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JP2532879B2 - Method for manufacturing electrode for organic electrolyte battery - Google Patents
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JP2532879B2 - Method for manufacturing electrode for organic electrolyte battery - Google Patents

Method for manufacturing electrode for organic electrolyte battery

Info

Publication number
JP2532879B2
JP2532879B2 JP62154523A JP15452387A JP2532879B2 JP 2532879 B2 JP2532879 B2 JP 2532879B2 JP 62154523 A JP62154523 A JP 62154523A JP 15452387 A JP15452387 A JP 15452387A JP 2532879 B2 JP2532879 B2 JP 2532879B2
Authority
JP
Japan
Prior art keywords
acid
battery
insoluble
infusible substance
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.)
Expired - Fee Related
Application number
JP62154523A
Other languages
Japanese (ja)
Other versions
JPH01650A (en
JPS64650A (en
Inventor
静邦 矢田
和朗 桜井
浩司 山口
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.)
Kanebo Ltd
Original Assignee
Kanebo Ltd
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 Kanebo Ltd filed Critical Kanebo Ltd
Priority to JP62154523A priority Critical patent/JP2532879B2/en
Publication of JPH01650A publication Critical patent/JPH01650A/en
Publication of JPS64650A publication Critical patent/JPS64650A/en
Application granted granted Critical
Publication of JP2532879B2 publication Critical patent/JP2532879B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/60Selection of substances as active materials, active masses, active liquids of organic compounds
    • 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
    • Y02E60/10Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は有機電解質電池用の電極の製造法に関する。TECHNICAL FIELD The present invention relates to a method for producing an electrode for an organic electrolyte battery.

[従来の技術] 近年、電子機器の小形化、薄形化或は軽量化は目覚ま
しく、それに伴い電源となる電池の小形化、薄形化、軽
量化の要望が大きい。小型で性能のよい電池として現在
は酸化銀電池が多用されており、又薄形化された乾電池
や、小形軽量な高性能電池としてリチウム電池が開発さ
れ実用化されている。しかし、これらの電池は一次電池
であるため充放電を繰り返して長時間使用することはで
きない。一方、高性能の二次電池としてニッケル−カド
ミウム電池が実用化されているが、小形化、薄形化、軽
量化という点で未だ不満足である。
[Prior Art] In recent years, miniaturization, thinning, or weight reduction of electronic devices has been remarkable, and accordingly, there has been a great demand for miniaturization, thinning, and weight reduction of a battery serving as a power source. Currently, silver oxide batteries are widely used as small size and high performance batteries, and thin dry batteries and lithium batteries have been developed and put into practical use as small and lightweight high performance batteries. However, since these batteries are primary batteries, they cannot be used for a long time by repeating charging and discharging. On the other hand, nickel-cadmium batteries have been put into practical use as high-performance secondary batteries, but they are still unsatisfactory in terms of miniaturization, thinning, and weight reduction.

又、大容量の二次電池として従来より鉛蓄電池が種々
の産業分野で用いられているが、この電池の最大の欠点
は重いことである。これは電極として過酸化鉛及び鉛を
用いているため宿命的なものである。近年、電気自動車
用電池として該電池の軽量化及び性能改善が試みられた
が実用するには至らなかった。しかし蓄電池として大容
量で且つ軽量な二次電池に対する要望は強いものがあ
る。
In addition, lead storage batteries have conventionally been used in various industrial fields as large capacity secondary batteries, but the biggest disadvantage of these batteries is that they are heavy. This is fatal because lead peroxide and lead are used as electrodes. In recent years, attempts have been made to reduce the weight and improve the performance of batteries for electric vehicles, but they have not been put to practical use. However, there is a strong demand for a large-capacity and lightweight secondary battery as a storage battery.

