JPH04348192A - Electro-viscous fluid - Google Patents
Electro-viscous fluidInfo
- Publication number
- JPH04348192A JPH04348192A JP3151136A JP15113691A JPH04348192A JP H04348192 A JPH04348192 A JP H04348192A JP 3151136 A JP3151136 A JP 3151136A JP 15113691 A JP15113691 A JP 15113691A JP H04348192 A JPH04348192 A JP H04348192A
- Authority
- JP
- Japan
- Prior art keywords
- polyaniline
- electrorheological
- powder
- electro
- aniline
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M171/00—Lubricating compositions characterised by purely physical criteria, e.g. containing as base-material, thickener or additive, ingredients which are characterised exclusively by their numerically specified physical properties, i.e. containing ingredients which are physically well-defined but for which the chemical nature is either unspecified or only very vaguely indicated
- C10M171/001—Electrorheological fluids; smart fluids
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2201/00—Inorganic compounds or elements as ingredients in lubricant compositions
- C10M2201/04—Elements
- C10M2201/041—Carbon; Graphite; Carbon black
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
- C10N2040/16—Dielectric; Insulating oil or insulators
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
- C10N2040/17—Electric or magnetic purposes for electric contacts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
- C10N2040/175—Pantographs, i.e. printing devices
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
- C10N2040/18—Electric or magnetic purposes in connection with recordings on magnetic tape or disc
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
- C10N2040/185—Magnetic fluids
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/30—Refrigerators lubricants or compressors lubricants
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/32—Wires, ropes or cables lubricants
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/34—Lubricating-sealants
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/36—Release agents or mold release agents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/38—Conveyors or chain belts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/40—Generators or electric motors in oil or gas winning field
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/42—Flashing oils or marking oils
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/44—Super vacuum or supercritical use
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/50—Medical uses
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Lubricants (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
【0001】0001
【産業の利用分野】本発明は、電気制御によりその粘性
特性を大きく、しかも可逆的に変えることができ、エン
ジンマウント、ショックアブソーバー、バルブ、アクチ
ュエーター、クラッチなどの機械装置の電気制御に好適
に利用される電気粘性(Electro Rheol
ogical)流体に関する。[Field of Industrial Application] The present invention can greatly and reversibly change its viscosity characteristics through electrical control, and is suitable for electrical control of mechanical devices such as engine mounts, shock absorbers, valves, actuators, and clutches. Electro Rheol
(logical) fluids.
【0002】0002
【従来の技術】油状媒体にある種の物質を分散させた流
体に電場を印加することにより、その見かけ粘度が大き
く変化する現象は、ウィンズロー効果として古くから知
られている。このようなウィンズロー効果を示す初期の
流体は、デンプンやスターチなどを鉱油や潤滑油に分散
させたものであるが、これらの流体は、電気粘性効果の
重要性を認識する上では十分であったが、効果の再現性
が欠如しており、各種の分野でその効果を利用すること
は不可能であった。2. Description of the Related Art The phenomenon in which the apparent viscosity of a fluid containing a certain kind of substance dispersed in an oily medium changes greatly by applying an electric field to the fluid has long been known as the Winslow effect. Early fluids that exhibited the Winslow effect were starch, starch, etc. dispersed in mineral oil or lubricating oil, but these fluids were not developed enough to recognize the importance of the electrorheological effect. However, the effects lacked reproducibility, making it impossible to utilize them in various fields.
【0003】そこで、電気粘性効果が高く、再現性の良
好な流体を得るため、これまで微粉体を中心として盛ん
に研究が行われ、多くの提案がなされている。例えば、
ポリアクリル酸のような酸基を有する高吸水性樹脂微粒
子(特開昭53−93186号公報)、イオン交換樹脂
(特公昭60−31211号公報)、アルミナシリケー
ト(特開昭62−95397号公報)などを用いたもの
が提案されている。[0003] Therefore, in order to obtain a fluid with a high electrorheological effect and good reproducibility, research has been actively conducted mainly on fine powder, and many proposals have been made. for example,
Highly water-absorbent resin fine particles having acid groups such as polyacrylic acid (JP-A-53-93186), ion exchange resin (JP-A-60-31211), alumina silicate (JP-A-62-95397) ) etc. have been proposed.
