JPH11140139A - Spherical fine particle of polymer having wrinkle structure on its surface and preparation thereof - Google Patents

Spherical fine particle of polymer having wrinkle structure on its surface and preparation thereof

Info

Publication number
JPH11140139A
JPH11140139A JP32230497A JP32230497A JPH11140139A JP H11140139 A JPH11140139 A JP H11140139A JP 32230497 A JP32230497 A JP 32230497A JP 32230497 A JP32230497 A JP 32230497A JP H11140139 A JPH11140139 A JP H11140139A
Authority
JP
Japan
Prior art keywords
fine particles
polymer fine
polymer
styrene
parts
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.)
Granted
Application number
JP32230497A
Other languages
Japanese (ja)
Other versions
JP3700997B2 (en
Inventor
Shunsaku Tanaka
俊作 田中
Hiroshi Asano
弘嗣 浅野
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.)
Ganz Chemical Co Ltd
Original Assignee
Ganz Chemical Co 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 Ganz Chemical Co Ltd filed Critical Ganz Chemical Co Ltd
Priority to JP32230497A priority Critical patent/JP3700997B2/en
Publication of JPH11140139A publication Critical patent/JPH11140139A/en
Application granted granted Critical
Publication of JP3700997B2 publication Critical patent/JP3700997B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a spherical fine particle of polymer, with an average particle diameter of 2 to 300 μm, having a regular wrinkle structure on its surface. SOLUTION: A styrene elastomer is dissolved in an amt. of 5 to 30 pts.wt. in a mixture of 40 to 90 pts.wt. hydrophobic polymerizable vinyl monomer with 1 to 40 pts.wt. crosslinkable monomer, followed by suspension polymn. in an aq. medium to prepare a spherical fine particle of a polymer having a regular wrinkle structure on its surface.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、粒子表面にシワ状
構造を有するポリマー微粒子に関するものである。この
ポリマー微粒子は、塗料や化粧品に添加して、それらに
粘性特性、光散乱特性や独特の表面特性を付与するのに
効果的である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to polymer fine particles having a wrinkled structure on the surface of the particles. These polymer microparticles are effective for adding to paints and cosmetics to give them viscous properties, light scattering properties and unique surface properties.

【0002】[0002]

【従来の技術】平均粒子径2〜300μmのポリマー微
粒子は、通常重合性ビニルモノマーを水性媒体中、分散
安定剤の存在下、ホモミキサー等により強制分散させて
液滴化したのち、懸濁重合させることにより製造され
る。懸濁重合によるポリマー微粒子の製造においては、
液状の重合性ビニルモノマーは、水性媒体中でその表面
張力のため通常は球状となり、重合して得られるポリマ
ー微粒子も表面が平滑な球状微粒子となる。球状でな
い、もしくは表面が平滑でない異形ポリマー粒子の製造
法としては、重合性ビニルモノマーとして親水性ビニル
モノマーを用い、架橋性モノマーを油溶性物質の存在下
で懸濁重合させ、椀状のポリマー微粒子を得る方法(特
開昭61-87734号,特開平2-255704号)が知られている。
しかし粒子表面が規則的なシワ状構造を有する球状ポリ
マー微粒子はまだ知られていない。
2. Description of the Related Art Polymer fine particles having an average particle diameter of 2 to 300 μm are usually prepared by forcibly dispersing a polymerizable vinyl monomer in an aqueous medium in the presence of a dispersion stabilizer using a homomixer or the like to form droplets. It is manufactured by having In the production of polymer fine particles by suspension polymerization,
The liquid polymerizable vinyl monomer is usually spherical due to its surface tension in an aqueous medium, and the polymer fine particles obtained by polymerization are also spherical fine particles having a smooth surface. As a method for producing irregularly shaped polymer particles that are not spherical or whose surface is not smooth, a hydrophilic vinyl monomer is used as a polymerizable vinyl monomer, and a crosslinkable monomer is subjected to suspension polymerization in the presence of an oil-soluble substance to form a bowl-shaped polymer fine particle. (JP-A-61-87734 and JP-A-2-255704) are known.
However, spherical polymer fine particles having a regular wrinkle-like structure on the particle surface have not yet been known.

【0003】[0003]

【発明が解決しようとする課題】本発明はポリマー微粒
子表面に規則的なシワ状構造を有する新規なポリマー微
粒子を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide novel polymer fine particles having a regular wrinkle-like structure on the surface of the polymer fine particles.

