JPS6050912A - Method of producing electric double layer capacitor - Google Patents
Method of producing electric double layer capacitorInfo
- Publication number
- JPS6050912A JPS6050912A JP58157172A JP15717283A JPS6050912A JP S6050912 A JPS6050912 A JP S6050912A JP 58157172 A JP58157172 A JP 58157172A JP 15717283 A JP15717283 A JP 15717283A JP S6050912 A JPS6050912 A JP S6050912A
- Authority
- JP
- Japan
- Prior art keywords
- activation
- double layer
- electric double
- cloth
- 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.)
- Granted
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
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は活性炭、特に活性炭繊維を分極性電極として用
いる電気二重層キヤ・ぐシタの製造法に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for producing an electric double layer capacitor using activated carbon, particularly activated carbon fibers, as a polarizable electrode.
(従来例の構成とその問題点)
第1図は活性炭を分極性電極として用いる電気二重層キ
ャパシタの基本構成を示すもので、分極性電極として機
能する活性炭層1及び2と、これらの集電電極として機
能する導電層3及び4とセ・(レータ5とから成る。活
性炭層1及び2には例えばプロピレンカーボネート、テ
トラエチルアンモニウムバークロレートの混合液が電解
液として含浸されている。(Conventional structure and its problems) Figure 1 shows the basic structure of an electric double layer capacitor that uses activated carbon as polarizable electrodes. It consists of conductive layers 3 and 4 that function as electrodes and a separator 5. The activated carbon layers 1 and 2 are impregnated with, for example, a mixed solution of propylene carbonate and tetraethylammonium barchlorate as an electrolyte.
このような基本構成を有する電気二重層キヤ・ぐシタは
、大別すると次の3種類の具体的溝成に分類される。第
1のものは第2図に示すもので、活性炭粉末と弗素樹脂
粉末のような有機バインダとの混合イースト10をアル
ミニウムネット11上に塗布したものであり、セ・やレ
ータ12と共に捲回したものを金属缶13に入れ、ゴム
栓14で密封したものである。捲回したものには前記の
ような電解液が含浸されておシ、15及び16は電極で
ある。第2のものは第3図に示すもので、水溶液系電解
液と活性炭粉末とを混ぜ合わせて得られた粘ちょう性の
ペース)20及び21を用いるものであシ、セパレータ
22を介して絶縁性リング23及び24と導電性エラス
ティック電極25及び26とから構成される。これら第
1.第2の型のものは、いずれも活性炭粉末を分極性電
極として用いておシ、それぞれ耐圧が高いこと、内部抵
抗が低いことなどの特徴を有している。一方これらに対
し、第3の型のものとして本発明者等の発EA(特開昭
55−99714)による活性炭繊維を分極電極として
用いる構成のものがある。Electric double layer capacitors having such a basic configuration can be roughly classified into the following three types of specific groove configurations. The first one is shown in FIG. 2, in which a mixed yeast 10 of activated carbon powder and an organic binder such as fluororesin powder is coated on an aluminum net 11, and the yeast is rolled up with a center layer 12. Items are placed in a metal can 13 and sealed with a rubber stopper 14. The wound material is impregnated with the electrolyte as described above, and 15 and 16 are electrodes. The second method is shown in FIG. 3, and uses viscous paste (20 and 21) obtained by mixing an aqueous electrolyte and activated carbon powder, and is insulated through a separator 22. It is composed of conductive elastic rings 23 and 24 and conductive elastic electrodes 25 and 26. These first. The second type uses activated carbon powder as a polarizable electrode, and each has characteristics such as high breakdown voltage and low internal resistance. On the other hand, as a third type, there is a structure in which activated carbon fibers are used as polarizing electrodes, developed by the present inventors (Japanese Unexamined Patent Publication No. 55-99714).
