JP4851772B2 - Conductive magnetic fluid and its use - Google Patents
Conductive magnetic fluid and its use Download PDFInfo
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- JP4851772B2 JP4851772B2 JP2005312287A JP2005312287A JP4851772B2 JP 4851772 B2 JP4851772 B2 JP 4851772B2 JP 2005312287 A JP2005312287 A JP 2005312287A JP 2005312287 A JP2005312287 A JP 2005312287A JP 4851772 B2 JP4851772 B2 JP 4851772B2
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Description
本発明は、導電性磁性流体及びその用途に関する。さらに詳しくは、磁界に感応する磁性流体中に特定の微細な導電性炭素繊維を添加した導電性磁性流体、及びそれを用いたシール装置並びにアクチュエーターに関する。 The present invention relates to a conductive magnetic fluid and its use. More specifically, the present invention relates to a conductive magnetic fluid obtained by adding a specific fine conductive carbon fiber to a magnetic fluid sensitive to a magnetic field, and a seal device and an actuator using the same.
磁性流体とは、強磁性体粒子を溶媒中に均一に分散させたコロイド溶液であり、磁石を近づけると液全体が磁石に引き寄せられ、見かけ上液全体が磁性を帯びたように挙動する。さらに、磁界の印加で磁性流体から大きな力を誘起できる特長を磁性流体は有する。この特長を活かして、磁性流体は回転軸シールに利用されており、さらにダンパー、アクチュエーター、比重差選別、インクジェットプリンター等への応用が期待されている。磁性流体の代表的な製造方法としては、特開昭51−44579記載の方法が挙げられる。この方法は、硫酸第1鉄塩水溶液と硫酸第2鉄塩水溶液より調製したマグネタイト水スラリーに界面活性剤を添加し、水洗、乾燥後、有機溶媒に分散させて磁性流体を作製する方法である。 The magnetic fluid is a colloidal solution in which ferromagnetic particles are uniformly dispersed in a solvent, and when the magnet is brought closer, the entire liquid is attracted to the magnet, and the entire liquid behaves like a magnet. Furthermore, the magnetic fluid has a feature that a large force can be induced from the magnetic fluid by applying a magnetic field. Taking advantage of this feature, magnetic fluids are used for rotating shaft seals, and are expected to be applied to dampers, actuators, specific gravity sorting, ink jet printers, and the like. As a typical method for producing a magnetic fluid, there is a method described in JP-A-51-44579. In this method, a surfactant is added to a magnetite water slurry prepared from a ferrous sulfate aqueous solution and a ferric sulfate aqueous solution, washed with water, dried, and then dispersed in an organic solvent to produce a magnetic fluid. .
一般に磁性流体はその電気抵抗値が高いので、例えば磁気デイスク装置等のシール機構に用いた場合、その磁気デイスク装置等(以下、帯電体という)内に蓄積される静電気を除去するためにアース機構を設ける必要があった。磁性流体そのものに導電性が付与されていれば、アース機構を設けることなく帯電を防止できるようになる。
また、磁場制御エネルギー変換MHD(Magneto Hydro Dynamics)発電では、導電性の作動流体が磁界を横切ることによって生じる起電力を二つの電極でとりだす。この作動流体に導電性磁性流体を用いることが検討されている。
In general, a magnetic fluid has a high electric resistance value. Therefore, when used in a sealing mechanism of a magnetic disk device, for example, an earth mechanism is used to remove static electricity accumulated in the magnetic disk device (hereinafter referred to as a charged body). It was necessary to provide. If conductivity is imparted to the magnetic fluid itself, charging can be prevented without providing a ground mechanism.
In magnetic field control energy conversion MHD (Magneto Hydrodynamics) power generation, an electromotive force generated by a conductive working fluid crossing a magnetic field is taken out by two electrodes. The use of a conductive magnetic fluid as the working fluid has been studied.
このような導電性磁性流体として、特許文献1には、表面に第四級アンモニウム塩等の陽イオン性界面活性剤の層を被覆した強磁性体粒子を用いた磁性流体が提案されている。また特許文献2には三級アミンと脂肪酸とを組み合わせた導電性付与物資を溶剤に溶解し、導電性を付与した溶剤を用いた磁性流体が提案されている。また、特許文献3には、前記導電性付与物質として有機酸第四級ホスホニウム塩を用いた磁性流体が提案されている。
さらに特許文献4には、有機液体に、マグナタイト粉、ニッケル粉、コバルト粉などの強磁性粉末と、金粉などの導電性粉末とを分散させてなる磁性流体が開示されている。
As such a conductive magnetic fluid, Patent Document 1 proposes a magnetic fluid using ferromagnetic particles having a surface coated with a layer of a cationic surfactant such as a quaternary ammonium salt. Patent Document 2 proposes a magnetic fluid using a solvent imparted with conductivity by dissolving a conductivity-imparting material in which a tertiary amine and a fatty acid are combined in a solvent.
Further, Patent Document 4 discloses a magnetic fluid in which a ferromagnetic powder such as a magnetite powder, a nickel powder, or a cobalt powder and a conductive powder such as a gold powder are dispersed in an organic liquid.
しかしながら、磁性流体には下記のような問題点がある。すなわち、応答性の目安となる透磁率が低く、速い応答速度が得られないことが挙げられる。また、シールとして用いる場合、そのシール力が小さいことも挙げられる。これらの問題点が、用途の広がりの障害となっている。 However, the magnetic fluid has the following problems. That is, the magnetic permeability that is a measure of responsiveness is low, and a high response speed cannot be obtained. Moreover, when using as a seal | sticker, the sealing force is also mentioned small. These problems are obstacles to the spread of applications.
本発明は、速い応答速度と大きなトルクが得られ、さらに大きなシール力を誘起する導電性磁性流体を提供することを目的とする。さらに本発明は、上記導電性磁性流体を用いた、応答速度が速く、高トルクでシール力の優れたシール装置、及びアクチェーターを提供することを目的とする。 An object of the present invention is to provide a conductive magnetic fluid that can obtain a high response speed and a large torque and induce a larger sealing force. A further object of the present invention is to provide a sealing device and an actuator using the above-described conductive magnetic fluid, which has a high response speed, a high torque and an excellent sealing force.
本発明者らは上記問題点に鑑みて、磁性流体について鋭意研究した結果、流体中に特定の形状の導電性炭素繊維を添加し、流体中の導電性ネットワークを発達させることにより、上記目的を達成できることを見い出し、この知見に基づいて本発明を完成するに至った。 In view of the above problems, the present inventors have conducted intensive research on magnetic fluid, and as a result, the conductive carbon fiber having a specific shape is added to the fluid to develop the conductive network in the fluid. Based on this finding, the present invention has been completed.
すなわち、本発明によれば、
(1)少なくとも一種の溶剤、少なくとも一種の強磁性体粒子、及び少なくとも一種の炭素系導電性粒子を含む導電性磁性流体であって、
少なくとも一種の炭素系導電性粒子が、平均繊維径10〜500nm、平均アスペクト比30〜200の炭素繊維であることを特徴とする導電性磁性流体が提供される。
That is, according to the present invention,
(1) A conductive magnetic fluid comprising at least one solvent, at least one ferromagnetic particle, and at least one carbon-based conductive particle,
Provided is a conductive magnetic fluid, wherein the at least one carbon-based conductive particle is a carbon fiber having an average fiber diameter of 10 to 500 nm and an average aspect ratio of 30 to 200.