【0004】[0004]

【課題を解決するための手段】本発明者らは、前記課題
のポリマー微粒子を得るため鋭意検討した結果、疎水性
の重合性ビニルモノマーおよび架橋性モノマーの混合物
にスチレン系エラストマーを溶解させ、水性媒体中で懸
濁重合させると、微粒子表面が規則的なシワ状構造を有
する新規な球状ポリマー微粒子が得られることを見い出
し、本発明を完成させるに至った。すなわち、本発明
は、(1)表面に規則的なシワ状構造を有する球状ポリ
マー微粒子、(2)平均粒子径が2〜300μmである
前記(1)記載の球状ポリマー微粒子、(3)疎水性の
重合性ビニルモノマー40〜90重量部および架橋性モ
ノマー1〜40重量部の混合物にスチレン系エラストマ
ー5〜30重量部を溶解させ、水性媒体中で懸濁重合さ
せる表面が規則的なシワ状構造を有する球状ポリマー微
粒子の製造法、および(4)重合性ビニルモノマーが
(メタ)アクリル酸アルキルエステルである前記(3)
記載の製造法、である。
Means for Solving the Problems The present inventors have conducted intensive studies to obtain the above polymer fine particles, and as a result, dissolved a styrene elastomer in a mixture of a hydrophobic polymerizable vinyl monomer and a crosslinkable monomer, It has been found that when suspension polymerization is carried out in a medium, novel spherical polymer fine particles having a fine wrinkle-like structure on the surface of the fine particles can be obtained, thereby completing the present invention. That is, the present invention provides (1) spherical polymer fine particles having a regular wrinkle-like structure on the surface, (2) the spherical polymer fine particles according to the above (1) having an average particle diameter of 2 to 300 μm, and (3) hydrophobicity. A styrene-based elastomer is dissolved in a mixture of 40 to 90 parts by weight of a polymerizable vinyl monomer and 1 to 40 parts by weight of a crosslinkable monomer, and the suspension is subjected to suspension polymerization in an aqueous medium. And (4) the method wherein the polymerizable vinyl monomer is an alkyl (meth) acrylate.
The production method described.

【0005】[0005]

【発明の実施の形態】本発明に用いられる疎水性の重合
性ビニルモノマーとしては、例えばスチレン、α−メチ
ルスチレン,ビニルトルエン等の芳香族ビニル単量体,
アクリル酸メチル,アクリル酸エチル,アクリル酸ブチ
ル等のアクリル酸アルキルエステル類、メタクリル酸メ
チル,メタクリル酸エチル,メタクリル酸ブチル等のメ
タクリル酸アルキルエステル類、酢酸ビニル,プロピオ
ン酸ビニル等のビニルエステル系単量体、(メタ)アク
リロニトリル等のビニルシアン系単量体、塩化ビニル、
塩化ビニリデン等のハロゲン化ビニル単量体など分子中
に、たとえば水酸基、カルボキシル基、アミノ基、スル
ホン酸基などの親水性基を有しない疎水性ビニル単量体
を使用することができる。本発明に用いられる架橋性ビ
ニルモノマーとしては、例えばジビニルベンゼン、ジビ
ニルトルエンなどの芳香族ジビニル化合物、エチレング
リコールジ(メタ)アクリレート、ジエチレングリコー
ルジ(メタ)アクリレート等のグリコールジ(メタ)ア
クリレート、例えばトリメチロールプロパントリ(メ
タ)アクリレート、ペンタエリスリトールテトラ(メ
タ)アクリレート等のトリ(メタ)アクリレート、テト
ラ(メタ)アクリレートなど重合性不飽和結合を1分子
中に2個以上有する化合物が挙げられる。
BEST MODE FOR CARRYING OUT THE INVENTION The hydrophobic polymerizable vinyl monomer used in the present invention includes, for example, aromatic vinyl monomers such as styrene, α-methylstyrene and vinyltoluene;
Alkyl acrylates such as methyl acrylate, ethyl acrylate, butyl acrylate, etc .; alkyl methacrylates such as methyl methacrylate, ethyl methacrylate, butyl methacrylate; vinyl ester such as vinyl acetate and vinyl propionate Monomer, vinyl cyanide monomer such as (meth) acrylonitrile, vinyl chloride,
A hydrophobic vinyl monomer having no hydrophilic group such as a hydroxyl group, a carboxyl group, an amino group, or a sulfonic acid group in a molecule such as a halogenated vinyl monomer such as vinylidene chloride can be used. Examples of the crosslinkable vinyl monomer used in the present invention include aromatic divinyl compounds such as divinylbenzene and divinyltoluene; glycol di (meth) acrylates such as ethylene glycol di (meth) acrylate and diethylene glycol di (meth) acrylate; Examples thereof include compounds having two or more polymerizable unsaturated bonds in one molecule such as tri (meth) acrylate such as methylolpropane tri (meth) acrylate and pentaerythritol tetra (meth) acrylate, and tetra (meth) acrylate.