以上のように現在実用化されている電池は、夫々一長
一短が有りそれぞれ用途に応じて使い分けされている
が、電池の小形化、薄形化、或は軽量化に対するニーズ
は大きい。このようなニーズに応える電池として、近
時、有機半導体である薄膜状ポリアセチレンに電子供与
物質又は電子受容性物質をドーピングしたものを電極活
性質として用いる電池が研究され提案されている。該電
池は二次電池として高性能で且つ薄形化、軽量化の可能
性を有しているが、大きな欠点がある。それは、有機半
導体であるポリアセチレンが極めて不安定な物質であ
り、空気中の酸素により容易に酸化を受け、又熱により
変質することである。従って電池製造は不活性ガス雰囲
気で行なわなければならず、又ポリアセチレンを電極に
適した形状に製造する事にも制約を受ける。
As described above, the batteries currently put into practical use each have advantages and disadvantages, and are used properly according to the application, but there is a great need for making the batteries smaller, thinner, or lighter. As a battery that meets such needs, a battery that uses a thin film polyacetylene, which is an organic semiconductor, doped with an electron donor or an electron acceptor as an electrode active substance has recently been studied and proposed. Although this battery has high performance as a secondary battery and has the potential of being thinner and lighter, it has major drawbacks. That is, polyacetylene, which is an organic semiconductor, is a very unstable substance, is easily oxidized by oxygen in the air, and is transformed by heat. Therefore, the battery must be manufactured in an inert gas atmosphere, and there is a limitation in manufacturing polyacetylene into a shape suitable for an electrode.

また、本願の出願人の出願にかかる特開昭60−170163
号公報には、炭素、水素および酸素からなる芳香族系縮
合ポリマーの熱処理物であって、水素原子/炭素原子の
原子比が0.5〜0.05であるポリアセン系骨格構造を有
し、かつBFT法による比表面積が少くとも600m2/gである
不溶不融性物質を正極および/または負極とし、電解に
より該電極にドーピング可能なイオンを生成しうる化合
物の非プロトン性有機溶媒溶液を電解液とすることを特
徴とする有機電解質電池が提案されている。
Further, Japanese Patent Application Laid-Open No. 60-170163 applied for by the applicant of the present application
Japanese Patent Laid-Open Publication No. 2003-187242 discloses a heat-treated product of an aromatic condensation polymer composed of carbon, hydrogen and oxygen, which has a polyacene skeleton structure in which the atomic ratio of hydrogen atoms / carbon atoms is 0.5 to 0.05 and is determined by the BFT method. An insoluble and infusible substance having a specific surface area of at least 600 m 2 / g is used as a positive electrode and / or a negative electrode, and an aprotic organic solvent solution of a compound capable of generating ions capable of doping in the electrode by electrolysis is used as an electrolytic solution. An organic electrolyte battery characterized by the above has been proposed.

該電池は、高性能で、薄形化、軽量化の可能性も有し
ており、電極活性質の酸化安定性も高く、さらにその成
形も容易であるなど将来有望な二次電池である。ところ
が該電池には、さらに改良すべき点が残っていた。すな
わち、電池の容量をより大きくするという事である。
The battery is a promising secondary battery having high performance, possibility of thinning and weight saving, high oxidation stability of electrode active material, and easy molding thereof. However, the battery still has some points to be improved. That is, to increase the capacity of the battery.

[発明が解決しようとする問題点] 本発明の目的は、高性能、薄形かつ軽量な電池を作る
ために用いられ、酸化安定性が高く、成形が容易であ
り、かつ高い電池容量を可能にする有機電解質電池用電
極を提供することにある。
[Problems to be Solved by the Invention] An object of the present invention is to produce a high-performance, thin and lightweight battery, which has high oxidation stability, is easy to mold, and enables a high battery capacity. Another object of the present invention is to provide an electrode for an organic electrolyte battery.

[問題点を解決するための手段] 本発明者は、上述した特開昭60−170163号公報に開示
されるタイプの電極物質に対して酸処理を行うという簡
単な手段により、意外にも電池容量を1〜3割近く向上
できることを見い出し、本発明を完成した。
[Means for Solving Problems] The present inventor has surprisingly found that a simple means of subjecting an electrode substance of the type disclosed in JP-A-60-170163 described above to an acid treatment makes it possible to obtain a battery. The present invention has been completed by finding that the capacity can be improved by about 10 to 30%.

すなわち本発明は、有機電解質電池用電極の製造法に
おいて、炭素、水素及び酸素から成る芳香族系縮合ポリ
マーの熱処理物であって、水素原子/炭素原子の原子数
比が0.5〜0.05であるポリアセン系骨格構造を有しかつB
ET法による比表面積値が少くとも600m2/gである不溶不
融性物質を、硫酸、硝酸、リン酸、亜硫酸またはこれら
の混合物で酸処理することを特徴とする方法である。
That is, the present invention relates to a method for producing an electrode for an organic electrolyte battery, which is a heat-treated product of an aromatic condensation polymer composed of carbon, hydrogen and oxygen, and has a hydrogen atom / carbon atom atomic ratio of 0.5 to 0.05. Has a skeletal structure and B
This is a method characterized in that an insoluble infusible substance having a specific surface area value of at least 600 m 2 / g by the ET method is acid-treated with sulfuric acid, nitric acid, phosphoric acid, sulfurous acid or a mixture thereof.