また、好適な態様として
(2)炭素繊維は、X線でのC0値が0.65nm〜0.68nmであり、かつ、その嵩密度を0.5g/cm3に圧縮したときの比抵抗が0.015Ωcm以下である(1)記載の導電性磁性流体。
(3)炭素繊維の表面が親水性を示すことを特徴とする(1)又は(2)に記載の導電性磁性流体。
(4)少なくとも一種の強磁性体粒子が、強磁性金属単体、強磁性金属合金、強磁性酸化物及び/又は強磁性窒化物の微粒子である(1)〜(3)のいずれかに記載の導電性磁性流体。
(5)少なくとも一種の強磁性体粒子が、
鉄、ニッケル又はコバルトの金属単体;
鉄、ニッケル及び/又はコバルトを含む合金;
鉄、ニッケル及び/又はコバルトを含む酸化物; 及び/又は
鉄、ニッケル及び/又はコバルトを含む窒化物の微粒子であることを特徴とする(1)〜(4)のいずれかに記載の導電性磁性流体。
(6)少なくとも一種の強磁性体粒子が、Ni−Fe合金、鉄、又はマグネタイトであることを特徴とする(1)〜(5)のいずれかに記載の導電性磁性流体。
(7)少なくとも1種の溶剤が、炭化水素溶媒、エステル系油、エーテル油、シリコーンオイル、及び/またはフッ素系オイルであることを特徴とする(1)〜(6)のいずれかに記載の導電性磁性流体。
As a preferred embodiment, (2) the carbon fiber has a C0 value in X-rays of 0.65 nm to 0.68 nm and a specific resistance when the bulk density is compressed to 0.5 g / cm 3. The conductive magnetic fluid according to (1), which is 0.015 Ωcm or less.
(3) The conductive magnetic fluid according to (1) or (2), wherein the surface of the carbon fiber is hydrophilic.
(4) The at least one ferromagnetic particle is a ferromagnetic metal simple substance, a ferromagnetic metal alloy, a ferromagnetic oxide and / or a ferromagnetic nitride fine particle according to any one of (1) to (3) Conductive magnetic fluid.
(5) At least one type of ferromagnetic particles
Simple metal of iron, nickel or cobalt;
Alloys containing iron, nickel and / or cobalt;
The oxide according to any one of (1) to (4), characterized in that it is an oxide containing iron, nickel and / or cobalt; and / or a nitride fine particle containing iron, nickel and / or cobalt. Magnetic fluid.
(6) The conductive magnetic fluid according to any one of (1) to (5), wherein the at least one ferromagnetic particle is a Ni—Fe alloy, iron, or magnetite.
(7) The solvent according to any one of (1) to (6), wherein the at least one solvent is a hydrocarbon solvent, ester oil, ether oil, silicone oil, and / or fluorine oil. Conductive magnetic fluid.
(8)少なくとも1種の溶剤が、鉱油、アルキルナフタレン、ポリアルファーオレフィン;フタル酸ブチル、セバチン酸ブチル;オリゴフェニレンオキサイド;シリコーンオイル;及び/またはフッ素系オイルであることを特徴とする(1)〜(7)のいずれかに記載の導電性磁性流体。
(9)炭素繊維が、導電性磁性流体中に0.1質量%以上30質量%以下含まれることを特徴とする(1)〜(8)のいずれかに記載の導電性磁性流体。
(10)強磁性体粒子が、導電性磁性流体中に3質量%以上80質量%以下含まれることを特徴とする(1)〜(9)のいずれかに記載の導電性磁性流体。
(11)25℃、無磁界状態における粘度が100mPa・sec以上100000mPa・sec以下である(1)〜(10)のいずれかに記載の導電性磁性流体。
(12)25℃において1,500エルステッドの磁界を印加したときの磁界方向の導電率が10−2S/cm以上であることを特徴とする(1)〜(11)のいずれかに記載の導電性磁性流体。
が提供される。
(8) The at least one solvent is mineral oil, alkylnaphthalene, polyalphaolefin; butyl phthalate, butyl sebacate; oligophenylene oxide; silicone oil; and / or fluorine oil (1) Conductive magnetic fluid according to any one of to (7).
(9) The conductive magnetic fluid according to any one of (1) to (8), wherein the carbon fiber is contained in the conductive magnetic fluid in an amount of 0.1% by mass to 30% by mass.
(10) The conductive magnetic fluid according to any one of (1) to (9), wherein the ferromagnetic particles are contained in the conductive magnetic fluid in an amount of 3% by mass to 80% by mass.
(11) The conductive magnetic fluid according to any one of (1) to (10), which has a viscosity of 100 mPa · sec to 100000 mPa · sec at 25 ° C. and no magnetic field.
(12) The conductivity in the direction of the magnetic field when a magnetic field of 1,500 oersted is applied at 25 ° C. is 10 −2 S / cm or more, according to any one of (1) to (11) Conductive magnetic fluid.
Is provided.
さらに本発明によれば、
(13)前記の導電性磁性流体を用いたシール装置。
(14)前記の導電性磁性流体を用いたアクチュエーター。
が提供される。
Furthermore, according to the present invention,
(13) A sealing device using the conductive magnetic fluid.
(14) An actuator using the conductive magnetic fluid.
Is provided.
本発明の導電性磁性流体は、導電性炭素粒子として、微細な炭素繊維を用いることにより、磁界に対して速い応答速度と大きなトルクが得られ、これによって大きなシール力が誘起される。さらに、この導電性磁性流体を用いることにより、応答速度が速く、高トルクでシール力の優れたシール装置及びアクチェーターが得られた。 The conductive magnetic fluid of the present invention uses a fine carbon fiber as the conductive carbon particles, whereby a fast response speed and a large torque are obtained with respect to a magnetic field, thereby inducing a large sealing force. Furthermore, by using this conductive magnetic fluid, a sealing device and an actuator having a high response speed, a high torque and an excellent sealing force were obtained.
本発明の導電性磁性流体は、少なくとも一種の溶剤、少なくとも一種の強磁性体粒子、及び少なくとも一種の炭素系導電性粒子を含むものである。そして、本発明は、前記少なくとも一種の炭素系導電性粒子が平均繊維径10〜500nm、平均アスペクト比30〜200の炭素繊維を含む導電性磁性流体である。 The conductive magnetic fluid of the present invention contains at least one solvent, at least one ferromagnetic particle, and at least one carbon-based conductive particle. And this invention is an electroconductive magnetic fluid in which the said at least 1 type of carbon type electroconductive particle contains carbon fiber with an average fiber diameter of 10-500 nm, and an average aspect-ratio of 30-200.
(炭素系導電性粒子)
本発明の導電性磁性流体を構成する炭素系導電性粒子は炭素繊維である。
この炭素繊維は、平均繊維径が10〜500nm、好ましくは20〜140nmである。炭素繊維は、その繊維径のバラツキが少ないものが好ましい。繊維径のばらつきは平均繊維径の±20%の範囲に全繊維の65%(本数基準)以上含まれることが好ましく、70%(本数基準)以上含まれることがより好ましく、75%以上(本数基準)含まれることが特に好ましい。この定義は、例えば平均繊維径が100nmの場合、80〜120nmの繊維径を有する炭素繊維の本数が全炭素繊維の本数の65%以上であることを示す。
本発明に用いる炭素繊維は、さらに平均アスペクト比が30〜200の範囲にある。
(Carbon-based conductive particles)
The carbon-based conductive particles constituting the conductive magnetic fluid of the present invention are carbon fibers.
This carbon fiber has an average fiber diameter of 10 to 500 nm, preferably 20 to 140 nm. The carbon fiber is preferably one having little variation in the fiber diameter. The variation in fiber diameter is preferably included in the range of ± 20% of the average fiber diameter by 65% (number basis) or more of all fibers, more preferably 70% (number basis) or more, and 75% or more (number) It is particularly preferred that it be included. For example, when the average fiber diameter is 100 nm, this definition indicates that the number of carbon fibers having a fiber diameter of 80 to 120 nm is 65% or more of the total number of carbon fibers.
