JPH0578607A - Production of coating - Google Patents

Production of coating

Info

Publication number
JPH0578607A
JPH0578607A JP3124891A JP12489191A JPH0578607A JP H0578607 A JPH0578607 A JP H0578607A JP 3124891 A JP3124891 A JP 3124891A JP 12489191 A JP12489191 A JP 12489191A JP H0578607 A JPH0578607 A JP H0578607A
Authority
JP
Japan
Prior art keywords
rotor
dispersion
peripheral surface
stator
paint
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.)
Withdrawn
Application number
JP3124891A
Other languages
Japanese (ja)
Inventor
Akira Morioka
章 森岡
Keiji Onishi
啓二 大西
Takeshi Matsuura
武志 松浦
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Maxell Holdings Ltd
Original Assignee
Hitachi Maxell Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Maxell Ltd filed Critical Hitachi Maxell Ltd
Priority to JP3124891A priority Critical patent/JPH0578607A/en
Publication of JPH0578607A publication Critical patent/JPH0578607A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE:To provide a method for efficiently producing a coating containing a pigment dispersed therein in a good state. CONSTITUTION:A pigment (e.g. magnetic powder such as gamma-Fe2O3),a binder component (e.g. vinyl chloride-vinyl acetate copolymer), an organic solvent (e.g. cyclohexanone) and other required components are mixed with each other. The mixture is fed into the mixing tank of a preliminary dispersing machine comprising a rotating column-like rotor and a cylindrical stationary stator surrounding the rotor, a gap being formed therebetween, subjected to a preliminary dispersion treatment, fed into a medium-dispersing type dispersing machine preliminarily received a dispersing medium which is repeatedly moved and corrided each other, and subsequently subjected to a final dispersion treatment to obtain the objective coating.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は塗料の製造方法に関
し、さらに詳しくは、顔料を良好に分散させた塗料を効
率よく製造する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a paint, and more particularly to a method for efficiently producing a paint in which a pigment is well dispersed.

【0002】[0002]

【従来の技術】一般に、塗料は、顔料、結合剤成分、有
機溶剤およびその他の必要成分を、適宜の順序で直接ボ
−ルミル等の分散機に配合して混合分散するか、あるい
はタンク中に配合した後、高速ディスパ−等の撹拌機で
予め予備混合を行い、さらに送液ポンプ等により任意の
速度でサンドミルなどの分散機に送液して混合分散する
などの方法で製造されている。
2. Description of the Related Art Generally, a paint is prepared by mixing a pigment, a binder component, an organic solvent and other necessary components directly in a suitable order in a disperser such as a ball mill or the like, or by mixing or dispersing them in a tank. After blending, pre-mixing is performed in advance with a stirrer such as a high-speed disperser, and further, liquid is fed to a disperser such as a sand mill at an arbitrary speed by a liquid feed pump or the like to mix and disperse.

【0003】[0003]

【発明が解決しようとする課題】ところが、これら従来
の方法では、高硬度の顔料やカ−ボンブラック等の微粒
子顔料等の分散を行う際、未分散の塊状の顔料が残った
り、所望の分散度に到達しないなどの問題点があり、所
望の分散度に仕上げるために多くの時間を費やしたりす
るため製造能率がきわめて悪い。
However, in these conventional methods, when a high hardness pigment or a fine particle pigment such as carbon black is dispersed, undispersed lumpy pigment may remain or the desired dispersion may occur. However, the manufacturing efficiency is extremely poor because it takes a lot of time to finish the dispersion to a desired degree.

【0004】[0004]

【課題を解決するための手段】この発明は、かかる問題
を解消するため鋭意検討を行った結果なされたもので、
顔料を、結合剤成分、有機溶剤およびその他の必要成分
とともに混合した後、この混合物を回転する円柱状のロ
−タとそれをとり囲む円筒状の静止ステ−タとのギャッ
プでもって形成された予備分散機の混合槽内に送り込ん
で予備分散し、しかる後、運動し互いに衝突をくり返す
分散媒体が予め収容された分散機に送り込んで仕上げ分
散することによって、顔料を充分に良好に分散させると
ともに、顔料を良好に分散した塗料が効率よく製造でき
るようにしたものである。
The present invention has been made as a result of extensive studies to solve the above problems.
After the pigment was mixed with the binder component, the organic solvent and other necessary ingredients, the mixture was formed with a gap between the rotating cylindrical rotor and the surrounding stationary cylindrical stator. The pigment is dispersed sufficiently well by sending it into the mixing tank of the pre-disperser for pre-dispersion, and then by sending it to a disperser in which a dispersion medium that moves and repeatedly collides with each other is pre-stored and finish-dispersed. At the same time, a paint in which the pigment is well dispersed can be efficiently produced.