上記の不溶不融性物質は芳香族系縮合ポリマーの熱処
理物であって、水素原子/炭素原子の原子比が0.05〜0.
5、BET法による比表面積が600m2/g以上であるポリアセ
ン系骨格構造を有する不溶不融性物質である。
The insoluble and infusible substance is a heat-treated product of an aromatic condensation polymer and has an atomic ratio of hydrogen atoms / carbon atoms of 0.05 to 0.
5. An insoluble and infusible substance having a polyacene skeleton structure with a specific surface area of 600 m 2 / g or more as measured by the BET method.

原料としての芳香族系縮合ポリマーは、例えばフェノ
ール性水酸基を有する芳香族炭化水素化合物とアルデヒ
ド類との縮合物である。芳香族炭化水素化合物として
は、例えばフェノール、クレゾール、キシレノールのご
ときいわゆるフェノール類が好適であるが、これらに限
られない。
The aromatic condensation polymer as a raw material is, for example, a condensation product of an aromatic hydrocarbon compound having a phenolic hydroxyl group and an aldehyde. Suitable aromatic hydrocarbon compounds include, but are not limited to, so-called phenols such as phenol, cresol, and xylenol.

アルデヒドとしては、ホルムアルデヒド、アセトアル
デヒド、フラフラール等を使用することができ、ホルム
アルデヒドが好適である。フェノールアルデヒド縮合物
としては、ノボラック型又はレゾール方或はそれらの複
合物のいずれであってもよい。
As the aldehyde, formaldehyde, acetaldehyde, furfural and the like can be used, and formaldehyde is preferable. The phenol aldehyde condensate may be a novolac type, a resole type, or a complex thereof.

本発明における不溶不融性物質は、上記の如き芳香族
系縮合ポリマーの熱処理物であって例えば次のようにし
て製造することができる。
The insoluble and infusible substance in the present invention is a heat-treated product of the aromatic condensation polymer as described above, and can be produced, for example, as follows.

前記した芳香族系縮合ポリマーと塩化亜鉛、リン酸ナ
トリウム等の無機塩を混合する。これにより、不溶不融
性物質に多孔性を付与することができる。混入する量
は、無機塩の種類及び目的とする電極の形状、性能によ
って異なるが、重量比で10/1〜1/7が好ましい。また、
多孔性でありかつ連通孔を有する物質を得る場合には、
無機塩を芳香族系縮合ポリマーの2.5〜10重量倍の量で
用いることが好ましい。このようにして得られた無機塩
と芳香族系縮合ポリマーの混合物を、フィルム状、板状
の目的とする形となし、50〜180℃の温度で2〜90分間
加熱することにより硬化成形する。
The aromatic condensation polymer described above is mixed with an inorganic salt such as zinc chloride or sodium phosphate. Thereby, porosity can be imparted to the insoluble and infusible substance. The amount to be mixed varies depending on the type of the inorganic salt and the shape and performance of the target electrode, but is preferably 10/1 to 1/7 by weight. Also,
To obtain a substance that is porous and has communicating pores,
It is preferable to use the inorganic salt in an amount of 2.5 to 10 times by weight the amount of the aromatic condensation polymer. The mixture of the inorganic salt and the aromatic condensation polymer thus obtained is formed into a desired shape in the form of a film or a plate, and is cured and molded by heating at a temperature of 50 to 180 ° C. for 2 to 90 minutes. .

かくして得られた硬化体を、次いで非酸化性雰囲気中
で350〜800℃の温度、好ましくは350〜700℃の温度、特
に好ましくは400〜600℃の温度まで加熱する。この熱処
理によって芳香族系縮合ポリマーは、脱水素脱水反応を
おこし、芳香環の縮合反応によって、ポリアセン系骨格
構造が形成される。
The cured product thus obtained is then heated in a non-oxidizing atmosphere to a temperature of from 350 to 800C, preferably from 350 to 700C, particularly preferably from 400 to 600C. By this heat treatment, the aromatic condensation polymer undergoes a dehydrogenation dehydration reaction, and a polyacene skeleton structure is formed by the condensation reaction of the aromatic ring.