The carbon fibers used in the present invention further have an average aspect ratio in the range of 30 to 200.
本発明に用いる炭素繊維は、嵩密度が好ましくは0.030g/cm3以下であり、より好ましくは0.010g/cm3以下である。嵩密度が0.030g/cm3を超える炭素繊維では、磁性流体の導電性向上効果が小さくなる傾向にある。
なお、嵩密度は、炭素繊維を1000℃にて15分間アルゴン雰囲気中で加熱し、ミキサー(ナショナル製MX−X62)にて1分間解砕し、該解砕物をメスシリンダーに入れ秤量し、震動機(ヤマト製試験管タッチミキサーMT−31)で1分間震動させ、解砕物の見かけ体積を測定し、秤量値と見かけ体積から求めた値である。
Carbon fiber used in the present invention, the bulk density is preferably at 0.030 g / cm 3 or less, more preferably 0.010 g / cm 3 or less. Carbon fibers having a bulk density of more than 0.030 g / cm 3 tend to reduce the conductivity improvement effect of the magnetic fluid.
The bulk density was determined by heating the carbon fiber at 1000 ° C. for 15 minutes in an argon atmosphere, crushing it with a mixer (National MX-X62) for 1 minute, placing the crushed material in a graduated cylinder and weighing it. This is a value obtained from a weighed value and an apparent volume by oscillating for 1 minute with a machine (Yamato test tube touch mixer MT-31), measuring the apparent volume of the crushed material.
本発明に用いる炭素繊維は、その比抵抗が0.015Ωcm以下であることが好ましい。比抵抗0.015Ωcm以下の炭素繊維を用いると、ペースト作製時の樹脂との複合において、2質量%程度の添加で電気伝導性が向上する。なお、比抵抗は、炭素繊維を嵩密度0.5g/cm3に圧密したときの圧密体について測定した値である。 The carbon fiber used in the present invention preferably has a specific resistance of 0.015 Ωcm or less. When a carbon fiber having a specific resistance of 0.015 Ωcm or less is used, the electrical conductivity is improved by adding about 2% by mass in the composite with the resin at the time of preparing the paste. In addition, specific resistance is the value measured about the compacted body when carbon fiber is compacted by the bulk density of 0.5 g / cm < 3 >.
本発明に用いる炭素繊維は、その製法によって特に制限されないが、遷移金属化合物と炭素源を気化させ、反応器内に噴射して、熱分解反応させることにより得ることができる、いわゆる気相法炭素繊維が好ましい。 The carbon fiber used in the present invention is not particularly limited by its production method, but it can be obtained by vaporizing a transition metal compound and a carbon source, and injecting the carbon fiber into a reactor to cause a thermal decomposition reaction, so-called vapor phase carbon. Fiber is preferred.
炭素繊維の原料となる炭素源(有機化合物)は、気化するものならいずれも使用可能であるが、より低い温度で気化するものが望ましい。具体的にはベンゼン、トルエン、キシレン等の芳香族化合物類;ヘキサン、ヘプタン等の直鎖状の炭化水素類;シクロヘキサン等の環式炭化水素類;メタノール、メタノール等のアルコール類;揮発油、灯油などが挙げられる。これらの中でも芳香族化合物が望ましく、ベンゼンが最も望ましい。これらの炭素源は1種を単独で用いてもよいし、2種類以上を混合して用いてもよい。 Any carbon source (organic compound) that can be used as a raw material for carbon fiber can be used as long as it vaporizes, but it is desirable that the carbon source vaporizes at a lower temperature. Specifically, aromatic compounds such as benzene, toluene and xylene; linear hydrocarbons such as hexane and heptane; cyclic hydrocarbons such as cyclohexane; alcohols such as methanol and methanol; volatile oil and kerosene Etc. Of these, aromatic compounds are desirable, and benzene is most desirable. These carbon sources may be used individually by 1 type, and 2 or more types may be mixed and used for them.
触媒となる遷移金属化合物としては、第4〜10族の遷移金属を含む有機金属化合物や無機化合物が適する。中でもFe、Ni、及びCoからなる群から選ばれる遷移金属を有する有機金属化合物が好ましい。本発明では、気化した状態で反応させるため、蒸気圧の高いもの、具体的には150℃での蒸気圧が133Pa(1mmHg)以上のものを用いることが好ましい。蒸気圧の高いものとしては、フェロセン、ニッケロセン等が挙げられる。 As the transition metal compound serving as a catalyst, an organometallic compound or an inorganic compound containing a Group 4-10 transition metal is suitable. Among these, an organometallic compound having a transition metal selected from the group consisting of Fe, Ni, and Co is preferable. In the present invention, since the reaction is performed in a vaporized state, it is preferable to use one having a high vapor pressure, specifically, a vapor pressure at 150 ° C. of 133 Pa (1 mmHg) or more. Examples of those having a high vapor pressure include ferrocene and nickelocene.
遷移金属化合物の濃度を調整することにより、生成する繊維の径、長さ、粒子の含有量を制御することが可能である。例えば、繊維径80nm以上の繊維を製造するためには、フェロセン濃度で炭素源の1〜5質量%とすることが好ましく、2〜4質量%がさらに好ましい。この範囲の濃度であれば、繊維径等の制御が容易である。また、原料に硫黄源を添加することにより生産性を更に向上させることが可能である。硫黄源としては、気化するものならいずれも使用可能であるが、蒸気圧の高いものが望ましく、50℃での蒸気圧が10mmHg以上のものが望ましい。例えば、チオフェン等の有機硫黄化合物、硫化水素等の無機硫黄化合物が挙げられ、特にチオフェンが望ましい。これらの硫黄源は1種を単独で用いてもよいし、2種類以上を混合して用いてもよい。 By adjusting the concentration of the transition metal compound, it is possible to control the diameter, length, and particle content of the produced fiber. For example, in order to produce a fiber having a fiber diameter of 80 nm or more, the ferrocene concentration is preferably 1 to 5% by mass of the carbon source, and more preferably 2 to 4% by mass. If the concentration is within this range, the fiber diameter and the like can be easily controlled. In addition, productivity can be further improved by adding a sulfur source to the raw material. Any sulfur source can be used as long as it vaporizes, but a high vapor pressure is desirable, and a vapor pressure at 50 ° C. of 10 mmHg or more is desirable. Examples thereof include organic sulfur compounds such as thiophene and inorganic sulfur compounds such as hydrogen sulfide, and thiophene is particularly desirable. These sulfur sources may be used individually by 1 type, and may mix and use 2 or more types.
本発明においては、上記の炭素源、遷移金属化合物及び任意成分としての硫黄源を気化した状態で反応器に噴射し反応させる。この際、炭素源、遷移金属化合物及び硫黄源をそれぞれ個別に気化し、混合してから、反応器に噴射することも可能だが、炭素源、遷移金属化合物及び硫黄源からなる原料液を調製し、これを気化して反応器に噴射する方法が好ましい。
気化した原料を反応器に噴射することにより、加熱効率が高くなり、原料の熱分解が促進され、炭素繊維の収率が向上する。またバラツキの小さな繊維径を有する炭素繊維を得ることができる。
In the present invention, the above carbon source, transition metal compound, and sulfur source as an optional component are vaporized into a reactor and reacted. At this time, it is possible to vaporize and mix the carbon source, transition metal compound and sulfur source separately, and then inject into the reactor, but prepare a raw material liquid consisting of the carbon source, transition metal compound and sulfur source. A method of vaporizing this and injecting it into the reactor is preferred.