第4図はこの第3の型のキャノeシタを示すもので、活
性炭布30及び31の表面に金属溶射膜32及び33を
有したものをセ・やレータ34を介して対向させ、ガス
ケット35と金属ケース36及び37とで封口組立てた
ものである。これは、平板コイン型が可能であり、製造
法が容易なことから、マイコンのバックアップ用小型回
路に適したものである。FIG. 4 shows this third type of canopy, in which activated carbon cloths 30 and 31 having metal sprayed films 32 and 33 are placed facing each other with a separator 34 in between, and a gasket 35 and metal cases 36 and 37 are sealed together. This is suitable for a small backup circuit for a microcomputer because it can be shaped like a flat coin and is easy to manufacture.
本発明は上記の第3の型のものに関するものであるが、
まず最初に、分極性型、極として用いる活性炭繊維布の
賦活過程について述べる。The present invention relates to the third type mentioned above,
First, we will describe the activation process of the polarizable activated carbon fiber cloth used as the pole.
活性炭繊維布はレーヨン系、ピンチ系、フェノール系、
PAN系などの繊維を用いて織られた織布を不活性ガ
ス中で炭化し炭素繊維布とし、つづいて適当な賦活ガス
を用いて炭素繊維を活性炭化し、活性炭繊維を得る。Activated carbon fiber cloth is rayon-based, pinch-based, phenolic-based,
A woven fabric woven using PAN-based fibers or the like is carbonized in an inert gas to obtain a carbon fiber cloth, and then the carbon fiber is activated carbonized using an appropriate activating gas to obtain an activated carbon fiber.
第5図は原反織布から炭化、活性炭化の工程を示す概略
図であり、40は原反織布、41は炭素繊維布、42は
活性炭繊維布、(5)は炭化工程、(B)は賦活工程、
(C)は炭化賦活工程を示し、(A) 、 (B)のよ
うに炭化と賦活の2段に分ける過程と、(C)のように
−挙に炭化賦活過程を通って活性炭繊維布を得る過程と
に大別される。ここで用いる適当な賦活条件は、例えば
850℃の高温下炉内にゾロノfンガスの燃焼によって
生成するハイドロカーボンガス、−酸化炭素、二酸化炭
素、水蒸気などの混合ガスを導入し、前述の織布、また
は炭素繊維布を炉内に一定時間保つことである。FIG. 5 is a schematic diagram showing the process of carbonizing and activated carbonizing from the raw woven fabric, 40 is the raw woven fabric, 41 is the carbon fiber cloth, 42 is the activated carbon fiber cloth, (5) is the carbonization process, (B ) is the activation process,
(C) shows the carbonization activation process, in which the activated carbon fiber cloth is produced through a two-step process of carbonization and activation as shown in (A) and (B), and a carbonization and activation process as shown in (C). It is broadly divided into the process of obtaining. Appropriate activation conditions used here include, for example, introducing a mixed gas of hydrocarbon gas, carbon oxide, carbon dioxide, water vapor, etc. produced by combustion of carbon gas into a high-temperature furnace at 850°C, and then , or keeping the carbon fiber cloth in the furnace for a certain period of time.
第6図は賦活装置の一例を示すもので、高温に保持され
た炉50の中に炭化または炭化賦活される織布51が収
容され、この炉50の導入口52に賦活ガス発生装置5
3からの賦活ガスが導入される。FIG. 6 shows an example of an activation device, in which a woven fabric 51 to be carbonized or carbonized is housed in a furnace 50 maintained at a high temperature, and an activation gas generator 5 is inserted into an inlet 52 of the furnace 50.
Activation gas from No. 3 is introduced.
