JP2837427B2 - Electrically conductive organic polymer materials - Google Patents
Electrically conductive organic polymer materialsInfo
- Publication number
- JP2837427B2 JP2837427B2 JP1103196A JP10319689A JP2837427B2 JP 2837427 B2 JP2837427 B2 JP 2837427B2 JP 1103196 A JP1103196 A JP 1103196A JP 10319689 A JP10319689 A JP 10319689A JP 2837427 B2 JP2837427 B2 JP 2837427B2
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- JP
- Japan
- Prior art keywords
- powder
- insoluble
- zinc chloride
- phenolic resin
- infusible
- 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 - Lifetime
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- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は電気伝導性有機高分子系材料に係り、更に詳
細にはフェノール系樹脂の熱処理物又は該熱処理物に電
子供与性ドーパント及び/又は電子受容性ドーパントを
ドーピングしてなる電気伝導性有機高分子系粉末材料の
製造方法に関する。The present invention relates to an electrically conductive organic polymer material, and more particularly, to a heat-treated phenolic resin or an electron-donating dopant and / or The present invention relates to a method for producing an electrically conductive organic polymer powder material obtained by doping an electron-accepting dopant.
高分子材料は成型性、軽量性および量産性に優れてい
る。そのため高分子材料のこれらの特性を生かして、電
気的に半導性を有する有機高分子材料がエレクトロニク
ス産業を始めとして多くの産業分野において希求されて
いる。初期の有機半導体はフイルム状あるいは板状体等
に成形することが困難であり、又n型あるいはp型の不
純物半導体としての性質を有していなかったため、用途
的にも限定されていた。近年、比較的成形性に優れた有
機半導体が得られるようになり、しかもこれらの半導体
に電子供与性ドーパントあるいは電子受容性ドーパント
をドーピングすることによってn型あるいはp型の有機
半導体とすることが可能となった。そのような有機半導
体の代表例として、ポリアセチレンがある。The polymer material is excellent in moldability, lightness and mass productivity. Therefore, by utilizing these characteristics of the polymer material, an organic polymer material having electrical semiconductivity is demanded in many industrial fields including the electronics industry. The early organic semiconductors were difficult to form into a film or plate, and did not have the properties of an n-type or p-type impurity semiconductor. In recent years, organic semiconductors having relatively good moldability have been obtained, and these semiconductors can be converted into n-type or p-type organic semiconductors by doping them with an electron-donating dopant or an electron-accepting dopant. It became. A typical example of such an organic semiconductor is polyacetylene.
ところがポリアセチレンは酸素によって酸化され易い
欠点がある。このため空気中で取り扱うことが困難であ
り、工業材料としては実用性に欠ける。However, polyacetylene has a disadvantage that it is easily oxidized by oxygen. For this reason, it is difficult to handle in air, and it is not practical as an industrial material.
本願の出願人の出願にかかる、特開昭59−3806号およ
び特開昭60−152554号公報には炭素、水素および酸素か
ら成る芳香族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0.60〜0.15で表わされるポリア
セン系骨格構造を含有する不溶不融性基体と、電子供与
性ドーピング剤又は電子受容性ドーピング剤とから成
り、電気伝導性が未ドープの該基体よりも大である電気
伝導性有機高分子材料が提案されている。該材料は空気
中で安定であり、工業材料として実用的である。JP-A-59-3806 and JP-A-60-152554, which are filed by the applicant of the present application, describe a heat-treated aromatic condensation polymer composed of carbon, hydrogen and oxygen, wherein hydrogen atom / carbon atom Consisting of an insoluble and infusible substrate having a polyacene skeleton structure represented by an atomic ratio of 0.60 to 0.15, and an electron-donating doping agent or an electron-accepting doping agent, wherein the electric conductivity is higher than that of the undoped substrate. Large electrically conductive organic polymer materials have been proposed. The material is stable in air and is practical as an industrial material.
この先願においてポリアセン系骨格構造を含有する不
溶不融性基体は、フェノール系樹脂の成型体を熱処理す
ることにより製造されている。しかし、生産性を考慮
し、該成形体を高充填率で大量に電気炉に仕込むと、例
えばクレータ状のふくれが生じるなど不均質な不溶不融
性基体しか得られない等の問題点があった。In this prior application, an insoluble and infusible substrate containing a polyacene-based skeletal structure is produced by heat-treating a phenolic resin molded body. However, in consideration of productivity, if a large amount of the compact is charged into an electric furnace at a high filling rate, there is a problem that only an inhomogeneous insoluble and infusible substrate such as crater-like blisters can be obtained. Was.