【0004】これらの電気粘性流体は、いずれも親水性
の微粉体を含水させ、絶縁性の油状媒体中に分散させた
ものであり、これらの電気粘性効果は、外部から高電圧
を印加した時、水の作用により微粉体に分極が生じ、こ
の分極により粒子間に電場方向の架橋が生じて流体の粘
度が増大するとものと考えられている。[0004] All of these electrorheological fluids are made by impregnating hydrophilic fine powder and dispersing it in an insulating oily medium, and these electrorheological effects occur when a high voltage is applied from the outside. It is believed that polarization occurs in fine powder due to the action of water, and that this polarization causes crosslinking between particles in the direction of the electric field, increasing the viscosity of the fluid.
【0005】このような水の作用による電気粘性流体の
研究がこれまで行われてきたが、近年例えばポリアセン
キノンなどの有機半導体微粒子を用いた流体(特開昭6
1−216202号公報)、有機固体粒子の表面に導電
性薄膜層を形成し、更にその上に電気絶縁性薄膜層を形
成した誘電体微粒子を用いた流体(特開昭63−976
94号公報)、空洞部分を有する誘電体微粒子を用いた
流体(特開平1−172496号公報)など強誘電体物
質や半導体粒子を用いた水分を含まない非水系電気粘性
流体が提案されてきている。Research on electrorheological fluids due to the action of water has been conducted so far, but in recent years, for example, fluids using organic semiconductor fine particles such as polyacenequinone (Japanese Patent Laid-Open No. 6
1-216202), a fluid using dielectric fine particles in which a conductive thin film layer is formed on the surface of organic solid particles, and an electrically insulating thin film layer is further formed thereon (JP-A-63-976).
Non-aqueous electrorheological fluids that do not contain water and that use ferroelectric substances or semiconductor particles have been proposed, such as fluids that use dielectric fine particles having cavities (Japanese Patent Application Laid-open No. 1-172496). There is.
【0006】[0006]
【発明が解決しようとする課題】このような非水系電気
粘性流体は、従来の流体における水の存在による種々の
欠陥、例えば水イオンの存在により電圧印加時に流れる
電流値の増大又は電気依存性が大きくなるなどの欠点を
解消する可能性が大きく期待され、更に研究が進められ
ている。即ち、ウィンズロー効果が外部電圧による微粒
子表面の分極に基ずくものであると仮定し、微粒子表面
に分極を生じさせる別の方法、とりわけ誘電体微粒子の
検討が盛んに行われている。しかしながら、従来提案さ
れてきた単層の化合物からなる半導体粒子又は表面に絶
縁層を形成した微粒子等を用いる非水系電気粘性流体は
、水を添加して引き起こされる電気粘性効果に比較して
効果が小さかったり、直流では電気泳動が生じてしまっ
たり、安定性が十分でない場合があるなどの欠点を有し
ている。[Problems to be Solved by the Invention] Such non-aqueous electrorheological fluids have various defects caused by the presence of water in conventional fluids, such as an increase in the value of current flowing when voltage is applied or electricity dependence due to the presence of water ions. There are great expectations that it will have the potential to eliminate drawbacks such as increased size, and further research is underway. That is, on the assumption that the Winslow effect is based on polarization of the surface of fine particles due to an external voltage, other methods of generating polarization on the surface of fine particles, particularly dielectric fine particles, are being actively investigated. However, conventionally proposed non-aqueous electrorheological fluids using semiconductor particles made of single-layer compounds or microparticles with an insulating layer formed on their surfaces are less effective than the electrorheological effect caused by adding water. They have drawbacks such as being small, electrophoresis may occur when using direct current, and stability may not be sufficient.
【0007】従って、このような欠点を解消することが
可能な新規な非水系電気粘性流体の開発が望まれる。[0007]Therefore, it is desired to develop a new non-aqueous electrorheological fluid that can overcome these drawbacks.