【0006】本発明で使用されるスチレン系エラストマ
ーは疎水性の重合性ビニルモノマーおよび架橋性モノマ
ーの混合物に室温または加温下に溶解するものでなけれ
ばならない。その例としては、スチレンとブタジエン、
イソプレン等の共重合体エラストマーをあげることがで
きる。なかでもスチレン−ブタジエン−スチレン、スチ
レン−イソプレン−スチレン、スチレン−(エチレン/
ブチレン)−スチレン、スチレン−(エチレン/プロピ
レン)−スチレン等のブロック共重合エラストマー体が
特に好ましい。これらスチレン系エラストマーの分子量
は疎水性の重合性ビニルモノマ−の混合液に室温もしく
は加熱して溶解するものであればとくに制限はないがポ
リマ−濃度25%のトルエン溶液の粘度が1000mPa・
sから、ポリマ−濃度15%のトルエン溶液の粘度が5
000mPa・sまでのものが好ましい。これらのスチレン
系エラストマーは一種あるいは二種以上の組み合わせで
用いることができる。前記疎水性の重合性ビニルモノマ
ー、架橋性モノマーおよびスチレン系エラストマーの各
使用量は、重量比で通常40〜90:1〜40:5〜3
0、好ましくは45〜80:3〜30:10〜25であ
る。疎水性の重合性ビニルモノマ−、架橋性モノマ−お
よびスチレン系エラストマ−の使用量が上記の範囲を外
れるとその粒子表面に充分且つ規則的なシワ構造を有す
る球状ポリマ−微粒子が得られない。
The styrenic elastomer used in the present invention must be soluble in a mixture of a hydrophobic polymerizable vinyl monomer and a crosslinkable monomer at room temperature or under heating. Examples include styrene and butadiene,
And copolymer elastomers such as isoprene. Among them, styrene-butadiene-styrene, styrene-isoprene-styrene, styrene- (ethylene /
Particularly preferred are block copolymer elastomers such as butylene) -styrene and styrene- (ethylene / propylene) -styrene. The molecular weight of these styrene-based elastomers is not particularly limited as long as they can be dissolved in a mixed solution of a hydrophobic polymerizable vinyl monomer at room temperature or by heating, but the viscosity of a toluene solution having a polymer concentration of 25% is 1000 mPa · s.
The viscosity of a toluene solution having a polymer concentration of 15% is 5
It is preferably up to 000 mPa · s. These styrene elastomers can be used alone or in combination of two or more. The amount of each of the hydrophobic polymerizable vinyl monomer, crosslinkable monomer and styrene-based elastomer used is usually 40 to 90: 1 to 40: 5 to 3 by weight.
0, preferably 45 to 80: 3 to 30:10 to 25. If the amount of the hydrophobic polymerizable vinyl monomer, cross-linkable monomer or styrene-based elastomer is out of the above range, spherical polymer fine particles having a sufficient and regular wrinkle structure on the particle surface cannot be obtained.

