JPH08162375A - Electrical double-layer capacitor and manufacture of polarizable electrode used therefor - Google Patents
Electrical double-layer capacitor and manufacture of polarizable electrode used thereforInfo
- Publication number
- JPH08162375A JPH08162375A JP22343795A JP22343795A JPH08162375A JP H08162375 A JPH08162375 A JP H08162375A JP 22343795 A JP22343795 A JP 22343795A JP 22343795 A JP22343795 A JP 22343795A JP H08162375 A JPH08162375 A JP H08162375A
- Authority
- JP
- Japan
- Prior art keywords
- double layer
- layer capacitor
- electric double
- polarizable electrode
- activated carbon
- 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
- 239000003990 capacitor Substances 0.000 title claims abstract description 38
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 76
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims abstract description 72
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 29
- 239000008151 electrolyte solution Substances 0.000 claims abstract description 16
- 239000003960 organic solvent Substances 0.000 claims abstract description 13
- 229920005989 resin Polymers 0.000 claims abstract description 10
- 239000011347 resin Substances 0.000 claims abstract description 10
- 239000005011 phenolic resin Substances 0.000 claims abstract description 9
- 239000007849 furan resin Substances 0.000 claims abstract description 8
- 229920006350 polyacrylonitrile resin Polymers 0.000 claims abstract description 8
- 230000004913 activation Effects 0.000 claims description 29
- 238000000034 method Methods 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 7
- 230000003213 activating effect Effects 0.000 claims description 5
- 238000010000 carbonizing Methods 0.000 claims description 4
- 239000011230 binding agent Substances 0.000 claims description 3
- 239000004020 conductor Substances 0.000 claims description 3
- 239000003792 electrolyte Substances 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 150000004714 phosphonium salts Chemical group 0.000 claims description 2
- 150000003242 quaternary ammonium salts Chemical class 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 229920001568 phenolic resin Polymers 0.000 abstract description 4
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 abstract description 3
- 238000001994 activation Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 238000003763 carbonization Methods 0.000 description 6
- 230000007423 decrease Effects 0.000 description 5
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 3
- 239000002006 petroleum coke Substances 0.000 description 3
- -1 phosphonium ion Chemical class 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- ZZXUZKXVROWEIF-UHFFFAOYSA-N 1,2-butylene carbonate Chemical compound CCC1COC(=O)O1 ZZXUZKXVROWEIF-UHFFFAOYSA-N 0.000 description 2
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 125000000524 functional group Chemical group 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical compound O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 description 2
- 235000005074 zinc chloride Nutrition 0.000 description 2
- 239000011592 zinc chloride Substances 0.000 description 2
- 229910020366 ClO 4 Inorganic materials 0.000 description 1
- 235000013162 Cocos nucifera Nutrition 0.000 description 1
- 244000060011 Cocos nucifera Species 0.000 description 1
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- JBTWLSYIZRCDFO-UHFFFAOYSA-N ethyl methyl carbonate Chemical compound CCOC(=O)OC JBTWLSYIZRCDFO-UHFFFAOYSA-N 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- HDNHWROHHSBKJG-UHFFFAOYSA-N formaldehyde;furan-2-ylmethanol Chemical compound O=C.OCC1=CC=CO1 HDNHWROHHSBKJG-UHFFFAOYSA-N 0.000 description 1
- 150000002596 lactones Chemical class 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 230000001590 oxidative effect Effects 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
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical compound [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 description 1
- 229910001950 potassium oxide Inorganic materials 0.000 description 1
- 125000001453 quaternary ammonium group Chemical group 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/30—Electrodes characterised by their material
- H01G11/32—Carbon-based
-
- 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
- Engineering & Computer Science (AREA)
- Power Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Electric Double-Layer Capacitors Or The Like (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、静電容量が大き
く、高耐電圧を有する電気二重層コンデンサと電気二重
層コンデンサ用分極性電極の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electric double layer capacitor having a large electrostatic capacity and a high withstand voltage, and a method for manufacturing a polarizable electrode for an electric double layer capacitor.