この反応は熱縮合重合の一種であり、反応度は最終生
成物の水素原子/炭素原子(以後H/Cと云う)で表され
る原子数比によって表される。不溶不融性物質のH/Cの
値は0.05〜0.5、好ましくは、0.1〜0.35である。不溶不
融性物質のH/Cの値が0.5より大きい場合は、ポリアセン
系骨格構造が未発達なため電気電導度が低く好ましくな
い。一方、H/Cの値が0.05より小さい場合は、炭素化が
進みすぎており、電極としての性能が低い。
This reaction is a type of thermal condensation polymerization, and the degree of reaction is represented by the atomic number ratio of hydrogen atoms / carbon atoms (hereinafter referred to as H / C) in the final product. The H / C value of the insoluble and infusible substance is 0.05 to 0.5, preferably 0.1 to 0.35. When the H / C value of the insoluble and infusible substance is larger than 0.5, the polyacene skeleton structure is undeveloped and the electric conductivity is low, which is not preferable. On the other hand, when the value of H / C is smaller than 0.05, carbonization has progressed too much, and the performance as an electrode is low.

得られた熱処理体を水あるいは希塩酸等で十分洗浄す
ることによって、熱処理体中に含まれている無機塩を除
去する。その後、これを乾燥すると、BET法による比表
面積が600m2/g以上の不溶不融性物質を得る。
The heat-treated body thus obtained is thoroughly washed with water, diluted hydrochloric acid or the like to remove the inorganic salt contained in the heat-treated body. Then, this is dried to obtain an insoluble and infusible substance having a specific surface area of 600 m 2 / g or more by the BET method.

本発明方法において、上記の不溶不融性物質を硫酸、
硝酸、リン酸、亜硫酸またはこれらの混合物で酸処理す
る。このようにして得られた酸処理不溶不融性物質は、
理由は定かではないが、酸処理されていない不溶不融性
物質に比べより多くのイオンを内部に蓄えることができ
るので容量の大きな電極材となるものと考えられる。
In the method of the present invention, the insoluble infusible substance is sulfuric acid,
Acid treatment with nitric acid, phosphoric acid, sulfurous acid or a mixture thereof. The acid-treated insoluble and infusible substance thus obtained is
Although the reason is not clear, it is considered that the electrode material has a large capacity because it can store a larger amount of ions in the inside as compared with an insoluble infusible substance that has not been acid-treated.

不溶不融性物質は極めて安定な物質であるため、酸処
理は強い酸性下でおこなうことが好ましい。酸処理に用
いることのできる酸は、硫酸、硝酸、リン酸、亜硫酸ま
たはこれらの混合物である。酸処理の方法は、不溶不融
性物質と酸を接触させるいかなる方法も行いうる。一般
的方法としては、上記の酸又はその溶液と不溶不融性物
質を常温又は好ましくは加熱下に接触させる。酸を混合
して王水、混酸などの極めて強力な酸化雰囲気を作り、
この中に不溶不融性物質を浸すことができる。あるい
は、酸の蒸気の中に不溶不融性物質を置く方法を採るこ
ともできる。必要な酸濃度、処理温度及び処理時間は相
互に関連し、たとえば酸濃度を低くした場合には処理温
度を上げることが好ましい。適当な条件は実験により簡
単に求めることができ、後述の実施例1,2,特に3を参照
することができる。
Since the insoluble and infusible substance is a very stable substance, it is preferable that the acid treatment is performed under strong acidity. Acids that can be used for the acid treatment are sulfuric acid, nitric acid, phosphoric acid, sulfurous acid or a mixture thereof. As the method of acid treatment, any method of bringing an insoluble and infusible substance into contact with an acid can be performed. As a general method, the above-mentioned acid or solution thereof and the insoluble and infusible substance are brought into contact with each other at room temperature or preferably under heating. Mixing acids creates an extremely strong oxidizing atmosphere such as aqua regia, mixed acid,
An insoluble and infusible substance can be immersed in this. Alternatively, a method of placing an insoluble and infusible substance in acid vapor can be adopted. The required acid concentration, treatment temperature and treatment time are interrelated, and it is preferable to raise the treatment temperature when the acid concentration is lowered, for example. Appropriate conditions can be easily determined by experiments, and reference can be made to Examples 1 and 2 below, especially 3 below.