【0007】疎水性の重合性ビニルモノマーと架橋性モ
ノマー混合物へのスチレン系エラストマーの溶解度を上
げたり、重合中に起こる液滴内の相分離を促進するた
め、必要に応じてモノマー混合物に相溶する油溶性溶剤
や、例えばポリブテン,ポリブタジエン,ポリイソプレ
ン等の低結晶性エラストマ−や液状ゴムを併用してもよ
い。前記油溶性溶剤としては、酢酸メチル,酢酸エチ
ル,酪酸ブチル,酪酸イソアミル等のエステル類:ジエ
チルケトン,メチルエチルケトン等のケトン類:さらに
はベンゼン,トルエン,キシレン等の芳香族炭化水素
類:ブタン,ペンタン,ヘキサン等の脂肪族炭化水素
類:オリーブ油,ラート油,ヤシ油,ヒマシ油等の長鎖
アルキル誘導体等をあげることができる。これらの油溶
性溶剤、低結晶性エラストマ−や液状ゴムはモノマ−混
合物100重量部に対し5〜20重量部程度用いられ
る。本発明に用いられる前記各モノマーとスチレン系エ
ラストマーを溶解した溶液を水性媒体中に液滴化した分
散液は次の工程で懸濁重合させるが、原料液滴及び生成
重合体粒子の分散性向上のため、各種の界面活性剤や高
分子保護コロイド等の分散安定剤の適量が用いられる。
[0007] In order to increase the solubility of the styrenic elastomer in the mixture of the hydrophobic polymerizable vinyl monomer and the crosslinkable monomer, and to promote the phase separation in the droplets occurring during the polymerization, the styrene-based elastomer must be compatible with the monomer mixture if necessary. An oil-soluble solvent, a low crystalline elastomer such as polybutene, polybutadiene, polyisoprene, or a liquid rubber may be used in combination. Examples of the oil-soluble solvent include esters such as methyl acetate, ethyl acetate, butyl butyrate, and isoamyl butyrate; ketones such as diethyl ketone and methyl ethyl ketone; and aromatic hydrocarbons such as benzene, toluene, and xylene: butane and pentane. And hydrocarbons such as hexane: long-chain alkyl derivatives such as olive oil, rat oil, coconut oil and castor oil. These oil-soluble solvents, low-crystalline elastomers and liquid rubbers are used in an amount of about 5 to 20 parts by weight based on 100 parts by weight of the monomer mixture. The dispersion obtained by dispersing a solution in which each of the monomers and the styrene-based elastomer used in the present invention are dissolved into an aqueous medium is subjected to suspension polymerization in the next step, but the dispersibility of the raw material droplets and the produced polymer particles is improved. Therefore, an appropriate amount of a dispersion stabilizer such as various surfactants and polymer protective colloids is used.

【0008】分散安定剤としては、ドデシルベンゼンス
ルホン酸ナトリウム,ラウリル硫酸ナトリウムなどの界
面活性剤、ゼラチン,メチルセルロース,ヒドロキシエ
チルセルロース,ポリビニルアルコール,ポリアクリル
酸塩等の水溶性高分子、リン酸三カルシウム,炭酸マグ
ネシウム等の難水溶性無機物が用いられる。これらの分
散安定剤は単独でもまた二種以上の組み合わせでも用い
られる。これらの分散安定剤は、通常の懸濁重合の際に
用いられる使用量で安定に重合を行うことができる。本
発明の懸濁重合に際しては重量開始剤の他、必要により
さらに連鎖移動剤、重合禁止剤などの適量を用いてもよ
い。重合開始剤としてはこの種の反応に通常用いられる
もの、例えば過酸化ベンゾイル,過酸化ラウロイル等の
過酸化物系開始剤、2,2′−アゾビスイソブチロニト
リル,2,2′−イソバレロニトリル等のアゾ重合開始
剤が挙げられる。これらの重合開始剤は重合性モノマー
に溶解させて使用される。連鎖移動剤もこの種の反応に
通常用いられるものでよく、例えばモノチオール,ポリ
チオール,キサントゲンジスルフィド,チウラムジスル
フィド,メルカプト酢酸2−エチルヘキシルエステル,
オクタン酸2−メルカプトエチルエステル,メルカプト
酢酸メトキシブチルエステル,メルカプトプロピオン酸
メトキシブチルエステル,α−メチルスチレンダイマ
ー,ターピノーレン等が好ましく用いられる。また、重
合禁止剤としては、例えば亜硝酸ナトリウム、亜硫酸ナ
トリウム、塩化第二銅などの通常用いられる重合禁止剤
の適量が用いられる。
Examples of the dispersion stabilizer include surfactants such as sodium dodecylbenzenesulfonate and sodium lauryl sulfate, water-soluble polymers such as gelatin, methylcellulose, hydroxyethylcellulose, polyvinyl alcohol and polyacrylate, tricalcium phosphate, and the like. A poorly water-soluble inorganic substance such as magnesium carbonate is used. These dispersion stabilizers can be used alone or in combination of two or more. These dispersion stabilizers can stably carry out the polymerization in the amounts used during normal suspension polymerization. In the suspension polymerization of the present invention, an appropriate amount of a chain transfer agent, a polymerization inhibitor, or the like may be used, if necessary, in addition to the weight initiator. As the polymerization initiator, those usually used in this type of reaction, for example, peroxide initiators such as benzoyl peroxide and lauroyl peroxide, 2,2'-azobisisobutyronitrile, 2,2'-iso An azo polymerization initiator such as valeronitrile is exemplified. These polymerization initiators are used after being dissolved in a polymerizable monomer. Chain transfer agents may also be those commonly used in this type of reaction, such as monothiol, polythiol, xanthogen disulfide, thiuram disulfide, mercaptoacetic acid 2-ethylhexyl ester,
Octanoic acid 2-mercaptoethyl ester, mercaptoacetic acid methoxybutyl ester, mercaptopropionic acid methoxybutyl ester, α-methylstyrene dimer, terpinolene and the like are preferably used. As the polymerization inhibitor, an appropriate amount of a commonly used polymerization inhibitor such as sodium nitrite, sodium sulfite, cupric chloride or the like is used.

