JPH0717723B2 - Process for producing cured resin spherical fine particles having a uniform particle size - Google Patents
Process for producing cured resin spherical fine particles having a uniform particle sizeInfo
- Publication number
- JPH0717723B2 JPH0717723B2 JP60206608A JP20660885A JPH0717723B2 JP H0717723 B2 JPH0717723 B2 JP H0717723B2 JP 60206608 A JP60206608 A JP 60206608A JP 20660885 A JP20660885 A JP 20660885A JP H0717723 B2 JPH0717723 B2 JP H0717723B2
- Authority
- JP
- Japan
- Prior art keywords
- cured resin
- fine particles
- spherical fine
- emulsion
- 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.)
- Expired - Fee Related
Links
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
- Phenolic Resins Or Amino Resins (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、プラスチツクフイルムの滑り性向上剤や液晶
表示装置用スペーサーなどの各種用途に有用な、メラミ
ンもしくはベンゾグアナミン系アミノ樹脂製の均一な粒
子径を有する硬化樹脂球状微粒子の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention is a uniform particle made of a melamine or benzoguanamine-based amino resin, which is useful in various applications such as a slipperiness improving agent for plastic films and spacers for liquid crystal display devices. The present invention relates to a method for producing spherical fine particles of a cured resin having a diameter.
(従来の技術) 従来より、均一な粒子径を有する球状微粒子の製法とし
ては、種々の方法が提案されている。例えば特開昭59−
59741号に特定のビニル単量体の乳化重合によつて得ら
れる熱可塑性樹脂微粒子が開示されているように、乳化
重合法による球状微粒子の製法は公知である。しかしな
がら、乳化重合法では架橋性単量体を部分的に使用する
としても、耐熱性、耐溶剤性に優れかつ強靱な球状微粒
子が得られないのが現状である。(Prior Art) Conventionally, various methods have been proposed as a method for producing spherical fine particles having a uniform particle diameter. For example, JP-A-59-
As disclosed in No. 59741 of thermoplastic resin fine particles obtained by emulsion polymerization of a specific vinyl monomer, a method for producing spherical fine particles by an emulsion polymerization method is known. However, in the emulsion polymerization method, it is not possible to obtain tough spherical fine particles having excellent heat resistance and solvent resistance even if the crosslinkable monomer is partially used.
また、熱硬化性樹脂であるアミノ樹脂の球状微粒子を得
る試みも種々行われている。例えばメラミンのN−メチ
ロール誘導体の稀薄水溶液に、水溶性酸触媒の存在下に
縮合を進め、透明な水溶液が混濁を開始した瞬間に多量
の水を添加する方法(特公昭32−5743号)、メラミン−
ホルムアルデヒド水性溶液を保護コロイドの存在下に固
相が形成されるまでpH値6.0〜8.0の範囲で反応させる方
法(特公昭43−29159号)が提案されている。Various attempts have also been made to obtain spherical fine particles of amino resin, which is a thermosetting resin. For example, a method of advancing the condensation in the presence of a water-soluble acid catalyst to a dilute aqueous solution of an N-methylol derivative of melamine, and adding a large amount of water at the moment when the transparent aqueous solution starts to become cloudy (Japanese Patent Publication No. 32-5743), Melamine-
A method (JP-B-43-29159) in which an aqueous solution of formaldehyde is reacted in the presence of a protective colloid at a pH value of 6.0 to 8.0 until a solid phase is formed has been proposed.
(発明が解決しようとする問題点) 前記したような乳化重合法では、均一な粒子径を有する
球状微粒子が比較的容易に得られるが、耐熱性、耐溶剤
性の不足や強度面での制約があり、特にプラスチツク中
や極性溶剤に混練して使用される改質剤や顔料用途に不
向きである。(Problems to be Solved by the Invention) In the emulsion polymerization method as described above, spherical fine particles having a uniform particle diameter can be relatively easily obtained, but heat resistance and solvent resistance are insufficient, and strength is limited. In particular, it is not suitable for use as a modifier or pigment used in plastics or kneaded with a polar solvent.
また、前記したアミノ樹脂の球状微粒子を得る方法で
は、均一な粒子径を有する球状微粒子を得ることは実用
上困難である。例えば特公昭32−5743号の方法では、大
量の水の添加によりメラミン樹脂の縮合を阻止して球状
微粒子の粗大化を防止しているため、得られる球状微粒
子は耐熱性、耐溶剤性に劣つたものとなり、また、該微
粒子の粗大化を完全に防止したまま粉体として取り出す
ことが困難であり、実質均一な粒子径の球状微粒子は得
られない。また、特公昭43−29159号の方法では、メラ
ミン樹脂の沈殿物が形成されるまで高温で反応させられ
るが、反応は安定な懸濁状態で行われていないため、反
応中に生成した球状微粒子は凝集や融着を起こし、実際
上均一な粒子径の球状微粒子を得ることは非常に困難で
あり、事実かさ密度の大きな粉体しか得られないのであ
る。Further, it is practically difficult to obtain spherical fine particles having a uniform particle diameter by the method for obtaining spherical fine particles of amino resin described above. For example, in the method of Japanese Examined Patent Publication (Kokoku) No. 32-5743, since the condensation of the melamine resin is prevented by adding a large amount of water to prevent the coarsening of the spherical fine particles, the obtained spherical fine particles have poor heat resistance and solvent resistance. Further, it is difficult to take out the powder as powder while completely preventing the coarsening of the fine particles, and spherical fine particles having a substantially uniform particle size cannot be obtained. Further, in the method of Japanese Patent Publication No. 43-29159, the reaction is carried out at a high temperature until the precipitate of the melamine resin is formed, but since the reaction is not carried out in a stable suspension state, the spherical fine particles produced during the reaction Causes agglomeration and fusion, and it is very difficult to obtain spherical fine particles having a practically uniform particle size, and in fact, only powder having a large bulk density can be obtained.