【0005】この発明によれば、分散媒体が収容された
サンドミル等のメディア媒体型分散機での仕上げ分散す
る前に、顔料、結合剤成分、有機溶剤およびその他の必
要成分等を混合した混合物を、回転する円柱状のロ−タ
とそれをとり囲む円筒状の静止ステ−タとのギャップで
もって形成された予備分散機の混合槽内に送り込み、剪
断エネルギを与えて予備分散しているため、この予備分
散でもって顔料粒子の凝集体が解砕される。従って、分
散媒体が収容されたメディア媒体型分散機での仕上げ分
散は、顔料粒子の粗大凝集体のない状態でもって行わ
れ、仕上げ分散工程で所望の分散度に到達するに要する
時間が短縮されると同時に分散度が充分に向上されて、
顔料が良好に分散された塗料が効率よく製造される。
According to the present invention, a mixture of a pigment, a binder component, an organic solvent and other necessary components is mixed before finishing dispersion in a media medium type disperser such as a sand mill containing a dispersion medium. , Because it is fed into a mixing tank of a predispersing machine formed with a gap between a rotating cylindrical rotor and a cylindrical stationary stator that surrounds it, and shear energy is applied to preliminarily disperse it. The aggregate of pigment particles is crushed by this preliminary dispersion. Therefore, the finish dispersion in the media medium type disperser containing the dispersion medium is performed without a coarse aggregate of pigment particles, and the time required to reach the desired dispersity in the finish dispersion step is shortened. At the same time, the degree of dispersion is sufficiently improved,
A paint in which a pigment is well dispersed is efficiently produced.

【0006】特に、磁気記録媒体を形成するとき製造さ
れる磁性塗料のように、微粒子強磁性粉末の他、高硬度
のα−Al2 3 、Cr2 3 等の粉体や、一般的に超
微粒子であり分散の困難なカ−ボンブラックなどを含む
塗料の分散には最適であり、生産性の向上や、磁性層の
表面平滑性の改善、さらにドロップアウトの低減などに
効果的である。
In particular, magnetic fine particles such as a magnetic paint produced when forming a magnetic recording medium, as well as fine-particle ferromagnetic powders, powders such as α-Al 2 O 3 and Cr 2 O 3 having high hardness, and general It is ideal for dispersing paints containing carbon black, which is extremely fine and difficult to disperse, and is effective in improving productivity, improving the surface smoothness of the magnetic layer, and reducing dropout. is there.

【0007】この発明において、仕上げ分散の前に行う
予備分散は、回転する円柱状のロ−タとそれをとり囲む
円筒状の静止ステ−タとのギャップでもって形成された
混合槽内に、顔料、結合剤成分、有機溶剤およびその他
の必要成分を混合した混合物が送り込まれ、回転する円
柱状のロ−タの高速回転によって強制撹拌して行われ
る。従って、回転する円柱状のロ−タとそれをとり囲む
円筒状の静止ステ−タとのギャップに剪断作用が働き、
この剪断エネルギでもって顔料粒子の凝集体が解砕され
る。
In the present invention, the pre-dispersion carried out before the finish dispersion is carried out in a mixing tank formed by a gap between a rotating cylindrical rotor and a cylindrical stationary stator surrounding the rotor. A mixture in which a pigment, a binder component, an organic solvent and other necessary components are mixed is fed, and the stirring is carried out by forcibly stirring by a high speed rotation of a rotating cylindrical rotor. Therefore, a shearing action acts on the gap between the rotating cylindrical rotor and the cylindrical stationary stator that surrounds it,
This shearing energy breaks up the aggregates of pigment particles.