【0009】ポリマー微粒子の平均粒径は疎水性の重合
性ビニルモノマー、架橋性モノマーおよびスチレン系エ
ラストマーの混合溶液を分散して、分散安定化した液滴
径とほぼ同径のものがその後の重合反応によって得られ
る。液滴径の大小は分散安定剤の種類と使用量の選択お
よびホモミキサー等の強制分散機の回転数等により、任
意に制御できる。目的の粒径の液滴を調整し、続いて重
合させることにより、任意に2〜300μmのポリマー
微粒子を製造することができる。本発明の重合反応にお
ける重合温度は用いる重合開始剤、モノマーや必要に応
じて添加される重合禁止剤、連鎖移動剤などの種類によ
って異なってくるが通常30〜100℃であり、好まし
くは50〜90℃である。懸濁重合後、球状ポリマー微
粒子を濾別し、水洗後乾燥することにより粒子表面が規
則的なシワ状構造を有する微粒子が得られる。
The average particle size of the polymer fine particles is approximately the same as the dispersion-stabilized droplet diameter of a mixed solution of a hydrophobic polymerizable vinyl monomer, a crosslinkable monomer, and a styrene-based elastomer. Obtained by reaction. The size of the droplet diameter can be arbitrarily controlled by selecting the type and amount of the dispersion stabilizer and the rotation speed of a forced disperser such as a homomixer. By adjusting droplets having a desired particle size and subsequently polymerizing, polymer fine particles of 2 to 300 μm can be arbitrarily produced. The polymerization temperature in the polymerization reaction of the present invention varies depending on the type of the polymerization initiator used, the monomer and the polymerization inhibitor optionally added, the chain transfer agent and the like, but is usually 30 to 100 ° C, preferably 50 to 100 ° C. 90 ° C. After the suspension polymerization, the spherical polymer fine particles are separated by filtration, washed with water, and dried to obtain fine particles having a regular wrinkle-like structure on the particle surface.

【0010】[0010]