By injecting the vaporized raw material into the reactor, the heating efficiency is increased, the thermal decomposition of the raw material is promoted, and the yield of carbon fiber is improved. Also, carbon fibers having a small variation in fiber diameter can be obtained.
本発明に好適な気相法炭素繊維の製造方法のフローを図1に示す。
原料液(1)は、送液ポンプ(図示せず)により、気化器(3)に導入され、原料ガスとされる。原料ガスの組成を安定させるためには原料液の全量を気化することが望ましい。気化器は原料液が分解しない範囲で原料が完全に蒸発するように加熱される。気化器の温度は、好ましくは200〜700℃、更に好ましくは350〜550℃である。原料液をスプレーノズルにより気化器壁に吹き付けるようにすると原料の気化が効率的に行われる。気化器内へは原料ガスの供給速度を調整するためにキャリヤガス(2a)を導入できるが、キャリアガスの流量はできるだけ少ない方が気化器のヒータにかかる負担が少なく好ましい。
FIG. 1 shows a flow of a method for producing vapor grown carbon fiber suitable for the present invention.
The raw material liquid (1) is introduced into the vaporizer (3) by a liquid feed pump (not shown) to be a raw material gas. In order to stabilize the composition of the raw material gas, it is desirable to vaporize the entire amount of the raw material liquid. The vaporizer is heated so that the raw material is completely evaporated as long as the raw material liquid is not decomposed. The temperature of the vaporizer is preferably 200 to 700 ° C, more preferably 350 to 550 ° C. When the raw material liquid is sprayed onto the vaporizer wall by the spray nozzle, the raw material is efficiently vaporized. The carrier gas (2a) can be introduced into the vaporizer in order to adjust the feed rate of the raw material gas, but it is preferable that the carrier gas flow rate be as small as possible because the burden on the heater of the vaporizer is small.
気化器を出た原料ガスにキャリアガス(2b)を混合する。キャリアガスは水素ガスをはじめとする還元性のガスを含んでいることが好ましい。還元性のガスを用いることによって遷移金属化合物の触媒活性が高くなり、失活し難くなる。キャリアガスの量は炭素源である有機化合物1.0モルに対して1〜100モルが適当である。原料ガスとキャリアガスとは混合器(スタティックミキサ(STP))(4)で均一混合される。均一混合することによって分散性の良い炭素繊維を製造することができる。 The carrier gas (2b) is mixed with the raw material gas exiting the vaporizer. The carrier gas preferably contains a reducing gas such as hydrogen gas. By using a reducing gas, the catalytic activity of the transition metal compound is increased and it is difficult to deactivate. The amount of the carrier gas is suitably 1 to 100 mol with respect to 1.0 mol of the organic compound as the carbon source. The source gas and the carrier gas are uniformly mixed by a mixer (static mixer (STP)) (4). By uniformly mixing, a carbon fiber with good dispersibility can be produced.
前記原料ガスとキャリアガスとの混合ガスを反応器(5)へ噴射する。これにより原料ガスが熱分解され、炭素繊維が生成する。反応器内の温度は800〜1300℃であり、好ましくは900〜1250℃である。反応器は1300℃の反応熱に耐える材料、例えばアルミナ、ジルコニア、マグネシア、窒化珪素、炭化珪素などからなるものを用いることができる。反応器としては管状のものが好ましい。管状反応器(反応管)の加熱は、管の外側にヒーターを設置して行う。原料の滞留時間は、原料が充分に分解するまで長くすることで収率が向上する。具体的には1250℃で2〜10秒、好ましくは4〜6秒が望ましい。 A mixed gas of the source gas and the carrier gas is injected into the reactor (5). As a result, the raw material gas is thermally decomposed to produce carbon fibers. The temperature in the reactor is 800 to 1300 ° C, preferably 900 to 1250 ° C. The reactor can be made of a material that can withstand the heat of reaction at 1300 ° C., such as alumina, zirconia, magnesia, silicon nitride, silicon carbide and the like. A tubular reactor is preferable. The tubular reactor (reaction tube) is heated by installing a heater on the outside of the tube. The yield is improved by increasing the residence time of the raw material until the raw material is sufficiently decomposed. Specifically, it is desirable that the temperature is 1250 ° C. for 2 to 10 seconds, preferably 4 to 6 seconds.
上記熱分解反応により得られた炭素繊維は、そのままでも使用できるが、800〜2000℃程度で加熱して不純物を除去したり、2000℃以上で加熱して結晶性を向上させ、黒鉛化させることもできる。本発明では2000℃以上で加熱処理することにより、黒鉛化した炭素繊維を用いた方が、高導電性となり、また不純物も少なく、安定性も増す為好ましい。黒鉛化した炭素繊維は、X線回折測定により得られるC0値で表される黒鉛化度が0.65〜0.68nmであることが好ましい。 The carbon fiber obtained by the pyrolysis reaction can be used as it is, but it is heated at about 800 to 2000 ° C. to remove impurities, or heated at 2000 ° C. or higher to improve crystallinity and graphitize. You can also. In the present invention, it is preferable to use graphitized carbon fiber by heat treatment at 2000 ° C. or higher because it becomes highly conductive, has few impurities, and increases stability. The graphitized carbon fiber preferably has a graphitization degree represented by a C0 value obtained by X-ray diffraction measurement of 0.65 to 0.68 nm.
また、炭素繊維は、マトリックスに対する濡れ性及びマトリックスへの分散性を向上させ且つ界面強度を強化させるために、表面を改質し、親水性を示すようにしたものであることがよい。表面改質法としては表面酸化法が好ましい。表面酸化法は、例えば、炭素繊維と酸化性ガスとを共存させて加熱する方法、酸化性液体に炭素繊維を浸漬し、必要に応じて浸漬状態で加熱する方法により行うことができる。これら表面酸化法のうち炭素繊維を空気中で300〜800℃で加熱する方法が簡便であることから望ましい。 Further, the carbon fiber is preferably one having a modified surface to show hydrophilicity in order to improve wettability to the matrix, dispersibility in the matrix, and enhance interfacial strength. A surface oxidation method is preferred as the surface modification method. The surface oxidation method can be performed by, for example, a method of heating in the presence of carbon fiber and an oxidizing gas, or a method of immersing the carbon fiber in an oxidizing liquid and heating in an immersed state as necessary. Among these surface oxidation methods, a method of heating carbon fibers at 300 to 800 ° C. in air is desirable because it is simple.
本発明の導電性磁性流体に用いることのできる炭素系導電性粒子としては、上記炭素繊維単独ではなく、他の導電性粒子を添加してもよい。上記炭素繊維は比較的低添加量でも十分な高導電性を発現することができるが、より高い導電性を望んでも炭素繊維は嵩高いために高添加量にすることが難しい。そこで、他の嵩の低い塊状または球状の炭素系導電性粒子を併用することによって、より高い導電性を発現させることができる。炭素繊維と塊状または球状の導電性粒子との併用は塊状または球状導電性粒子を高濃度で用いる場合の沈降も抑えることができ、両者の特徴が効果的に発揮されるため好ましい。 As the carbon-based conductive particles that can be used in the conductive magnetic fluid of the present invention, other conductive particles may be added instead of the carbon fiber alone. The carbon fiber can exhibit a sufficiently high conductivity even with a relatively low addition amount, but it is difficult to increase the addition amount because the carbon fiber is bulky even if higher conductivity is desired. Therefore, higher conductivity can be expressed by using other low-bulk massive or spherical carbon-based conductive particles in combination. The combined use of carbon fibers and massive or spherical conductive particles is preferable because sedimentation in the case of using massive or spherical conductive particles at a high concentration can be suppressed, and the characteristics of both are effectively exhibited.