本発明は従来技術の前記した如き問題点を解消するもの
である。したがつて、本発明の目的は耐熱性、耐溶剤性
に優れかつ均一な粒子径を有する硬化樹脂球状微粒子を
各種用途に利用可能な粉体として提供することにある。The present invention solves the above-mentioned problems of the prior art. Accordingly, an object of the present invention is to provide cured resin spherical fine particles having excellent heat resistance and solvent resistance and having a uniform particle size as a powder that can be used for various purposes.
(問題点を解決するための手段) 本発明者らは、均一な粒子径を有する硬化樹脂の安定な
乳濁液を経由して球状微粒子を得るべく研究した結果、
メラミン及び/又はベンゾグアナミンとホルムアルデヒ
ドとの水親和性初期縮合物が水性液中で特定のスルホン
酸と特異な界面化学的挙動を起こして安定な乳濁液を生
成するという知見に基いて、本発明を完成したものであ
る。(Means for Solving the Problems) The present inventors have conducted research to obtain spherical fine particles via a stable emulsion of a cured resin having a uniform particle size,
The present invention is based on the finding that a water-affinity precondensate of melamine and / or benzoguanamine and formaldehyde undergoes a specific interfacial chemical behavior with a specific sulfonic acid in an aqueous liquid to form a stable emulsion. Is completed.
すなわち本発明は、メラミン及び/又はベンゾグアナミ
ンとホルムアルデヒドとの水親和性初期縮合物を、界面
活性剤を含む水性液中で、炭素数10〜18のアルキル基を
有するアルキルベンゼンスルホン酸の存在下に縮合硬化
して硬化樹脂の乳濁液を生成せしめた後、乳濁液より硬
化樹脂を分離、乾燥することを特徴とする均一な粒子径
を有する硬化樹脂球状微粒子の製造方法に関するもので
ある。That is, the present invention condenses a water-affinity initial condensate of melamine and / or benzoguanamine and formaldehyde in an aqueous liquid containing a surfactant in the presence of an alkylbenzenesulfonic acid having an alkyl group having 10 to 18 carbon atoms. The present invention relates to a method for producing spherical fine particles of a cured resin having a uniform particle diameter, which comprises curing and forming an emulsion of a cured resin, and separating the cured resin from the emulsion and drying.
本発明で用いられるメラミン及び/又はベンゾグアナミ
ンとホルムアルデヒドとの水親和性初期縮合物は、メラ
ミン又はベンゾグアナミンあるいはそれらの混合物とホ
ルムアルデヒドとを常法に従つて反応させて得られる水
溶性あるいは水分散性の樹脂状物である。水親和性の程
度は、一般に15℃で初期縮合物に水を滴下して白濁を生
じるまでの水滴下量の初期縮合物に対する重量%(以
下、これを水混和度という。)によつて測定されるが、
本発明に好適な初期縮合物の水混和度は100%以上であ
る。水混和度が100%未満の初期縮合物では界面活性剤
を含んだ水性液中で、いかに分散しても粒子径の比較的
大きい不均一な乳濁液しか形成せず、最終的に得られる
球状微粒子は均一な粒子径のものとなりにくい。また、
ホルムアルデヒドとしては、ホルマリン、トリオキサ
ン、パラホルムアルデヒドなどのホルムアルデヒドを発
生するものであればいずれも使用することができる。The water-affinity initial condensate of melamine and / or benzoguanamine and formaldehyde used in the present invention is a water-soluble or water-dispersible product obtained by reacting melamine or benzoguanamine or a mixture thereof with formaldehyde according to a conventional method. It is a resinous material. The degree of water affinity is generally measured by adding water to the initial condensate at 15 ° C and then adding the amount of water to the initial condensate in terms of weight% (hereinafter referred to as water miscibility) with respect to the initial condensate. Will be
The water miscibility of the initial condensate suitable for the present invention is 100% or more. An initial condensate with a water miscibility of less than 100% can be obtained in the final stage, even if dispersed in an aqueous solution containing a surfactant, only a non-uniform emulsion with a relatively large particle size is formed. Spherical particles are less likely to have a uniform particle size. Also,
As the formaldehyde, any formaldehyde, such as formalin, trioxane, and paraformaldehyde, can be used.