【実施例】以下に実施例によって本発明をさらに具体的
に説明するが、本発明はこれらの実施例により限定され
るものではない。なお実施例中「部」は重量部を表す。 実施例1 メチルメタクリレート75部およびエチレングリコール
ジメタクリレート5部の混合液にスチレン−ブタジエン
−スチレン ブロックコポリマー(シェルジャパン
(株)製、KX408P)20部とアゾビスイソバレロ
ニトリル0.5部を溶解させたものにポリビニルアルコ
ール(クラレ(株)製、PVA205)の10%水溶液
25部、1%エチレンオキサイド−プロピレンオキサイ
ド系ノニオン界面活性剤(日本油脂(株)製、プロノン
208)1部およびイオン交換水275部を注入した。
得られた混合液をホモミキサー(特殊機化工業(株)
製)を用いて、7,000rpmで20分間撹拌し、原料分
散液を調製した。この原料分散液を撹拌機及び還流冷却
器を備えた重合反応容器内に仕込み、窒素気流下撹拌し
ながら80℃に昇温し、3時間重合させた。得られたポ
リマー微粒子分散液を脱水、洗浄、乾燥し、篩別するこ
とにより平均粒径36μmの粒子表面にシワ状構造を有
するポリマー微粒子〔図1〕85重量部を得た。
EXAMPLES The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples. In the examples, "parts" represents parts by weight. Example 1 In a mixed solution of 75 parts of methyl methacrylate and 5 parts of ethylene glycol dimethacrylate, 20 parts of a styrene-butadiene-styrene block copolymer (KX408P, manufactured by Shell Japan K.K.) and 0.5 part of azobisisovaleronitrile were dissolved. 25 parts of a 10% aqueous solution of polyvinyl alcohol (PVA205, manufactured by Kuraray Co., Ltd.), 1 part of a 1% ethylene oxide-propylene oxide nonionic surfactant (Pronon 208, manufactured by NOF Corporation) and ion-exchanged water 275 parts were injected.
The resulting mixture is mixed with a homomixer (Special Kika Kogyo Co., Ltd.)
Was stirred at 7,000 rpm for 20 minutes to prepare a raw material dispersion. This raw material dispersion was charged into a polymerization reaction vessel equipped with a stirrer and a reflux condenser, and the temperature was raised to 80 ° C. while stirring under a nitrogen stream to carry out polymerization for 3 hours. The obtained polymer fine particle dispersion was dehydrated, washed, dried, and sieved to obtain 85 parts by weight of polymer fine particles having an average particle diameter of 36 μm and having a wrinkle-like structure on the surface of the particles (FIG. 1).

【0011】実施例2 メチルメタクリレート75部およびエチレングリコール
ジメタクリレート5部の混合液にスチレン−イソプレン
−スチレン ブロックコポリマー(シェルジャパン
(株)製、D−1107CP)15部とポリブテン(日
本石油化学(株)製、日石ポリブテンHV300)5部
とアゾビスイソバレロニトリル0.5部を溶解させたも
のを実施例1と同様の操作を行い(ただしホモミキサー
の回転数は9,000rpm)、平均粒径が21μmの表面
にシワ状構造を有するポリマー微粒子〔図2〕86重量
部を得た。 実施例3 実施例1のモノマー混合液に5部のトルエンを追加し、
他は同様の操作を行うことにより、平均粒径30μmの
粒子表面のシワがやや大きめのポリマー微粒子86重量
部を得た。 比較例1 実施例1においてブロックコポリマーの使用量を20部
から1部に変更した他は同様の操作を行ったが、粒子表
面は平滑でありシワ状構造を有する球状ポリマー微粒子
を得ることができなかった。 比較例2 実施例1においてエチレングリコールジメタクリレート
5部を添加しない他は同様の操作を行ったが、粒子表面
は平滑であり、シワ状構造を有するポリマー微粒子を得
ることができなかった。
Example 2 A mixture of 75 parts of methyl methacrylate and 5 parts of ethylene glycol dimethacrylate was mixed with 15 parts of a styrene-isoprene-styrene block copolymer (D-1107CP, manufactured by Shell Japan KK) and polybutene (Nippon Petrochemical Co., Ltd.). 5 parts of Nisseki Polybutene HV300) and 0.5 part of azobisisovaleronitrile were dissolved in the same manner as in Example 1 (however, the rotation speed of the homomixer was 9,000 rpm) to obtain an average particle size. 86 parts by weight of polymer fine particles having a wrinkle-like structure on the surface with a diameter of 21 μm (FIG. 2) were obtained. Example 3 To the monomer mixture of Example 1 was added 5 parts of toluene,
Otherwise, the same operation was performed to obtain 86 parts by weight of polymer fine particles having an average particle diameter of 30 μm and having slightly larger wrinkles on the particle surface. Comparative Example 1 The same operation was performed as in Example 1 except that the amount of the block copolymer was changed from 20 parts to 1 part, but spherical polymer fine particles having a smooth particle surface and a wrinkle-like structure could be obtained. Did not. Comparative Example 2 The same operation was performed as in Example 1 except that 5 parts of ethylene glycol dimethacrylate was not added, but the particle surface was smooth, and polymer fine particles having a wrinkle-like structure could not be obtained.