本発明において炭素繊維と併用できる塊状または球状の炭素系導電性粒子は特に限定されるものではなく、カーボンブラック、天然黒鉛粒子、人造黒鉛粒子等の炭素粒子が挙げられる。これら塊状または球状炭素系導電性粒子の平均粒径は、分散、粘度、作業性を考慮すると、0.1〜10μmが好ましく、0.2〜3μmがさらに好ましい。なお、平均粒径は、レーザ散乱型流動分布測定装置等で測定することができる。 In the present invention, the massive or spherical carbon-based conductive particles that can be used in combination with the carbon fiber are not particularly limited, and examples thereof include carbon particles such as carbon black, natural graphite particles, and artificial graphite particles. The average particle size of these massive or spherical carbon-based conductive particles is preferably 0.1 to 10 μm, and more preferably 0.2 to 3 μm in consideration of dispersion, viscosity, and workability. The average particle diameter can be measured with a laser scattering type flow distribution measuring device or the like.
炭素繊維と他の塊状または球状の炭素系導電性粒子とを併用する場合、その比率は特に限定されないが、質量比で、塊状または球状の炭素系導電性粒子100質量部に対して、炭素繊維を好ましくは100〜500質量部、より好ましくは200〜400質量部である。 When the carbon fiber and other massive or spherical carbon-based conductive particles are used in combination, the ratio is not particularly limited, but the carbon fiber is 100 mass parts of the massive or spherical carbon-based conductive particles in mass ratio. Is preferably 100 to 500 parts by mass, more preferably 200 to 400 parts by mass.
本発明の導電性磁性流体を製造する際に、炭素繊維および/または他の炭素系導電性粒子の分散性を向上させるために分散剤やカップリング剤を添加使用してもよい。
分散剤は特に限定されないが、例えば、パルミチン酸、ステアリン酸等の高炭素数飽和脂肪酸及びその金属塩;オレイン酸、リノレン酸等の高炭素数不飽和脂肪酸及びその金属塩が挙げられる。これら分散剤の配合量は、炭素系導電性粒子100質量部に対して一般に1〜100質量部である。分散剤の配合量が1質量部未満であれば、炭素繊維および/または他の導電性粒子の分散性に効果が少なく、また、100質量部を超えると導電性磁性流体の安定性を損なう場合がある。
In producing the conductive magnetic fluid of the present invention, a dispersant or a coupling agent may be added and used to improve the dispersibility of carbon fibers and / or other carbon-based conductive particles.
Although a dispersing agent is not specifically limited, For example, high carbon number saturated fatty acids, such as palmitic acid and a stearic acid, and its metal salt; High carbon number unsaturated fatty acids, such as oleic acid and linolenic acid, and its metal salt are mentioned. The blending amount of these dispersants is generally 1 to 100 parts by mass with respect to 100 parts by mass of the carbon-based conductive particles. If the blending amount of the dispersant is less than 1 part by mass, the dispersibility of the carbon fibers and / or other conductive particles is less effective, and if it exceeds 100 parts by mass, the stability of the conductive magnetic fluid is impaired. There is.
カップリング剤としては、ビニルメトキシシラン、ビニルトリエトキシシラン、ビニルトリス(β―メトキシエトキシ)シラン等のシラン系カップリング剤や、チタネート系カップリング剤、アルミネート系カップリング剤等が挙げられる。これらカップリング剤の配合量は、炭素系導電性粒子100質量部に対して、30質量部以下の添加量で添加することが好ましい。添加量が多すぎると、分散剤同様、導電性磁性流体の安定性を損なう場合がある。 Examples of the coupling agent include silane coupling agents such as vinylmethoxysilane, vinyltriethoxysilane, and vinyltris (β-methoxyethoxy) silane, titanate coupling agents, and aluminate coupling agents. The amount of these coupling agents added is preferably 30 parts by mass or less with respect to 100 parts by mass of the carbon-based conductive particles. If the amount added is too large, the stability of the conductive magnetic fluid may be impaired as in the case of the dispersant.
(強磁性体粒子)
本発明の導電性磁性流体を構成する強磁性体粒子としては、強磁性金属単体、強磁性金属合金、強磁性酸化物及び/又は強磁性窒化物の微粒子が挙げられる。具体的には鉄、ニッケル又はコバルトの金属単体の微粒子;鉄、ニッケル及び/又はコバルトを含む合金の微粒子;鉄、ニッケル及び/又はコバルトを含む酸化物の微粒子;及び/又は鉄、ニッケル及び/又はコバルトを含む窒化物の微粒子が挙げられる。さらに、サマリウム、ネオジム、セリウムなどの希土類金属を含む磁性粒子を挙げることができる。これらの中で、磁性が比較的大きく、取り扱いが容易という観点で、鉄、コバルト、ニッケル、Ni−Fe合金などの金属磁性粒子やフェライトやマグネタイトのような金属酸化物磁性粒子などが好ましい。なお、本発明において、磁性とは磁界に感応することであり、例えば磁石に引きつけられることを意味する。
(Ferromagnetic particles)
Examples of the ferromagnetic particles constituting the conductive magnetic fluid of the present invention include fine particles of a ferromagnetic metal alone, a ferromagnetic metal alloy, a ferromagnetic oxide and / or a ferromagnetic nitride. Specifically, fine particles of simple metal such as iron, nickel or cobalt; fine particles of alloy containing iron, nickel and / or cobalt; fine particles of oxide containing iron, nickel and / or cobalt; and / or iron, nickel and / or Or the nitride fine particle containing cobalt is mentioned. Furthermore, the magnetic particle containing rare earth metals, such as samarium, neodymium, and cerium, can be mentioned. Among these, metal magnetic particles such as iron, cobalt, nickel, and Ni—Fe alloy and metal oxide magnetic particles such as ferrite and magnetite are preferable from the viewpoint of relatively large magnetism and easy handling. In the present invention, magnetism means to be sensitive to a magnetic field, for example, to be attracted to a magnet.
本発明に用いられる強磁性体粒子は、その粒径が0.003〜200μmであることが好ましい。粒径が0.003μm未満では磁性を弱くなる傾向になり、200μmを超えると流体中での分散性が低下する傾向になる。本発明に用いる強磁性体粒子には硬質磁性体粒子と軟質磁性体粒子とがある。硬質磁性体粒子では0.003〜0.5μm、軟質磁性体粒子では0.1〜200μmが好ましく用いられる。非常に大きな力を得ようとする場合は、粒径が1〜100μmの軟質磁性体粒子が好ましく用いられる。 The ferromagnetic particles used in the present invention preferably have a particle size of 0.003 to 200 μm. When the particle size is less than 0.003 μm, the magnetism tends to be weakened, and when it exceeds 200 μm, the dispersibility in the fluid tends to decrease. The ferromagnetic particles used in the present invention include hard magnetic particles and soft magnetic particles. 0.003 to 0.5 μm is preferably used for hard magnetic particles, and 0.1 to 200 μm is preferably used for soft magnetic particles. When trying to obtain a very large force, soft magnetic particles having a particle diameter of 1 to 100 μm are preferably used.
(溶剤)
本発明の導電性磁性流体を構成する溶剤は特に限定されないが、大気中、低温及び高温で安定であるものが好ましい。本発明に好適な溶剤は、沸点が好ましくは150〜700℃(常圧)、より好ましくは200〜650℃(常圧)であり、且つ粘度が好ましくは10〜5000mPa・S(40℃)、より好ましくは50〜3000mPa・S(40℃)の液体である。溶剤としては、鉱油、アルキルナフタレン、ポリアルファーオレフィンなどの炭化水素溶媒;フタル酸ブチル、セバチン酸ブチルなどのエステル系油;オリゴフェニレンオキサイドなどのエーテル油;シリコーンオイル、フッ素系オイルなどが挙げられる。
(solvent)
Although the solvent which comprises the electroconductive magnetic fluid of this invention is not specifically limited, What is stable in air | atmosphere, low temperature and high temperature is preferable. The solvent suitable for the present invention has a boiling point of preferably 150 to 700 ° C. (normal pressure), more preferably 200 to 650 ° C. (normal pressure), and a viscosity of preferably 10 to 5000 mPa · S (40 ° C.), More preferably, the liquid is 50 to 3000 mPa · S (40 ° C.). Examples of the solvent include hydrocarbon solvents such as mineral oil, alkylnaphthalene and polyalphaolefin; ester oils such as butyl phthalate and butyl sebacate; ether oils such as oligophenylene oxide; silicone oils and fluorine oils.
(導電性磁性流体)
本発明の導電性磁性流体は磁界のない状態では、流動性のある粘性液体である。無磁界状態での好ましい粘度は25℃で100mPa・sec以上100000mPa・sec以下である。粘度が低いと磁界のない状態において粒子が分離しやすい。逆に粘度が高いと、取り扱いが難しく、応答性が低くなる傾向になる。
(Conductive magnetic fluid)
The conductive ferrofluid of the present invention is a fluid viscous liquid in the absence of a magnetic field. A preferred viscosity in the absence of a magnetic field is 100 mPa · sec or more and 100000 mPa · sec or less at 25 ° C. When the viscosity is low, particles are easily separated in the absence of a magnetic field. Conversely, if the viscosity is high, handling tends to be difficult and responsiveness tends to be low.
本発明の導電性磁性流体は、25℃、1,500エルステッドの磁界を印加したときに磁界方向の導電率が10−2S/cm以上であることが好ましい。10−2S/cmより低いと炭素繊維の配向が不十分であり、応答速度の向上効果が得がたい傾向になる。 The conductive magnetic fluid of the present invention preferably has a conductivity in the magnetic field direction of 10 −2 S / cm or more when a magnetic field of 1,500 oersted is applied at 25 ° C. If it is lower than 10 −2 S / cm, the orientation of the carbon fibers is insufficient, and the effect of improving the response speed tends to be difficult to obtain.
本発明の導電性磁性流体は、強磁性体粒子と溶剤との質量比が好ましくは1/99〜90/10、より好ましくは5/95〜60/40である。溶剤が少ないと磁性流体の粘度が増大し、流体としての機能が損なわれる傾向になる。逆に溶剤が多いと磁性効果を低くなる傾向になる。また、本発明の効果を損なわない範囲で、界面活性剤のような添加剤を配合してもよい。 In the conductive magnetic fluid of the present invention, the mass ratio of the ferromagnetic particles to the solvent is preferably 1/99 to 90/10, more preferably 5/95 to 60/40. When there is little solvent, the viscosity of a magnetic fluid will increase and it will become the tendency for the function as a fluid to be impaired. On the other hand, when the amount of the solvent is large, the magnetic effect tends to be lowered. Moreover, you may mix | blend additives, such as surfactant, in the range which does not impair the effect of this invention.
本発明の導電性磁性流体は、炭素繊維の量が導電性磁性流体中に好ましくは0.1質量%以上30質量%以下、より好ましくは0.1質量%以上20質量%以下、特に好ましくは0.5質量%以上15質量%以下である。炭素繊維の量が少ないと導電性が低下傾向になり、逆に多いと磁性流体の粘度が増大する傾向になる。また、強磁性体粒子は導電性磁性流体中に3質量%以上80質量%以下含まれていることが好ましい。 In the conductive magnetic fluid of the present invention, the amount of carbon fibers in the conductive magnetic fluid is preferably 0.1% by mass to 30% by mass, more preferably 0.1% by mass to 20% by mass, and particularly preferably. It is 0.5 mass% or more and 15 mass% or less. If the amount of carbon fiber is small, the conductivity tends to decrease, and conversely if it is large, the viscosity of the magnetic fluid tends to increase. The ferromagnetic particles are preferably contained in the conductive magnetic fluid in an amount of 3% by mass to 80% by mass.
(用途)
本発明の導電性磁性流体は、エンジンマウント、ショックアブソーバーなどの減衰装置、クラッチ、トルクコンバーター、ブレーキシステム、バルブ、ダンパー、サスペンション、アクチュエーター、バイブレーター、インクジェットプリンター、シール、比重差選別、軸受け、研磨、パッキン、制御弁、防振材料等の用途に利用できる。
(Use)
The conductive magnetic fluid of the present invention includes an engine mount, a damping device such as a shock absorber, a clutch, a torque converter, a brake system, a valve, a damper, a suspension, an actuator, a vibrator, an inkjet printer, a seal, a specific gravity selection, a bearing, a polishing, It can be used for applications such as packing, control valves, and vibration isolation materials.
特に、本発明の高導電性で大きな磁性を有する導電性磁性流体を用いることにより、高トルクでシール性が優れ、安定な、ハードディスクドライブ等に用いられるシール装置を得ることができる。また、本発明の導電性磁性流体は速い応答速度で動作できるため、各種アクチュエーターにも好適である。 In particular, by using the conductive magnetic fluid having high conductivity and large magnetism according to the present invention, it is possible to obtain a high-torque, excellent sealing property, and a stable sealing device used for a hard disk drive or the like. Further, since the conductive magnetic fluid of the present invention can operate at a high response speed, it is also suitable for various actuators.
以下に、本発明を実施例により具体的に説明するが、本発明はそれらに限定されるものではない。
製造例
(気相法炭素繊維の製造)
図1にフローを示した装置を用いて気相法炭素繊維を製造した。
反応管(5)としては、頂部に原料ガス供給ノズルを取り付けた縦型加熱炉(内径370mm、長さ2000mm)を用いた。
フェロセン0.5kgとチオフェン0.13kgをベンゼン14kgに溶解して原料液を調製した。原料液中のフェロセンの割合は3.5質量%、チオフェンの割合は0.9質量%であった。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples.
Production example (production of vapor grown carbon fiber)
Vapor grown carbon fiber was produced using the apparatus shown in the flow in FIG.
As the reaction tube (5), a vertical heating furnace (inner diameter: 370 mm, length: 2000 mm) having a source gas supply nozzle attached to the top was used.
A raw material solution was prepared by dissolving 0.5 kg of ferrocene and 0.13 kg of thiophene in 14 kg of benzene. The proportion of ferrocene in the raw material liquid was 3.5% by mass, and the proportion of thiophene was 0.9% by mass.
気化器(3)を温度500℃にした。そして気化器内に窒素ガスを流通し、酸素ガスを追い出した。次いで水素ガスを流通して水素ガス雰囲気に置換した。
反応管(5)の温度を1250℃まで上げた。ポンプで気化器に前記原料液を30g/minで供給し、気化させ原料ガスを得た。原料ガスをキャリアガス(2a)として供給した50L/minの水素ガスで気化器から排出した。原料ガスにキャリアガス(2b)として400L/minの水素ガスを供給し、スタティックミキサー(4)によって均一に混合した。この混合ガスを反応管(5)内に噴射し、滞留時間1時間で反応させた。反応生成物をアルゴン雰囲気中で2800℃で30分間加熱して炭素繊維を得た。
The vaporizer (3) was brought to a temperature of 500 ° C. Then, nitrogen gas was circulated in the vaporizer to expel oxygen gas. Subsequently, hydrogen gas was circulated and replaced with a hydrogen gas atmosphere.