本発明に用いられる界面活性剤には特に制限はなく、ア
ニオン性界面活性剤、カチオン性界面活性剤、非イオン
性界面活性剤、両性界面活性剤など全ての界面活性剤が
使用できるが、特にアニオン性界面活性剤または非イオ
ン性界面活性剤あるいはそれらの混合物が好ましい。ア
ニオン性界面活性剤としては、ナトリウムドデシルサル
フエート、カリウムドデシルサルフエートなどの如きア
ルカリ金属アルキルサルフエート;アンモニウムドデシ
ルサルフエートなどの如きアンモニウムアルキルサルフ
エート;ナトリウムドデシルポリグリコールエーテルサ
ルフエート;ナトリウムスルホリシノエート;スルホン
化パラフインのアルカリ金属塩、スルホン化パラフイン
のアンモニウム塩などの如きアルキルスルホン酸塩;ナ
トリウムラウレート、トリエタノールアミンオレエー
ト、トリエタノールアミンアビエテートなどの如き脂肪
酸塩;ナトリウムドデシルベンゼンスルホネート、アル
カリフエノールヒドロキシエチレンのアルカリ金属サル
フエートなどの如きアルキルアリールスルホン酸塩;高
アルキルナフタレンスルホン酸塩;ナフタレンスルホン
酸ホルマリン縮合物;ジアルキルスルホコハク酸塩;ポ
リオキシエチレンアルキルサルフエート塩;ポリオキシ
エチレンアルキルアリールサルフエート塩などが使用で
き、非イオン性界面活性剤としては、ポリオキシエチレ
ンアルキルエーテル;ポリオキシエチレンアルキルアリ
ールエーテル;ソルビタン脂肪酸エステル;ポリオキシ
エチレンソルビタン脂肪酸エステル;グリセロールのモ
ノラウレートなどの如き脂肪酸モノグリセライド;ポリ
オキシエチレンオキシプロピレン共重合体;エチレンオ
キサイドと脂肪属アミン、アミドまたは酸との縮合生成
物などが使用できる。The surfactant used in the present invention is not particularly limited, and all surfactants such as anionic surfactant, cationic surfactant, nonionic surfactant and amphoteric surfactant can be used, but especially Anionic or nonionic surfactants or mixtures thereof are preferred. Examples of the anionic surfactant include alkali metal alkyl sulphates such as sodium dodecyl sulphate and potassium dodecyl sulphate; ammonium alkyl sulphates such as ammonium dodecyl sulphate; sodium dodecyl polyglycol ether sulphate; sodium sulpholysino Alkyl sulfonates such as alkali metal salts of sulfonated paraffins and ammonium salts of sulfonated paraffins; fatty acid salts such as sodium laurate, triethanolamine oleate, triethanolamine abietate; sodium dodecylbenzene sulfonate; Alkyl aryl sulfonates such as alkali phenol hydroxyethylene alkali metal sulphates; high alkyl naphthales Sulfonates; naphthalene sulfonic acid formalin condensates; dialkyl sulfosuccinates; polyoxyethylene alkyl sulphate salts; polyoxyethylene alkyl aryl sulphate salts and the like can be used, and nonionic surfactants include polyoxyethylene alkyl Ethers; polyoxyethylene alkylaryl ethers; sorbitan fatty acid esters; polyoxyethylene sorbitan fatty acid esters; fatty acid monoglycerides such as glycerol monolaurate; polyoxyethyleneoxypropylene copolymers; ethylene oxide and fatty amines, amides or acids A condensation product with and the like can be used.
界面活性剤の使用量は特に制限はないが、好ましくは初
期縮合物100重量部に対し0.01〜10重量部の範囲であ
る。0.01重量部未満の少量では硬化樹脂の安定な乳濁液
が得られないことがあり、また、10重量部を超える多量
では乳濁液に不必要な泡立ちを起こしたり最終的に得ら
れる球状微粒子の物性に悪影響を与えることがある。The amount of the surfactant used is not particularly limited, but is preferably in the range of 0.01 to 10 parts by weight with respect to 100 parts by weight of the initial condensate. If the amount is less than 0.01 parts by weight, a stable emulsion of the cured resin may not be obtained, and if the amount is more than 10 parts by weight, the emulsion may cause unnecessary foaming or the final spherical fine particles may be obtained. The physical properties of may be adversely affected.
本発明に用いられる炭素数10〜18のアルキル基を有する
アルキルベンゼンスルホン酸は、前記初期縮合物の水性
液中で、特異な界面活性能を発揮して、硬化樹脂の安定
な乳濁液を生成するために必須の成分であり、例えばデ
シルベンゼンスルホン酸、ドデシルベンゼンスルホン
酸、テトラデシルベンゼンスルホン酸、ヘキサデシルベ
ンゼンスルホン酸、オクタデシルベンゼンスルホン酸な
どの中から1種又は2種以上を選んで使用することがで
きる。The alkylbenzene sulfonic acid having an alkyl group having 10 to 18 carbon atoms used in the present invention exerts a unique surface-active ability in the aqueous liquid of the initial condensation product to form a stable emulsion of a cured resin. It is an essential component for the purpose of using, for example, one or more selected from decylbenzenesulfonic acid, dodecylbenzenesulfonic acid, tetradecylbenzenesulfonic acid, hexadecylbenzenesulfonic acid, octadecylbenzenesulfonic acid, etc. can do.
アルキルベンゼンスルホン酸の使用量は、初期縮合物10
0重量部に対し0.1〜20重量部の範囲、より好ましくは0.
5〜10重量%の範囲である。0.1重量部未満の少量では縮
合硬化に長時間を要し、また、硬化樹脂の安定な乳濁液
が得られず、最終的に凝集粗大化した粒子しか得られな
い。また、20重量部を超える多量では、生成した乳濁液
中の樹脂粒子中に必要以上にアルキルベンゼンスルホン
酸が分配される結果、樹脂粒子が可塑化されて縮合硬化
中に粒子間の凝集、融着が生じやすくなり、最終的に均
一な粒子径を有する球状微粒子が得られない。The amount of alkylbenzene sulfonic acid used is 10
0.1 to 20 parts by weight relative to 0 parts by weight, more preferably 0.
It is in the range of 5 to 10% by weight. If the amount is less than 0.1 part by weight, the condensation curing takes a long time, and a stable emulsion of the cured resin cannot be obtained, and only aggregated and coarse particles are finally obtained. Further, when the amount is more than 20 parts by weight, the alkylbenzene sulfonic acid is excessively distributed in the resin particles in the produced emulsion, and as a result, the resin particles are plasticized and agglomerate or melt between the particles during condensation curing. Adhesion tends to occur, and spherical fine particles having a uniform particle size cannot be finally obtained.