賦活反応とは(1)式で示すように、炭素繊維から酸化
反応によって徐々に炭素が抜かれ、繊維表面に数X〜数
10Xの細孔をあけるものである。As shown in equation (1), the activation reaction is a process in which carbon is gradually removed from the carbon fiber by an oxidation reaction, creating pores of several X to several 10 times in size on the fiber surface.
cn+202→Cn−1十Co↑ ・・・・・・(1)
(1)式の酸化反応が均一に速やかに進行するためには
、賦活ガスと繊維との接触が系全体にわたって均一でな
ければならず、また、賦活ガスが充分量供給されなけれ
ばならない。cn+202→Cn-10Co↑ ・・・・・・(1)
In order for the oxidation reaction of formula (1) to proceed uniformly and quickly, contact between the activation gas and the fibers must be uniform throughout the system, and a sufficient amount of the activation gas must be supplied.
(1)式からもわかるように、賦活反応の進行度合は繊
維量の変化によっても知ることができる。As can be seen from equation (1), the degree of progress of the activation reaction can also be determined by changes in the amount of fiber.
第7図は従来の賦活法による3種類の織布の賦活時間(
横軸)と重量減(縦軸)との関係を示すものである。こ
こで、(A) 、 (B)及び(C)は目付がそれぞれ
100.!9r/m2.300F/m2及び500gr
/m2の平織りで、フェノール系ノRラック繊維使用の
3種類の織布を用いた場合のものである。この図から、
賦活時間が進むに従っていずれの布も徐々に重量が減少
していくことが明かであるが、特に、目付の小さい(4
)の布の重量減が大きく、目付の大きい(C)の布の重
量減が小さいことがわかる。たたし、ここで用いた賦活
条件は、800℃炉中、賦活ガスとしてプロ・ぐン燃焼
ガスを用いた。この重量減速度の差は、第8図のように
説明される。Figure 7 shows the activation time (
It shows the relationship between weight loss (horizontal axis) and weight loss (vertical axis). Here, (A), (B) and (C) each have a basis weight of 100. ! 9r/m2.300F/m2 and 500gr
/m2 plain weave using three types of woven fabrics using phenolic Norac fibers. From this figure,
It is clear that the weight of all fabrics gradually decreases as the activation time progresses, but in particular, the weight of fabrics with a small basis weight (4
It can be seen that the weight loss of the fabric (C), which has a large basis weight, is large, and the weight loss of the fabric (C), which has a large basis weight, is small. However, the activation conditions used here were a furnace at 800° C. and Pro-Gun combustion gas used as the activation gas. This difference in weight deceleration can be explained as shown in FIG.
第8図は原反布の厚さと賦活反応の進行度合との関係を
示す模式図である。即ち、第8図(a)に示す目付のl
」・さい布では、単位面面積当シの繊維の数が少なく、
布の厚さも薄いため短時間で賦活ガスが布全体と均一に
完全に反応し賦活が完了する。FIG. 8 is a schematic diagram showing the relationship between the thickness of the original fabric and the degree of progress of the activation reaction. That is, l of the basis weight shown in FIG. 8(a)
”・The number of fibers per unit surface area of sai cloth is small,
Because the fabric is thin, the activation gas reacts uniformly and completely with the entire fabric in a short time, completing activation.
なお図中、破線部が賦活完了部分である。ところが、第
8図(b)のように単位布面積の大きな織布では、単位
面積あたシの繊維の本数も多く厚さも厚いため、(a)
と比較した場合、賦活反応の進行がおそく々る。このよ
うな賦活のされ方の差をなくすために1例えば目付の大
きな布では長時間賦活をしたシ、賦活ガス量を増すなど
の方法がある。しかし々から、総賦活時間を増すと、布
の表面部の賦活が進みすぎ面全体の強度が弱くなる。ま
た賦活ガスを増す方法は優れた方法であるが実際上送入
できるガス量には限度があシ、濃度を精度よく制御する
ことは難しい。In addition, in the figure, the broken line part is the part where activation is completed. However, in a woven fabric with a large unit fabric area as shown in Figure 8 (b), the number of fibers per unit area is large and the thickness is thick, so (a)
The activation reaction progresses slowly when compared to In order to eliminate such differences in the way the fabric is activated, there are methods such as activating for a long time for fabrics with a large basis weight or increasing the amount of activating gas. However, if the total activation time is increased, the activation of the surface portion of the cloth progresses too much and the strength of the entire surface weakens. Furthermore, although increasing the amount of activating gas is an excellent method, there is a limit to the amount of gas that can actually be fed, and it is difficult to control the concentration with precision.