The temperature of the reaction tube (5) was increased to 1250 ° C. The raw material liquid was supplied to the vaporizer with a pump at 30 g / min and vaporized to obtain a raw material gas. The source gas was discharged from the vaporizer with 50 L / min of hydrogen gas supplied as the carrier gas (2a). 400 L / min hydrogen gas was supplied to the source gas as a carrier gas (2b), and mixed uniformly by a static mixer (4). This mixed gas was injected into the reaction tube (5) and reacted for a residence time of 1 hour. The reaction product was heated at 2800 ° C. for 30 minutes in an argon atmosphere to obtain carbon fibers.
炭素繊維の嵩密度は0.012g/minであった。嵩密度0.5g/cm3に圧縮したときの比抵抗は0.007Ωcmであった。また、走査型電子顕微鏡観察により繊維100本の平均をとったところ、繊維径は平均96.9nm、繊維径の標準偏差は23.4nm、繊維長は平均13μmであった(平均アスペクト比=130)。図2に繊維径分布を示す。平均繊維径の±20%の範囲に全繊維の75%(本数基準)が含まれていた。また、炭化回収率(=得られた炭素繊維の質量/供給したベンゼンの質量)は50%であった。 The bulk density of the carbon fiber was 0.012 g / min. The specific resistance when compressed to a bulk density of 0.5 g / cm 3 was 0.007 Ωcm. Further, when the average of 100 fibers was observed by scanning electron microscope observation, the average fiber diameter was 96.9 nm, the standard deviation of the fiber diameter was 23.4 nm, and the average fiber length was 13 μm (average aspect ratio = 130). ). FIG. 2 shows the fiber diameter distribution. The range of ± 20% of the average fiber diameter included 75% (based on the number) of all fibers. The carbonization recovery rate (= mass of obtained carbon fiber / mass of supplied benzene) was 50%.
(BET比表面積および細孔容積の測定)
Quantachrome社製、NOVA1200を使用し、液体窒素温度における窒素の吸着等温線を求め、これからBET法およびBJH法を用いて算出した。
(Measurement of BET specific surface area and pore volume)
Using NOVA1200 manufactured by Quantachrome, an adsorption isotherm of nitrogen at a liquid nitrogen temperature was determined, and calculated using the BET method and the BJH method.
実施例1
平均粒径10μmのパーマロイ(Ni−Fe合金)粉30gと製造例で得られた気相法炭素繊維3gを粘度200mPa・S(25℃)のシリコーンオイル(信越シリコーン製KF−96)70gに分散し、磁性流体(A)を調製した。この磁性流体(A)は飽和磁化量が40ガウスであり、磁石を近づけると引き寄せられた。
面積400mm2の2枚の電極が1mmのクリアランスで向かい合ったセルの両電極上に電磁石を取り付けた測定装置を横置きに設置し、セルの中に磁性流体(A)を充てんし、磁気特性を評価した。この際のトルクは、上部電極を水平方向に変位させることにより測定した。また応答速度はオシログラフを用い、磁界の印加に追随するトルクの遅れを測定して求めた。
磁界を印加していないときの磁性流体(A)の25℃の粘度は3530mPa・secであった。また、25℃、1,500エルステッドの磁界を印加したときの磁界方向の導電率が3.5×10−1S/cmであった。
磁界を印加していないときの磁性流体(A)のトルクは24gf・cmであった。磁性流体(A)に1,500エルステッドの磁界を印加したときのトルクは240gf・cmであり、応答速度は0.10秒であった。
Example 1
Disperse 30 g of permalloy (Ni-Fe alloy) powder with an average particle size of 10 μm and 3 g of vapor grown carbon fiber obtained in the production example in 70 g of silicone oil (KF-96 manufactured by Shin-Etsu Silicone) with a viscosity of 200 mPa · S (25 ° C.). The magnetic fluid (A) was prepared. The magnetic fluid (A) had a saturation magnetization of 40 gauss and was attracted when the magnet was brought closer.
A measuring device with an electromagnet attached on both electrodes of a cell where two electrodes with an area of 400 mm 2 face each other with a clearance of 1 mm is installed horizontally, and the cell is filled with magnetic fluid (A), and the magnetic properties are measured. evaluated. The torque at this time was measured by displacing the upper electrode in the horizontal direction. The response speed was obtained by measuring the delay of the torque following the application of the magnetic field using an oscillograph.
The viscosity at 25 ° C. of the magnetic fluid (A) when no magnetic field was applied was 3530 mPa · sec. The conductivity in the magnetic field direction when a magnetic field of 25 ° C. and 1,500 oersted was applied was 3.5 × 10 −1 S / cm.
The torque of the magnetic fluid (A) when no magnetic field was applied was 24 gf · cm. When a magnetic field of 1,500 oersted was applied to the magnetic fluid (A), the torque was 240 gf · cm, and the response speed was 0.10 seconds.
実施例2:
実施例1で用いた気相法炭素繊維の量を2.0gに変え、人造黒鉛微粉(UFG10:昭和電工製、平均粒径5μm)1.0gを添加した以外は、実施例1と同様にして磁性流体(B)を調製した。この磁性流体(B)は、その飽和磁化量が560ガウスであり、磁石を近づけると引き寄せられた。面積400mm2の2枚の電極が1mmのクリアランスで向かい合ったセルの両電極上に電磁石を取り付けた測定装置を横置きに設置し、セルの中に磁性流体(B)を充てんし、磁気特性を評価した。この際のトルクは、上部電極を水平方向に変位させることにより測定した。また応答速度はオシログラフを用い、磁界の印加に追随するトルクの遅れを測定して求めた。
磁界を印加していないときの磁性流体(B)の25℃の粘度は4280mPa・secであった。また、25℃、1,500エルステッドの磁界を印加したときの磁界方向の導電率が2.5×10−1S/cmであった。
磁界を印加していないときの磁性流体(B)のトルクは20gf・cmであった。磁性流体(B)に1,500エルステッドの磁界を印加したときのトルクは280gf・cmであり、応答速度は0.15秒であった。
Example 2:
Except for changing the amount of vapor grown carbon fiber used in Example 1 to 2.0 g and adding 1.0 g of artificial graphite fine powder (UFG10: Showa Denko, average particle size 5 μm), the same as in Example 1 Thus, a magnetic fluid (B) was prepared. The magnetic fluid (B) had a saturation magnetization of 560 gauss, and was attracted when the magnet was brought closer. A measuring device with an electromagnet attached on both electrodes of a cell where two electrodes with an area of 400 mm 2 face each other with a clearance of 1 mm is installed horizontally, and the cell is filled with magnetic fluid (B) to provide magnetic properties. evaluated. The torque at this time was measured by displacing the upper electrode in the horizontal direction. The response speed was obtained by measuring the delay of the torque following the application of the magnetic field using an oscillograph.
The viscosity at 25 ° C. of the magnetic fluid (B) when no magnetic field was applied was 4280 mPa · sec. Moreover, the electrical conductivity in the magnetic field direction when applying a magnetic field of 1,500 oersted at 25 ° C. was 2.5 × 10 −1 S / cm.
The torque of the magnetic fluid (B) when no magnetic field was applied was 20 gf · cm. When a magnetic field of 1,500 oersted was applied to the magnetic fluid (B), the torque was 280 gf · cm, and the response speed was 0.15 seconds.