本発明において水親和性初期縮合物を水性液中で縮合硬
化させるには、初期縮合物の水溶液もしくは初期縮合物
が水中に微分散した乳白色の分散液に前記界面活性剤と
アルキルベンゼンスルホン酸を加えて、0℃の低温から
加圧下100℃以上の高温で攪拌下に保持すればよい。界
面活性剤及びアルキルベンゼンスルホン酸の添加方法に
は特に制限はなく、例えば水性液中に予め界面活性剤や
アルキルベンゼンスルホン酸を混合しておいてから初期
縮合物を水性液中に添加する方法でもよく、また、水性
液中に初期縮合物を混合しておいてから界面活性剤やア
ルキルベンゼンスルホン酸を添加する方法でもよい。ま
た、初期縮合物の水性液中の濃度は、得られる乳濁液の
取り扱い易さや操作の経済性を考慮すれば、5〜20重量
%が好ましい。To condense and cure the water-affinity precondensate in the present invention in the present invention, the surfactant and alkylbenzenesulfonic acid are added to an aqueous solution of the precondensate or a milky white dispersion in which the precondensate is finely dispersed in water. Then, the temperature may be maintained from a low temperature of 0 ° C. to a high temperature of 100 ° C. or higher under pressure with stirring. The method of adding the surfactant and the alkylbenzene sulfonic acid is not particularly limited, and for example, a method of previously mixing the surfactant and the alkylbenzene sulfonic acid in the aqueous liquid and then adding the initial condensate to the aqueous liquid may be used. Alternatively, a method may be used in which the initial condensate is mixed in the aqueous liquid and then the surfactant or the alkylbenzene sulfonic acid is added. Further, the concentration of the initial condensate in the aqueous liquid is preferably 5 to 20% by weight in consideration of the ease of handling the obtained emulsion and the economical efficiency of the operation.
縮合硬化は、一般には90℃あるいはそれ以上の温度に昇
温して一定時間保持することにより完結されるが、必ず
しも高温での硬化は必要でなく、低温短時間であつて
も、乳濁液中の樹脂粒子がメタノールやアセトンで膨潤
しなくなる程度まで硬化されていれば充分である。Condensation curing is generally completed by raising the temperature to 90 ° C. or higher and holding it for a certain period of time, but curing at a high temperature is not always necessary, and even at a low temperature for a short time, an emulsion It is sufficient that the resin particles therein are cured to the extent that they do not swell with methanol or acetone.
以上のようにして得られた硬化樹脂の乳濁液は、均一な
粒子径を有する球状微粒子が凝集もなく非常に安定に存
在してなつている。硬化樹脂の乳濁液より硬化樹脂を分
離、乾燥するには公知の方法によればよく、例えば自然
沈降あるいは遠心沈降法とデカンテーシヨンによる分
離、ろ過による分離など各種分離法や自然乾燥、減圧乾
燥、熱風乾燥など各種乾燥法が自由に採用できる。ま
た、分離に先立つて、硫酸アルミニウム等の凝集剤を添
加して分離を促進することもできる。In the emulsion of the cured resin obtained as described above, spherical fine particles having a uniform particle size are present in a very stable manner without aggregation. A known method may be used for separating and drying the cured resin from the emulsion of the cured resin, for example, various separation methods such as natural sedimentation or centrifugal sedimentation and separation by decantation, separation by filtration, natural drying, and reduced pressure. Various drying methods such as drying and hot air drying can be freely adopted. Further, prior to the separation, a flocculant such as aluminum sulfate may be added to accelerate the separation.
乾燥して得られる硬化樹脂はボールモル等の極く軽い力
で容易に乳濁液中の硬化樹脂粒子と同じ球状で均一な粒
子径を有する微粒子とすることができる。The cured resin obtained by drying can be easily made into fine particles having the same spherical and uniform particle diameter as the cured resin particles in the emulsion with an extremely light force such as ball mol.
(作用) 本発明において、界面活性剤と特定のアルキルベンゼン
スルホン酸を用いることにより、メラミン及び/又はベ
ンゾグアナミンとホルムアルデヒドとの均一な粒子径を
有する硬化樹脂の安定な乳濁液が得られる理由について
は明らかではない。しかし、アルキルベンゼンスルホン
酸を用いず他の酸を用いて縮合硬化した場合、一たん生
成した乳濁液が直ちに凝集したりあるいは乳濁液中の硬
化樹脂粒子の粗大化が起こることを考慮すれば、アルキ
ルベンゼンスルホン酸が初期縮合物との間で界面化学的
に作用して、生成した乳濁液中の硬化樹脂粒子を安定に
保つていることは明らかである。(Function) In the present invention, the reason why a stable emulsion of a cured resin having a uniform particle size of melamine and / or benzoguanamine and formaldehyde can be obtained by using a surfactant and a specific alkylbenzene sulfonic acid is as follows. Not clear. However, if condensation curing is performed using another acid instead of alkylbenzene sulfonic acid, considering that the emulsion that has just formed immediately aggregates or the cured resin particles in the emulsion become coarse. It is clear that the alkylbenzene sulfonic acid acts interfacially with the precondensate to keep the cured resin particles in the resulting emulsion stable.
本発明者らは、アルキルベンゼンスルホン酸の一部が乳
濁液中の硬化樹脂粒子の界面付近に配向して存在する結
果、硬化樹脂粒子界面の性質をメラミンもしくはベンゾ
グアナミン系アミノ樹脂本来の乳濁化しにくい性質から
本発明で用いる界面活性剤で安定に乳濁化しやすい性質
に変えているためではないかと推測している。しかし、
この理由から本発明は何ら制限されることはないが、本
発明に用いられる界面活性剤と特定のアルキルベンゼン
スルホン酸の硬化樹脂粒子の乳濁液中での安定化に与え
る相乗作用は驚くべきものである。As a result of the presence of a part of the alkylbenzene sulfonic acid oriented near the interface of the cured resin particles in the emulsion, the properties of the interface of the cured resin particles are melamine- or benzoguanamine-based amino resin originally emulsified. It is speculated that it is because the surfactant used in the present invention is changed to a property that is stable and easily emulsified due to the difficult property. But,
For this reason, the present invention is not limited at all, but the synergistic effect of the surfactant used in the present invention and the stabilization of the cured resin particles of the specific alkylbenzene sulfonic acid in the emulsion is surprising. Is.