【0008】[0008]
【課題を解決するための手段及び作用】本発明者は、上
記要望に応えるため、鋭意検討を重ねた結果、これまで
提案されてきた誘電体物質や半導体粒子を用いる方法で
は、電気粘性効果をこれ以上向上させること、直流通電
下においての電気泳動の発生を確実に防止すること、十
分な安定性を確保することなどの要望をすべて満足する
ことは困難であるという結論に達した。そこで、従来よ
り知られている誘電体物質や半導体粒子の他に電気粘性
効果を生じる粒子を見出すべく、更に検討を重ねた結果
、ポリアニリンを熱処理することにより得られる炭素質
粒子が、水を含んでいなくても有効な電気粘性効果を生
じ、これを油状媒体に分散することにより、新規な電気
粘性流体が得られることを知見し、本発明を完成したも
のである。[Means and effects for solving the problem] In order to meet the above-mentioned needs, the present inventor has made extensive studies and found that the methods using dielectric materials and semiconductor particles that have been proposed so far have no effect on the electrorheological effect. We have come to the conclusion that it is difficult to satisfy all of the requirements such as further improvement, reliably preventing electrophoresis from occurring under direct current flow, and ensuring sufficient stability. Therefore, in addition to the conventionally known dielectric materials and semiconductor particles, we conducted further studies to find particles that produce electrorheological effects.As a result, we found that carbonaceous particles obtained by heat-treating polyaniline do not contain water. The present invention was completed based on the finding that a new electrorheological fluid can be obtained by dispersing the electrorheological effect in an oily medium.
【0009】従って、本発明は、電気絶縁性を有する油
状媒体中に、ポリアニリン粉末を熱処理して得られた炭
素質粉体を分散してなることを特徴とする電気粘性流体
を提供するものである。Therefore, the present invention provides an electrorheological fluid characterized by dispersing carbonaceous powder obtained by heat treating polyaniline powder in an oily medium having electrical insulation properties. be.
【0010】以下、本発明につき更に詳しく説明すると
、本発明の電気粘性流体は、上述したように、電気絶縁
性を有する油状媒体中にポリアニリン粉末を熱処理して
得た炭素質粉体を分散させたもので、電気粘性効果を得
るための水の添加を必要としない非水系電気粘性流体で
ある。[0010] The present invention will be explained in more detail below. As mentioned above, the electrorheological fluid of the present invention is produced by dispersing carbonaceous powder obtained by heat-treating polyaniline powder in an oily medium having electrical insulation properties. It is a nonaqueous electrorheological fluid that does not require the addition of water to obtain the electrorheological effect.
【0011】上記ポリアニリン粉末は、アニリンを電気
的又は化学的に酸化重合させることにより得ることがで
き、この場合その手法にとくに制限はなく、アニリンに
重合するに至る電位を何らかの方法により与えてやれば
よい。具体的には、電気的酸化重合によりポリアニリン
を得る場合、アニリンモノマーを含む溶液中に作用極及
び対極となる一対の電極板を浸漬し、両極間にアニリン
の酸化電位以上の電圧を印加するか、またはアニリンが
重合するに十分な電圧が確保できるような条件の電流を
通電してやればよく、これにより作用極上にポリアニリ
ンが生成するものである。また、化学的酸化重合法では
、アニリンモノマーを含む溶液中に酸化還元電位がアニ
リンの重合電位程度となる酸化剤、例えば(NH4)2
S2O8、MnO2、PbO2、FeCl3などを投与
すればよい。[0011] The above polyaniline powder can be obtained by electrically or chemically oxidatively polymerizing aniline. In this case, there are no particular restrictions on the method, as long as a potential that leads to polymerization of aniline is applied by some method. Bye. Specifically, when polyaniline is obtained by electrolytic oxidation polymerization, a pair of electrode plates serving as a working electrode and a counter electrode are immersed in a solution containing an aniline monomer, and a voltage higher than the oxidation potential of aniline is applied between the two electrodes. Alternatively, a current may be applied under such conditions as to ensure a voltage sufficient to polymerize aniline, thereby producing polyaniline on the working electrode. In addition, in the chemical oxidative polymerization method, an oxidizing agent whose redox potential is about the polymerization potential of aniline is added to the solution containing the aniline monomer, such as (NH4)2.
S2O8, MnO2, PbO2, FeCl3, etc. may be administered.
【0012】ここで、ポリアニリンを電気的又は化学的
酸化重合により得る場合、重合原料のアニリンと共にH
BF4、H2SO4、HCl、HClO4などの酸を混
在させると、酸の負イオンがドーパントとして合成され
るポリアニリン中に取り込まれ、良導電性のポリアニリ
ンが得られることが知られている。例えば重合原料のア
ニリンをHBF4を混在させた状態で酸化重合して得ら
れるポリアニリンは通常下記式(A)〜(D)に示した
ように、ベンゾノイド=アミン状態(式A)、ベンゾノ
イド=アンモニウム状態(式B)、ドープ=セミキノン
ラジカル状態(式C)及びキノイド=ジイミン状態(式
D)の4種のポリアニリンが混在した状態になり、この
ようなドープ=セミキノンラジカル状態(式C)を含ん
だポリアニリンが良導電性を示すことが知られているが
、これらの混合比は最終的に電気粘性効果に特に影響す
ることはなく、本発明においては、いずれの混合比のも
のも使用することができる。Here, when polyaniline is obtained by electrical or chemical oxidative polymerization, H
It is known that when acids such as BF4, H2SO4, HCl, HClO4, etc. are mixed, the negative ions of the acids are incorporated as dopants into the synthesized polyaniline, resulting in polyaniline with good conductivity. For example, polyaniline obtained by oxidative polymerization of aniline as a polymerization raw material in the presence of HBF4 is usually in a benzonoid=amine state (formula A) or a benzonoid=ammonium state, as shown in the following formulas (A) to (D). (Formula B), doped = semiquinone radical state (Formula C), and quinoid = diimine state (Formula D), four types of polyaniline are mixed together, and such doped = semiquinone radical state (Formula C) is formed. Although it is known that polyaniline contained in polyaniline exhibits good conductivity, these mixing ratios do not particularly affect the final electrorheological effect, and in the present invention, any mixing ratio is used. be able to.
【0013】[0013]
【化1】[Chemical formula 1]
【0014】このようなポリアニリンの合成法としてよ
り具体的な例を挙げると、電気的酸化重合法によるポリ
アニリンの合成方法としては、作用極及び対極としてス
テンレススチール、白金、カーボン等の良導電性物質か
らなる板や多孔質材などを用い、これらをH2SO4,
HBF4等の酸及びアニリンモノマーを含む電解溶液中
に浸漬し、両極間に0.1〜100mA/cm2程度の
電流を通電して、作用極側にポリアニリンを重合析出さ
せる方法などが例示され、また化学的酸化重合法による
ポリアニリンの合成方法としては、酸化剤として過硫酸
アニモニウム[(NH4)2S2O8]0.5モル/リ
ットルをH2SO41モル/リットル及びアニリン0.
4モル/リットルを含む水溶液中に投与し、過硫酸アン
モニウムのもつ酸化還元電位2.0V(標準電極対比)
によりアニリンを酸化重合させ、ポリアニリンを重合析
出させる方法などが例示される。なお、このときの反応
は下記は反応式で表すことができる。To give a more specific example of such a method for synthesizing polyaniline, a method for synthesizing polyaniline by electrolytic oxidation polymerization uses a highly conductive material such as stainless steel, platinum, or carbon as a working electrode and a counter electrode. Using plates and porous materials made of H2SO4,
Examples include a method in which polyaniline is polymerized and precipitated on the working electrode side by immersing it in an electrolytic solution containing an acid such as HBF4 and an aniline monomer and passing a current of about 0.1 to 100 mA/cm2 between the two electrodes. A method for synthesizing polyaniline using a chemical oxidative polymerization method involves adding 0.5 mol/liter of ammonium persulfate [(NH4)2S2O8] as an oxidizing agent to 1 mol/liter of H2SO4 and 0.5 mol/liter of aniline.
Ammonium persulfate has a redox potential of 2.0 V (compared to standard electrode) when administered into an aqueous solution containing 4 mol/liter.
Examples include a method in which aniline is oxidatively polymerized and polyaniline is polymerized and precipitated. The reaction at this time can be expressed by the reaction formula below.
【0015】[0015]
【化2】[Chemical 2]
【0016】なお、上記方法により酸を混在させてポリ
アニリンを合成する際、酸の種類によって得られるポリ
アニリンの構造状態が異なり、例えばHBF4を用いた
場合はフィブリル状に、H2SO4を用いた場合には粒
状となり、また微粉状となる場合もある。本発明におい
ては、適宜な粉末化プロセスや造粒プロセスによって処
理することにより、これらのいずれのものも使用するこ
とができるが、特に合成時に適度な粒度分布を持つよう
な条件で重合を行うことが好ましい。また、この場合、
ポリアニリン粉末の粒度としては、特に制限されるもの
ではないが、平均粒径で0.05〜200μm、特に1
〜100μmとすることが好ましい。[0016] When polyaniline is synthesized by mixing acids by the above method, the structural state of the polyaniline obtained differs depending on the type of acid. For example, when HBF4 is used, it is fibrillar, and when H2SO4 is used, it is fibrillar. It may become granular or finely powdered. In the present invention, any of these can be used by processing through an appropriate powdering process or granulation process, but in particular, it is important to carry out polymerization under conditions that provide an appropriate particle size distribution during synthesis. is preferred. Also, in this case,
The particle size of the polyaniline powder is not particularly limited, but the average particle size is 0.05 to 200 μm, especially 1
It is preferable to set it to 100 micrometers.
【0017】次に、上述したように、このポリアニリン
を熱処理することにより炭素質粉体を得るが、この場合
の処理温度に特に制限はなく、必要な電気粘性効果と電
流値に応じて適宜設定されるが、通常は250〜800
℃、特に450〜600℃とすることが好ましい。処理
温度が250℃未満であると、ポリアニリンの合成条件
によっては、十分な電気粘性効果が得られない場合があ
り、一方800℃を超えると導電率が高くなり過ぎて電
流が流れ過ぎるようになってしまう場合がある。また、
処理温度以外の条件については、昇温速度、処理時間、
処理温度等のいずれの条件についても特に制限はなく、
適宜設定することができる。例えば、処理雰囲気に関し
ては、非酸化性雰囲気とすることが好ましいが、400
℃未満の処理温度においては酸化性雰囲気とすることも
でき、更に酸化性雰囲気と非酸化性雰囲気とを組み合わ
せることも可能である。なお、ポリアニリンを熱処理す
ることにより得られる炭素質粉体の残炭率は20〜80
%、特に25〜70%とすることが好ましい。Next, as described above, carbonaceous powder is obtained by heat-treating this polyaniline, but the treatment temperature in this case is not particularly limited and can be set as appropriate depending on the required electrorheological effect and current value. However, usually 250 to 800
The temperature is preferably 450 to 600°C. If the treatment temperature is less than 250°C, sufficient electrorheological effects may not be obtained depending on the polyaniline synthesis conditions, whereas if it exceeds 800°C, the conductivity becomes too high and too much current flows. There are cases where this happens. Also,
Conditions other than processing temperature include temperature increase rate, processing time,
There are no particular restrictions on any conditions such as processing temperature,
It can be set as appropriate. For example, regarding the processing atmosphere, it is preferable to use a non-oxidizing atmosphere;
At a processing temperature below .degree. C., an oxidizing atmosphere can be used, and it is also possible to combine an oxidizing atmosphere and a non-oxidizing atmosphere. In addition, the carbonaceous powder obtained by heat-treating polyaniline has a residual carbon percentage of 20 to 80
%, particularly preferably 25 to 70%.
【0018】本発明の電気粘性流体は、このようにして
得られた炭素質粉体を電気絶縁性を有する油状媒体に分
散したものであるが、この場合上記油状媒体としては、
特に制限はなく、シリコーン油、鉱物油、変圧器油、パ
ラフィン油、ハロゲン化芳香族油など電気絶縁性を有す
るものであればいずれのものも使用することができる。The electrorheological fluid of the present invention is obtained by dispersing the carbonaceous powder thus obtained in an oily medium having electrical insulation properties, and in this case, the oily medium is:
There are no particular limitations, and any oil having electrical insulation properties such as silicone oil, mineral oil, transformer oil, paraffin oil, and halogenated aromatic oil can be used.
【0019】また、分散条件に特に制限はないが、特に
分散時の炭素質粉体は、適度な粒度分布を有し、平均粒
径0.05〜200μm、特に1〜100μm程度であ
ることが好ましい。この場合、ポリアニリン粉末の粒度
を上記好適範囲に制御しておけば、通常は好適な平均粒
径を有する炭素質粉体が上記熱処理により得られるが、
熱処理により得られた炭素質物質の平均粒径が極端に小
さかったり、又は極端に大きかったりした場合には、適
宜な手段により造粒したり、粉末化したりすることがで
きる。Although there are no particular restrictions on the dispersion conditions, it is particularly important that the carbonaceous powder at the time of dispersion has an appropriate particle size distribution, with an average particle size of about 0.05 to 200 μm, particularly about 1 to 100 μm. preferable. In this case, if the particle size of the polyaniline powder is controlled within the above-mentioned suitable range, carbonaceous powder having a suitable average particle size can usually be obtained by the above-mentioned heat treatment.
If the average particle size of the carbonaceous material obtained by heat treatment is extremely small or extremely large, it can be granulated or powdered by appropriate means.
【0020】更に、炭素質粉体の分散量は、得られる電
気粘性流体の用途等により適宜設定され、必要とする粘
度変化量などに応じて適宜変更される。なお、分散方法
には特に制限はなく、炭素質粉体を均一に分散し得る乾
式の方法であればいずれの方法も採用することができる
。Furthermore, the amount of carbonaceous powder to be dispersed is appropriately set depending on the intended use of the obtained electrorheological fluid, and is appropriately changed depending on the required amount of viscosity change. Note that the dispersion method is not particularly limited, and any dry method that can uniformly disperse the carbonaceous powder can be employed.
【0021】[0021]
【実施例】以下、実施例,比較例を示して本発明を具体
的に説明するが、本発明は下記実施例に制限されるもの
ではない。EXAMPLES The present invention will be specifically explained below with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples.
【0022】[実施例1]アニリン0.4モル/リット
ル及びH2SO41.0モル/リットルを含む水溶液1
リットル中に過酸化アンモニウム0.5モルを投与し、
5時間撹拌して重合を行った。得られた懸濁液を濾過し
、固相分を乾燥してポリアニリン粉末40gを得た。[Example 1] Aqueous solution 1 containing 0.4 mol/liter of aniline and 1.0 mol/liter of H2SO4
administering 0.5 moles of ammonium peroxide in a liter;
Polymerization was carried out by stirring for 5 hours. The resulting suspension was filtered and the solid phase was dried to obtain 40 g of polyaniline powder.
【0023】このポリアニリン粉末を窒素雰囲気中、3
℃/分の昇温速度で530℃まで加熱し、1時間焼成処
理して、図1に示した粒度分布を有する残炭率68%の
炭素質粉体を得た。[0023] This polyaniline powder was heated in a nitrogen atmosphere for 3
The powder was heated to 530° C. at a temperature increase rate of ° C./min and fired for 1 hour to obtain a carbonaceous powder having a particle size distribution shown in FIG. 1 and a residual carbon content of 68%.
【0024】得られた炭素質粉体50gをシリコーン油
(東芝シリコーン(株)製 TSF451−10)1
50gに分散させて電気粘性流体を得た。50 g of the obtained carbonaceous powder was mixed with silicone oil (TSF451-10 manufactured by Toshiba Silicone Corporation) 1
An electrorheological fluid was obtained by dispersing it in 50 g.
【0025】この電気粘性流体について、電気粘性効果
の測定を行った。電気粘性効果は、二重円筒型粘度計を
使用し、内外円筒間に0−2kVの電圧を印加した時の
せん断速度366sec−1、温度25℃における粘度
で評価した。結果を表1に示す。The electrorheological effect of this electrorheological fluid was measured. The electrorheological effect was evaluated using a double cylindrical viscometer and the viscosity at a shear rate of 366 sec-1 and a temperature of 25° C. when a voltage of 0-2 kV was applied between the inner and outer cylinders. The results are shown in Table 1.
【0026】[実施例2]市販のアニリンブラック(東
洋色材工業(株)製 No.13アニリンブラック)
を窒素雰囲気中、3℃/分の昇温速度で480℃まで加
熱し、1時間焼成処理して、図2に示した粒度分布を有
する残炭率68%の炭素質粉体を得た。[Example 2] Commercially available aniline black (No. 13 aniline black manufactured by Toyo Shikizai Kogyo Co., Ltd.)
was heated to 480° C. at a temperature increase rate of 3° C./min in a nitrogen atmosphere and fired for 1 hour to obtain a carbonaceous powder having a particle size distribution shown in FIG. 2 and a residual carbon content of 68%.
【0027】得られた炭素質粉体50gをシリコーン油
(東芝シリコーン(株)製 TSF451−10)1
50gに分散させて電気粘性流体を調製し、実施例1と
同様の方法で電気粘性効果を測定した。結果を表1に示
す。50 g of the obtained carbonaceous powder was mixed with silicone oil (TSF451-10 manufactured by Toshiba Silicone Co., Ltd.) 1
An electrorheological fluid was prepared by dispersing it in 50 g, and the electrorheological effect was measured in the same manner as in Example 1. The results are shown in Table 1.
【0028】[比較例1]市販のアニリンブラック(東
洋色材工業(株)製 No.13アニリンブラック)
50gをそのままシリコーン油(東芝シリコーン(株)
製 TSF451−10)150gに分散させて電気
粘性流体を調製し、実施例1と同様の方法で電気粘性効
果を測定した。結果を表1に示す。[Comparative Example 1] Commercially available aniline black (No. 13 aniline black manufactured by Toyo Shikizai Kogyo Co., Ltd.)