(発明の目的)
本発明は、上記のような問題点を解決しようとするもの
で、用いる活性炭繊維布の賦活のばらつきをなくシ、短
時間で均一で優れた細孔を有する活性炭布を得ることを
可能にした賦活方法に関し、この活性炭布を用いた高性
能電気二重層キャパシタを提供することを目的とする。(Purpose of the Invention) The present invention aims to solve the above-mentioned problems by eliminating variations in the activation of the activated carbon fiber cloth used and obtaining an activated carbon cloth having uniform and excellent pores in a short time. The purpose of this invention is to provide a high-performance electric double layer capacitor using this activated carbon cloth.
(発明の構成)
本発明は、水を含浸した布を高温化ガス雰囲気中に保持
して炭化賦活し、′得られた活性炭布を分極性電極とし
て用いるようにした電気二重層キャパシタの製造法であ
り、この方法によれば布の中に予め含浸された水分子が
蒸発して賦活ガスとして作用するとともに、繊維の水に
対するぬれが好寸しい状態になっているために後から導
入される賦活ガスと繊維との接触酸化反応がよシスムー
スに進む。とのために単位布面積当たりの目付量の大き
な、厚さの厚い布を賦活する場合も、従来の方法に比し
て賦活が面全体に均一に速かに進行し、短時間で優れた
活性炭布を得ることができる。そしてこの活性炭布を用
いて、容積効率の優れた大容量電気二重層キヤ・ぐシタ
を提供することができる。(Structure of the Invention) The present invention provides a method for manufacturing an electric double layer capacitor in which a water-impregnated cloth is held in a high-temperature gas atmosphere to activate carbonization, and the obtained activated carbon cloth is used as a polarizable electrode. According to this method, water molecules that have been impregnated into the cloth in advance evaporate and act as an activating gas, and since the fibers are in a suitable state for wetting with water, they are introduced later. The catalytic oxidation reaction between the activation gas and the fibers proceeds smoothly. Even when activating thick fabrics with a large basis weight per unit fabric area for purposes of Activated carbon cloth can be obtained. Using this activated carbon cloth, it is possible to provide a large capacity electric double layer capacitor with excellent volumetric efficiency.
(実施例の説明)
本発明の大きな特徴は賦活に先立って被賦活繊維布に水
を含浸することである。この工程により、■含浸された
水が賦活時に気化し賦活ガスとして作用する。■予め繊
維が水に浸漬されているため、繊維の水蒸気ガスに対す
るぬれがよく、賦活ガスとの接触酸化反応がスムースに
進む。など優れた結果が得られる。(Description of Examples) A major feature of the present invention is that the fiber cloth to be activated is impregnated with water prior to activation. Through this process, (1) the impregnated water is vaporized during activation and acts as an activation gas. ■Since the fibers are immersed in water in advance, the fibers are well wetted by water vapor gas, and the catalytic oxidation reaction with the activating gas proceeds smoothly. Excellent results can be obtained.
第9図は本発明の詳細な説明するだめの特性図で、10
crnX 10cmz厚さ1喘、目付2001 r/m
2のノボラック繊維布の賦活時間と重量減との関係を示
すもので、賦活温度は800℃、賦活ガスはプロ・ぐン
燃焼ガスである。図中(ト)は本発明のように予め水を
含浸した布を賦活した時のデータ、(B)は、従来法に
よるものである。この図のように、(4)が20分間で
約90係の減量を示すのに対し、(B)は約倍の40分
間で(A)と同等の重量減を示す。FIG. 9 is a characteristic diagram for detailed explanation of the present invention.
crnX 10cmz thickness 1mm, basis weight 2001r/m
This figure shows the relationship between the activation time and weight loss of the novolac fiber cloth in No. 2. The activation temperature is 800°C, and the activation gas is Pro-Gun combustion gas. In the figure (G) is data obtained when a cloth pre-impregnated with water is activated as in the present invention, and (B) is data obtained by a conventional method. As shown in this figure, (4) shows a weight loss of about 90 times in 20 minutes, while (B) shows a weight loss equivalent to (A) in about twice as much, 40 minutes.