(発明の効果) 本発明の方法によれば、初期縮合物の縮合度すなわち水
親和性の程度、界面活性剤やドデシルベンゼンスルホン
酸の使用量を調節することにより、均一な粒子径を有す
る硬化樹脂球状微粒子を0.1〜20ミクロンの範囲の任意
の粒子径で調製することができる。また、本発明の方法
で得られた効果樹脂球状微粒子は、メラミンあるいはベ
ンゾグアナミン系アミノ樹脂が本来有している耐熱性、
耐水性、耐溶剤性などの優れた諸性能を備えていること
に加え、均一な球状で水、有機溶媒、プラスチツク等の
各種媒体への分散性が極めて優れている。したがつて、
本発明の方法で得られた硬化樹脂球状微粒子は、プラス
チツクフイルム・シートの滑り性向上剤、ブロツキング
防止剤、艶消し仕上げ剤、光拡散剤、表面硬度向上剤等
の各種改質剤;液晶表示装置用スペーサー;測定・分析
用標準粒子などの各種用途に有用であり、また、本発明
における各工程の途中もしくはその前後に、酸性染料、
塩基性染料、蛍光染料、蛍光増白剤などの各種染料を添
加することにより着色された硬化樹脂球状微粒子とする
こともでき、この着色された微粒子は塗料、インキ、プ
ラスチツク着色用の顔料として使用することもできる。(Effects of the Invention) According to the method of the present invention, curing having a uniform particle diameter can be achieved by adjusting the condensation degree of the initial condensate, that is, the degree of water affinity, and the amount of the surfactant or dodecylbenzenesulfonic acid used. The resin spherical microparticles can be prepared with any particle size in the range of 0.1 to 20 microns. Further, the effect resin spherical fine particles obtained by the method of the present invention, heat resistance originally possessed by melamine or benzoguanamine-based amino resin,
In addition to having excellent properties such as water resistance and solvent resistance, it has a uniform spherical shape and is extremely excellent in dispersibility in various media such as water, organic solvents, and plastics. Therefore,
The cured resin spherical fine particles obtained by the method of the present invention are various modifiers such as a slip film improving agent for plastic film sheets, an anti-blocking agent, a matte finishing agent, a light diffusing agent and a surface hardness improving agent; liquid crystal display. Spacer for device; useful for various purposes such as standard particles for measurement / analysis, and also, before or after each step in the present invention, an acidic dye,
It is also possible to make spherical particles of cured resin colored by adding various dyes such as basic dyes, fluorescent dyes and optical brighteners, and these colored particles are used as pigments for paints, inks and plastic coloring. You can also do it.
以下、実施例によつて本発明をさらに詳しく説明する。
なお、特にことわらない限り、部は重量部、%は重量%
を表わす。Hereinafter, the present invention will be described in more detail with reference to examples.
Unless otherwise specified, parts are parts by weight and% is% by weight.
Represents
実施例1 攪拌機、還流冷却器、温度計を備えた四つ口フラスコに
メラミン150部、濃度37%のホルマリン290部及び濃度28
%のアンモニア水溶液1.5部を仕込み、混合物とし、系
のpHを8.0に調整した。この混合物を攪拌しながら70℃
に昇温し、同温度で30分間反応させ、水混和度∞%の初
期縮合物を得た。Example 1 In a four-necked flask equipped with a stirrer, a reflux condenser and a thermometer, 150 parts of melamine, 290 parts of formalin having a concentration of 37% and a concentration of 28
% Aqueous ammonia solution (1.5 parts) was added to prepare a mixture, and the system pH was adjusted to 8.0. 70 ° C. with stirring this mixture
The temperature was raised to 0 ° C., and the reaction was carried out at the same temperature for 30 minutes to obtain an initial condensate having a water miscibility of ∞%.
別にアニオン系界面活性剤のネオペレツクス05パウダー
(花王石鹸(株)製、ナトリウムドデシルベンゼンスル
ホネート)12部を水2240部に溶解しておき、この界面活
性剤水溶液の温度を90℃に昇温し攪拌した。攪拌状態下
にある界面活性剤水溶液に上記初期縮合物を投入し、つ
いで10%ドデシルベンゼンスルホン酸水溶液75部を加
え、徐々に昇温し90℃で2時間保持して縮合硬化し、硬
化樹脂の乳濁液を得た。この乳濁液を光学顕微鏡(倍率
800部)で観察すると、粒子径が約0.5μの球状の微粒子
からなり、それぞれの微粒子は激しくブラウン運動して
いることがわかつた。Separately, 12 parts of anionic surfactant Neoperex 05 powder (Kao Soap Co., Ltd., sodium dodecylbenzene sulfonate) was dissolved in 2240 parts of water, and the temperature of the surfactant aqueous solution was raised to 90 ° C and stirred. did. The above initial condensate was added to a surfactant aqueous solution under stirring condition, then 75 parts of 10% dodecylbenzenesulfonic acid aqueous solution was added, and the temperature was gradually raised and held at 90 ° C for 2 hours for condensation curing to obtain a cured resin. To obtain an emulsion. This emulsion is light microscope (magnification
When observed at 800 parts), it was found that the particles consisted of spherical fine particles with a particle size of about 0.5μ, and each fine particle was violently in Brownian motion.