50g directly into silicone oil (Toshiba Silicone Co., Ltd.)
An electrorheological fluid was prepared by dispersing it in 150 g of TSF451-10 (manufactured by TSF451-10), and the electrorheological effect was measured in the same manner as in Example 1. The results are shown in Table 1.
【0029】[比較例2]実施例1で製造したものと同
様のポリアニリン粉末50gを熱処理を行わずにそのま
まシリコーン油(東芝シリコーン(株)製 TSF4
51−10)150gに分散させて電気粘性流体を調製
し、実施例1と同様の方法で電気粘性効果を測定した。
結果を表1に示す。[Comparative Example 2] 50 g of polyaniline powder similar to that produced in Example 1 was directly mixed with silicone oil (TSF4 manufactured by Toshiba Silicone Co., Ltd.) without heat treatment.
51-10) An electrorheological fluid was prepared by dispersing it in 150 g, and the electrorheological effect was measured in the same manner as in Example 1. The results are shown in Table 1.
【0030】[0030]
【表1】
* 800Vを超えると測定不能なため、800Vで
測定した[Table 1] * Measurement was performed at 800V because it is impossible to measure above 800V.
【0031】表1の結果から、本発明の電気粘性流体が
良好な電気粘性効果を有することが確認された。From the results shown in Table 1, it was confirmed that the electrorheological fluid of the present invention has a good electrorheological effect.
【0032】[0032]
【発明の効果】以上説明したように、本発明の電気粘性
流体は、良好な電気粘性効果を有する全く新規な非水系
電気粘性流体である。As explained above, the electrorheological fluid of the present invention is a completely new non-aqueous electrorheological fluid having good electrorheological effects.
【図1】実施例1で用いた炭素質粉体の粒度分布を示す
グラフである。FIG. 1 is a graph showing the particle size distribution of carbonaceous powder used in Example 1.
【図2】実施例2で用いた炭素質粉体の粒度分布を示す
グラフである。FIG. 2 is a graph showing the particle size distribution of carbonaceous powder used in Example 2.
Claims (1)
リアニリン粉末を熱処理して得られた炭素質粉体を分散
してなることを特徴とする電気粘性流体。1. An electrorheological fluid comprising carbonaceous powder obtained by heat treating polyaniline powder dispersed in an oily medium having electrical insulation properties.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3151136A JPH04348192A (en) | 1991-05-27 | 1991-05-27 | Electro-viscous fluid |
| EP92304793A EP0516394A1 (en) | 1991-05-27 | 1992-05-27 | Electrorheological fluid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3151136A JPH04348192A (en) | 1991-05-27 | 1991-05-27 | Electro-viscous fluid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04348192A true JPH04348192A (en) | 1992-12-03 |
Family
ID=15512158
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3151136A Pending JPH04348192A (en) | 1991-05-27 | 1991-05-27 | Electro-viscous fluid |
Country Status (2)
| Country | Link |
|---|---|
| EP (1) | EP0516394A1 (en) |
| JP (1) | JPH04348192A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5536426A (en) * | 1993-05-21 | 1996-07-16 | Nippon Oil Company, Ltd. | Electrorheological fluid containing carbonaceous particles |
| KR100418914B1 (en) * | 2001-08-14 | 2004-02-14 | 한국과학기술원 | Process for Preparing Electrochemical Fluid Employing Polyaniline-coated Layered Silicate |
| CN100526367C (en) * | 2007-08-28 | 2009-08-12 | 厦门大学 | Method for preparing polyaniline nano thread |
| CN111498850B (en) * | 2020-04-26 | 2021-08-20 | 江南大学 | A kind of two-dimensional transition metal carbonitride and its preparation method and application |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE68904031T2 (en) * | 1988-08-29 | 1993-04-29 | Bridgestone Corp | ELECTROVISCOSE LIQUIDS. |
| GB8908825D0 (en) * | 1989-04-19 | 1989-06-07 | Block Hermann | Electrorheological fluid |
-
1991
- 1991-05-27 JP JP3151136A patent/JPH04348192A/en active Pending
-
1992
- 1992-05-27 EP EP92304793A patent/EP0516394A1/en not_active Withdrawn
Also Published As
| Publication number | Publication date |
|---|---|
| EP0516394A1 (en) | 1992-12-02 |
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