【0002】[0002]
【従来の技術】電気二重層コンデンサを小型で軽量なも
のとするには、コンデンサに蓄えうる単位体積当たりの
蓄電エネルギーの量(以下、エネルギー密度という)を
高める必要がある。コンデンサの蓄電エネルギーは、コ
ンデンサの静電容量に比例し、かつ印加電圧(耐電圧又
は使用電圧)の2乗に比例する。したがってコンデンサ
のエネルギー密度を大きくするには、単位体積当たりの
静電容量を大きくし、かつ高耐電圧のものとすればよ
い。2. Description of the Related Art In order to make an electric double layer capacitor small and lightweight, it is necessary to increase the amount of stored energy per unit volume (hereinafter referred to as energy density) that can be stored in the capacitor. The energy stored in the capacitor is proportional to the electrostatic capacity of the capacitor and is also proportional to the square of the applied voltage (withstand voltage or working voltage). Therefore, in order to increase the energy density of the capacitor, the capacitance per unit volume should be increased and the capacitor should have a high withstand voltage.
【0003】従来、静電容量の大きい電気二重層コンデ
ンサを得るため、分極性電極には高比表面積の活性炭が
用いられてきた。高比表面積の活性炭としては、炭素材
を水蒸気を用いる水蒸気賦活処理法や塩化亜鉛などを用
いる薬品賦活処理法によって賦活処理した活性炭が主に
使用されている。しかし、これらの活性炭は分極性電極
としたときの単位体積当たりの静電容量密度と、高電圧
印加時の性能劣化が速い点で、将来有望とされている、
高エネルギー密度を必要とする用途には充分なものでな
い。Conventionally, in order to obtain an electric double layer capacitor having a large electrostatic capacity, activated carbon having a high specific surface area has been used for the polarizable electrode. As the activated carbon having a high specific surface area, activated carbon in which a carbon material is activated by a steam activation treatment method using steam or a chemical activation treatment method using zinc chloride or the like is mainly used. However, these activated carbons are promising in the future because of the capacitance density per unit volume when used as a polarizable electrode and the rapid performance deterioration when a high voltage is applied,
It is not sufficient for applications that require high energy density.
【0004】ところで、特開昭63−78513には、
溶融水酸化カリウムを用いる高温賦活処理法によって石
油コークスを賦活処理した高比表面積の活性炭と有機溶
媒系電解液とを用いる電気二重層コンデンサが提案され
ている。この活性炭は比表面積が非常に大きいことによ
って従来の電気二重層コンデンサよりエネルギー密度を
高くできる点で有利である。しかし、その耐電圧はせい
ぜい2.8V前後であるため、耐電圧を向上させてさら
にエネルギー密度を向上させることが期待される。By the way, Japanese Patent Laid-Open No. 63-78513 discloses that
There has been proposed an electric double layer capacitor using activated carbon having a high specific surface area, which is obtained by activating petroleum coke by a high temperature activation treatment method using molten potassium hydroxide, and an organic solvent-based electrolytic solution. This activated carbon is advantageous in that it can have a higher energy density than conventional electric double layer capacitors because of its very large specific surface area. However, since the withstand voltage is about 2.8 V at most, it is expected that the withstand voltage is improved and the energy density is further improved.
【0005】[0005]
【発明が解決しようとする課題】本発明は、電気二重層
コンデンサの従来技術における上記課題を解決し、耐電
圧が高く、高電圧印加が可能なさらに高エネルギー密度
を有する電気二重層コンデンサの提供を目的とする。DISCLOSURE OF THE INVENTION The present invention solves the above problems in the prior art of electric double layer capacitors, and provides an electric double layer capacitor having a high withstand voltage and a high energy density capable of applying a high voltage. With the goal.
【0006】[0006]
【課題を解決するための手段】本発明の電気二重層コン
デンサは、分極性電極と、該分極性電極の表面に電気二
重層を形成する電解液とを有する電気二重層コンデンサ
において、該分極性電極が、フェノール樹脂、フラン樹
脂及びポリアクリロニトリル樹脂から選ばれる一種以上
の樹脂を原料とする炭素材を溶融状態の水酸化カリウム
を用いる賦活処理法で賦活してなる活性炭を主体とする
ものであり、該電解液が有機溶媒系電解液であることを
特徴とする。The electric double layer capacitor of the present invention is an electric double layer capacitor having a polarizable electrode and an electrolytic solution for forming an electric double layer on the surface of the polarizable electrode. The electrode is mainly composed of activated carbon obtained by activating a carbon material made of one or more resins selected from phenol resin, furan resin and polyacrylonitrile resin by an activation treatment method using potassium hydroxide in a molten state. The electrolytic solution is an organic solvent-based electrolytic solution.