【0012】[0012]

【発明の効果】本発明によれば、疎水性の重合性ビニル
ポリマーと架橋性モノマーの混合物にスチレン系エラス
トマーを溶解させ、これを水性媒体中で懸濁重合させる
ことにより、表面に規則的なシワの構造を有する球状ポ
リマー微粒子を得ることができる。このようにして得ら
れた特異な表面構造を有する球状ポリマー微粒子は、例
えば塗料や化粧料に配合すると層分離を起こさない均一
な組成物を与え、その粘性特性、光散乱特性や表面特性
を変化、調整するのに有利に用いることができる。特
に、塗料における艶消剤として威力を発揮する。
According to the present invention, a styrene-based elastomer is dissolved in a mixture of a hydrophobic polymerizable vinyl polymer and a crosslinkable monomer, and this is subjected to suspension polymerization in an aqueous medium to form a regular surface on the mixture. Spherical polymer fine particles having a wrinkle structure can be obtained. The spherical polymer particles having a unique surface structure obtained in this way give a uniform composition that does not cause layer separation when blended in, for example, paints and cosmetics, and change its viscosity, light scattering and surface properties. , Can be advantageously used for adjustment. In particular, it exerts its power as a matting agent in paints.

【図面の簡単な説明】[Brief description of the drawings]

【図1】は実施例1で得たポリマー微粒子の電子顕微鏡
写真である。
FIG. 1 is an electron micrograph of the polymer fine particles obtained in Example 1.

【図2】は実施例2で得たポリマー微粒子の電子顕微鏡
写真である。
FIG. 2 is an electron micrograph of the polymer fine particles obtained in Example 2.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】表面に規則的なシワ状構造を有する球状ポ
リマー微粒子。
1. Spherical polymer fine particles having a regular wrinkle-like structure on the surface.
【請求項2】平均粒子径が2〜300μmである請求項
1記載の球状ポリマー微粒子。
2. The spherical polymer fine particles according to claim 1, having an average particle size of 2 to 300 μm.
【請求項3】疎水性の重合性ビニルモノマー40〜90
重量部および架橋性モノマー1〜40重量部の混合物に
スチレン系エラストマー5〜30重量部を溶解させ、水
性媒体中で懸濁重合させる表面に規則的なシワ状構造を
有する球状ポリマー微粒子の製造法。
3. A hydrophobic polymerizable vinyl monomer 40 to 90.
A method for producing spherical polymer fine particles having a regular wrinkle-like structure on the surface by dissolving 5 to 30 parts by weight of a styrene-based elastomer in a mixture of 1 part by weight and 1 to 40 parts by weight of a crosslinkable monomer and suspension polymerizing in an aqueous medium .
【請求項4】重合性ビニルモノマーが(メタ)アクリル
酸アルキルエステルである請求項3記載の製造法。
4. The method according to claim 3, wherein the polymerizable vinyl monomer is an alkyl (meth) acrylate.
JP32230497A 1997-11-07 1997-11-07 Spherical polymer fine particles having a wrinkle-like structure on the surface and method for producing the same Expired - Fee Related JP3700997B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32230497A JP3700997B2 (en) 1997-11-07 1997-11-07 Spherical polymer fine particles having a wrinkle-like structure on the surface and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32230497A JP3700997B2 (en) 1997-11-07 1997-11-07 Spherical polymer fine particles having a wrinkle-like structure on the surface and method for producing the same

Publications (2)

Publication Number Publication Date
JPH11140139A true JPH11140139A (en) 1999-05-25
JP3700997B2 JP3700997B2 (en) 2005-09-28

Family

ID=18142142

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32230497A Expired - Fee Related JP3700997B2 (en) 1997-11-07 1997-11-07 Spherical polymer fine particles having a wrinkle-like structure on the surface and method for producing the same

Country Status (1)

Country Link
JP (1) JP3700997B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004285013A (en) * 2003-03-24 2004-10-14 Kose Corp Solid water-in-oil type emulsified cosmetic
WO2006075711A1 (en) * 2005-01-14 2006-07-20 Sumitomo Seika Chemicals Co., Ltd. Cosmetic preparation
JP2006265214A (en) * 2005-03-25 2006-10-05 Kose Corp Powder cosmetic
JP2009029951A (en) * 2007-07-27 2009-02-12 Jsp Corp Method for producing vinyl crosslinked resin particles
JP2009029953A (en) * 2007-07-27 2009-02-12 Jsp Corp Method for producing vinyl resin particle
JP2009203391A (en) * 2008-02-29 2009-09-10 Gantsu Kasei Kk Method for producing spherical polymer particles having regular rumple structure on its surface, and scrub agent containing the same
WO2013027849A1 (en) 2011-08-25 2013-02-28 積水化成品工業株式会社 Irregularly shaped resin particles, method for producing same, and use of same