このようにして得られた酸処理不溶不融性物質はおそ
らく酸化されており、かつ、酸処理前の不溶不融性物質
中には存在しなかった元素が存在する。例えば、H2SO4,
H2SO3で処理した場合にはイオウ元素が、HNO3で処理す
ると窒素元素が存在する。該酸処理された不溶不融性物
質は有機電解質電池の電極として用いることができ、す
ると電池の容量は、酸処理しない不溶不融性物質を用い
た電池に比べ、10〜30%大きくなる。
The acid-treated insoluble infusible substance thus obtained is probably oxidized, and there are elements which were not present in the insoluble infusible substance before the acid treatment. For example, H 2 SO 4 ,
Elemental sulfur is present when treated with H 2 SO 3 , and elemental nitrogen is present when treated with HNO 3 . The acid-treated insoluble and infusible substance can be used as an electrode of an organic electrolyte battery, and the capacity of the battery is increased by 10 to 30% as compared with a battery using the acid-treated insoluble and infusible substance.

ここで有機電解質電池とは典型的には、上記の酸処理
した不溶不融性物質を正極又は負極、又は正負両極と
し、電解によって酸処理不溶不融性物質にドーピング可
能なイオンを生成しうる化合物を非プロトン性有機溶媒
に溶解させた溶液を電解液とする有機電解質電池であ
る。
Here, the organic electrolyte battery is typically the positive electrode or negative electrode, or both positive and negative electrodes, the acid-treated insoluble infusible substance, it is possible to generate ions capable of doping the acid-treated insoluble infusible substance by electrolysis An organic electrolyte battery using a solution of a compound dissolved in an aprotic organic solvent as an electrolytic solution.

酸処理した不溶不融性物質を正極のみに用いるか、負
極のみに用いるか、また正負両極に用いるかは、たとえ
ば電池の用途によって異なる。例えば、酸処理不溶不融
性物質を正極に用い、負極にLi金属またはLiを含む合金
を用いると、起電圧の高い、電源用電池ができる。酸処
理不溶不融性物質を負極に用い、正極に酸未処理不溶不
融性物質から成る電極を用いると、ICなどのバックアッ
プ用キャパンタータイプの電池となる。
Whether the acid-treated insoluble and infusible substance is used only for the positive electrode, only the negative electrode, or both the positive and negative electrodes depends on the application of the battery, for example. For example, when an acid-treated insoluble and infusible substance is used for the positive electrode and Li metal or an alloy containing Li is used for the negative electrode, a power source battery with high electromotive voltage can be obtained. When the acid-treated insoluble infusible substance is used for the negative electrode and the electrode made of the acid untreated insoluble infusible substance is used for the positive electrode, a capantor type battery for backup such as IC is obtained.

電極にドーピングされうるイオンを生成しうる化合物
としては、例えばアルカリ金属又はテトラアルキルアン
モニウムのハロゲン化物、過塩素酸塩などが用いられ
る。
As the compound capable of generating ions that can be doped into the electrode, for example, a halide of alkali metal or tetraalkylammonium, a perchlorate and the like are used.

具体的にはLiI,NaI,KI,NH4I,LiClO4,LiBF4,LiAsF6,Li
PF6,NaClO4,NaBF4,NaAsF6,NaPF6,KClO4,KBF4,KAsF6,KPF
6,(C2H54NClO4,(n−C4H94NClO4,(t−C4H94N
ClO4,(C2H54NBF4,(n−C4H94NBF4,(t−C4H94
NBF4,(C2H54NPF6,(n−C4H94NPF6,(t−C4H94
NPF6,LiB(CH34,LiB(C2H54,LiB(C6H54,LiHF2
の化合物である。
Specifically, LiI, NaI, KI, NH 4 I, LiClO 4 , LiBF 4 , LiAsF 6 , Li
PF 6 , NaClO 4 , NaBF 4 , NaAsF 6 , NaPF 6 , KClO 4 , KBF 4 , KAsF 6 , KPF
6 , (C 2 H 5 ) 4 NClO 4 , (n-C 4 H 9 ) 4 NClO 4 , (t-C 4 H 9 ) 4 N
ClO 4, (C 2 H 5 ) 4 NBF 4, (n-C 4 H 9) 4 NBF 4, (t-C 4 H 9) 4
NBF 4 , (C 2 H 5 ) 4 NPF 6 , (n-C 4 H 9 ) 4 NPF 6 , (t-C 4 H 9 ) 4
It is a compound such as NPF 6 , LiB (CH 3 ) 4 , LiB (C 2 H 5 ) 4 , LiB (C 6 H 5 ) 4 , LiHF 2 .

前記化合物を溶解する溶媒として非プロトン性有機溶
媒が用いられる。例えばエチレンカーボネート、プロピ
レンカーボネート、γ−ブチロラクトン、ジメチルホル
ムアミド、ジメチルアセトアミド、ジメチルスルホキシ
ド、アセトニトリル、ジメトキシエタン、テトラヒドロ
フラン、スルホラン、ジオキソラン、塩化メチレン又は
これらの混合物が挙げられる。これらのうちから電解質
として用いられる前記化合物の溶解性、電池性能等を考
慮して選択される。
An aprotic organic solvent is used as a solvent for dissolving the compound. Examples thereof include ethylene carbonate, propylene carbonate, γ-butyrolactone, dimethylformamide, dimethylacetamide, dimethylsulfoxide, acetonitrile, dimethoxyethane, tetrahydrofuran, sulfolane, dioxolane, methylene chloride, and mixtures thereof. Among them, the material is selected in consideration of the solubility of the compound used as the electrolyte, battery performance, and the like.

電解液中の前記化合物の濃度は、電解液による内部抵
抗を小さくするため少なくとも0.1モル/以上とする
のが望ましく、通常0.2〜3モル/とするのがより好
ましい。
The concentration of the compound in the electrolytic solution is preferably at least 0.1 mol / more in order to reduce the internal resistance due to the electrolytic solution, and more preferably 0.2 to 3 mol / normal.

[発明の効果] 本発明に従い、不溶不融性物質を酸処理したものを有
機電解質電池の電極として用いることにより、電池容量
を顕著に向上できる。
[Effect of the Invention] According to the present invention, by using an insoluble infusible substance treated with an acid as an electrode of an organic electrolyte battery, the battery capacity can be significantly improved.

[実 施 例] 以下、実施例により本発明を更に説明する。実施例に
おいて電池容量測定に用いた電池は、第1図に示すよう
な構成である。
[Examples] Hereinafter, the present invention will be further described with reference to Examples. The battery used for measuring the battery capacity in the examples has a structure as shown in FIG.

第1図において、1は正極であり、2は負極であり、
3,3′は各電極から外部に電流を取り出したり、充電す
るために電流を供給するための集電体であり、各電流及
び外部端子7,7′に電圧降下を生じないように接続され
ている。4は電解液であり、5はガラスセパレータであ
る。正負極及びセパレータは電池ケース6内に実用上問
題が生じないように固定される。
In FIG. 1, 1 is a positive electrode, 2 is a negative electrode,
Reference numerals 3 and 3'are current collectors for extracting current from each electrode to the outside or supplying current for charging, and are connected so as not to cause a voltage drop to each current and the external terminals 7 and 7 '. ing. 4 is an electrolytic solution, and 5 is a glass separator. The positive and negative electrodes and the separator are fixed in the battery case 6 so that there is no practical problem.

実施例 1 (1) 不溶不融性物質を作った。Example 1 (1) An insoluble and infusible substance was prepared.

水溶性レゾール(約60%濃度)/塩化亜鉛/水を重量
比で10/25/4の割合で混合した水溶液をフィルムアプリ
ケーターでガラス板上に成膜した。次に成膜した水溶液
上にガラス板を載せ水分が蒸発しない様にした後、約10
0℃の温度で1時間加熱して硬化させた。
An aqueous solution prepared by mixing water-soluble resol (about 60% concentration) / zinc chloride / water at a weight ratio of 10/25/4 was formed on a glass plate with a film applicator. Next, place a glass plate on the formed aqueous solution to prevent water from evaporating, then
It was cured by heating at a temperature of 0 ° C. for 1 hour.

該フェノール樹脂フィルムをシリコニット電気炉中に
入れ窒素気流下で40℃/時間の速度で昇温して、500℃
まで熱処理を行った。次に該熱処理物を希塩酸で洗った
後、水洗し、その後乾燥することによってフィルム状の
多孔体を得た。該フィルムの厚みは約200μmであり、
見掛け密度は約0.35g/cm3であり、機械的強度に優れた
フィルムであった。次に該フィルムの電気伝導度を室温
で直流4端子法で測定したところ、10-3Scmであった。
元素分析を行ったところ水素原子/炭素原子の原子比は
0.27であった。
The phenol resin film was placed in a siliconite electric furnace and heated at a rate of 40 ° C./hour under a nitrogen stream to 500 ° C.
Heat treatment was performed. Next, the heat-treated product was washed with dilute hydrochloric acid, washed with water, and then dried to obtain a film-shaped porous body. The thickness of the film is about 200 μm,
The apparent density was about 0.35 g / cm 3 , and the film was excellent in mechanical strength. Next, the electric conductivity of the film was measured at room temperature by a DC 4-terminal method and found to be 10 −3 Scm.
Elemental analysis showed that the atomic ratio of hydrogen atoms / carbon atoms was
It was 0.27.

BET法による比表面積値の測定を行ったところ、2100m
2/gと極めて大きな値であった。
When the specific surface area was measured by the BET method, it was 2100 m
It was an extremely large value of 2 / g.

(2) この不溶不融性物質を100℃の濃硫酸中に30分
間置いて酸処理した。次に蒸留水で十分に洗浄し、70℃
で12時間減圧乾燥した。
(2) The insoluble and infusible substance was placed in concentrated sulfuric acid at 100 ° C. for 30 minutes for acid treatment. Next, wash thoroughly with distilled water, 70 ℃
And dried under reduced pressure for 12 hours.

この酸処理不溶不融性物質及び酸処理していない不溶
不融性物質の元素分析をCHN分析及び螢光X線分析の手
法を用いて行なった。元素分析の結果を表1にまとめて
示す。表1に示すように、未処理不溶不融性物質には含
まれていなかった新たな元素Sが酸処理不溶不融性物質
に含まれていた。
Elemental analysis of the acid-treated insoluble infusible substance and the insoluble infusible substance not treated with acid was carried out by the techniques of CHN analysis and fluorescent X-ray analysis. The results of elemental analysis are summarized in Table 1. As shown in Table 1, a new element S, which was not contained in the untreated insoluble infusible substance, was contained in the acid-treated insoluble infusible substance.

(3) 酸処理不溶不融性物質を正極とし、リチウム金
属を負極として第1図に示すように電池を組んだ。電池
におけるドーピング量は炭素原子1個当りにドーピング
されるイオンの数で表すこととし、本発明ではドーピン
グされたイオンの数はドーピング時に回路に流れた電流
値の和より求めた。電解液として1モル/のLiClO4/
プロピレンカーボネート溶液を用いた。電池を組んだ直
後の電圧は3.1Vであり、4Vの電圧を印加することにより
電池を充電した。1時間充電した後、起電圧を測定する
と4Vであった。次に1時間あたりのアンドープ量が5%
となる速度で放電したところ、電池の電圧が2Vになるま
でに要した時間は80分間であった。
(3) A battery was assembled as shown in FIG. 1 using the acid-treated insoluble and infusible substance as a positive electrode and lithium metal as a negative electrode. The doping amount in the battery is represented by the number of ions doped per carbon atom, and in the present invention, the number of doped ions is obtained from the sum of the current values flowing in the circuit at the time of doping. 1 mol / LiClO 4 / as electrolyte
A propylene carbonate solution was used. The voltage immediately after the battery was assembled was 3.1V, and the battery was charged by applying a voltage of 4V. After charging for 1 hour, the electromotive voltage was measured and found to be 4V. Next, the undoped amount per hour is 5%
When discharged at a rate of, the time required for the voltage of the battery to reach 2 V was 80 minutes.

比較例 1 実施例1(3)において用いた酸処理不溶不融性物質
を未処理不溶不融性物質に変え、他は実施例1(3)と
同一にして電池の特性を測定した。比較例1の結果を、
実施例1の結果と共に表2に示す。本発明により、容量
が顕著に向上した。
Comparative Example 1 The characteristics of the battery were measured in the same manner as in Example 1 (3) except that the acid-treated insoluble infusible substance used in Example 1 (3) was replaced with an untreated insoluble infusible substance. The result of Comparative Example 1
The results are shown in Table 2 together with the results of Example 1. The present invention significantly improved the capacity.

実施例 2 (a) 実施例1(1)で得た不溶不融性物質を正極と
し、実施例1(2)で作った酸処理不溶不融性物質を負
極として第1図の様に電池を組んだ。電池を組んだ直後
の起電圧は0.1Vであった。次に外部電源により2.5Vの電
圧を印加することによって電池を充電した。次に1時間
当りの放電量が、酸処理不溶不融性物質の炭素原子に対
して5%となる速度で放電したところ約50分間で電池の
電圧が0Vとなった。
Example 2 (a) Using the insoluble infusible substance obtained in Example 1 (1) as a positive electrode and the acid-treated insoluble infusible substance prepared in Example 1 (2) as a negative electrode, a battery was prepared as shown in FIG. Teamed up. Immediately after the battery was assembled, the electromotive voltage was 0.1V. Next, the battery was charged by applying a voltage of 2.5 V from an external power source. Next, when the discharge amount per hour was 5% with respect to the carbon atoms of the acid-treated insoluble and infusible substance, the voltage of the battery became 0 V in about 50 minutes.