比較例1
気相法炭素繊維3gを添加しない以外は、実施例1と同様な方法で磁性流体(C)を調製した。この磁性流体(C)は、その飽和磁化量が430ガウスであり、磁石を近づけると引き寄せられた。さらに実施例1と同様な方法で磁気特性を調べた。
磁界を印加していないときの磁性流体(C)の25℃の粘度は2730mPa・secであった。また、25℃、1,500エルステッドの磁界を印加したときの磁界方向の導電率が3.5×10−3S/cmであった。
磁界を印加していないときの磁性流体(C)のトルクは18gf・cmであった。磁性流体(C)の1,500エルステッドの磁界を印加したときのトルクは188gf・cmであり、応答速度は3.50秒であった。
Comparative Example 1
A magnetic fluid (C) was prepared in the same manner as in Example 1 except that 3 g of vapor grown carbon fiber was not added. The magnetic fluid (C) had a saturation magnetization of 430 gauss and was attracted when the magnet was brought closer. Further, the magnetic properties were examined in the same manner as in Example 1.
The viscosity at 25 ° C. of the magnetic fluid (C) when no magnetic field was applied was 2730 mPa · sec. The conductivity in the magnetic field direction when a magnetic field of 25 ° C. and 1,500 oersted was applied was 3.5 × 10 −3 S / cm.
The torque of the magnetic fluid (C) when no magnetic field was applied was 18 gf · cm. The torque of the magnetic fluid (C) when a 1,500 oersted magnetic field was applied was 188 gf · cm, and the response speed was 3.50 seconds.
実施例3
パーマロイ粉の代わりに、平均粒径0.4μm鉄粉を用いた他は実施例2と同様な方法で磁性流体(D)を調製した。この磁性流体(D)は、その飽和磁化量が380ガウスであり、磁石を近づけると引き寄せられた。さらに実施例2と同様な方法で磁気特性を調べた。
磁界を印加していないときの磁性流体(D)の25℃の粘度は4830mPa・secであった。また、25℃、1,500エルステッドの磁界を印加したときの磁界方向の導電率が8.1×10−1S/cmであった。
磁界を印加していないときの磁性流体(D)のトルクは35gf・cmであった。磁性流体(D)の1,500エルステッドの磁界を印加したときのトルクは215gf・cm、応答速度は0.06秒であった。
Example 3
A magnetic fluid (D) was prepared in the same manner as in Example 2 except that iron powder having an average particle size of 0.4 μm was used instead of permalloy powder. The magnetic fluid (D) had a saturation magnetization of 380 gauss and was attracted when the magnet was brought closer. Further, the magnetic characteristics were examined in the same manner as in Example 2.
The viscosity at 25 ° C. of the magnetic fluid (D) when no magnetic field was applied was 4830 mPa · sec. The conductivity in the magnetic field direction when applying a magnetic field of 25 ° C. and 1,500 oersteds was 8.1 × 10 −1 S / cm.
The torque of the magnetic fluid (D) when no magnetic field was applied was 35 gf · cm. When a magnetic field of 1,500 oersted magnetic fluid (D) was applied, the torque was 215 gf · cm, and the response speed was 0.06 seconds.
比較例2
パーマロイ粉の代わりに、平均粒径0.4μm鉄粉を用いた他は比較例1と同様な方法で磁性流体(E)を調製した。この磁性流体(E)は、その飽和磁化量が380ガウスであり、磁石を近づけると引き寄せられた。さらに比較例1と同様な方法で磁気特性を調べた。
磁界を印加していないときの磁性流体(E)の25℃の粘度は3180mPa・secであった。また、25℃、1,500エルステッドの磁界を印加したときの磁界方向の導電性が7.2×10−3S/cmであった。
磁界を印加していないときの磁性流体(E)のトルクは28gf・cmであった。磁性流体(E)の1,500エルステッドの磁界を印加したときのトルクは159gf・cmであり、応答速度は0.30秒であった。
Comparative Example 2
A magnetic fluid (E) was prepared in the same manner as in Comparative Example 1 except that iron powder having an average particle size of 0.4 μm was used instead of permalloy powder. The magnetic fluid (E) had a saturation magnetization of 380 gauss and was attracted when the magnet was brought closer. Further, the magnetic characteristics were examined by the same method as in Comparative Example 1.
The viscosity at 25 ° C. of the magnetic fluid (E) when no magnetic field was applied was 3180 mPa · sec. The conductivity in the magnetic field direction when applying a magnetic field of 25 ° C. and 1,500 oersteds was 7.2 × 10 −3 S / cm.
The torque of the magnetic fluid (E) when no magnetic field was applied was 28 gf · cm. The torque of the magnetic fluid (E) when a 1,500 oersted magnetic field was applied was 159 gf · cm, and the response speed was 0.30 seconds.
実施例4
パーマロイ粉の代わりに、平均粒径1.0μmマグネタイト粉を用いた他は実施例2と同様な方法で磁性流体(F)を調製した。この磁性流体(F)は、その飽和磁化量が380ガウスであり、磁石を近づけると引き寄せられた。さらに実施例2と同様な方法で磁気特性を調べた。
磁界を印加していないときの磁性流体(F)の25℃の粘度は3830mPa・secであった。また、25℃、1,500エルステッドの磁界を印加したときの磁界方向の導電率が1.5×10−1S/cmであった。
磁界を印加していないときの磁性流体(F)のトルクは35gf・cmであった。磁性流体(F)の1,500エルステッドの磁界を印加したときのトルクは215gf・cm、応答速度は0.06秒であった。
Example 4
A magnetic fluid (F) was prepared in the same manner as in Example 2 except that magnetite powder having an average particle size of 1.0 μm was used instead of permalloy powder. The magnetic fluid (F) had a saturation magnetization of 380 gauss and was attracted when the magnet was brought closer. Further, the magnetic characteristics were examined in the same manner as in Example 2.
The viscosity of the magnetic fluid (F) at 25 ° C. when no magnetic field was applied was 3830 mPa · sec. The conductivity in the magnetic field direction when a magnetic field of 25 ° C. and 1,500 oersted was applied was 1.5 × 10 −1 S / cm.
The torque of the magnetic fluid (F) when no magnetic field was applied was 35 gf · cm. When a magnetic field of 1,500 oersted magnetic fluid (F) was applied, the torque was 215 gf · cm, and the response speed was 0.06 seconds.
1 原料
2a,2b キャリアガス
3 気化器
4 撹拌装置
5 反応管
1 Raw material 2a,
Claims (15)
少なくとも一種の炭素系導電性粒子が、2000℃以上の温度で加熱処理された、平均繊維径10〜500nmで且つ平均アスペクト比30〜200の炭素繊維であることを特徴とする導電性磁性流体。 A conductive magnetic fluid comprising at least one solvent, at least one ferromagnetic particle, and at least one carbon-based conductive particle,
A conductive magnetic fluid, wherein at least one carbon-based conductive particle is a carbon fiber having an average fiber diameter of 10 to 500 nm and an average aspect ratio of 30 to 200, which is heat-treated at a temperature of 2000 ° C. or higher .
鉄、ニッケル又はコバルトの金属単体;
鉄、ニッケル及び/又はコバルトを含む合金;
鉄、ニッケル及び/又はコバルトを含む酸化物; 及び/又は
鉄、ニッケル及び/又はコバルトを含む窒化物の微粒子であることを特徴とする請求項1〜4のいずれか一項に記載の導電性磁性流体。 At least one type of ferromagnetic particle
Simple metal of iron, nickel or cobalt;
Alloys containing iron, nickel and / or cobalt;
Iron oxide containing nickel and / or cobalt; and / or iron, electrically conductive according to any one of claims 1 to 4, characterized in that fine particles of nitrides containing nickel and / or cobalt Magnetic fluid.
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