この乳濁液を30℃まで冷却し、これに1%硫酸アルミニ
ウム水溶液を200部添加したのち、吸引ろ過し、固液分
離した。分離して得た硬化樹脂を160℃の熱風乾燥機で
2時間乾燥し、183部の硬化樹脂球状微粒子の集塊物を
得た。この集塊物をボールミルで解集塊し、白色の硬化
樹脂球状微粒子の粉体とした。この粉体を走査型電子顕
微鏡で調べたところ、平均粒子径0.5μの均一な球状微
粒子であることが確認できた。また、この硬化樹脂球状
微粒子は、メタノール、エタノール、イソプロピルアル
コール、ブタノール、酢酸エチル、酢酸ブチル、メチル
セロソルブ、エチルセロソルブ、アセトン、メチルエチ
ルケトン、トルエン、キシレン、ジメチルホルムアミド
などの各種有機溶剤による膨潤あるいは溶解は皆無であ
つた。さらに、この硬化樹脂球状微粒子は250℃以上の
温度に加熱しても融着、溶融等の現象は認められなかつ
た。This emulsion was cooled to 30 ° C., 200 parts of a 1% aqueous solution of aluminum sulfate was added thereto, and suction filtration was carried out to perform solid-liquid separation. The separated cured resin was dried with a hot air dryer at 160 ° C. for 2 hours to obtain an aggregate of 183 parts of cured resin spherical fine particles. This agglomerate was disaggregated and agglomerated with a ball mill to obtain a powder of white cured resin spherical fine particles. When the powder was examined by a scanning electron microscope, it was confirmed that the powder was uniform spherical fine particles having an average particle diameter of 0.5 μ. The cured resin spherical fine particles are not swollen or dissolved by various organic solvents such as methanol, ethanol, isopropyl alcohol, butanol, ethyl acetate, butyl acetate, methyl cellosolve, ethyl cellosolve, acetone, methyl ethyl ketone, toluene, xylene and dimethylformamide. There was nothing. Furthermore, even if the cured resin spherical fine particles were heated to a temperature of 250 ° C. or higher, no phenomenon such as fusion or melting was observed.
実施例2 実施例1で使用したのと同じ四つ口フラスコにメラミン
75部、ベンゾグアナミン75部、濃度37%のホルマリン29
0部及び濃度10%の炭酸ナトリウム水溶液1.16部を仕込
み混合物とし、系のpHを8.0に調整した。この混合物を
攪拌しながら85℃に昇温し同温度で1.5時間反応させ、
水混和度200%の初期縮合物を得た。別にノニオン系界
面活性剤のエマルゲン430(花王石鹸(株)製、ボリオ
キシエチレンオレイルエーテル)7.5部を水2455部に溶
解しておき、この界面活性剤水溶液の温度を50℃に昇温
し攪拌した。攪拌状態下にある界面活性剤水溶液に上記
初期縮合物を投入して、初期縮合物の乳濁液を得た。こ
れに5%ドデシルベンゼンスルホン酸水溶液90部を加
え、50〜60℃の温度で3時間保つて縮合硬化し、硬化樹
脂の乳濁液を得た。この乳濁液を冷水3000部に投入し急
冷した。この冷却された乳濁液を光学顕微鏡(倍率600
倍)で観察すると、粒子径が約8μの非常に均一な球状
の微粒子からなつていることがわかつた。次いで、この
乳濁液から硬化樹脂を沈降分離して得られたペースト
を、エマルゲン430、7.5部及びドデシルベンゼンスルホ
ン酸4.5部を水2000部に溶解させて得た水溶液中に超音
波分散機を用いて分散した。分散して得られた乳濁液を
攪拌しながら徐々に90℃まで昇温し、同温度で1時間保
持して完全硬化させ、十分に硬化した樹脂の懸濁液を得
た。この乳濁液から硬化樹脂を遠心沈降分離し、これを
150℃の熱風乾燥機で4時間乾燥し、120部の硬化樹脂球
状微粒子の集塊物を得た。この集塊物をボールミルで解
集塊し、白色の硬化樹脂球状微粒子の粉体とした。Example 2 Melamine was placed in the same four-necked flask used in Example 1.
75 parts, benzoguanamine 75 parts, concentration 37% formalin 29
The pH of the system was adjusted to 8.0 by adding 0 parts and 1.16 parts of a 10% aqueous sodium carbonate solution as a mixture. While stirring this mixture, the temperature was raised to 85 ° C. and the mixture was reacted at the same temperature for 1.5 hours,
An initial condensate having a water miscibility of 200% was obtained. Separately, 7.5 parts of nonionic surfactant Emulgen 430 (manufactured by Kao Soap Co., Ltd., polyoxyethylene oleyl ether) is dissolved in 2455 parts of water, and the temperature of this surfactant aqueous solution is raised to 50 ° C. and stirred. did. The above-mentioned initial condensate was added to a surfactant aqueous solution under stirring to obtain an emulsion of the initial condensate. To this was added 90 parts of a 5% aqueous solution of dodecylbenzenesulfonic acid, and the mixture was kept at a temperature of 50 to 60 ° C. for 3 hours for condensation curing to obtain an emulsion of cured resin. This emulsion was poured into 3000 parts of cold water and rapidly cooled. This cooled emulsion is then examined under an optical microscope (magnification 600
It was found that the particles consisted of very uniform spherical fine particles having a particle size of about 8 μ. Then, the paste obtained by sedimentation of the cured resin from this emulsion, emulgen 430, 7.5 parts and dodecylbenzenesulfonic acid 4.5 parts ultrasonic dispersion in an aqueous solution obtained by dissolving 2000 parts in water. Dispersed using. The emulsion obtained by dispersion was gradually heated to 90 ° C. with stirring and kept at the same temperature for 1 hour to be completely cured to obtain a sufficiently cured resin suspension. From this emulsion, the hardened resin was centrifuged and separated, and
It was dried with a hot air dryer at 150 ° C. for 4 hours to obtain 120 parts of an aggregate of cured resin spherical fine particles. This agglomerate was disaggregated and agglomerated with a ball mill to obtain a powder of white cured resin spherical fine particles.
この粉体の粉度分布を粒度分布測定機(コールターカウ
ンターモデルTA−II、C−1000、Coulter Electronics
Inc.製)で測定すると、平均粒子径8.0μ、標準偏差0.5
μであり、非常に狭い粒度分布であることがわかつた。The fineness distribution of this powder is measured by a particle size distribution measuring instrument (Coulter Counter Model TA-II, C-1000, Coulter Electronics).
Inc.), average particle size 8.0μ, standard deviation 0.5
It was μ, and it was found that the particle size distribution was very narrow.
また、この粉体を走査型電子顕微鏡で調べたところ、平
均粒子径8μの均一な球状微粒子であることが確認でき
た。Further, when the powder was examined by a scanning electron microscope, it was confirmed that the powder was uniform spherical fine particles having an average particle diameter of 8 μ.
この硬化樹脂球状微粒子はメタノール、エタノール、イ
ソプロピルアルコール、ブタノール、酢酸エチル、酢酸
ブチル、メチルセロソルブ、エチルセロソルブ、アセト
ン、メチルエチルケトン、トルエン、キシレン、ジメチ
ルホルムアミドなどの各種有機溶剤による膨潤あるいは
溶解は皆無であつた。さらに、硬化樹脂球状微粒子を25
0℃以上の温度に加熱しても融着、溶融等の現象は認め
られなかつた。The cured resin spherical fine particles are not swollen or dissolved by various organic solvents such as methanol, ethanol, isopropyl alcohol, butanol, ethyl acetate, butyl acetate, methyl cellosolve, ethyl cellosolve, acetone, methyl ethyl ketone, toluene, xylene and dimethylformamide. It was In addition, 25 particles of cured resin spherical particles
No phenomenon such as fusion or melting was observed even when heated to a temperature of 0 ° C. or higher.
実施例3 メラミン・ホルムアルデヒド初期縮合物(日本カーバイ
ド(株)製、ニカレジンS−260)250部及びノニオン系
界面活性剤のエマルゲン930(花王石鹸(株)製、ポリ
オキシエチレンノニルフエニルエーテル)7.5部を水234
0部に加えて、攪拌しながら70℃に昇温して溶解した。
得られた初期縮合物の水溶液に5%ドデシルベンゼンス
ルホン酸水溶液90部を加え、70℃で30分間保持した後徐
々に90℃まで昇温し90℃で1時間保持して縮合硬化させ
た。Example 3 250 parts of melamine-formaldehyde initial condensate (Nikaresin S-260 manufactured by Nippon Carbide Co., Ltd.) and Emulgen 930 (polyoxyethylene nonylphenyl ether manufactured by Kao Soap Co., Ltd.) 7.5 which is a nonionic surfactant. Part 234
In addition to 0 parts, the temperature was raised to 70 ° C. with stirring to dissolve.
To the obtained aqueous solution of the initial condensate, 90 parts of a 5% aqueous solution of dodecylbenzenesulfonic acid was added, and the mixture was kept at 70 ° C. for 30 minutes, then gradually heated to 90 ° C. and kept at 90 ° C. for 1 hour for condensation curing.
縮合硬化して得られた硬化樹脂の乳濁液を光学顕微鏡で
観察すると、粒子径が約1μの均一な球状の微粒子から
なつていることがわかつた。この乳濁液を30℃まで冷却
しこれに1%硫酸アルミニウム水溶液を200部添加した
のち、遠心沈降して固液分離した。分離して得た硬化樹
脂を160℃の熱風乾燥機で3時間乾燥し、178部の硬化樹
脂球状微粒子の集塊物を得た。この集塊物をボールミル
で解集塊し、白色の硬化樹脂球状微粒子の粉体とした。When an emulsion of the cured resin obtained by condensation curing was observed with an optical microscope, it was found that the emulsion consisted of uniform spherical fine particles having a particle diameter of about 1 μm. This emulsion was cooled to 30 ° C., 200 parts of a 1% aqueous solution of aluminum sulfate was added thereto, and then centrifugal sedimentation was performed to perform solid-liquid separation. The separated cured resin was dried for 3 hours with a hot air dryer at 160 ° C. to obtain an aggregate of 178 parts of cured resin spherical fine particles. This agglomerate was disaggregated and agglomerated with a ball mill to obtain a powder of white cured resin spherical fine particles.
この粉体を走査型電子顕微鏡で調べたところ、平均粒子
径1.0μの均一な球状微粒子であることが確認できた。When the powder was examined by a scanning electron microscope, it was confirmed that the powder was uniform spherical fine particles having an average particle diameter of 1.0 μ.
また、粒度分布測定機(コールターカウンターモデルTA
−II)で測定したところ、平均粒子径1.0μ、標準偏差
0.2μの粒度分布の狭い硬化樹脂球状微粒子であること
がわかつた。この硬化樹脂球状微粒子はメタノール、エ
タノール、イソプロピルアルコール、ブタノール、酢酸
エチル、酢酸ブチル、メチルセロソルブ、エチルセロソ
ルブ、アセトン、メチルエチルケトン、トルエン、キシ
レン、ジメチルホルムアミドなどの各種有機溶剤による
膨潤あるいは溶解は皆無であつた。さらに、硬化樹脂球
状微粒子を250℃以上の温度に加熱しても融着、溶融等
の現象は認められなかつた。In addition, particle size distribution measuring machine (Coulter counter model TA
-II), average particle size 1.0μ, standard deviation
It was found that the particles were spherical particles of cured resin having a narrow particle size distribution of 0.2μ. The cured resin spherical fine particles are not swollen or dissolved by various organic solvents such as methanol, ethanol, isopropyl alcohol, butanol, ethyl acetate, butyl acetate, methyl cellosolve, ethyl cellosolve, acetone, methyl ethyl ketone, toluene, xylene and dimethylformamide. It was Furthermore, even when the cured resin spherical fine particles were heated to a temperature of 250 ° C. or higher, no phenomenon such as fusion or melting was observed.