【0008】しかして、この予備分散後、さらに分散媒
体が収容されたメディア媒体型分散機で仕上げ分散が行
われると、顔料粒子の粗大凝集体のない状態でもって分
散されるため迅速かつ良好に分散され、顔料が、たとえ
分散しにくい微粒子磁性粉末や高硬度のα−Al
2 3 、Cr2 3 等の粉体、さらにカ−ボンブラック
であっても一次粒子まで良好に分散される。
However, after this preliminary dispersion, when the final dispersion is carried out with a media medium type disperser containing a dispersion medium, the dispersion is carried out in a state without coarse aggregates of pigment particles, so that the dispersion is carried out quickly and satisfactorily. Dispersed pigments, even if it is difficult to disperse fine magnetic powder or high hardness α-Al
Even with powders of 2 O 3 , Cr 2 O 3, etc., and even carbon black, primary particles are well dispersed.

【0009】このように回転する円柱状のロ−タとそれ
をとり囲む円筒状の静止ステ−タとのギャップでもって
形成される混合槽は、混合槽の内壁を構成する円柱状の
ロ−タの高速回転によって、強い剪断作用を加えて顔料
粒子の凝集体を解砕するものであるため、この混合槽を
形成するロ−タとステ−タとのギャップを、充分な剪断
エネルギが得られるように1mm以内にするのが好まし
く、これよりギャップを広くすると混合槽内の混合物に
充分な剪断作用を加えることができず、顔料粒子の凝集
体を充分に解砕することができない。
The mixing tank formed by the gap between the rotating cylindrical rotor and the cylindrical stationary stator surrounding the rotating rotor is a cylindrical rotor forming the inner wall of the mixing tank. By rotating the rotor at high speed, a strong shearing action is applied to disintegrate the aggregates of pigment particles, so that sufficient shearing energy can be obtained in the gap between the rotor and the stator forming this mixing tank. It is preferably within 1 mm so that if the gap is wider than this, sufficient shearing action cannot be applied to the mixture in the mixing tank, and the aggregate of pigment particles cannot be sufficiently crushed.

【0010】また、混合槽内に送り込んだ混合物にさら
に強い剪断作用が加えられるようにするため、ロ−タの
外周面とステ−タの内周面に、それぞれ角錐、または角
錐の先端を切り落としたような形状の突起を多数設ける
のが好ましく、さらにこれらの突起は、ロ−タ側および
ステ−タ側の両突起の角錐の斜面同士、ロ−タ側突起の
先端とステ−タの内周面、ステ−タ側突起の先端とロ−
タの外周面が、それぞれ対向するようにするのが好まし
い。
Further, in order to apply a stronger shearing action to the mixture sent into the mixing tank, the pyramid or the tip of the pyramid is cut off on the outer peripheral surface of the rotor and the inner peripheral surface of the stator, respectively. It is preferable to provide a large number of protrusions having such a shape.Furthermore, these protrusions are formed by the pyramidal slopes of the rotor-side and stator-side protrusions, the tip of the rotor-side protrusion, and the inside of the stator. Circumferential surface, tip of stator side protrusion
It is preferable that the outer peripheral surfaces of the tabs face each other.

【0011】さらに、このような回転する円柱状のロ−
タとそれをとり囲む円筒状の静止ステ−タとのギャップ
でもって形成された混合槽内で混合物を混合分散するに
当たってのロ−タの回転速度は、周速にして20〜30
m/sec の範囲内で行うのが好ましく、回転速度が遅す
ぎると混合物の混合分散が良好に行えず、速すぎると混
合槽内で強制撹拌される際、極めて多量の熱が発生し、
塗料に悪影響を及ぼすおそれがある。
Further, such a rotating cylindrical rod
The rotating speed of the rotor for mixing and dispersing the mixture in the mixing tank formed with the gap between the rotor and the cylindrical stationary stator surrounding the rotor is 20 to 30 in terms of peripheral speed.
It is preferable to carry out in the range of m / sec. If the rotation speed is too slow, the mixture cannot be mixed and dispersed well, and if it is too fast, an extremely large amount of heat is generated when the mixture is forcibly stirred in the mixing tank.
May adversely affect paint.