このことは、本発明による賦活進行速度が約倍のスピー
ドで進んでいることを示すものである。This indicates that the activation progress rate according to the present invention is approximately twice as fast.
第10図は本発明による賦活法を用いた時の賦活時間と
重量減との関係を示すもので、前記第7図に示した従来
の賦活法に対応するものである。FIG. 10 shows the relationship between activation time and weight loss when the activation method according to the present invention is used, and corresponds to the conventional activation method shown in FIG. 7 above.
(A) 、 (B)及び(C)は目付がそれぞれ100
11r 7m2゜300gr/m”及び5001/r/
m2の布を用いた場合のもので、いずれも賦活前に布に
水を含浸したものであるが、第7図の結果に比していず
れも同一目付で重量減が1.5倍〜3倍速かに見られ、
目付の大きな布はどこの効果が大きい。なお水の含浸時
間は繊維布の目付にもよるが長いほど効果的である。ま
た、含浸する水にアルカリ、アルカリ土類金属イオン、
などを注入しておくと、これらのイオンの触媒作用によ
り賦活により生成する細孔の径を制御できる。(A), (B) and (C) each have a basis weight of 100
11r 7m2゜300gr/m” and 5001/r/
These are the results when a cloth of m2 was used, and in both cases the cloth was impregnated with water before activation, but compared to the results in Figure 7, the weight reduction was 1.5 to 3 times with the same basis weight. It seems to be twice as fast,
The effect of cloth with a large basis weight is significant. Note that the longer the water impregnation time, the more effective it is, although it depends on the basis weight of the fiber cloth. In addition, alkali, alkaline earth metal ions,
By injecting ions, etc., the diameter of the pores generated by activation can be controlled by the catalytic action of these ions.
次に本発明の具体的々実施例を示す。Next, specific examples of the present invention will be shown.
実施例−1
目付100 gr 7m2及び500,9r 7m2の
ノボラック系フェノール繊維により構成される布■及び
■を蒸留水に10分間浸漬する。水より引上げ5分間風
乾後、800℃、10分間炉内に保持する。この時炉内
には(イ)プロ・ぐン燃焼ガス、(ロ)30III+l
lHg の水蒸気を含む窒素がス、を導入する。賦活終
了後、布の片面にアルミニウムプラズマ溶射膜を形成し
、直径10岨に打ぬいた布2枚と、セ・やレータと、プ
ロピレンカービネートにテトラエチルアンモニウム・ぐ
−クロレート’を加えた混合液を電解液として用い、第
4図に示すようにケースを用いてコイン型キヤ・ぐシタ
を完成する。第1表に本実施例のキャパシタの特性を掲
げる。同表に、本実施例と同じだが、賦活前に水に含浸
する工程を行なわない従来の方法によシつくられた活性
炭布を用いたキャパシタの特性も併記する。Example-1 Cloths (1) and (2) made of novolac phenolic fibers with a basis weight of 100 gr 7 m2 and 500.9 r 7 m2 are immersed in distilled water for 10 minutes. After being pulled out of the water and air-dried for 5 minutes, it was kept in a furnace at 800°C for 10 minutes. At this time, inside the furnace is (a) Pro Gun combustion gas, (b) 30III+l
A nitrogen gas containing 1 Hg of water vapor is introduced. After activation, an aluminum plasma sprayed film was formed on one side of the cloth, and two pieces of cloth were punched out to a diameter of 10 mm, a separator, and a mixture of propylene carbinate and tetraethylammonium glucorate. As an electrolyte, a coin-shaped cashier is completed using a case as shown in Figure 4. Table 1 lists the characteristics of the capacitor of this example. The same table also shows the characteristics of a capacitor using activated carbon cloth made by the conventional method, which is the same as this example, but without the step of impregnating it with water before activation.
第 1 表
実施例−2
目付5009r /m2の7ビラツク系フエノール繊維
によシ構成される布’11wt%の硝酸カルシウム水溶
液に30分間浸漬する。水よ逆引上げ後10分間風乾後
、800℃、30分間炉内に保持する。Table 1 Example-2 A cloth composed of 7-virion phenol fibers with a basis weight of 5009 r/m2 was immersed in an 11 wt % calcium nitrate aqueous solution for 30 minutes. After being pulled up from water and air-dried for 10 minutes, it was kept in a furnace at 800°C for 30 minutes.
この時炉内には、プロパン燃焼ガスを導入する。At this time, propane combustion gas is introduced into the furnace.
賦活終了後10分間水洗し、乾燥後、布の片面にアルミ
ニウムプラズマ溶射膜を形成し、直径10叫に打ち抜く
。このようにしてできた面電極2枚と、セパレータと、
iowt%の硫酸水溶液を電解液として用い、第4図に
示すようにケースを用いてコイン型キヤ・ぐシタを完成
する。第2表は、本実施例のキャパシタ特性であり、同
表に本実施例と同じだが、賦活前に硝酸カルシウム水溶
液に浸漬する工程を行なわない従来の方法によりつくら
れた活性炭布を用いたキヤ・ぐシタ特性も併記する。After activation, the cloth is washed with water for 10 minutes, dried, an aluminum plasma sprayed film is formed on one side of the cloth, and punched out to a diameter of 10 mm. The two surface electrodes made in this way and the separator,
Using an iowt% sulfuric acid aqueous solution as an electrolyte, a coin-shaped cashier is completed using a case as shown in FIG. Table 2 shows the characteristics of the capacitor of this example, and the same table shows the characteristics of the capacitor using the activated carbon cloth made by the conventional method, which is the same as this example, but without the step of immersing it in an aqueous calcium nitrate solution before activation.・Gushita characteristics are also listed.
第 2 表
(発明の効果)
以上説明したように本発明によれば、予め被賦活繊維に
含浸された水のために賦活が均一に速かに進行し、高強
度、最適細孔径を有する活性炭布が得られる。この活性
炭布を分極性電極として用いるキャパシタは、容量の容
積効率、温度特性に優れ、工業的価値は非常に大なるも
のである。Table 2 (Effects of the Invention) As explained above, according to the present invention, activation proceeds uniformly and quickly due to the water impregnated into the activated fibers in advance, and activated carbon has high strength and an optimum pore diameter. Cloth is obtained. A capacitor using this activated carbon cloth as a polarizable electrode has excellent volumetric efficiency and temperature characteristics, and has great industrial value.
第1図は活性炭を分極性電極として用いる電気二重層キ
ヤ・やシタの基本構成を示す図、第2図、第3図及び第
4図は従来の電気二重層キャパシタの具体的構成例を示
す図、第5図は原反織布から炭化、活性炭化の工程を示
す概略図、第6図は賦活装置の一例を示す図、第7図は
従来の賦活法による3種類の織布の賦活時間と重量減と
の関係を示す図、第8図は原反布の厚さと賦活反応の進
行度合との関係を示す模式図、第9図は本発明の詳細な
説明するだめの特性図、第10図は本発明による賦活法
を用いた時の賦活時間と重量減との関係を示す図である
。
1.2・・・活性炭層、3・4・・・導電層、5・・・
セ/ぐレータ、10・・・混合ペースト、11・・・ア
ルミニウムネット、12・・・セパレータ、13・・・
金属缶、14・・・コゝム栓、15.16・・・電極、
20.21・・・被−スト、22・・・セノぐし〜り、
23.24・・・絶縁性リング、25.26・・・エラ
スティック電極、30・・・活性炭布、32.33・・
・金属溶射膜、34・・・セパレータ、35・・・ガス
ケツ)、36゜37・・・金属ケース、4o・・・原反
織布、41・・・炭素繊維、42・・・活性炭繊維布、
50・・・炉、51・・・織布、52・・・導入口、5
3・・・賦活ガス発生装置。
特許出願人 松下電器産業株式会社
d゛
代 理 人 星 野 恒 司5・1
1−イ
第1図
第2図
第3図
34 33 31 J’/
第5図
第6図
’+1”1
第7図
第8図Figure 1 shows the basic configuration of an electric double layer capacitor using activated carbon as a polarizable electrode, and Figures 2, 3, and 4 show specific configuration examples of conventional electric double layer capacitors. Figure 5 is a schematic diagram showing the process of carbonization and activated carbonization from raw woven fabric, Figure 6 is a diagram showing an example of an activation device, and Figure 7 is the activation of three types of woven fabrics using the conventional activation method. A diagram showing the relationship between time and weight loss, FIG. 8 is a schematic diagram showing the relationship between the thickness of the raw fabric and the degree of progress of the activation reaction, and FIG. 9 is a characteristic diagram for detailed explanation of the present invention. FIG. 10 is a diagram showing the relationship between activation time and weight loss when using the activation method according to the present invention. 1.2... activated carbon layer, 3.4... conductive layer, 5...
separator, 10...mixed paste, 11...aluminum net, 12...separator, 13...
Metal can, 14... Comb stopper, 15.16... Electrode,
20.21...Stowed, 22...Senogushiri,
23.24... Insulating ring, 25.26... Elastic electrode, 30... Activated carbon cloth, 32.33...
・Metal sprayed film, 34... Separator, 35... Gasket), 36° 37... Metal case, 4o... Original fabric fabric, 41... Carbon fiber, 42... Activated carbon fiber cloth ,
50...furnace, 51...woven fabric, 52...inlet, 5
3... Activating gas generator. Patent Applicant Matsushita Electric Industrial Co., Ltd. Managing Director Tsuneji Hoshino 5.1 1-I Figure 1 Figure 2 Figure 3 34 33 31 J'/ Figure 5 Figure 6'+1"1 Figure 7 Figure 8
Claims (5)
て炭化賦活し、得られた活性炭布を分極性電極として用
いることを特徴とする電気二重層キャパシタの製造法。(1) A method for producing an electric double layer capacitor, characterized in that a water-impregnated cloth is held in a gas atmosphere at high temperature to activate carbonization, and the obtained activated carbon cloth is used as a polarizable electrode.
ンを含むものであ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ャパシタの製造法。(2) The method for manufacturing an electric double layer capacitor according to claim (1), wherein the water contains ions of alkali metals and alkaline earth metals.
特徴とする特許請求の範囲第(1)項記載の電気二重層
キャパシタの製造法。(3) The method for manufacturing an electric double layer capacitor according to claim (1), wherein the gas contains at least nitrogen and water vapor.
構成材料として含む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ャパシタの製造法。(4) The method for manufacturing an electric double layer capacitor according to claim (1), wherein the cloth contains at least phenolic novolac fiber as a constituent material.
とを特徴とする特許請求の範囲第(1)項記載の電気二
重層キャパシタの製造法。(5) The method for manufacturing an electric double layer capacitor according to claim (1), wherein the water vapor partial pressure of the gas is 20 mmH, 9 or more.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58157172A JPS6050912A (en) | 1983-08-30 | 1983-08-30 | Method of producing electric double layer capacitor |
EP84305362A EP0134706B1 (en) | 1983-08-08 | 1984-08-07 | Electric double layer capacitor and method for producing the same |
US06/638,656 US4597028A (en) | 1983-08-08 | 1984-08-07 | Electric double layer capacitor and method for producing the same |
DE8484305362T DE3484812D1 (en) | 1983-08-08 | 1984-08-07 | ELECTRIC DOUBLE LAYER CAPACITOR AND METHOD FOR PRODUCING THE SAME. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58157172A JPS6050912A (en) | 1983-08-30 | 1983-08-30 | Method of producing electric double layer capacitor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6050912A true JPS6050912A (en) | 1985-03-22 |
JPH0449248B2 JPH0449248B2 (en) | 1992-08-11 |
Family
ID=15643760
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58157172A Granted JPS6050912A (en) | 1983-08-08 | 1983-08-30 | Method of producing electric double layer capacitor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6050912A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2018048063A (en) * | 2016-09-01 | 2018-03-29 | ファラッドパワー,インコーポレイテッド | Manufacturing method of chemical active carbon |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4971217A (en) * | 1972-11-15 | 1974-07-10 | ||
JPS557583A (en) * | 1978-07-03 | 1980-01-19 | Nippon Kainoole Kk | Manufacture of activated carbon fiber or activated carbon fiber structure |
-
1983
- 1983-08-30 JP JP58157172A patent/JPS6050912A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4971217A (en) * | 1972-11-15 | 1974-07-10 | ||
JPS557583A (en) * | 1978-07-03 | 1980-01-19 | Nippon Kainoole Kk | Manufacture of activated carbon fiber or activated carbon fiber structure |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2018048063A (en) * | 2016-09-01 | 2018-03-29 | ファラッドパワー,インコーポレイテッド | Manufacturing method of chemical active carbon |
Also Published As
Publication number | Publication date |
---|---|
JPH0449248B2 (en) | 1992-08-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4597028A (en) | Electric double layer capacitor and method for producing the same | |
JPS6015138B2 (en) | electric double layer capacitor | |
EP0134706B1 (en) | Electric double layer capacitor and method for producing the same | |
KR102585145B1 (en) | Surface-activated carbon fiber electrode, manufacturing method of the same, flexible fibrous supercapacitor comprising the same and manufacturing method of flexible fibrous supercapacitor | |
JPH09320906A (en) | Activated carbon for electric double layer capacitor electrode, its manufacture, and electric double layer capacitor electrode | |
CN110937589B (en) | High internal phase emulsion template method for preparing and regulating high-nitrogen-doped porous carbon | |
JP3165478U (en) | Battery electrode | |
JPH07161588A (en) | Polarizing electrode for electric double-layer capacitor, its manufacture and electric double-layer capacitor using polarizing electrode described above | |
JPH0558253B2 (en) | ||
JPS60263420A (en) | Energy storing device | |
JPS6050912A (en) | Method of producing electric double layer capacitor | |
JPS59105312A (en) | Wet type electric double layer capacitor | |
RU2223911C1 (en) | Method for production of activated carbon for electrical engineering purposes | |
JPH05239720A (en) | Electrode material for metal-halogen secondary battery | |
KR100453922B1 (en) | Spherical active carbon and methods for preparing the same, and electric double layer capacitor using the same | |
JPS6378513A (en) | Electric double-layer capacitor | |
KR100715873B1 (en) | Increasing method of meso porous amount activated carbon for supercapacitor electrode | |
KR100715872B1 (en) | Preparation method of meso porous activated carbon by KOH for supercapacitor electrode | |
JPS6043810A (en) | Method of producing electric double layer capacitor | |
JPH011221A (en) | Method for manufacturing polarizable electrodes | |
JPH0795503B2 (en) | Method of manufacturing polarizable electrodes | |
JPS61187322A (en) | Polarizing electrode | |
JP2001044082A (en) | Production of electric double-layer capacitor | |
JP2006169058A (en) | Method of manufacturing porous vitreous carbon sheet and polarizing electrode material for electric double layer capacitor comprising the sheet | |
JPS6290916A (en) | Electrode for electric double-layer capacitor |