比較例 2 実施例2において、負極も酸未処理不溶不融性物質と
する以外はまったく同様にして電池を組み容量を測定し
た。放電時間は約40分間であった。本発明に従う上記実
施例2を比較例2と比べると、本発明により容量が著し
く向上したことが明瞭である。
Comparative Example 2 A battery was assembled and the capacity was measured in the same manner as in Example 2 except that the negative electrode was also an acid untreated insoluble and infusible substance. The discharge time was about 40 minutes. Comparing Example 2 above according to the present invention with Comparative Example 2, it is clear that the present invention significantly improved the capacity.

実施例 3 酸処理を表3に示す条件で行う以外は実施例1(2)
とまったく同様にして酸処理不溶不融性基体を得た。次
に実施例1(3)の方法で電池を組み容量を測定した。
Example 3 Example 1 (2) except that the acid treatment is performed under the conditions shown in Table 3.
An acid-treated insoluble and infusible substrate was obtained in exactly the same manner as in. Next, a battery was assembled by the method of Example 1 (3) and the capacity was measured.

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

第1図は本発明に係る基本の構成を示すものであり、1
は正極、2は負極、3,3′は集電体、4は電解液、5は
セパレータ、6は電池ケース、7,7′は外部端子を表わ
す。
FIG. 1 shows a basic configuration according to the present invention.
Is a positive electrode, 2 is a negative electrode, 3, 3'is a current collector, 4 is an electrolytic solution, 5 is a separator, 6 is a battery case, and 7 and 7'are external terminals.

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】有機電解質電池用電極の製造法において、
炭素、水素及び酸素から成る芳香族系縮合ポリマーの熱
処理物であって、水素原子/炭素原子の原子数比が0.5
〜0.05であるポリアセン系骨格構造を有しかつBET法に
よる比表面積値が少くとも600m2/gである不溶不融性物
質を、硫酸、硝酸、リン酸、亜硫酸またはこれらの混合
物で酸処理することを特徴とする方法。
1. A method of manufacturing an electrode for an organic electrolyte battery, comprising:
A heat-treated product of an aromatic condensation polymer composed of carbon, hydrogen and oxygen, wherein the atomic ratio of hydrogen atoms / carbon atoms is 0.5.
Acid treatment of sulfuric acid, nitric acid, phosphoric acid, sulfurous acid, or a mixture thereof, which has a polyacene skeleton structure of ~ 0.05 and a specific surface area by BET method of at least 600 m 2 / g A method characterized by the following.
【請求項2】芳香族系縮合ポリマーがフェノールとホル
ムアルデヒドとの縮合ポリマーである特許請求の範囲第
1項記載の方法。
2. The method according to claim 1, wherein the aromatic condensation polymer is a condensation polymer of phenol and formaldehyde.
【請求項3】酸処理を、硫酸、硝酸、リン酸又はこれら
の混合物で行う特許請求の範囲第1項記載の方法。
3. The method according to claim 1, wherein the acid treatment is carried out with sulfuric acid, nitric acid, phosphoric acid or a mixture thereof.
JP62154523A 1987-06-23 1987-06-23 Method for manufacturing electrode for organic electrolyte battery Expired - Fee Related JP2532879B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62154523A JP2532879B2 (en) 1987-06-23 1987-06-23 Method for manufacturing electrode for organic electrolyte battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62154523A JP2532879B2 (en) 1987-06-23 1987-06-23 Method for manufacturing electrode for organic electrolyte battery

Publications (3)

Publication Number Publication Date
JPH01650A JPH01650A (en) 1989-01-05
JPS64650A JPS64650A (en) 1989-01-05
JP2532879B2 true JP2532879B2 (en) 1996-09-11

Family

ID=15586118

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62154523A Expired - Fee Related JP2532879B2 (en) 1987-06-23 1987-06-23 Method for manufacturing electrode for organic electrolyte battery

Country Status (1)

Country Link
JP (1) JP2532879B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0658799B2 (en) * 1985-03-30 1994-08-03 鐘紡株式会社 Battery electrode manufacturing method

Also Published As

Publication number Publication date
JPS64650A (en) 1989-01-05

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