本発明者らは、上記問題点に鑑み鋭意研究を続けた結
果、フェノール系樹脂の初期縮合物水溶液と塩化亜鉛水
溶液とを撹拌下で反応を進行させることによって得られ
た粉末状のフェノール系樹脂・塩化亜鉛複合体を非酸化
性雰囲気下で熱処理することにより、上述の問題点を解
決し得ることを見い出し本発明を完成したものである。The present inventors have conducted intensive studies in view of the above problems, and as a result, a powdery phenolic resin obtained by agitating an aqueous solution of an initial condensate of a phenolic resin and an aqueous solution of zinc chloride with stirring. The inventors have found that the above-mentioned problems can be solved by heat-treating the zinc chloride composite in a non-oxidizing atmosphere, and have completed the present invention.
本発明の目的は、経済的で大量生産可能な電気伝導性
有機高分子系粉末材料の製造方法を提供するにある。An object of the present invention is to provide a method for producing an electrically conductive organic polymer-based powder material that is economical and can be mass-produced.
本発明の他の目的は半導性ないし伝導性の電気伝導性
を有し、且つ比表面積が高い為、ドーパントを大量にそ
して迅速にドーピング可能な電気伝導性有機高分子系粉
末材料の製造方法を提供するにある。Another object of the present invention is to provide a method for producing an electrically conductive organic polymer-based powder material which has a semiconductive or conductive electrical conductivity and has a high specific surface area, so that a large amount of dopant can be rapidly doped. To provide.
更に他の目的および効果は以下の説明から明らかにさ
れよう。Still other objects and advantages will be apparent from the following description.
上述の目的は、水溶性フェノール系樹脂初期縮合物
と、塩化亜鉛とを水性媒体中で撹拌下で縮合反応させる
ことにより生成されたフェノール系樹脂と塩化亜鉛との
複合体粉末を非酸化性雰囲気下で熱処理してなるポリア
セン系骨格構造を含有し、水素原子/炭素原子の原子比
が0.05〜0.6であり、且つBET法による比表面積値が少な
くとも600m2/g以上である不溶不融性の電気伝導性有機
高分子系粉末材料の製造方法、並びに水溶性フェノール
系樹脂初期縮合物と塩化亜鉛とを水性媒体中で撹拌混合
して縮合反応させることにより生成されたフェノール系
樹脂と塩化亜鉛との複合体を非酸化性雰囲気下で熱処理
してなるポリアセン系骨格構造を含有し、水素原子/炭
素原子の原子比が0.05〜0.6であり、且つBET法による比
表面積値が少なくとも600m2/g以上である不溶不融性の
粉末に電子供与性ドーパント及び/又は電子受容性ドー
パントをドーピングしてなる電気伝導性有機高分子系粉
末材料の製造方法により達成される。The above-described object is to provide a composite powder of a phenolic resin and zinc chloride produced by subjecting a water-soluble phenolic resin precondensate and a zinc chloride to a condensation reaction in an aqueous medium with stirring, in a non-oxidizing atmosphere. It contains a polyacene-based skeletal structure obtained by heat treatment under the following conditions. The atomic ratio of hydrogen atoms / carbon atoms is 0.05 to 0.6, and the specific surface area value by the BET method is at least 600 m 2 / g. A method for producing an electrically conductive organic polymer-based powder material, and a phenolic resin and zinc chloride formed by stirring and mixing a water-soluble phenolic resin precondensate and zinc chloride in an aqueous medium to cause a condensation reaction. Containing a polyacene-based skeleton structure obtained by heat-treating the composite under a non-oxidizing atmosphere, having an atomic ratio of hydrogen atoms / carbon atoms of 0.05 to 0.6, and a specific surface area value of at least 600 m 2 / g by the BET method. Less than It is achieved by the method for manufacturing an electro-conductive organic polymer-based powder material insoluble infusible powder formed by doping an electron donating dopant and / or electron-accepting dopant to be.
本発明に用いられるフェノール系樹脂としては、
(a)フェノール・ホルムアルデヒド樹脂の如き、フェ
ノール性水酸基を有する芳香族系炭化水素化合物とアル
デヒド類との縮合物、(b)キシレン変性フェノール・
ホルムアルデヒド樹脂(フェノールの一部をキシレンで
置換したもの)の如き、フェノール性水酸基を有する芳
香族系炭化水素化合物が挙げられる。As the phenolic resin used in the present invention,
(A) a condensate of an aldehyde with an aromatic hydrocarbon compound having a phenolic hydroxyl group, such as a phenol-formaldehyde resin, and (b) a xylene-modified phenol.
An aromatic hydrocarbon compound having a phenolic hydroxyl group, such as a formaldehyde resin (in which a part of phenol is substituted with xylene), may be mentioned.
本発明における不溶不融性基体は例えば次の様にして
製造することができる。The insoluble and infusible substrate in the present invention can be produced, for example, as follows.
まずフェノール系樹脂の初期縮合物水溶液と塩化亜鉛
水溶液より粉末状のフェノール系樹脂・塩化亜鉛複合体
を調製する。First, a powdery phenolic resin / zinc chloride composite is prepared from an aqueous solution of an initial condensate of a phenolic resin and an aqueous solution of zinc chloride.