【0007】また、本発明の電気二重層コンデンサ用分
極性電極の製造方法は、フェノール樹脂、フラン樹脂及
びポリアクリロニトリル樹脂から選ばれる一種以上の樹
脂を炭化して炭素材とし、該炭素材に水酸化カリウムを
加えた混合物を600〜1000℃に加熱することによ
って該炭素材を溶融状態の水酸化カリウムの存在下で活
性炭とし、該活性炭の粉末に結合材と導電材を加えた混
合物を集電体に固定して分極性電極とすることを特徴と
する。The method for producing a polarizable electrode for an electric double layer capacitor according to the present invention comprises carbonizing one or more resins selected from phenolic resins, furan resins and polyacrylonitrile resins into carbonaceous materials, and watering the carbonaceous materials. By heating the mixture to which potassium oxide is added to 600 to 1000 ° C., the carbon material is activated carbon in the presence of potassium hydroxide in a molten state, and the mixture of the powder of the activated carbon and the binder and the conductive material is collected. It is characterized by being fixed to the body and used as a polarizable electrode.
【0008】本発明の電気二重層コンデンサでは、分極
性電極に特定の樹脂を原料とする炭素材、すなわち、フ
ェノール樹脂、フラン樹脂及びポリアクリロニトリル樹
脂から選ばれる一種以上を炭化処理した炭素材を、溶融
状態の水酸化カリウムを用いる賦活処理法により賦活し
た活性炭を使用する。In the electric double layer capacitor of the present invention, the polarizable electrode is made of a carbon material made of a specific resin as a raw material, that is, a carbon material obtained by carbonizing one or more selected from phenol resin, furan resin and polyacrylonitrile resin. Activated carbon activated by an activation treatment method using molten potassium hydroxide is used.
【0009】この活性炭は、前記特定の樹脂を炭化処理
して得られた炭素材と水酸化カリウムとを混合した状態
で加熱し、溶融状態の水酸化カリウムの存在下で炭素材
を賦活して得られる。この活性炭は、比表面積が大きい
とともに、上記石油コークスを溶融水酸化カリウムを用
いる賦活処理法で賦活処理した従来の活性炭と比べて表
面官能基の濃度が低く、かつ出発原料に由来する重金属
の不純物が少ないという特徴がある。This activated carbon is heated in a state in which a carbon material obtained by carbonizing the above-mentioned specific resin and potassium hydroxide are mixed, and the carbon material is activated in the presence of molten potassium hydroxide. can get. This activated carbon has a large specific surface area, has a lower concentration of surface functional groups than the conventional activated carbon obtained by activating the petroleum coke by an activation treatment method using molten potassium hydroxide, and impurities of heavy metals derived from the starting material. There is a characteristic that there is little.
【0010】本発明者らは、上記特定の炭素材を溶融水
酸化カリウム賦活処理法で賦活した活性炭を分極性電極
に使用することによって、電気二重層コンデンサを高耐
電圧化できるという知見を得、高静電容量を有するとと
もに高耐電圧の電気二重層コンデンサを実現した。高耐
電圧の電気二重層コンデンサが得られる理由は、活性炭
の表面官能基や重金属の不純物の存在に起因する高電圧
印加時の性能劣化を極力低減できたことによると推定さ
れる。The present inventors have obtained the finding that an electric double layer capacitor can be made to have a high withstand voltage by using activated carbon obtained by activating the above-mentioned specific carbon material by a molten potassium hydroxide activation treatment method as a polarizable electrode. , An electric double layer capacitor with high electrostatic capacity and high withstand voltage was realized. It is presumed that the reason why an electric double layer capacitor having a high withstand voltage can be obtained is that the performance deterioration at the time of applying a high voltage due to the presence of surface functional groups of activated carbon and impurities of heavy metals could be reduced as much as possible.
