tatsuya Yamazaki 5-36-11 Shinbashi, Minato-ku, Tokyo Fuji Electric Chemical Co., Ltd. In the company

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 活性炭粉末を含む粉末合剤を所定の形状
に成形して得られる電極に有機電解液を含浸させてなる
正極と負極とを備え、該正極と負極とをセパレータを介
して対峙させ、偏平容器状の金属製ケース及び金属製カ
バーに収装してなる電気二重層コンデンサの製造方法に
おいて、前記有機電解液含浸後で前記金属製ケースと金
属製カバーとの封口前に、前記正極と負極との間に所定
の電圧を印加して、該正極及び負極中に含有される水分
を電気分解させて除去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 positive electrode and a negative electrode obtained by impregnating an electrode obtained by molding a powder mixture containing activated carbon powder into a predetermined shape with an organic electrolytic solution, and facing the positive electrode and the negative electrode with a separator interposed therebetween. Then, in a method for manufacturing an electric double layer capacitor which is housed in a flat container-shaped metal case and a metal cover, before the sealing of the metal case and the metal cover after the organic electrolyte impregnation, A method for producing an electric double layer capacitor, which comprises applying a predetermined voltage between a positive electrode and a negative electrode to electrolyze and remove water contained in the positive electrode and the negative electrode.
【請求項2】 前記電極に前記有機電解液を含浸させて
から所定時間経過した後に前記電気分解を行うことを特
徴とする請求項1に記載の電気二重層コンデンサの製造
方法。
2. The method for producing an electric double layer capacitor according to claim 1, wherein the electrolysis is performed after a predetermined time has elapsed after the electrodes were impregnated with the organic electrolytic solution.
【請求項3】 前記有機電解液の含浸を45〜70℃の
雰囲気温度で行うことを特徴とする請求項1に記載の電
気二重層コンデンサの製造方法。
3. The method for manufacturing an electric double layer capacitor according to claim 1, wherein the impregnation with the organic electrolytic solution is performed at an ambient temperature of 45 to 70 ° C.
【請求項4】 前記電気分解の際に前記正極と負極との
間に印加される電圧が1.8〜2.3V であることを特
徴とする請求項1に記載の電気二重層コンデンサの製造
方法。
4. The manufacture of the electric double layer capacitor according to claim 1, wherein the voltage applied between the positive electrode and the negative electrode during the electrolysis is 1.8 to 2.3V. Method.
JP5147388A 1993-06-18 1993-06-18 Production of electric double layer capacitor Pending JPH0722295A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5147388A JPH0722295A (en) 1993-06-18 1993-06-18 Production of electric double layer capacitor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5147388A JPH0722295A (en) 1993-06-18 1993-06-18 Production of electric double layer capacitor

Publications (1)

Publication Number Publication Date
JPH0722295A true JPH0722295A (en) 1995-01-24

Family

ID=15429137

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5147388A Pending JPH0722295A (en) 1993-06-18 1993-06-18 Production of electric double layer capacitor

Country Status (1)

Country Link
JP (1) JPH0722295A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11102843A (en) * 1997-07-28 1999-04-13 Matsushita Electric Ind Co Ltd Electrical double layer capacitor and manufacture thereof
WO2000016354A1 (en) * 1998-09-14 2000-03-23 Asahi Glass Company Ltd. Method for manufacturing large-capacity electric double-layer capacitor
WO2000031764A1 (en) * 1998-11-25 2000-06-02 Ngk Insulators, Ltd. Method for producing electrochemical capacitor
EP1033728A1 (en) * 1999-03-03 2000-09-06 Asahi Glass Co., Ltd. Method for producing an electric double layer capacitor
WO2000075941A1 (en) * 1999-06-04 2000-12-14 Mitsui Chemicals, Inc. Nonaqueous electrolytic solution, electrode, and capacitor containing the same
US6466428B1 (en) * 1998-09-29 2002-10-15 General Electric Company Ultracapacitor having residual water removed under vacuum
KR100578158B1 (en) * 2004-12-23 2006-05-10 비나텍주식회사 The electric double layer capacitors
WO2006098518A1 (en) * 2005-03-18 2006-09-21 Japan Gore-Tex Inc. Production method for electric double layer capacitor
WO2007058422A1 (en) * 2005-11-16 2007-05-24 Vina Technology Co., Ltd. Electric double-layer capacitor

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11102843A (en) * 1997-07-28 1999-04-13 Matsushita Electric Ind Co Ltd Electrical double layer capacitor and manufacture thereof
US6379402B1 (en) * 1998-09-14 2002-04-30 Asahi Glass Company, Limited Method for manufacturing large-capacity electric double-layer capacitor
WO2000016354A1 (en) * 1998-09-14 2000-03-23 Asahi Glass Company Ltd. Method for manufacturing large-capacity electric double-layer capacitor
US6466428B1 (en) * 1998-09-29 2002-10-15 General Electric Company Ultracapacitor having residual water removed under vacuum
WO2000031764A1 (en) * 1998-11-25 2000-06-02 Ngk Insulators, Ltd. Method for producing electrochemical capacitor
US6309428B1 (en) 1998-11-25 2001-10-30 Ngk Insulators, Ltd. Method for producing electrochemical capacitor
EP1033728A1 (en) * 1999-03-03 2000-09-06 Asahi Glass Co., Ltd. Method for producing an electric double layer capacitor
WO2000075941A1 (en) * 1999-06-04 2000-12-14 Mitsui Chemicals, Inc. Nonaqueous electrolytic solution, electrode, and capacitor containing the same
KR100578158B1 (en) * 2004-12-23 2006-05-10 비나텍주식회사 The electric double layer capacitors
US7911767B2 (en) 2004-12-23 2011-03-22 Vina Technology Co., Ltd. Electric double-layer capacitor
WO2006098518A1 (en) * 2005-03-18 2006-09-21 Japan Gore-Tex Inc. Production method for electric double layer capacitor
US7771495B2 (en) 2005-03-18 2010-08-10 Japan Gore-Tex Inc. Production method for electric double layer capacitor
WO2007058422A1 (en) * 2005-11-16 2007-05-24 Vina Technology Co., Ltd. Electric double-layer capacitor

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