【0012】このような予備分散後、さらに行われる仕
上げ分散は、分散媒体が予め収容されたサンドミル、ボ
−ルミルなどのメディア媒体型分散機で行われ、この仕
上げ分散においては、顔料粒子の粗大凝集体のない状態
でもって分散されるため迅速かつ良好な分散が行われ、
顔料が、たとえ分散しにくい微粒子磁性粉末や高硬度の
α−Al2 3 、Cr2 3等の粉体、さらにカ−ボン
ブラックであっても一次粒子まで良好に分散される。
After such preliminary dispersion, further finish dispersion is carried out by a media medium type disperser such as a sand mill or a ball mill in which a dispersion medium is stored in advance. In this final dispersion, coarse pigment particles are used. Since it is dispersed without agglomerates, quick and good dispersion is achieved,
Even if the pigment is a fine magnetic powder that is difficult to disperse, a powder of high hardness α-Al 2 O 3 , Cr 2 O 3 or the like, or even carbon black, the primary particles are well dispersed.

【0013】このようなメディア媒体型分散機で仕上げ
れ分散が行われる際、予め収容される分散媒体は、塗料
中の顔料を充分に均一に混合分散できるように、粒子径
が、0.5〜2.0 mmのものを使用するのが好ましく、粒子
径が大きすぎると衝撃力は増すものの分散が粗くなって
充分に微細な分散が行えず、小さすぎると混合分散後、
塗料と分散媒体の分離に支障をきたす場合がある。ま
た、分散媒体の塗料に対する使用割合は80〜150容
量%の範囲内で使用するのが好ましく、少なすぎると分
散媒体同士の剪断回数が少なくなって分散性が悪くな
り、多すぎると分散媒体同士の衝突が激しくなり分散媒
体の摩耗が極めて多くなる。このような分散媒体として
は、ガラス、セラミック、スチ−ル等従来から使用され
ている種々の材質のものがいずれも好適に使用される。
When finishing and dispersing with such a media medium type disperser, the dispersion medium to be contained in advance has a particle diameter of 0.5 to 2.0 so that the pigment in the paint can be mixed and dispersed sufficiently uniformly. It is preferable to use the one having a particle size of 0.1 mm, and if the particle size is too large, the impact force increases, but the dispersion becomes coarse and cannot be sufficiently finely dispersed, and if it is too small, after mixing and dispersing,
It may interfere with the separation of the paint and the dispersion medium. Further, the use ratio of the dispersion medium to the paint is preferably within the range of 80 to 150% by volume, and if it is too small, the number of shearing of the dispersion medium is reduced and the dispersibility is deteriorated. And the dispersion medium is extremely worn. As such a dispersion medium, any of various materials conventionally used such as glass, ceramics and steel is preferably used.

【0014】このように、回転する円柱状のロ−タとそ
れをとり囲む円筒状の静止ステ−タとのギャップでもっ
て形成された混合槽内で予備分散を行い、さらにサンド
ミル、ボ−ルミルなどのメディア媒体型分散機でもって
仕上げ分散を行うと、顔料が充分に良好に分散された塗
料が効率よく製造され、磁気記録媒体を製造するとき使
用される磁性塗料をこの方法で製造すると、回転する円
柱状のロ−タとそれをとり囲む円筒状の静止ステ−タと
のギャップでもって強い剪断作用が加えられて顔料粒子
の凝集体が良好に解砕され、さらに仕上げ分散が行われ
て特に分散性の悪い微粒子磁性粉末やカ−ボンブラック
なども良好に分散されて、これらの分散性の良好な磁性
塗料が調製され、この磁性塗料を基体上に塗布、乾燥し
て磁性層を形成すると、一段と電磁変換特性に優れた磁
気記録媒体が得られる。
As described above, preliminary dispersion is performed in a mixing tank formed with a gap between a rotating cylindrical rotor and a cylindrical stationary stator surrounding the rotor, and further, a sand mill and a ball mill. When finish dispersion is performed with a media medium type disperser such as, a pigment in which the pigment is sufficiently well dispersed is efficiently produced, and when the magnetic coating used for producing a magnetic recording medium is produced by this method, A strong shearing action is applied by the gap between the rotating cylindrical rotor and the cylindrical stationary stator that surrounds it, and the pigment particle agglomerates are crushed well, and further finish dispersion is performed. In particular, fine magnetic powder and carbon black having poor dispersibility are also well dispersed to prepare a magnetic coating having good dispersibility. The magnetic coating is applied onto a substrate and dried to form a magnetic layer. Form When a magnetic recording medium having excellent electromagnetic conversion characteristics can be obtained more.

【0015】ここで、磁性塗料の製造において使用する
磁性粉末としては、たとえば、γ−Fe2 3 粉末、F
3 4 粉末、Co含有γ−Fe2 3 粉末、Co含有
Fe3 4 粉末の他、Fe粉末、Co粉末、Fe−Ni
粉末などの金属粉末など従来公知の各種磁性粉末が広く
使用される。
Here, as the magnetic powder used in the production of the magnetic paint, for example, γ-Fe 2 O 3 powder, F
e 3 O 4 powder, Co-containing γ-Fe 2 O 3 powder, Co-containing Fe 3 O 4 powder, Fe powder, Co powder, Fe-Ni
Various conventionally known magnetic powders such as metal powders such as powders are widely used.

【0016】また、結合剤成分としては、塩化ビニル−
酢酸ビニル系共重合体、繊維素系樹脂、ブチラ−ル系樹
脂、ポリウレタン系樹脂、ポリエステル系樹脂、エポキ
シ系樹脂、ポリエ−テル系樹脂、イソシアネ−ト化合物
など従来から磁気記録媒体に汎用されている結合剤樹脂
がいずれも用いられる。
As the binder component, vinyl chloride-
Vinyl acetate-based copolymers, fibrin-based resins, butyral-based resins, polyurethane-based resins, polyester-based resins, epoxy-based resins, polyether-based resins, isocyanate compounds, etc. Any binder resin that is present is used.

【0017】さらに、有機溶剤としては、シクロヘキサ
ノン、メチルエチルケトン、メチルイソブチルケトンな
どのケトン系溶剤、酢酸エチル、酢酸ブチルなどのエス
テル系溶剤、ベンゼン、トルエン、キシレンなどの芳香
族炭化水素系溶剤、ジメチルスルホキシドなどのスルホ
キシド系溶剤、テトラヒドロフラン、ジオキサンなどの
エ−テル系溶剤など、使用する結合剤樹脂を溶解するの
に適した溶剤が、特に制限されることなく単独または二
種以上混合して使用される。
As the organic solvent, ketone solvents such as cyclohexanone, methyl ethyl ketone and methyl isobutyl ketone, ester solvents such as ethyl acetate and butyl acetate, aromatic hydrocarbon solvents such as benzene, toluene and xylene, and dimethyl sulfoxide. Solvents suitable for dissolving the binder resin to be used, such as sulfoxide-based solvents such as, ether solvents such as tetrahydrofuran and dioxane, are used alone or in combination of two or more without particular limitation. ..

【0018】[0018]

【実施例】次に、この発明の実施例について説明する。 実施例1 Co−γ−Fe2 3 (比表面積30m2 /g) 100.0重量部 α−Al2 3 (平均粒子径 0.4μm) 8.0 〃 カ−ボンブラック(平均粒子径25mμm) 2.5 〃 ステアリン酸亜鉛 0.5 〃 塩化ビニル−酢酸ビニル−ビニルアルコ−ル共重合体 61.5 〃 (20重量%シクロヘキサノン/トルエン溶液) シクロヘキサノン/トルエン=1/1の混合溶剤 151.2 〃 この組成物をタンク中に適宜の順序で添加して配合し、
高速ディスパ−で撹拌を行った。
EXAMPLES Next, examples of the present invention will be described. Example 1 Co-γ-Fe 2 O 3 (specific surface area 30 m 2 / g) 100.0 parts by weight α-Al 2 O 3 (average particle size 0.4 μm) 8.0 〃 carbon black (average particle size 25 mμm) 2.5 〃 stearin Zinc acid salt 0.5 〃 Vinyl chloride-vinyl acetate-vinyl alcohol copolymer 61.5 〃 (20 wt% cyclohexanone / toluene solution) Cyclohexanone / toluene = 1/1 mixed solvent 151.2 〃 This composition in a tank in an appropriate order Add and mix,
Stirring was performed with a high speed disperser.

【0019】次いで、この混合物を、周速22.5m/sec
で回転するロ−タと静止ステ−タとのギャップ幅が約5
00μmの予備分散機(突起の数160個/m2 、突起
の高さ8mm)の混合槽内に送り込み、滞留時間にして1
0秒間混合分散した。しかる後、さらにサンドミルに送
り込んで滞留時間にして45分間混合分散した。
Then, this mixture was subjected to a peripheral speed of 22.5 m / sec.
The gap between the rotating rotor and the stationary stator is about 5
It was fed into the mixing tank of a 00 μm preliminary disperser (160 protrusions / m 2 , protrusion height 8 mm), and the residence time was 1
Mix and disperse for 0 seconds. After that, the mixture was further sent to a sand mill and mixed and dispersed for a retention time of 45 minutes.

【0020】次ぎに、これに ポリウレタン樹脂(20重量%シクロヘキサノン/トルエ 34.1重量部 ン溶液) ミリスチン酸 1.5 〃 ステアリン酸nブチル 1.2 〃 コロネ−トL(日本ポリウレタン工業社製;三官能性低分 6.1 〃 子量イソシアネ−ト化合物の75重量%酢酸エチル溶液) シクロヘキサノン/トルエン=1/1の混合溶剤 33.2 〃 の組成物を適宜の順序で加え、1時間混合分散して磁性
塗料を製造した。
Next, a polyurethane resin (20% by weight cyclohexanone / toluene 34.1 parts by weight solution) myristic acid 1.5 〃 n-butyl stearate 1.2 〃 Coronet L (manufactured by Nippon Polyurethane Industry Co .; (75% by weight ethyl acetate solution of isocyanate amount of isocyanate compound) A mixed solvent of cyclohexanone / toluene = 1/1 mixed solvent 33.2 was added in an appropriate order and mixed and dispersed for 1 hour to produce a magnetic paint.

【0021】次いで、得られた磁性塗料を公称 0.3μm
のフィルタ−を通した後、公称14μm厚さのポリエス
テルフィルム上に塗布し、カレンダ処理後、1/2イン
チ幅に裁断してビデオテ−プを作成した。
Then, the obtained magnetic paint is nominally 0.3 μm.
After passing through the filter of No. 1 above, it was applied on a polyester film having a nominal thickness of 14 μm, calendered, and cut into ½ inch width to prepare a video tape.

【0022】実施例2 実施例1において、サンドミルでの混合分散を、滞留時
間にして45分から滞留時間にして30分間に変更した
以外は、実施例1と同様にして磁性塗料を製造し、ビデ
オテ−プを作成した。
Example 2 A magnetic paint was produced in the same manner as in Example 1 except that the mixing and dispersion in the sand mill was changed from 45 minutes as the residence time to 30 minutes as the residence time. -Created a page.

【0023】実施例3 実施例1においてタンク中で高速ディスパ−によって撹
拌する組成物において、予め組成物中のシクロヘキサノ
ン/トルエン混合溶剤量を適当に減らし、混練機で混練
してペ−スト化した後、減らしたシクロヘキサノン/ト
ルエン混合溶剤を加えて調製し、これをタンクに移送し
高速ディスパ−で撹拌した以外は、実施例1と同様にし
て磁性塗料を製造し、ビデオテ−プを作成した。
Example 3 In the composition of Example 1, which was stirred by a high speed disperser in a tank, the amount of cyclohexanone / toluene mixed solvent in the composition was appropriately reduced in advance, and the mixture was kneaded by a kneader to form a paste. After that, a reduced amount of cyclohexanone / toluene mixed solvent was added to prepare a mixed solution, which was transferred to a tank and stirred with a high speed disperser to prepare a magnetic coating material in the same manner as in Example 1 to prepare a video tape.

【0024】実施例4 実施例3において、サンドミルでの混合分散を、滞留時
間にして45分から滞留時間にして30分間に変更した
以外は、実施例3と同様にして磁性塗料を製造し、ビデ
オテ−プを作成した。
Example 4 A magnetic paint was produced in the same manner as in Example 3 except that the mixing and dispersing in the sand mill was changed from 45 minutes as the residence time to 30 minutes as the residence time. -Created a page.

【0025】比較例1 実施例1において、回転するロ−タと静止ステ−タとの
ギャップでもって形成された混合槽での混合分散を省い
た以外は、実施例1と同様にして磁性塗料を製造し、ビ
デオテ−プを作成した。
Comparative Example 1 A magnetic coating material was prepared in the same manner as in Example 1 except that the mixing and dispersing in the mixing tank formed with the gap between the rotating rotor and the stationary stator was omitted. Was manufactured to prepare a video tape.

【0026】比較例2 実施例3において、回転するロ−タと静止ステ−タとの
ギャップでもって形成された混合槽での混合分散を省い
た以外は、実施例3と同様にして磁性塗料を製造し、ビ
デオテ−プを作成した。
Comparative Example 2 A magnetic coating material was prepared in the same manner as in Example 3 except that the mixing and dispersing in the mixing tank formed with the gap between the rotating rotor and the stationary stator was omitted. Was manufactured to prepare a video tape.

【0027】各実施例および比較例で作成されたビデオ
テ−プについて、磁性層の表面粗さ、RF出力およびド
ロップアウトを測定した。磁性層の表面粗さは、触針式
表面粗さ計を用いて測定し、中心線平均粗さ(Ra)で
示した。また、RF出力は、標準記録電流でRF信号を
記録し、その再生出力を基準テ−プとの相対値で示し
た。さらに、ドロップアウトは、標準記録電流で50%
グレ−信号を記録、再生し、NCSC方式で5μsec 、
−18dBの条件にてドロップアウトカウンタ−で測定し
た。下記表1はその結果である。
The surface roughness, RF output and dropout of the magnetic layer were measured for the video tapes produced in each of the examples and comparative examples. The surface roughness of the magnetic layer was measured using a stylus type surface roughness meter, and indicated by the center line average roughness (Ra). As the RF output, an RF signal was recorded with a standard recording current, and the reproduction output was shown as a relative value with respect to the reference tape. Furthermore, the dropout is 50% at standard recording current.
It records and reproduces gray signals, and uses the NCSC method for 5 μsec.
It was measured with a dropout counter under the condition of -18 dB. Table 1 below shows the results.

【0028】 [0028]

【0029】[0029]

【発明の効果】上記表1から明らかなように、この発明
で得られたビデオテ−プ(実施例1ないし4)は、従来
のビデオテ−プ(比較例1および2)に比べて、いずれ
も表面粗さが平滑で、RF出力が高く、またドロップア
ウトが少なく、さらに実施例2および4でサンドミルで
の分散処理速度を速くしたものでも良好な結果が得られ
ており、このことからこの発明によって得られる塗料
は、顔料の分散性が良好で塗料の生産性向上にも有効で
あることがわかる。
As is apparent from Table 1 above, the video tapes obtained in the present invention (Examples 1 to 4) are all compared with the conventional video tapes (Comparative Examples 1 and 2). Even when the surface roughness was smooth, the RF output was high, the dropout was small, and the dispersion treatment speed in the sand mill was high in Examples 2 and 4, good results were obtained. It can be seen that the paint obtained by the method has good dispersibility of the pigment and is effective for improving the productivity of the paint.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 顔料を、結合剤成分、有機溶剤およびそ
の他の必要成分とともに混合し、次いで、この混合物を
回転する円柱状のロ−タとそれをとり囲む円筒状の静止
ステ−タとのギャップでもって形成された予備分散機の
混合槽内に送り込んで予備分散し、しかる後、運動し互
いに衝突をくり返す分散媒体が予め収容された分散機に
送り込んで仕上げ分散することを特徴とする塗料の製造
方法
1. A pigment is mixed with a binder component, an organic solvent and other necessary ingredients, and the mixture is then rotated into a cylindrical rotor and a cylindrical stationary stator surrounding the rotor. It is characterized in that it is fed into a mixing tank of a pre-disperser formed with a gap to carry out pre-dispersion, and then a dispersion medium that moves and repeatedly collides with each other is sent to a pre-stored disperser for finish dispersion. Paint manufacturing method
【請求項2】 予備分散を行うロ−タ外周面とステ−タ
内周面に互いに対向する突起を設けて、これらのロ−タ
外周面とステ−タ内周面間のギャップでもって形成され
た混合槽内で予備分散する請求項1記載の塗料の製造方
2. An outer peripheral surface of a rotor for performing preliminary dispersion and an inner peripheral surface of a stator are provided with projections opposed to each other, and are formed with a gap between the outer peripheral surface of the rotor and the inner peripheral surface of the stator. The method for producing a paint according to claim 1, wherein the paint is pre-dispersed in a mixed tank.
【請求項3】 ロ−タ外周面とステ−タ内周面に互いに
対向させて設けた突起が、角錐または角錐の先端を切り
落としたような形状であって、ロ−タ側およびステ−タ
側の両突起の角錐の斜面同士、ロ−タ側突起の先端とス
テ−タの内周面、ステ−タ側突起の先端とロ−タの外周
面を対向させたギャップでもって形成された混合槽内で
予備分散する請求項2記載の塗料の製造方法
3. The protrusions provided on the outer peripheral surface of the rotor and the inner peripheral surface of the stator so as to face each other have a pyramid shape or a shape in which the tip of the pyramid is cut off, and the rotor side and the stator are formed. Side projections are formed with a gap in which the pyramidal slopes of the two side projections, the tip of the rotor side projection and the inner peripheral surface of the stator, and the tip of the stator side projection and the outer peripheral surface of the rotor face each other. The method for producing a paint according to claim 2, wherein the dispersion is pre-dispersed in a mixing tank.
【請求項4】 予め分散媒体が収容された分散機が、メ
ディア媒体型分散機である請求項1ないし3記載の塗料
の製造方法
4. The method for producing a coating composition according to claim 1, wherein the dispersing machine in which the dispersing medium is contained in advance is a media medium type dispersing machine.
【請求項5】 メディア媒体型分散機がサンドミルであ
る請求項4記載の塗料の製造方法
5. The method for producing a paint according to claim 4, wherein the media medium type disperser is a sand mill.
【請求項6】 顔料として磁性粉末を使用し、磁性塗料
を製造する請求項1ないし5記載の塗料の製造方法
6. The method for producing a paint according to claim 1, wherein a magnetic powder is used as a pigment to produce a magnetic paint.
JP3124891A 1991-04-25 1991-04-25 Production of coating Withdrawn JPH0578607A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3124891A JPH0578607A (en) 1991-04-25 1991-04-25 Production of coating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3124891A JPH0578607A (en) 1991-04-25 1991-04-25 Production of coating

Publications (1)

Publication Number Publication Date
JPH0578607A true JPH0578607A (en) 1993-03-30

Family

ID=14896665

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3124891A Withdrawn JPH0578607A (en) 1991-04-25 1991-04-25 Production of coating

Country Status (1)

Country Link
JP (1) JPH0578607A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2005122700A1 (en) * 2004-06-22 2008-04-10 日本ゼオン株式会社 Method for producing polymerized toner
KR100965736B1 (en) * 2007-12-11 2010-06-24 삼화페인트 공업주식회사 Precoating composition
US8553398B2 (en) 2009-04-14 2013-10-08 Fujitsu Limited Electronic apparatus

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2005122700A1 (en) * 2004-06-22 2008-04-10 日本ゼオン株式会社 Method for producing polymerized toner
US7767375B2 (en) 2004-06-22 2010-08-03 Zeon Corporation Production process of polymerized toner
JP4665900B2 (en) * 2004-06-22 2011-04-06 日本ゼオン株式会社 Method for producing polymerized toner
KR100965736B1 (en) * 2007-12-11 2010-06-24 삼화페인트 공업주식회사 Precoating composition
US8553398B2 (en) 2009-04-14 2013-10-08 Fujitsu Limited Electronic apparatus

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Effective date: 19980711