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004285013A (en) * 2003-03-24 2004-10-14 Kose Corp Solid water-in-oil type emulsified cosmetic
WO2006075711A1 (en) * 2005-01-14 2006-07-20 Sumitomo Seika Chemicals Co., Ltd. Cosmetic preparation
JPWO2006075711A1 (en) * 2005-01-14 2008-06-12 住友精化株式会社 Cosmetics
JP2006265214A (en) * 2005-03-25 2006-10-05 Kose Corp Powder cosmetic
JP2009029951A (en) * 2007-07-27 2009-02-12 Jsp Corp Method for producing vinyl crosslinked resin particles
JP2009029953A (en) * 2007-07-27 2009-02-12 Jsp Corp Method for producing vinyl resin particle
JP2009203391A (en) * 2008-02-29 2009-09-10 Gantsu Kasei Kk Method for producing spherical polymer particles having regular rumple structure on its surface, and scrub agent containing the same
WO2013027849A1 (en) 2011-08-25 2013-02-28 積水化成品工業株式会社 Irregularly shaped resin particles, method for producing same, and use of same
KR20140063592A (en) 2011-08-25 2014-05-27 세키스이가세이힝코교가부시키가이샤 Irregularly shaped resin particles, method for producing same, and use of same
US9187632B2 (en) 2011-08-25 2015-11-17 Sekisui Plastics Co., Ltd. Non-spherical resin particles, manufacturing method thereof, and use thereof

Also Published As

Publication number Publication date
JP3700997B2 (en) 2005-09-28

Similar Documents

Publication Publication Date Title
US20100036055A1 (en) Method For Producing Core-Shell Fine Particle and Method for Producing Intermediate Which is Used for Production of the Core-Shell Fine Particle
JP2002542319A (en) Method for producing polymer particles
JP3940620B2 (en) Method for producing non-spherical polymer fine particles
JPH05317688A (en) Bowl-shaped fine particle and its production
JPH11140139A (en) Spherical fine particle of polymer having wrinkle structure on its surface and preparation thereof
EP1046658B1 (en) Monodisperse particles, process for producing the same, and uses thereof
JP4939925B2 (en) Wrinkled polymer fine particles and method for producing the same
JP4692335B2 (en) Method for producing core-shell fine particles and method for producing monodisperse crosslinked fine particles containing alkoxyamine groups as intermediates thereof
JP3165472B2 (en) Method for producing polymer particles containing inner pores
JP3130437B2 (en) Method for producing polymer particles of uniform size
JP3784336B2 (en) Method for producing polymer particles
JP5020861B2 (en) Method for producing spherical polymer fine particles having a regular wrinkle structure on the surface, and a scrub agent comprising the fine particles
JPS63189413A (en) Production of crosslinked polymer particle
JP3380131B2 (en) Method for producing polymer particles
JP2000053720A (en) Particulate aggregate and its production
JP4488182B2 (en) Method for producing crosslinked polymer particles
JPS5966406A (en) Preparation of fine particulate polymer
JP2722661B2 (en) Method for producing aqueous dispersion of reactive polymer particles
JPH08100006A (en) Production of monodisperse polymer particle
JPH0717688B2 (en) Highly crosslinked polymer particles and method for producing the same
JP2921308B2 (en) Method for removing residual unreacted monomer from acrylate polymer particles
US8404762B2 (en) Method for production of core-shell microparticle, and method for production of monodisperse crosslinked microparticle having alkoxyamine group for use as intermediate for the production of the core-shell microparticle
JPH0692443B2 (en) Method for producing polymer particles
JP4183478B2 (en) Spacers for liquid crystal display elements
KR100472553B1 (en) Method of Preparing Micron-Sized Acrylic Polymer Bead

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20041026

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20050301

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050315

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050513

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050621

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050711

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080722

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110722

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120722

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120722

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130722

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130722

Year of fee payment: 8

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130722

Year of fee payment: 8

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees