JP2849146B2 - Plate-shaped polymer fine particles and method for producing the same - Google Patents

Plate-shaped polymer fine particles and method for producing the same

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Publication number
JP2849146B2
JP2849146B2 JP2029880A JP2988090A JP2849146B2 JP 2849146 B2 JP2849146 B2 JP 2849146B2 JP 2029880 A JP2029880 A JP 2029880A JP 2988090 A JP2988090 A JP 2988090A JP 2849146 B2 JP2849146 B2 JP 2849146B2
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Japan
Prior art keywords
polymer
plate
fine particles
dispersion
temperature
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JP2029880A
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Japanese (ja)
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JPH03234734A (en
Inventor
裕 柴田
貴史 松尾
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Kao Corp
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Kao Corp
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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、板状ポリマー微粒子及びその製造法、詳し
くは、化粧料、塗料、イオン交換樹脂の母材、クロマト
グラフィー用の充填剤などに使用し得る均一な板状ポリ
マー微粒子、及びその製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to plate-like polymer fine particles and a method for producing the same, and more particularly, to cosmetics, paints, base materials for ion-exchange resins, fillers for chromatography, and the like. The present invention relates to uniform plate-like polymer fine particles that can be used and a method for producing the same.

〔従来の技術〕[Conventional technology]

板状ポリマー微粒子の製造法としては、従来よりポリ
マーフィルム及び球状ポリマー粉体を機械的に粉砕、偏
平化する方法がある。例えば、ポリマーフィルム成形
後、液体窒素下で冷却粉砕する方法(特開昭57−78466
号公報)、球状ポリマー粉末を、(ガラス)ビーズ存在
下で該ポリマーに対し不活性な溶媒中で混合撹拌するこ
とにより偏平化する方法(特開昭62−164731号公報)が
ある。またこれらの他に、ポリマー溶液の微小液滴を平
板上で固化させる方法(特開昭63−117040号公報)もあ
る。
As a method for producing plate-shaped polymer fine particles, there is a method of mechanically pulverizing and flattening a polymer film and a spherical polymer powder. For example, a method in which a polymer film is formed and then cooled and pulverized under liquid nitrogen (JP-A-57-78466)
JP-A-62-164731 discloses a method of flattening a spherical polymer powder by mixing and stirring in a solvent inert to the polymer in the presence of (glass) beads. In addition to these methods, there is also a method of solidifying fine droplets of a polymer solution on a flat plate (JP-A-63-117040).

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

上記のような従来の製造法では、均一かつ確実に板状
ポリマー粒子が得られなかったり、操作が複雑で困難で
あったり、ポリマー種の選択の幅が狭いなどの問題があ
る。その上、従来の製造法では、より微細な板状ポリマ
ー粒子(平均厚みが1μm以下のもの)を得ることは容
易ではなかった。
The conventional production methods as described above have problems that plate-like polymer particles cannot be uniformly and reliably obtained, the operation is complicated and difficult, and the selection range of polymer species is narrow. Furthermore, it was not easy to obtain finer plate-like polymer particles (having an average thickness of 1 μm or less) by the conventional production method.

従って、本発明の目的は、均一な板状ポリマー微粒子
を提供すること、及びその製造法、即ち、操作が簡便か
つ容易で、しかも均一かつ確実に板状ポリマー微粒子を
得ることができ、また製造条件の選択によって板状ポリ
マー微粒子の厚み及びサイズ(長片)を容易に制御で
き、より微細(例えば、平均厚みが約0.1μmが長片が
厚みの約10倍程度)な板状ポリマー微粒子の製造も容易
に可能で、その上、熱や溶剤に対し安定な架橋型ポリマ
ーについても板状への成形加工が可能で、更にポリマー
種の選択の幅の非常に広い、板状ポリマー微粒子の製造
法を提供することにある。
Therefore, an object of the present invention is to provide uniform plate-like polymer fine particles and a method for producing the same, that is, a simple and easy operation, and moreover, to obtain uniform and reliable plate-like polymer fine particles. By selecting the conditions, the thickness and size (long piece) of the plate-like polymer fine particles can be easily controlled, and the finer plate-like polymer fine particles (for example, the average thickness of about 0.1 μm is about 10 times the thickness of the long piece) can be obtained. It is easy to manufacture, and furthermore, it is possible to form into a plate even a cross-linked polymer that is stable against heat and solvents, and to produce plate-shaped polymer fine particles with a very wide choice of polymer types. Is to provide a law.

〔課題を解決するための手段〕[Means for solving the problem]

本発明は、上記目的を、下記(1)の板状ポリマー微
粒子を提供すること、及びその製造法として下記(2)
の板状ポリマー微粒子の製造法を提供することにより達
成したものである。
The object of the present invention is to provide plate-like polymer fine particles of the following (1), and to provide the following method (2).
The present invention has been attained by providing a method for producing plate-like polymer fine particles.

(1)微粒子ポリマー分散液を、分散媒の凍結温度以下
に冷却した後、該ポリマーのガラス転移温度未満まで昇
温させて得られた、平均厚みが0.01〜100μm、長片が
厚みの10倍以上である板状ポリマー微粒子。
(1) After cooling the fine particle polymer dispersion below the freezing temperature of the dispersion medium and then raising the temperature to below the glass transition temperature of the polymer, the average thickness is 0.01 to 100 μm, and the long piece is 10 times the thickness. The above-mentioned plate-like polymer fine particles.

(2)平均粒径が500nm以下の微粒子ポリマー分散液
を、分散媒の凍結温度以下に冷却した後、該ポリマーの
ガラス転移温度未満まで昇温させ、平均厚みが0.01〜10
0μm、長片が厚みの10倍以上である板状ポリマー微粒
子を得ることを特徴とする板状ポリマー微粒子の製造
法。
(2) After cooling the fine particle polymer dispersion having an average particle size of 500 nm or less to a temperature lower than the freezing temperature of the dispersion medium, the temperature is raised to a temperature lower than the glass transition temperature of the polymer, and the average thickness is 0.01 to 10
A method for producing plate-shaped polymer fine particles, comprising obtaining plate-shaped polymer fine particles having a length of 0 μm and a long piece having a thickness of 10 times or more.

以下、本発明の板状ポリマー微粒子を、本発明の製造
法に基づいて詳述する。
Hereinafter, the plate-shaped polymer fine particles of the present invention will be described in detail based on the production method of the present invention.

本発明で原料として用いられるポリマーとしては、そ
の種類が特に制限されるものではなく、汎用ポリマー、
例えば、スチレン系、アクリル酸系、メタクリル酸系及
びこれらの共重合体、ジビニルベンゼンなどにより架橋
されたものなどを用いることができ、一般に知られてい
る乳化重合法によって容易に微粒子ポリマー分散液が得
られるものが好ましい。
The type of the polymer used as a raw material in the present invention is not particularly limited, and a general-purpose polymer,
For example, styrene-based, acrylic acid-based, methacrylic acid-based and copolymers thereof, and those crosslinked with divinylbenzene can be used, and a fine particle polymer dispersion can be easily formed by a generally known emulsion polymerization method. Those obtained are preferred.

上記ポリマーとしては、平均粒径が500nm以下、好ま
しくは30〜250nmの微粒子ポリマーを用いる。平均粒径
が500nm超のポリマーを用いると、微粒子間の融着が弱
く、板状成形が困難となる。
As the polymer, a fine particle polymer having an average particle diameter of 500 nm or less, preferably 30 to 250 nm is used. When a polymer having an average particle diameter of more than 500 nm is used, fusion between the fine particles is weak, and plate-like molding becomes difficult.

ポリマーの粒径は、サブミクロン粒子分析器(サブミ
クロン パーティクル アナライザー COULTER N4、コ
ールターエレクトロニック カンパニー社製)により測
定することができる。
The particle size of the polymer can be measured by a submicron particle analyzer (submicron particle analyzer COULTER N4, manufactured by Coulter Electronic Company).

また、ポリマー分散液の分散媒としては、ポリマーを
溶解させず分散できるものであれば、いずれのものでも
用いることができ、例えば、水及び水と相溶性のある溶
剤などが用いられ、分散の簡便さから、水、低級アルコ
ール及びそれらの混合物が好ましい。
Further, as the dispersion medium of the polymer dispersion, any one can be used as long as it can be dispersed without dissolving the polymer, for example, water and a solvent compatible with water are used, and For convenience, water, lower alcohols and mixtures thereof are preferred.

上記分散媒には分散剤を添加することが好ましく、か
かる分散剤としては、水溶性ポリマー、アニオン界面活
性剤、カチオン界面活性剤、両性界面活性剤、引イオン
界面活性剤及びこれらの混合物が用いられ、特に、アニ
オン界面活性剤、カチオン界面活性剤などが好ましい。
It is preferable to add a dispersant to the dispersion medium. As such a dispersant, a water-soluble polymer, an anionic surfactant, a cationic surfactant, an amphoteric surfactant, a ionic surfactant and a mixture thereof are used. In particular, an anionic surfactant and a cationic surfactant are preferred.

而して、本発明の板状ポリマー微粒子の製造法を実施
するには、まず、上記微粒子ポリマーを上記分散媒に分
散させた分散液を、分散媒の凍結温度以下に冷却し分散
媒を凍結させる。
Therefore, in order to carry out the method for producing plate-shaped polymer fine particles of the present invention, first, a dispersion liquid in which the fine particle polymer is dispersed in the dispersion medium is cooled to a temperature lower than the freezing temperature of the dispersion medium to freeze the dispersion medium. Let it.

この際、凍結時の製造条件、即ち、冷却凍結温度、ポ
リマー分散液の微粒子ポリマー濃度、微粒子ポリマーの
粒径、分散剤の種類、凍結容器の形状などを適宜変化さ
せることにより、生成する板状ポリマー微粒子のサイズ
及び厚みの制御が容易に可能である。
At this time, by appropriately changing the manufacturing conditions at the time of freezing, namely, the cooling freezing temperature, the fine particle polymer concentration of the polymer dispersion, the particle size of the fine particle polymer, the type of the dispersant, the shape of the freezing container, etc. The size and thickness of the polymer fine particles can be easily controlled.

例えば、ポリマー分散液の冷却を急激に行うことによ
り、より微細な板状ポリマー微粒子が得られる。即ち、
冷却冷凍温度を低くしたり、凍結容器の形状をポリマー
分散液と冷却媒との接触面積が大きくなる形状とするな
どの条件を選択することにより、より微細は板状ポリマ
ー微粒子が得られる。
For example, by rapidly cooling the polymer dispersion, finer plate-shaped polymer fine particles can be obtained. That is,
By selecting conditions such as lowering the cooling / freezing temperature or setting the shape of the freezing container so as to increase the contact area between the polymer dispersion and the cooling medium, finer plate-like polymer fine particles can be obtained.

また、ポリマー分散液のポリマー濃度を低くすること
によっても、より微細な板状ポリマー微粒子が得られ
る。
Also, by reducing the polymer concentration of the polymer dispersion, finer plate-shaped polymer fine particles can be obtained.

凍結は、完全に行えばその条件は問わないが、ポリマ
ー分散液を内部まで完全に凍結させるため、凍結状態を
15分間以上保持することが好ましい。
The conditions for the freezing are not limited as long as the polymer dispersion is completely frozen.
It is preferable to hold for 15 minutes or more.

また、ポリマー分散液の調製は、例えば、上記微粒子
ポリマー、上記分散媒及び上記分散剤を混合撹拌すれば
良く、また、ポリマーとして乳化重合法によって容易に
微粒子ポリマー分散液が得られるものを用いる場合は、
乳化重合によって得られる乳化重合液をそのままポリマ
ー分散液として使用できる。
In addition, the preparation of the polymer dispersion may be performed, for example, by mixing and stirring the fine particle polymer, the dispersion medium and the dispersant, and using a polymer that can easily obtain a fine particle polymer dispersion by an emulsion polymerization method. Is
The emulsion polymerization solution obtained by emulsion polymerization can be used as it is as a polymer dispersion.

また、ポリマー分散液のポリマー濃度は、ポリマー種
や目的とする板状ポリマー微粒子のサイズ及び厚みなど
によっても異なるが、通常1〜20重量%が好ましい。
The polymer concentration of the polymer dispersion varies depending on the type of the polymer and the size and thickness of the target plate-like polymer fine particles, but is usually preferably 1 to 20% by weight.

次に、上述の如くして凍結したポリマー分散液を、該
ポリマーのガラス転移温度未満、好ましくは該ガラス転
移温度より5℃程低い温度まで昇温させ融解させる。昇
温方法としては、例えば、凍結したポリマー分散液を常
温もしくは加熱した水に溶解し、必要に応じてさらに加
熱する方法、上記分散液を凍結乾燥し加熱する方法、上
記分散液を室温に放置する方法、及び上記分散液を容器
のまま加熱する方法などが挙げられ、凍結したポリマー
分散液を室温に放置する方法など、上記分散液を徐々に
加温する方法が好ましい。
Next, the polymer dispersion frozen as described above is heated to a temperature lower than the glass transition temperature of the polymer, preferably about 5 ° C. lower than the glass transition temperature, and is thawed. Examples of the method of raising the temperature include a method in which a frozen polymer dispersion is dissolved in room temperature or heated water and further heated as necessary, a method in which the dispersion is freeze-dried and heated, and a method in which the dispersion is left at room temperature. And a method of heating the dispersion liquid gradually, such as a method of leaving the frozen polymer dispersion liquid at room temperature.

昇温時、ガラス転移温度を越えるとポリマー表面が粘
弾性を有し、ポリマー同士の融着により形状が保持され
ない。従って、原料として用いるポリマーは、ガラス転
移温度が好ましくは室温以上、より好ましくは50℃以上
のものであり、製造時の昇温条件を考慮すればガラス転
移温度が50〜90℃のものが特に好ましい。
If the temperature exceeds the glass transition temperature when the temperature is raised, the polymer surface has viscoelasticity, and the shape is not maintained due to fusion between the polymers. Therefore, the polymer used as a raw material has a glass transition temperature of preferably room temperature or higher, more preferably 50 ° C. or higher, and especially those having a glass transition temperature of 50 to 90 ° C. in consideration of the temperature raising conditions during production. preferable.

このようにして、本発明の板状ポリマー微粒子が形成
される。
Thus, the plate-like polymer fine particles of the present invention are formed.

形成された板状ポリマー微粒子は、吸引濾過法、遠心
分離法など公知の方法により分散媒から単離することが
できる。
The formed plate-like polymer fine particles can be isolated from the dispersion medium by a known method such as a suction filtration method and a centrifugal separation method.

このようにして得られる本発明の板状ポリマー微粒子
は、平均厚みが0.01〜100μm、長片が厚みの10倍以上
のもので、微細な板状で形状も均一なため、化粧品用粉
体、着色料等に有用である。
The plate-like polymer fine particles of the present invention obtained in this way have an average thickness of 0.01 to 100 μm, and the long pieces have a thickness of 10 times or more, and have a uniform fine plate-like shape. Useful for coloring and the like.

〔実施例〕〔Example〕

以下に実施例を示し、本発明を更に詳しく説明する。 Hereinafter, the present invention will be described in more detail with reference to Examples.

実施例1 窒素ガス導入管、還流冷却器、温度計及び撹拌装置
(撹拌片は弦の長さ6cmの半月形のもの)を備えた1000m
lの五つ口セパラブルフラスコ中に3%のドデシル硫酸
ナトリウム水溶液400mlを加え、そこに重合開始剤であ
る過硫酸アンモニウムを1.0g加え、系内に窒素ガスを吹
き込みながらかつオイルバスを65℃に保ち、100rpm.で
撹拌しながら100gのスチレンモノマーを1時間で滴下し
た。そして、3時間重合を行い、その後、系内の温度を
75℃に昇温し撹拌を止め、1時間程熟成すると、残存モ
ノマー臭がほとんどなくなった。そして、室温まで徐冷
しポリスチレンエマルジョン(粒径が72.3nm)を得た。
次いで、この20%ポリスチレンエマルジョン5mlを直径2
cmのサンプル瓶に入れ、液体窒素中で15分間冷却凍結さ
せた。そして、これを室温にて放置して融解させた。そ
の結果、平均厚みが5μm、長片が厚みの約10倍である
板状ポリスチレンが得られた。
Example 1 1000 m equipped with a nitrogen gas inlet tube, a reflux condenser, a thermometer and a stirrer (a stirrer is a half-moon type having a string length of 6 cm).
400 ml of a 3% aqueous solution of sodium dodecyl sulfate was added to a 5-neck separable flask, and 1.0 g of ammonium persulfate, a polymerization initiator, was added to the flask. While keeping the mixture at 100 rpm, 100 g of styrene monomer was added dropwise over 1 hour. Then, polymerization is performed for 3 hours, and then the temperature in the system is reduced.
When the temperature was raised to 75 ° C., stirring was stopped, and the mixture was aged for about 1 hour, the residual monomer odor almost disappeared. Then, the mixture was gradually cooled to room temperature to obtain a polystyrene emulsion (particle size: 72.3 nm).
Then, 5 ml of this 20% polystyrene emulsion was added
The samples were placed in cm sample bottles and refrigerated in liquid nitrogen for 15 minutes. This was left to melt at room temperature. As a result, plate-like polystyrene having an average thickness of 5 μm and a long piece about 10 times the thickness was obtained.

実施例2 実施例1で得られた20%ポリスチレンエマルジョンを
5%に希釈し、これを実施例1と同様に凍結、溶解を行
った。その結果、平均厚みが1μm、長片が厚みの約20
倍である板状ポリスチレンが得られた。
Example 2 The 20% polystyrene emulsion obtained in Example 1 was diluted to 5% and frozen and melted in the same manner as in Example 1. As a result, the average thickness was 1 μm,
A double-fold plate-like polystyrene was obtained.

実施例3 窒素ガス導入管、還流冷却器、温度計及び撹拌装置
(撹拌片は弦の長さ6cmの半月形のもの)を備えた1000m
lの五つ口セパラブルフラスコ中に3%のラウリルトリ
メチルアンモニウムクロライド水溶液400mlを加え、そ
こに重合開始剤である2,2アゾビス(2−アミジノプロ
パン)二塩酸塩0.7g加え、系内に窒素ガスを吹き込みな
がらかつオイルバスを65℃に保ち、100rpm.で撹拌しな
がら100gのメタクリル酸エチルとメタクリル酸n−ブチ
ルとの1:1混合物を1時間で滴下した。そして、3時間
重合を行い、その後、系内の温度を75℃に昇温し撹拌を
止め、1時間程熟成すると、残存モノマー臭がほとんど
なくなった。そして、室温まで徐冷しポリメタクリル酸
エチル/n−ブチル共重合体エマルジョン(粒径が80.8n
m)を得た。次いで、この20%ポリメタクリル酸エチル/
n−ブチル共重合体エマルジョン5mlを直径2cmのサンプ
ル瓶に入れ、液体窒素中で15分間冷却凍結させた。そし
て、これを室温にて放置して融解させ、50℃の水溶中に
浸し、1時間熱処理・焼結した(板状ポリマーの機械強
度が増大)。次にそれを濾過することにより平均厚み3
μm、長片が厚みの約30倍である板状ポリメタクリル酸
エチル/n−ブチル共重合体が粉体として得られた。
Example 3 1000 m equipped with a nitrogen gas inlet tube, a reflux condenser, a thermometer and a stirrer (the stirrer is a half-moon type having a string length of 6 cm).
400 ml of a 3% aqueous solution of lauryltrimethylammonium chloride was added to a 5-neck separable flask, and 0.7 g of 2,2 azobis (2-amidinopropane) dihydrochloride as a polymerization initiator was added thereto. 100 g of a 1: 1 mixture of ethyl methacrylate and n-butyl methacrylate was added dropwise over 1 hour while blowing the gas and keeping the oil bath at 65 ° C. and stirring at 100 rpm. Then, the polymerization was carried out for 3 hours, and then the temperature in the system was raised to 75 ° C., stirring was stopped, and the mixture was aged for about 1 hour. Then, the mixture was gradually cooled to room temperature, and a polyethyl methacrylate / n-butyl copolymer emulsion (having a particle size of 80.8 n
m). Next, the 20% polyethyl methacrylate /
5 ml of the n-butyl copolymer emulsion was placed in a sample bottle having a diameter of 2 cm, and cooled and frozen in liquid nitrogen for 15 minutes. Then, it was left to melt at room temperature, immersed in an aqueous solution at 50 ° C., and heat-treated and sintered for 1 hour (the mechanical strength of the platy polymer increased). Then it is filtered to obtain an average thickness of 3
A plate-shaped polyethyl methacrylate / n-butyl copolymer having a length of about 30 μm and a length of about 30 times the thickness was obtained as a powder.

実施例4 実施例3で得られた20%ポリメタクリル酸エチル/n−
ブチル共重合体エマルジョン(粒径が80.8nm)5mlを直
径2cmのサンプル瓶に入れ、−23℃で冷却、凍結、融解
と行った。その結果、平均厚みが20μm、長片が厚みの
約15倍である板状ポリメタクリル酸エチル/n−ブチル共
重合体が得られた。
Example 4 20% polyethyl methacrylate / n- obtained in Example 3
5 ml of a butyl copolymer emulsion (having a particle size of 80.8 nm) was placed in a sample bottle having a diameter of 2 cm, and cooled, frozen and thawed at -23 ° C. As a result, a plate-like poly (ethyl methacrylate / n-butyl) copolymer having an average thickness of 20 μm and a long piece about 15 times the thickness was obtained.

実施例5 実施例3で得られた20%ポリメタクリル酸エチル/n−
ブチル共重合体エマルジョン(粒径が80.8nm)5mlを直
径4cmのサンプル瓶に入れ、液体窒素中で15分間冷却
し、凍結、融解させた。その結果、平均厚みが2μm、
長片が厚みの約30倍である板状ポリメタクリル酸エチル
/n−ブチル共重合体が得られた。
Example 5 20% polyethyl methacrylate / n- obtained in Example 3
5 ml of a butyl copolymer emulsion (having a particle size of 80.8 nm) was placed in a sample bottle having a diameter of 4 cm, cooled in liquid nitrogen for 15 minutes, frozen and thawed. As a result, the average thickness was 2 μm,
Plate-shaped poly (ethyl methacrylate) whose long piece is about 30 times the thickness
/ n-butyl copolymer was obtained.

実施例6 窒素ガス導入管、還流冷却器、温度計及び撹拌装置
(撹拌片は弦の長さ6cmの半月形のもの)を備えた1000m
lの五つ口セパラブルフラスコ中に4%のドデシル硫酸
ナトリウム水溶液400mlを加え、そこに重合開始剤であ
る過硫酸カリウムを1.5g加え、系内に窒素ガスを吹き込
みながらかつオイルバスを65℃に保ち、300rpm.で撹拌
しながら100gのスチレンモノマーを1時間で滴下した。
そして、3時間重合を行い、その後、系内の温度を75℃
に昇温し撹拌を止め、1時間程熟成すると、残存モノマ
ー臭がほとんどなくなった。そして、室温まで徐冷しポ
リスチレンエマルジョン(粒径が29.0nm)を得た。次い
で、この20%ポリスチレンエマルジョン5mlを直径2cmの
サンプル瓶に入れ、液体窒素中で15分間冷却凍結させ
た。そして、これを室温にて放置して融解させた。その
結果、平均厚みが0.5μm、長片が厚みの約50倍である
板状ポリスチレンが得られた。
Example 6 1000 m provided with a nitrogen gas inlet tube, a reflux condenser, a thermometer and a stirring device (the stirring piece is a half-moon type having a string length of 6 cm).
400 ml of a 4% aqueous solution of sodium dodecyl sulfate was added to a 5-neck separable flask, and 1.5 g of potassium persulfate as a polymerization initiator was added thereto. The nitrogen bath was blown into the system at 65 ° C. while blowing nitrogen gas into the system. , And 100 g of styrene monomer was added dropwise over 1 hour while stirring at 300 rpm.
Then, polymerization was performed for 3 hours, and then the temperature in the system was increased to 75 ° C.
When the temperature was raised to a low level and the stirring was stopped, the mixture was aged for about 1 hour. Then, the mixture was gradually cooled to room temperature to obtain a polystyrene emulsion (particle size: 29.0 nm). Then, 5 ml of this 20% polystyrene emulsion was placed in a sample bottle having a diameter of 2 cm, and cooled and frozen in liquid nitrogen for 15 minutes. This was left to melt at room temperature. As a result, plate-like polystyrene having an average thickness of 0.5 μm and a long piece of about 50 times the thickness was obtained.

〔発明の効果〕〔The invention's effect〕

本発明の板状ポリマー微粒子は、平均厚みが0.01〜10
0μm、長片が厚みの10倍以上のもので、微細な板状で
形状も均一なため、化粧料、塗料、イオン交換樹脂の母
材、クロマトグラフィー用の充填剤などに使用できる。
The plate-like polymer fine particles of the present invention have an average thickness of 0.01 to 10
Since it has a thickness of 0 μm and a length of 10 or more times the thickness, and has a fine plate shape and a uniform shape, it can be used as a cosmetic, a paint, a base material of an ion exchange resin, a filler for chromatography, and the like.

また、本発明の板状ポリマー微粒子の製造法は、操作
が簡便かつ容易で、しかも均一かつ確実に本発明の板状
ポリマー微粒子を得ることができ、また製造条件の選択
によって板状ポリマー微粒子の厚み及びサイズ(長片)
を容易に制御でき、より微細(例えば、平均厚みが約0.
1μmで長片が厚みの約10倍程度)な板状ポリマー微粒
子の製造も容易に可能で、その上、熱や溶剤に対し安定
な架橋型ポリマーについても板上への成形加工が可能
で、更にポリマー種の選択の幅が非常に広いなどの効果
を有する。
In addition, the method for producing the plate-like polymer fine particles of the present invention is simple and easy to operate, and can uniformly and reliably obtain the plate-like polymer fine particles of the present invention. Thickness and size (long piece)
Can be easily controlled and finer (for example, an average thickness of about 0.
It is also possible to easily produce plate-like polymer fine particles (1 μm, the length of which is about 10 times the thickness), and it is also possible to mold cross-linked polymers that are stable against heat and solvents on the plate. Further, there is an effect that the selection range of the polymer type is very wide.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】微粒子ポリマー分散液を、分散媒の凍結温
度以下に冷却した後、該ポリマーのガラス転移温度未満
まで昇温させて得られた、平均厚みが0.01〜100μm、
長片が厚みの10倍以上である板状ポリマー微粒子。
An average thickness of a fine particle polymer dispersion obtained by cooling the dispersion to a temperature lower than the glass transition temperature of the polymer after cooling the dispersion to a temperature lower than the freezing temperature of the dispersion medium.
Plate-shaped polymer fine particles whose long pieces are 10 times or more the thickness.
【請求項2】平均粒径が500nm以下の微粒子ポリマー分
散液を、分散媒の凍結温度以下に冷却した後、該ポリマ
ーのガラス転移温度未満まで昇温させ、平均厚みが0.01
〜100μm、長片が厚みの10倍以上である板状ポリマー
微粒子を得ることを特徴とする板状ポリマー微粒子の製
造法。
2. A fine particle polymer dispersion having an average particle size of 500 nm or less is cooled to a temperature lower than the freezing temperature of the dispersion medium, and then heated to a temperature lower than the glass transition temperature of the polymer.
A method for producing plate-like polymer fine particles, wherein plate-like polymer fine particles having a length of 100 μm or more and a long piece having a thickness of 10 times or more are obtained.
JP2029880A 1990-02-09 1990-02-09 Plate-shaped polymer fine particles and method for producing the same Expired - Fee Related JP2849146B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
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Publications (2)

Publication Number Publication Date
JPH03234734A JPH03234734A (en) 1991-10-18
JP2849146B2 true JP2849146B2 (en) 1999-01-20

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6794448B2 (en) 2000-03-21 2004-09-21 Sekisui Plastics Co., Ltd. Resin particles and process for producing the same
JP4509770B2 (en) * 2004-12-28 2010-07-21 花王株式会社 Method for producing organic plate-like particles
JP5525326B2 (en) * 2009-05-11 2014-06-18 株式会社コーセー Hydrophilic / hydrophobic anisotropic plate-like particle, method for producing the same, and emulsifier comprising the same
CN104084179B (en) * 2014-07-07 2015-12-02 中国科学院化学研究所 A kind of polyalcohol integral pole and preparation method thereof and application

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Publication number Publication date
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