【0011】これら炭素材の出発原料であるフェノール
樹脂、フラン樹脂及びポリアクリロニトリル樹脂は、い
ずれも分子構造中に多くの二重結合を有していることに
よって、炭化処理後の炭化収率が高い点で共通する。こ
れらの樹脂のうち、得られる活性炭の特性が良好であっ
て値段が安い点でフェノール樹脂が最適である。The phenolic resin, furan resin, and polyacrylonitrile resin, which are the starting materials for these carbon materials, all have many double bonds in the molecular structure, so that the carbonization yield after carbonization is high. Common in points. Of these resins, the phenolic resin is the most suitable because the characteristics of the resulting activated carbon are good and the price is low.
【0012】これらの樹脂の炭化処理は、500〜12
00℃の非酸化性雰囲気中で行うのが好ましい。炭化処
理の温度が500℃より低いと、炭化処理に長い時間を
必要とする。また、。炭化処理の温度が1200℃より
高いと、大比表面積を有する活性炭が得にくくなる。The carbonization treatment of these resins is 500 to 12
It is preferably carried out in a non-oxidizing atmosphere at 00 ° C. If the temperature of the carbonization treatment is lower than 500 ° C, the carbonization treatment requires a long time. Also,. When the carbonization temperature is higher than 1200 ° C, it becomes difficult to obtain activated carbon having a large specific surface area.
【0013】活性炭の比表面積の大きさや気孔の大きさ
等を左右する、溶融状態の水酸化カリウムを用いる炭素
材の賦活条件としては、炭素材に混合する水酸化カリウ
ムの量と賦活処理温度が重要である。好ましい特性を有
する活性炭を得るには、炭素材1重量部に対して水酸化
カリウムを2〜6重量部、特には炭素材1重量部に対し
2.5〜4.5重量部加えて混合するのが好ましい。The activation conditions of the carbon material using the potassium hydroxide in a molten state, which influences the size of the specific surface area and the size of the pores of the activated carbon, are the amount of potassium hydroxide mixed with the carbon material and the activation treatment temperature. is important. In order to obtain activated carbon having preferable characteristics, 2 to 6 parts by weight of potassium hydroxide is added to 1 part by weight of carbon material, and particularly 2.5 to 4.5 parts by weight is added and mixed with 1 part by weight of carbon material. Is preferred.
【0014】炭素材1重量部に対する水酸化カリウムの
混合量を2重量部以上にすれば、賦活処理時に炭素材と
溶融水酸化カリウムの良好な接触状態を確保でき、炭素
材を速やかに賦活できる。しかし、炭素材の一定量に対
して混合する水酸化カリウムの量が多すぎると、処理す
る混合物の量が増えて賦活処理炉の賦活処理容量が減少
し、水酸化カリウムの無駄な消費量が増えるので6重量
部以下とする。If the mixing amount of potassium hydroxide to 1 part by weight of the carbon material is 2 parts by weight or more, a good contact state between the carbon material and the molten potassium hydroxide can be ensured during the activation treatment, and the carbon material can be quickly activated. . However, if the amount of potassium hydroxide mixed with a certain amount of the carbon material is too large, the amount of the mixture to be treated increases and the activation treatment capacity of the activation treatment furnace decreases, resulting in a wasteful consumption of potassium hydroxide. Since it will increase, the amount is 6 parts by weight or less.
【0015】炭素材の賦活処理温度は好ましくは600
〜1000℃、特に好ましくは700〜900℃とす
る。賦活処理温度が低いと大比表面積の活性炭を得るの
に必要な賦活処理時間が長くなる。このため、賦活処理
温度は600℃以上とするのが好ましい。また、賦活処
理温度が高すぎると活性炭の気孔が大きくなって分極性
電極の単位体積当たりの静電容量が低下する他、賦活処
理に使用する炉の部材の損耗が増え、賦活処理炉のエネ
ルギー消費量も増える。このため、賦活処理温度は10
00℃以下とするのが好ましい。The activation temperature of the carbon material is preferably 600.
-1000 degreeC, Especially preferably, it is 700-900 degreeC. When the activation treatment temperature is low, the activation treatment time required to obtain activated carbon having a large specific surface area becomes long. Therefore, the activation treatment temperature is preferably 600 ° C. or higher. Further, if the activation treatment temperature is too high, the pores of the activated carbon become large and the electrostatic capacity per unit volume of the polarizable electrode decreases, and the wear of members of the furnace used for the activation treatment increases, and the energy of the activation treatment furnace increases. Consumption will also increase. Therefore, the activation treatment temperature is 10
The temperature is preferably set to 00 ° C or lower.
【0016】活性炭の比表面積は大きいほど活性炭の単
位重量当たりの電気二重層による静電容量は大きくな
る。しかし、逆に賦活が進みすぎて比表面積が過大にな
ると活性炭の細孔容積が増えて電極の見かけ密度が低下
する。活性炭の見かけ密度が低下すると分極性電極の単
位体積当たりの静電容量が低下する。したがって、活性
炭の比表面積は、好ましくは1500〜2500m2 /
gの範囲に制御する。活性炭の比表面積がこの範囲内に
あれば、単位体積当たりの静電容量が大きい分極性電極
が得られる。The larger the specific surface area of activated carbon, the larger the electrostatic capacity of the electric double layer per unit weight of activated carbon. However, on the contrary, if the activation proceeds too much and the specific surface area becomes too large, the pore volume of the activated carbon increases and the apparent density of the electrode decreases. When the apparent density of activated carbon decreases, the electrostatic capacity per unit volume of the polarizable electrode decreases. Therefore, the specific surface area of the activated carbon is preferably 1500 to 2500 m 2 /
Control in the range of g. When the specific surface area of the activated carbon is within this range, a polarizable electrode having a large capacitance per unit volume can be obtained.
【0017】分極性電極を製造するには、活性炭を主体
とする電極材料を電気的接合を保った状態で集電体上に
成形固定する必要がある。その方法としては、従来から
行われている分極性電極の成形固定方法を採用できる。In order to manufacture a polarizable electrode, it is necessary to mold and fix an electrode material mainly composed of activated carbon on a current collector while maintaining electrical connection. As the method, a conventional method of molding and fixing a polarizable electrode can be adopted.
【0018】本発明では、コンデンサの高耐電圧を確保
するため、電解液についてもその分解電圧が高い有機溶
媒系電解液が使用される。有機溶媒系電解液の電解質と
しては、R4 N+ で表される第4級アンモニウムイオ
ン、R4 P+ で表される第4級ホスホニウムイオン(た
だしRはCn H2n+1で示されるアルキル基)などの第4
級オニウムカチオンとBF4 -、PF6 -、ClO4 -、CF
3 SO3 -等のアニオンとを組合せた塩を使用するのが好
ましい。In the present invention, in order to secure a high withstand voltage of the capacitor, an organic solvent type electrolytic solution having a high decomposition voltage is used as the electrolytic solution. As the electrolyte of the organic solvent-based electrolytic solution, a quaternary ammonium ion represented by R 4 N + and a quaternary phosphonium ion represented by R 4 P + (wherein R is represented by C n H 2n + 1 ) Fourth such as alkyl group)
Grade onium cation and BF 4 -, PF 6 -, ClO 4 -, CF
It is preferred to use salts in combination with anions such as 3 SO 3 − .
【0019】これらの塩のうち、第4級アンモニウム塩
又は第4級ホスホニウム塩を使用するのが特に好まし
い。有機溶媒系電解液には、高い分解電圧が得られるよ
うに低水分の有機溶媒を使用するのが好ましい。Of these salts, it is particularly preferable to use a quaternary ammonium salt or a quaternary phosphonium salt. It is preferable to use an organic solvent having a low water content in the organic solvent-based electrolytic solution so that a high decomposition voltage can be obtained.
【0020】電解液に使用する有機溶媒としては、分解
電圧の高い電解液が得られる点で、プロピレンカーボネ
ート、ブチレンカーボネート、ジエチルカーボネート、
エチルメチルカーボネート等のカーボネート類、γ−ブ
チロラクトン等のラクトン類、スルホラン及びその誘導
体から選ばれる一種以上を使用するのが好ましい。As the organic solvent used in the electrolytic solution, propylene carbonate, butylene carbonate, diethyl carbonate,
It is preferable to use one or more selected from carbonates such as ethylmethyl carbonate, lactones such as γ-butyrolactone, sulfolane and derivatives thereof.
【0021】[0021]
【実施例】以下に本発明の実施例(例1〜13)及び比
較例(例14〜19)を挙げてさらに説明するが、本発
明はこれらの実施例に限定されない。EXAMPLES The present invention will be further described below with reference to Examples (Examples 1 to 13) of the present invention and Comparative Examples (Examples 14 to 19), but the present invention is not limited to these Examples.
【0022】表1に示す樹脂等を出発原料とする約70
0℃で炭化処理された粒径10mm程度の各種炭素材
(A:フェノール樹脂、B:フラン樹脂、C:ポリアク
リロニトリル樹脂、D:石油コークス、E:やしがら、
F:おがくず)と3種の賦活処理法(G、G’及び
G”:溶融KOH賦活処理法、H:水蒸気賦活処理法、
I:塩化亜鉛賦活処理法)を用い、表1に示す比表面積
(単位:m2 /g)を有する活性炭を得た。なお、溶融
水酸化カリウムを用いる活性炭の賦活処理条件G、G’
及びG”は、炭素材1重量部に対する水酸化カリウムの
混合量をそれぞれ3重量部、2.5重量部及び2.5重
量部とし、賦活温度はそれぞれ800℃、800℃及び
700℃とした。Approximately 70 using the resins shown in Table 1 as starting materials
Various carbon materials carbonized at 0 ° C. and having a particle size of about 10 mm (A: phenol resin, B: furan resin, C: polyacrylonitrile resin, D: petroleum coke, E: coconut shell,
F: sawdust) and three types of activation treatment methods (G, G'and G ": molten KOH activation treatment method, H: steam activation treatment method,
I: zinc chloride activation treatment method) was used to obtain activated carbon having a specific surface area (unit: m 2 / g) shown in Table 1. The activation treatment conditions G and G'of activated carbon using molten potassium hydroxide
And G "are 3 parts by weight, 2.5 parts by weight and 2.5 parts by weight of potassium hydroxide with respect to 1 part by weight of the carbon material, and the activation temperatures are 800 ° C, 800 ° C and 700 ° C, respectively. .
【0023】上記の賦活処理法で得られた各活性炭を粉
砕した粉末(平均粒径はいずれも約10μm)80重量
%に、結合材のポリテトラフルオロエチレン10重量%
と、導電性を高める導電材であるカーボンブラック10
重量%とを混合した。次いで、この混合物にエタノール
を加えて混練し、シート状に成形後さらに0.6mmの
厚さにロール圧延し、直径12mmの円形に打ち抜い
た。80% by weight of powder (average particle size is about 10 μm) obtained by crushing each activated carbon obtained by the above activation treatment method and 10% by weight of polytetrafluoroethylene as a binder.
And carbon black 10 which is a conductive material for enhancing conductivity
% By weight. Next, ethanol was added to this mixture, and the mixture was kneaded, formed into a sheet shape, further rolled into a thickness of 0.6 mm, and punched into a circle having a diameter of 12 mm.
【0024】この直径12mmのシートを、コイン型コ
ンデンサセルの集電体兼容器部材であるステンレス製ケ
ースと蓋のそれぞれの内側に、カーボン系導電性接着剤
を用いて接着固定し、両者を真空中で加熱処理して両分
極性電極中に含まれる水分等を除去した。The sheet having a diameter of 12 mm was adhered and fixed to the inside of each of the stainless steel case and the lid, which are the collector and container member of the coin-type capacitor cell, by using a carbon-based conductive adhesive, and both were vacuumed. By heat-treating in it, water and the like contained in both polarizable electrodes were removed.
【0025】表1に示す水分の含有量が少ない(いずれ
も50ppm以下)有機溶媒(PC:プロピレンカーボ
ネート、BC:ブチレンカーボネート、SL:スルホラ
ン)に表1に示す濃度(単位:モル濃度)の電解質(C
2 H5 )4 NBF4 を溶かした有機溶媒系電解液を調製
し、この有機溶媒系電解液を活性炭を主体とする両分極
性電極中に充分含浸させるとともに、ポリプロピレン繊
維不織布からなるセパレータ紙を両分極性電極の間に配
置してステンレス製のコイン型容器中にかしめ封口し、
直径18.4mm、厚さ2.0mmのコイン型電気二重
層コンデンサを得た。An electrolyte having a concentration (unit: molar concentration) shown in Table 1 in an organic solvent (PC: propylene carbonate, BC: butylene carbonate, SL: sulfolane) having a low water content shown in Table 1 (50 ppm or less in each case). (C
2 H 5 ) 4 NBF 4 was dissolved in an organic solvent-based electrolytic solution, and the organic solvent-based electrolytic solution was sufficiently impregnated into a bi-polarizable electrode mainly composed of activated carbon, and a separator paper made of polypropylene fiber non-woven fabric was used. Placed between both polarizable electrodes and crimped and sealed in a coin-shaped container made of stainless steel,
A coin-type electric double layer capacitor having a diameter of 18.4 mm and a thickness of 2.0 mm was obtained.
【0026】得られた各電気二重層コンデンサについ
て、その初期の静電容量(単位:F)と内部抵抗(単
位:Ω)を測定した。次いで各コンデンサを70℃の恒
温槽中に入れて3.0Vの電圧を印加し、1000時間
経過後の静電容量(単位:F)および内部抵抗(単位:
Ω)を測定した。前後の性能変化の程度を比べる方法で
高電圧印加条件下におけるコンデンサの長期的な作動信
頼性を加速的に評価した。得られた各電気二重層コンデ
ンサの評価結果を表1にまとめて示す。The initial capacitance (unit: F) and internal resistance (unit: Ω) of each of the obtained electric double layer capacitors were measured. Next, each capacitor was placed in a constant temperature bath of 70 ° C., a voltage of 3.0 V was applied, and the electrostatic capacity (unit: F) and internal resistance (unit: after 1000 hours) were applied.
Ω) was measured. The long-term operational reliability of the capacitor under high voltage application conditions was acceleratedly evaluated by comparing the degree of performance change before and after. Table 1 summarizes the evaluation results of the obtained electric double layer capacitors.
【0027】[0027]
【表1】 [Table 1]
【0028】[0028]
【発明の効果】表1から分かるように、本発明の電気二
重層コンデンサは耐電圧が高く、3.0Vという高電圧
を1000時間印加した後の特性の劣化が少なく、かつ
静電容量が大きい。したがって、本発明によれば、信頼
性が高く、エネルギー密度の大きい電気二重層コンデン
サを提供できる。As can be seen from Table 1, the electric double layer capacitor of the present invention has a high withstand voltage, little deterioration in characteristics after applying a high voltage of 3.0 V for 1000 hours, and a large capacitance. . Therefore, according to the present invention, an electric double layer capacitor having high reliability and high energy density can be provided.
Claims (5)
二重層を形成する電解液とを有する電気二重層コンデン
サにおいて、該分極性電極が、フェノール樹脂、フラン
樹脂及びポリアクリロニトリル樹脂から選ばれる一種以
上の樹脂を原料とする炭素材を溶融状態の水酸化カリウ
ムを用いる賦活処理法で賦活してなる活性炭を主体とす
るものであり、該電解液が有機溶媒系電解液であること
を特徴とする電気二重層コンデンサ。1. An electric double layer capacitor having a polarizable electrode and an electrolytic solution for forming an electric double layer on the surface of the polarizable electrode, wherein the polarizable electrode comprises phenol resin, furan resin and polyacrylonitrile resin. It is mainly composed of activated carbon obtained by activating a carbon material using one or more selected resins as a raw material by an activation treatment method using potassium hydroxide in a molten state, and the electrolytic solution is an organic solvent-based electrolytic solution. Electric double layer capacitor characterized by.
ム塩又は第4級ホスホニウム塩を電解質として含むもの
である請求項1に記載の電気二重層コンデンサ。2. The electric double layer capacitor according to claim 1, wherein the organic solvent-based electrolytic solution contains a quaternary ammonium salt or a quaternary phosphonium salt as an electrolyte.
0m2 /gである請求項1又は2に記載の電気二重層コ
ンデンサ。3. The specific surface area of the activated carbon is 1500 to 250.
It is 0 m < 2 > / g, The electric double layer capacitor of Claim 1 or 2.
リロニトリル樹脂から選ばれる一種以上の樹脂を炭化し
て炭素材とし、該炭素材に水酸化カリウムを加えた混合
物を600〜1000℃に加熱することによって該炭素
材を溶融状態の水酸化カリウムの存在下で活性炭とし、
該活性炭の粉末に結合材と導電材を加えた混合物を集電
体に固定して分極性電極とすることを特徴とする電気二
重層コンデンサ用分極性電極の製造方法。4. A carbon material obtained by carbonizing one or more resins selected from a phenol resin, a furan resin and a polyacrylonitrile resin, and heating a mixture obtained by adding potassium hydroxide to the carbon material to 600 to 1000 ° C. The carbon material is activated carbon in the presence of molten potassium hydroxide,
A method for producing a polarizable electrode for an electric double layer capacitor, comprising fixing a mixture of a powder of the activated carbon and a binder and a conductive material to a collector to form a polarizable electrode.
となるように前記炭素材に水酸化カリウムを加えて混合
する請求項4に記載の電気二重層コンデンサ用分極性電
極の製造方法。5. A weight ratio of potassium hydroxide / carbon material of 2 to 6
The method for producing a polarizable electrode for an electric double layer capacitor according to claim 4, wherein potassium hydroxide is added to and mixed with the carbon material so that
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JP22343795A JP4128233B2 (en) | 1994-10-06 | 1995-08-31 | Manufacturing method of electric double layer capacitor |
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1064759A (en) * | 1996-08-26 | 1998-03-06 | Toyota Motor Corp | Electric double layer capacitor |
JPH1079327A (en) * | 1996-09-04 | 1998-03-24 | Toyota Motor Corp | Electric double layer capacitor |
JP2006261516A (en) * | 2005-03-18 | 2006-09-28 | Honda Motor Co Ltd | Electric double layer capacitor |
JP2007214553A (en) * | 2006-01-11 | 2007-08-23 | Hitachi Chem Co Ltd | Electrode material for electric double layer capacitor, method of manufacturing the same, and electric double layer capacitor |
KR100759103B1 (en) * | 2006-06-19 | 2007-09-19 | 주식회사 나노테크닉스 | Method of preparing for pan/phenolic-resin-based carbon nanofibers and activated carbon nanofibers by electrospinning |
JP2008050258A (en) * | 2007-09-12 | 2008-03-06 | Mitsubishi Chemicals Corp | Carbonaceous substance and electrical double layer capacitor using the same |
JP2008153694A (en) * | 2006-01-11 | 2008-07-03 | Hitachi Chem Co Ltd | Electrode material for electric double layer capacitor, method of manufacturing the same, and electric double layer capacitor |
KR101360465B1 (en) * | 2006-12-20 | 2014-02-07 | 주식회사 포스코 | Activated fiber for siloxane removal and manufacturing method thereof |
CN110015663A (en) * | 2019-02-08 | 2019-07-16 | 桂林理工大学 | A kind of preparation method and application of the porous carbon materials based on phenolic resin |
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1995
- 1995-08-31 JP JP22343795A patent/JP4128233B2/en not_active Expired - Fee Related
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1064759A (en) * | 1996-08-26 | 1998-03-06 | Toyota Motor Corp | Electric double layer capacitor |
JPH1079327A (en) * | 1996-09-04 | 1998-03-24 | Toyota Motor Corp | Electric double layer capacitor |
JP2006261516A (en) * | 2005-03-18 | 2006-09-28 | Honda Motor Co Ltd | Electric double layer capacitor |
JP4597727B2 (en) * | 2005-03-18 | 2010-12-15 | 本田技研工業株式会社 | Electric double layer capacitor |
JP2007214553A (en) * | 2006-01-11 | 2007-08-23 | Hitachi Chem Co Ltd | Electrode material for electric double layer capacitor, method of manufacturing the same, and electric double layer capacitor |
JP2008153694A (en) * | 2006-01-11 | 2008-07-03 | Hitachi Chem Co Ltd | Electrode material for electric double layer capacitor, method of manufacturing the same, and electric double layer capacitor |
KR100759103B1 (en) * | 2006-06-19 | 2007-09-19 | 주식회사 나노테크닉스 | Method of preparing for pan/phenolic-resin-based carbon nanofibers and activated carbon nanofibers by electrospinning |
KR101360465B1 (en) * | 2006-12-20 | 2014-02-07 | 주식회사 포스코 | Activated fiber for siloxane removal and manufacturing method thereof |
JP2008050258A (en) * | 2007-09-12 | 2008-03-06 | Mitsubishi Chemicals Corp | Carbonaceous substance and electrical double layer capacitor using the same |
CN110015663A (en) * | 2019-02-08 | 2019-07-16 | 桂林理工大学 | A kind of preparation method and application of the porous carbon materials based on phenolic resin |
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