従来の方法では、上記原料を十分に冷却しながら撹拌
混合することにより原料の均一混合液として、その後加
熱硬化させるという2段法で成型板として該複合体を製
造していたのであるが、本方法では上記原料を十分な冷
却なしに強制的に撹拌混合することにより混合時に発生
した熱で縮合反応を進行させ、かつ強制撹拌によって、
微粉化して粉末状の該複合体を調製する。撹拌中の冷却
あるいは加熱温度条件は原料組成によって変わるが縮合
反応が進行する程度の熱量が発生すればよい。しかし反
応系の温度が20℃以下では塩化亜鉛水溶液中の塩化亜鉛
が析出し易い等の問題が生じる為20℃以上であることが
好ましい。また得られた該複合体粉末の粒径は製造条件
によって異なるが、本発明の目的には100μm以下の粉
末として生成させるのが好適である。またこれらの微粒
の2次凝集体として得られることもある。塩化亜鉛の混
入量はフェノール系樹脂に対して重量比で1/20〜10/1が
好ましい。塩化亜鉛が1/20より少ないと該複合体の粒径
が100μm以上となり、後の熱処理工程で大量に電気炉
に仕込んだ場合、均質なポリアセン骨格構造を有する不
溶不融性基体が得られ難くなる。In the conventional method, the composite was manufactured as a molded plate by a two-stage method in which the above-mentioned raw materials were stirred and mixed while being sufficiently cooled to form a uniform mixed liquid of the raw materials, and then heated and cured. In the method, the condensation reaction is advanced by heat generated during mixing by forcibly stirring and mixing the raw materials without sufficient cooling, and by forced stirring,
The powder is pulverized to prepare the composite. The cooling or heating temperature conditions during stirring vary depending on the composition of the raw materials, but it is sufficient that heat is generated to such an extent that the condensation reaction proceeds. However, if the temperature of the reaction system is 20 ° C. or lower, it is preferable that the temperature be 20 ° C. or higher because problems such as easy precipitation of zinc chloride in the zinc chloride aqueous solution occur. The particle size of the obtained composite powder varies depending on the production conditions, but for the purpose of the present invention, it is preferable to produce the powder as a powder having a size of 100 μm or less. In addition, they may be obtained as secondary aggregates of these fine particles. The mixing amount of zinc chloride is preferably 1/2 to 10/1 by weight relative to the phenolic resin. When zinc chloride is less than 1/20, the particle size of the composite becomes 100 μm or more. Become.
また塩化亜鉛水溶液の濃度も該混合物の形状、サイズ
に影響を与えるが、水と塩化亜鉛とを重量比で0.1〜1
の範囲で用いるのが好ましい。濃度が0.1より低いと塩
化亜鉛が析出固化し、均一な混合が行えない。また1を
上廻ると粒径が100μm以上となり、前述と同様大量に
電気炉に仕込んだ場合に後の熱処理工程で均質なものが
得られ難くなる。The concentration of the aqueous zinc chloride solution also affects the shape and size of the mixture.
It is preferable to use in the range of. If the concentration is lower than 0.1, zinc chloride precipitates and solidifies, and uniform mixing cannot be performed. On the other hand, if it exceeds 1, the particle size becomes 100 μm or more, and it becomes difficult to obtain a homogeneous product in the subsequent heat treatment step when a large amount is charged into an electric furnace as described above.
さらに撹拌下での縮合反応を制御するために略球状の
フェノール系樹脂例えばベルパール(鐘紡(株)社製)
等の市販品を撹拌混合中に混入してもよい。ただし、該
略球状フェノール系樹脂の混入量が多すぎると混合物の
嵩密度が低下し、生産性が低下する。Further, in order to control the condensation reaction under stirring, a substantially spherical phenolic resin such as Bellpearl (manufactured by Kanebo Co., Ltd.)
And the like may be mixed during the stirring and mixing. However, if the mixing amount of the substantially spherical phenolic resin is too large, the bulk density of the mixture decreases, and the productivity decreases.
この様にして得られた粉末状のフェノール系樹脂と塩
化亜鉛複合体とを非酸化性雰囲気中で400〜800℃の温
度、好ましくは450〜750℃の温度、特に好ましくは500
〜700℃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、脱水素脱水反応を生起し、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 powdery phenolic resin thus obtained and the zinc chloride composite are subjected to a temperature of 400 to 800 ° C. in a non-oxidizing atmosphere, preferably to a temperature of 450 to 750 ° C., particularly preferably 500
Heat to a temperature of ~ 700 ° C. The aromatic condensation polymer causes a dehydrogenation dehydration reaction by the heat treatment, 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。不溶不融性基体のH/Cの
値は0.05〜0.6、好ましくは、0.15〜0.50である。不溶
不融性基体のH/Cの値が0.6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伝導度が低く一方、H/
Cの値が0.05より小さい場合、ドーピングできるドーパ
ント量が少なくなる。This reaction is a kind of thermal condensation polymerization, and the degree of reactivity is represented by the atomic ratio represented by hydrogen atoms / carbon atoms (hereinafter referred to as H / C) in the final product. The H / C value of the insoluble infusible substrate is 0.05 to 0.6, preferably 0.15 to 0.50. When the value of H / C of the insoluble infusible substrate is larger than 0.6, the electric conductivity is low because the polyacene-based skeletal structure is not developed, while the H / C
When the value of C is smaller than 0.05, the amount of dopant that can be doped becomes small.
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。The obtained heat-treated body is sufficiently washed with water or diluted hydrochloric acid to remove the inorganic salt contained in the heat-treated body.
その後、これを乾燥することにより、本発明の不溶不
融性基体粉末が得られる。Thereafter, by drying this, the insoluble infusible substrate powder of the present invention is obtained.
かくして得られる本発明の不溶不融性基体粉末の粒径
は原料の種類、組成あるいは各工程の製造条件により変
わるが通常は100μm以下である。またこれらの微粒の
2次凝集体として得られることもある。The particle size of the thus obtained insoluble and infusible substrate powder of the present invention varies depending on the kind and composition of the raw materials or the production conditions in each step, but is usually 100 μm or less. In addition, they may be obtained as secondary aggregates of these fine particles.
さらに該不溶不融性基体粉末は、BET法による比表面
積値が、少なくとも600m2/gである。Further, the insoluble infusible base powder has a specific surface area value of at least 600 m 2 / g by the BET method.
該粉末の比表面積値が600m2/g未満である場合、Cl
O4 -、BF4−、AsF5等のイオン半径の大きなドーパントを
大量にかつスムーズにドーピングするのが難しく、また
後に示す様に活性吸着材として使用する時、吸着量が低
下し好ましくない。If the specific surface value of the powder is less than 600 m 2 / g, Cl
It is difficult to dope a large amount of a dopant having a large ionic radius, such as O 4 − , BF 4 −, or AsF 5 , in a large amount and smoothly, and when used as an active adsorbent as described later, the amount of adsorption is undesirably reduced.
該ポリアセン系骨格構造を含有する不溶不融性基体粉
末はBET法による比表面積値が600m2/g以上と非常に大き
な値を示すため、酸素等のガスが侵入し、劣化い易いと
考えられるが、現実には空気中に長時間放置しても物性
等に変化はなく、酸化安定性に優れているものである。Since the insoluble and infusible base powder containing the polyacene-based skeleton structure has a very large specific surface area value of 600 m 2 / g or more according to the BET method, it is considered that a gas such as oxygen invades and easily deteriorates. However, in reality, there is no change in physical properties and the like even when left in the air for a long time, and it is excellent in oxidation stability.
本発明によれば、上記不溶不融性基板粉末に電子供与
性ドーパント又は電子受容性ドーパントあるいはこれら
の両方のドーパントをドーピングした電気伝導性有機高
分子系粉末材料が得られる。According to the present invention, an electrically conductive organic polymer powder material obtained by doping the insoluble and infusible substrate powder with an electron-donating dopant, an electron-accepting dopant, or both of these dopants is obtained.
すなわち、本発明によればフェノール系樹脂の初期縮
合物水溶液と塩化亜鉛水溶液とを撹拌混合中に縮合反応
を進行させることによって得られる粉末状のフェノール
系樹脂・塩化亜鉛複合体を非酸化性雰囲気中で熱処理す
ることにより得られ水素原子/炭素原子の原子比が0.6
〜0.05であるポリアセン系骨格構造を含有する不溶不融
性基体粉末であり、かつBET法による比表面積値が少な
くとも600m2/g以上であり、電子供与性ドーパント及び
/または電子受容性ドーパントより成る電気伝導性有機
高分子系粉末材料が得られる。That is, according to the present invention, a powdery phenolic resin / zinc chloride composite obtained by advancing a condensation reaction while stirring and mixing an aqueous solution of an initial condensate of a phenolic resin and an aqueous solution of zinc chloride is mixed in a non-oxidizing atmosphere. Hydrogen atom / carbon atom ratio of 0.6 obtained by heat treatment in
An insoluble infusible substrate powder containing a polyacene-based skeletal structure of from 0.05 to 0.05, and a specific surface area value of at least 600 m 2 / g or more by a BET method, comprising an electron-donating dopant and / or an electron-accepting dopant. An electrically conductive organic polymer powder material is obtained.
電子供与性ドーパントとしては電子を離し易い物質が
用いられる。例えばリチウム、ナトリウム、カリウム、
ルビジウムあるいはセシウムの如き周期律表の第1A族金
属が好ましく用いられる。As the electron donating dopant, a substance that easily separates electrons is used. For example, lithium, sodium, potassium,
A Group 1A metal of the periodic table, such as rubidium or cesium, is preferably used.
電子供与性ドーパントとしては、同様に、テトラ(C1
〜C4アルキル)アンモニウムカチオン例えば(CH3)4N+
あるいは(C4H9)4N+を用いることができる。Similarly, as the electron donating dopant, tetra (C 1
-C 4 alkyl) ammonium cation example (CH 3) 4 N +
Alternatively, (C 4 H 9 ) 4 N + can be used.
また、電子受容性ドーパントとしては電子を受け取り
易い物質が用いられる。例えばフッ素、塩素、臭素、沃
素の如きハロゲン;AsF5,PF5,BF3,BCl3,BBr3,FeCl3の如
きハロゲン化合物;SO3あるいはN2O5の如き非金属元素の
酸化物;あるいはH2SO4,HNO3又はHClO4の如き無機酸に
由来する陰イオン等が好ましく用いられる。In addition, a substance that easily accepts electrons is used as the electron-accepting dopant. Such as fluorine, chlorine, bromine, halides such as iodine; AsF 5, PF 5, BF 3, BCl 3, BBr 3, such as halogen compounds FeCl 3; SO 3 or an oxide of such non-metallic elements of the N 2 O 5; Alternatively, an anion derived from an inorganic acid such as H 2 SO 4 , HNO 3 or HClO 4 is preferably used.
かかるドーパントのドーピング方法としては、ポリア
セチレンあるいはポリフェニレンについて従来用いられ
ているドーピング法と本質的に同じ方法を使用すること
ができる。As the doping method of such a dopant, essentially the same doping method as conventionally used for polyacetylene or polyphenylene can be used.
例えば、ドーパントがアルカリ金属の場合には、溶融
したアルカリ金属あるいはアルカリ金属の蒸気と不溶不
融性基体粉末とを接触せしめてドーピングすることがで
き、また例えばテトラヒドロフラン中で生成せしめたア
ルカリ金属ナフタレン錯体と不溶不融性基体とを接触せ
しめてドーピングすることもできる。For example, when the dopant is an alkali metal, it can be doped by bringing a molten alkali metal or a vapor of the alkali metal into contact with an insoluble and infusible substrate powder, and, for example, an alkali metal naphthalene complex formed in tetrahydrofuran. The insoluble and infusible substrate may be brought into contact with and doped.
ドーパントがハロゲン、ハロゲン化合物あるいは非金
属元素の酸化物である場合にはこれらのガスを不溶不融
性基体粉末と接触せしめることにより、容易にドーピン
グを行うことができる。When the dopant is a halogen, a halogen compound or an oxide of a nonmetallic element, doping can be easily performed by bringing these gases into contact with the insoluble and infusible substrate powder.
ドーピング剤が無機酸に由来する陰イオンである場合
には、無機酸を不溶不融性基体粉末に含浸せしめること
によって行うことができる。When the doping agent is an anion derived from an inorganic acid, the doping can be carried out by impregnating the insoluble and infusible substrate powder with the inorganic acid.
また、不溶不融性基体粉末を成形して電極とし電気化
学的に、リチウム、ナトリウム等の電子供与性ドーパン
トあるいはClO4 -,BF4 -等の電子受容性ドーパントをドー
ピングすることも可能である。It is also possible to form an insoluble infusible substrate powder into an electrode and electrochemically dope it with an electron donating dopant such as lithium and sodium or an electron accepting dopant such as ClO 4 − and BF 4 −. .
ドーピング剤は、一般に芳香族系縮合ポリマーの繰返
し単位に対して10-5モル以上の割合で、得られる本発明
の不溶不融性基体粉末に存在するように用いられる。The doping agent is generally used in the insoluble infusible substrate powder of the present invention in a proportion of 10 -5 mol or more based on the repeating unit of the aromatic condensation polymer.
かくして得られる本発明の製造方法で得た不溶不融性
基体粉末は、ドーピング前の不溶不融性基体粉末の電気
伝導度(例えば10-12〜102Ω-1・cm-1)よりも高い電気
伝導度、例えばドーピング前の不溶不融性基体粉末より
も数倍ないし1010倍に増大する。電子供与性ドーパント
をドーピングしたときにはn型半導体を与え、電子受容
性ドーパントをドーピングしたときにはp型半導体を与
える。本発明によればドーパントとして電子供与性ドー
パントと電子受容性ドーパントとを一緒に用いることも
できる。これらのドーパントが本発明の不溶不融性基体
粉末にほぼ均一に混在する場合にはいずれか一方の多く
存在する方のドーパントによってp型又はn型となる。
例えば、電子供与性ドーパントが多く存在する場合には
n型となり、電子受容性ドーパントが多く存在する場合
にはp型となる。The insoluble infusible substrate powder obtained by the production method of the present invention thus obtained has a higher conductivity than the insoluble infusible substrate powder before doping (for example, 10 -12 to 10 2 Ω -1 · cm -1 ). high electrical conductivity, increases for example, several times to 10 10 times greater than insoluble and infusible base powder before doping. When doped with an electron-donating dopant, an n-type semiconductor is provided, and when doped with an electron-accepting dopant, a p-type semiconductor is provided. According to the present invention, an electron-donating dopant and an electron-accepting dopant can be used together as a dopant. When these dopants are almost uniformly mixed in the insoluble and infusible base powder of the present invention, the dopant becomes p-type or n-type depending on which one of the dopants is present most.
For example, it becomes n-type when there are many electron-donating dopants, and becomes p-type when there are many electron-accepting dopants.
本発明の製造方法で得たポリアセン系骨格構造を含有
する不溶不融性基体はその大部分が粉末状であり、他の
大部分が簡単な粉砕により粉末状となる微粉の2次凝集
体であるため、バインダーを加える方法等により、フィ
ルム状、板状、円筒状等任意の形状とすることが可能で
あり極めて実用性の高い材料である。The insoluble and infusible substrate containing the polyacene-based skeleton structure obtained by the production method of the present invention is mostly in the form of powder, and most of the other is a secondary agglomerate of fine powder which becomes powder by simple pulverization. Therefore, the material can be formed into an arbitrary shape such as a film shape, a plate shape, or a cylindrical shape by a method of adding a binder and the like, and is an extremely practical material.
本発明の製造方法で得た不溶不融性基体粉末の高い比
表面積値を利用して界面で生じる各種の化学反応を迅速
に進めることも可能である。例えば電池の電極材等に好
適である。また各種の物理的吸着もスムーズに、均一に
しかも大量に生じるため、吸着材あるいは分離材として
好適である。By utilizing the high specific surface area value of the insoluble and infusible substrate powder obtained by the production method of the present invention, various chemical reactions occurring at the interface can be rapidly advanced. For example, it is suitable for an electrode material of a battery. In addition, since various physical adsorptions occur smoothly, uniformly and in large quantities, they are suitable as adsorbents or separation materials.
更にH2O、O2等のガスの吸着によっても若干の電気伝
導度の変化が生じるため、センサー材としても好適に用
いることができる。Further, since slight change in electric conductivity occurs due to adsorption of gas such as H 2 O and O 2 , it can be suitably used as a sensor material.
また、本発明の製造方法で得た不溶不融性基体粉末
は、ポリアセン系骨格構造を含有しているため、耐薬品
性に優れており、しかも細孔が多いので成型することに
より、過酷な条件下で使用する濾材としても好適であ
る。In addition, the insoluble and infusible base powder obtained by the production method of the present invention contains a polyacene-based skeletal structure, is excellent in chemical resistance, and has many pores, so that the molding is severe. It is also suitable as a filter medium used under conditions.
以上の様に本発明の製造方法で得た不溶不融性基体粉
末は、耐熱性、耐酸化性に優れ、しかも高い比表面積を
有しているため、電子受容性あるいは電子供与性ドーパ
ントが迅速にそして大量にしかも均一にドーピングでき
る有機半導体であり、また化学的に活性機能を有し、し
かも機械的強度に優れたフィルム状、板状等の任意の形
状に成形できるため、多方面に応用出来る産業上有用な
材料である。As described above, the insoluble and infusible substrate powder obtained by the production method of the present invention has excellent heat resistance and oxidation resistance, and has a high specific surface area. Organic semiconductor that can be doped in large quantities and uniformly, and has a chemically active function, and can be formed into any shape such as a film or plate with excellent mechanical strength, so it can be applied to various fields. It is an industrially useful material that can be used.
以下、実施例を挙げて本発明を具体的に説明する。 Hereinafter, the present invention will be described specifically with reference to examples.
実施例1 (1)ポリアセン系骨格構造を含有する不溶不融性基体
の製造 水溶性レゾール(60%濃度)に塩化亜鉛水溶液(85%
濃度)を10:30の割合で加え、40℃で加温しながら撹拌
具としてスクリュービーターを装着したDMV型万能混合
撹拌機((株)三英製作所製)にて70r.p.mで撹拌混合
を行ったところ、約30分で硬化反応による変色がおこり
始め、10分後に100μm以下の粉末状のフェノール系樹
脂・塩化亜鉛複合体を得た。該複合体10kgを角型電気炉
に仕込み、窒素気流下40℃/時間の速度で昇温して500
℃まで熱処理を行った。次にこの熱処理物を希塩酸で洗
浄した後、水洗しその後乾燥したところ不溶不融性基体
粉末が得られた。Example 1 (1) Production of an insoluble and infusible substrate containing a polyacene-based skeleton structure A water-soluble resol (60% concentration) was added to an aqueous zinc chloride solution (85%).
Concentration) at a ratio of 10:30, and stirring and mixing at 70 rpm using a DMV type universal mixing stirrer (manufactured by Sanei Seisakusho) equipped with a screw beater as a stirrer while heating at 40 ° C. The discoloration due to the curing reaction began to occur in about 30 minutes, and after 10 minutes, a powdery phenolic resin / zinc chloride composite of 100 μm or less was obtained. 10 kg of the composite was charged into a square electric furnace, and heated at a rate of 40 ° C./hour under a nitrogen stream to 500
Heat treatment was performed up to ° C. Next, the heat-treated product was washed with dilute hydrochloric acid, washed with water, and then dried to obtain an insoluble and infusible base powder.
該不溶不融性基体粉末のBET法による比表面積値は230
0m2/gであり、また水素原子/炭素原子の原子比は0.24
であった。The specific surface area value of the insoluble infusible substrate powder by the BET method is 230.
0 m 2 / g, and the atomic ratio of hydrogen atom / carbon atom is 0.24
Met.
(2)上記の不溶不融性基体粉末100部に対し、ポリ四
フッ化エチレンをバインダーとして5部加え充分に混練
し、厚さ1mmの板状に加圧成型した。(2) To 100 parts of the insoluble and infusible base powder, 5 parts of polytetrafluoroethylene as a binder was added and kneaded sufficiently, followed by pressure molding into a plate having a thickness of 1 mm.
(3)次に充分に脱水したプロピレンカーボネートにLi
ClO4を溶解させて約1.0モル/の溶液とした。そして
リチウム金属を陰極として上記した溶液を電解液とし、
(2)の板状成型体を陽極として、両極間に約4Vの電圧
を印加して約1時間COl4 -イオンをドーピングした。ド
ーピング量は該不溶不融性基体の炭素原子1個当りのCl
O4 -イオンの数で表わすこととした。(3) Lithium is then added to propylene carbonate that has been sufficiently dehydrated.
ClO 4 was dissolved to a solution of about 1.0 mol /. And the above solution is used as an electrolyte with lithium metal as a cathode,
(2) a sheet-like molded body as an anode of, about 1 hour COL 4 by applying a voltage of approximately 4V between the two electrodes - doped with ions. The doping amount is Cl per carbon atom of the insoluble infusible substrate.
O 4 - was decided to represent the number of ions.
本発明ではこのClO4 -イオンの数はドーピング時に回
路に流れた電流値より求めたものである。電流値は3.0
%であった。In the present invention this ClO 4 - number of ions are those obtained from the current value flowing in the circuit at the time of doping. The current value is 3.0
%Met.
比較例1 実施例1と同様の組成比で20℃の温度で十分に冷却し
ながら均一な原料混合溶液を調製し、50×50×5mmの型
枠に流し込み、100℃の温度で60分間硬化反応を進め、
厚み約5mmの板状複合成型体を得た。該複合成型体10kg
を実施例1と同じ角型電気炉に仕込み、窒素気流下40℃
/時間の速度で昇温して500℃まで熱処理を行ったが、
クレータ状のふくれが多量に発生し取出が非常に困難で
あった。Comparative Example 1 A uniform raw material mixed solution was prepared at the same composition ratio as in Example 1 while sufficiently cooling at a temperature of 20 ° C., poured into a mold of 50 × 50 × 5 mm, and cured at a temperature of 100 ° C. for 60 minutes. Proceed with the reaction,
A plate-like composite molded body having a thickness of about 5 mm was obtained. 10 kg of the composite molding
Was placed in the same square electric furnace as in Example 1, and heated at 40 ° C. under a nitrogen stream.
The temperature was raised at a rate of / hour and the heat treatment was performed up to 500 ° C.
A large amount of crater-like blisters were generated, making removal very difficult.
実施例2〜4 (1)表1に示す混合組成で実施例1と同様の方法によ
り不溶不融性基体粉末を得た。いずれの場合も該基体粉
末は均質であり、ふくれ等の発生はなかった。Examples 2 to 4 (1) Insoluble and infusible substrate powders were obtained in the same manner as in Example 1 with the mixed compositions shown in Table 1. In each case, the substrate powder was homogeneous, and no blistering or the like occurred.
(2)該基体を実施例1と同様の方法で成型板とした。
これらの成型板は充分な強度を有していた。表1に該基
体の比表面積、水素/炭素原子数比および該成型板のド
ープ量をまとめて示す。(2) The substrate was formed into a molded plate in the same manner as in Example 1.
These molded plates had sufficient strength. Table 1 summarizes the specific surface area of the substrate, the hydrogen / carbon atom ratio, and the doping amount of the molded plate.
実施例5,6 (1)実施例1と同様の方法で製造した複合体10kgを角
型電気炉に仕込み、窒素気流下40℃/時間の速度で昇温
して400℃まで熱処理を行った。さらに同複合体10kgを
同条件下700℃まで熱処理を行い、不溶不融性基体粉末
を得た。どちらの場合も該基体粉末は均質であり、ふく
れ等の発生はなかった。 Examples 5 and 6 (1) 10 kg of the composite produced in the same manner as in Example 1 was charged into a rectangular electric furnace, and heated at a rate of 40 ° C./hour under a nitrogen stream and heat-treated to 400 ° C. . Further, 10 kg of the composite was heat-treated to 700 ° C under the same conditions to obtain an insoluble and infusible base powder. In both cases, the substrate powder was homogeneous and no blistering or the like occurred.
(2)該基体を実施例1と同様の方法で成型板とした。
これらの成型板は充分な強度を有していた。表2に該基
体の比表面積、水素/炭素原子数比および該成型板のド
ープ量をまとめて示す。(2) The substrate was formed into a molded plate in the same manner as in Example 1.
These molded plates had sufficient strength. Table 2 summarizes the specific surface area of the substrate, the hydrogen / carbon atom number ratio, and the doping amount of the molded plate.
実施例7 (1)ポリアセン系骨格構造を含有する不溶不融性基体
粉末の製造 水溶性レゾール(75%濃度)に球状フェノール樹脂
(鐘紡(株)社製ベルパール)と塩化亜鉛水溶液(85%
濃度)とを10/10/50を割合で加え60℃で10分間撹拌混合
することにより、粉末状のフェノール系樹脂・塩化亜鉛
複合体を得た。該複合体を実施例1と同様の条件で熱処
理を行い、不溶不融性基体粉末とした。 Example 7 (1) Production of an insoluble and infusible base powder containing a polyacene-based skeleton structure A water-soluble resol (75% concentration) was mixed with a spherical phenol resin (Bellepearl manufactured by Kanebo Co., Ltd.) and an aqueous zinc chloride solution (85%).
Phenolic resin / zinc chloride composite powder was obtained by adding 10/10/50 to the mixture at a ratio of 10/50 and stirring and mixing at 60 ° C. for 10 minutes. The composite was heat-treated under the same conditions as in Example 1 to obtain an insoluble and infusible base powder.
(2)該不溶不融性基体粉末を実施例1と同様の方法で
成型板とした。該基体の比表面積は2300m2/g、該成型板
のClO4 -イオンのドープ量は3%であった。(2) The insoluble infusible base powder was formed into a molded plate in the same manner as in Example 1. The specific surface area of the substrate was 2,300 m 2 / g, and the doping amount of ClO 4 − ions in the molded plate was 3%.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 岡本 種男 大阪府大阪市東淀川区上新庄2丁目15番 24号 (72)発明者 矢田 静邦 兵庫県加古郡播磨町宮西2丁目6―13 審査官 關 政立 (56)参考文献 特開 昭62−127341(JP,A) ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Taneo Okamoto 2-15-24 Kamishinjo, Higashiyodogawa-ku, Osaka-shi, Osaka Masaru Seki (56) References JP-A-62-127341 (JP, A)
Claims (2)
亜鉛とを水性媒体中で撹拌混合して縮合反応させること
により生成されたフェノール系樹脂と塩化亜鉛との複合
体粉末を非酸化性雰囲気下で熱処理してなるポリアセン
系骨格構造を含有し、水素原子/炭素原子の原子比が0.
05〜0.6であり、且つBET法による比表面積値が少なくと
も600m2/g以上である不溶不融性の電気伝導性有機高分
子系粉末材料の製造方法。1. A composite powder of a phenolic resin and zinc chloride formed by stirring and mixing a water-soluble phenolic resin precondensate and zinc chloride in an aqueous medium to cause a condensation reaction. It contains a polyacene-based skeleton structure that is heat-treated under the following conditions, and has an atomic ratio of hydrogen atoms / carbon atoms of 0.
A method for producing an insoluble, infusible, electrically conductive organic polymer-based powder material having a specific surface area of at least 600 m 2 / g by a BET method, which is from 0.05 to 0.6.
亜鉛とを水性媒体中で撹拌混合して縮合反応させること
により生成されたフェノール系樹脂と塩化亜鉛との複合
体粉末を非酸化性雰囲気下で熱処理してなるポリアセン
系骨格構造を含有し、水素原子/炭素原子の原子比が0.
05〜0.6であり、且つBET法による比表面積値が少なくと
も600m2/g以上である不溶不融性の粉末に電子供与性ド
ーパント及び又は電子受容性ドーパントをドーピングし
てなる電気伝導性有機高分子系粉末材料の製造方法。2. A composite powder of a phenolic resin and zinc chloride produced by stirring and mixing a water-soluble phenolic resin initial condensate and zinc chloride in an aqueous medium to cause a condensation reaction, and subjecting the mixture to a non-oxidizing atmosphere. It contains a polyacene-based skeleton structure that is heat-treated under the following conditions, and has an atomic ratio of hydrogen atoms / carbon atoms of 0.
An electrically conductive organic polymer obtained by doping an insoluble and infusible powder having a specific surface value of at least 600 m 2 / g by BET method with an electron donating dopant and / or an electron accepting dopant which is from 0.05 to 0.6. Manufacturing method of powder based materials.
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JP2837427B2 true JP2837427B2 (en) | 1998-12-16 |
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