比較例1 実施例1における10%ドデシルベンゼンスルホン酸水溶
液の代わりに10%硫酸水溶液を10部加える他は、実施例
1と全く同様にして縮合硬化したが、硬化樹脂の乳濁化
後すぐに硬化樹脂の凝集を生じ、沈降及び器壁や攪拌機
への付着が発生し、攪拌不能となつた。Comparative Example 1 Condensation curing was carried out in the same manner as in Example 1 except that 10 parts of 10% sulfuric acid aqueous solution was added instead of 10% dodecylbenzenesulfonic acid aqueous solution in Example 1, but immediately after emulsification of the cured resin. Aggregation of the cured resin occurred, sedimentation and adhesion to the vessel wall and stirrer occurred, and stirring became impossible.
比較例2 実施例2における5%ドデシルベンゼンスルホン酸水溶
液の代わりに5%のスルフアミン酸水溶液を60部加える
他は、実施例2と全く同様にして縮合硬化したが、硬化
樹脂の乳濁化後すぐに硬化樹脂の凝集を生じ、沈降及び
器壁や攪拌機への付着が発生し、攪拌不能となつた。Comparative Example 2 The procedure of Example 2 was repeated except that 60 parts of a 5% aqueous solution of sulfamic acid was added instead of the 5% aqueous solution of dodecylbenzene sulfonic acid, and condensation curing was carried out in the same manner as in Example 2 except that the cured resin was emulsified. Immediately, the cured resin agglomerated, settling out and adhering to the vessel wall and the stirrer, which made stirring impossible.
比較例3 実施例3における5%ドデシルベンゼンスルホン酸水溶
液の代わりに5%塩化アンモニウム水溶液を90部を加え
る他は、実施例3と全く同様にして縮合硬化したが、硬
化樹脂の乳濁化後すぐに硬化樹脂の凝集を生じ、沈降及
び器壁や攪拌機への付着が発生し、攪拌不能となつた。Comparative Example 3 Condensation curing was carried out in the same manner as in Example 3 except that 90 parts of a 5% aqueous solution of ammonium chloride was added instead of the 5% aqueous solution of dodecylbenzenesulfonic acid in Example 3, but after the emulsion of the cured resin was obtained. Immediately, the cured resin agglomerated, settling out and adhering to the vessel wall and the stirrer, which made stirring impossible.
実施例4 実施例1における初期縮合物中に蛍光増白剤(カヤライ
トACR、日本化薬(株)製)1.5部を加える以外は実施例
1と全く同じ手順で蛍光を有した白色度の高い硬化樹脂
球状微粒子の粉末を得た。これを走査型電子顕微鏡で調
べたところ平均粒子径0.5μの均一な球状微粒子である
ことが確認できた。Example 4 Except for adding 1.5 parts of a fluorescent whitening agent (Kayalite ACR, manufactured by Nippon Kayaku Co., Ltd.) to the initial condensate in Example 1, the procedure was exactly the same as in Example 1 except that fluorescent whiteness was high. A powder of cured resin spherical fine particles was obtained. When examined by a scanning electron microscope, it was confirmed that the particles were uniform spherical particles having an average particle diameter of 0.5 μ.
Claims (1)
ルムアルデヒドとの水親和性初期縮合物を、界面活性剤
を含む水性液中で、炭素数10〜18のアルキル基を有する
アルキルベンゼンスルホン酸の存在下に縮合硬化して、
硬化樹脂の乳濁液を生成せしめた後、乳濁液より硬化樹
脂を分離、乾燥することを特徴とする均一な粒子径を有
する硬化樹脂球状微粒子の製造方法。1. A water-affinity initial condensate of melamine and / or benzoguanamine and formaldehyde is condensed in an aqueous liquid containing a surfactant in the presence of an alkylbenzenesulfonic acid having an alkyl group having 10 to 18 carbon atoms. Cure
A method for producing spherical fine particles of a cured resin having a uniform particle diameter, which comprises producing an emulsion of a cured resin, separating the cured resin from the emulsion and drying the emulsion.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60206608A JPH0717723B2 (en) | 1985-09-20 | 1985-09-20 | Process for producing cured resin spherical fine particles having a uniform particle size |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60206608A JPH0717723B2 (en) | 1985-09-20 | 1985-09-20 | Process for producing cured resin spherical fine particles having a uniform particle size |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6268811A JPS6268811A (en) | 1987-03-28 |
JPH0717723B2 true JPH0717723B2 (en) | 1995-03-01 |
Family
ID=16526203
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60206608A Expired - Fee Related JPH0717723B2 (en) | 1985-09-20 | 1985-09-20 | Process for producing cured resin spherical fine particles having a uniform particle size |
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JP (1) | JPH0717723B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007186721A (en) * | 2002-07-19 | 2007-07-26 | Nippon Shokubai Co Ltd | Method for producing crosslinked amino-resin particle |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63315256A (en) * | 1987-06-19 | 1988-12-22 | Ricoh Co Ltd | Image forming device |
JP2527006B2 (en) * | 1988-09-28 | 1996-08-21 | 旭硝子株式会社 | Aldehyde condensation resin particle dispersion and method for producing the same |
DE3929052A1 (en) * | 1989-09-01 | 1991-03-07 | Basf Ag | METHOD FOR PRODUCING SPHERICAL, HARD MONO- OR OLIGODISPERSE PARTICLES MELAMINE RESIN |
DE19954189A1 (en) * | 1999-11-11 | 2001-05-17 | Basf Ag | Melamine resin dispersions |
KR100543545B1 (en) * | 2000-12-28 | 2006-01-20 | 니폰 쇼쿠바이 컴파니 리미티드 | Process for producing amino resin particles |
WO2002070576A1 (en) * | 2001-03-02 | 2002-09-12 | Nissan Chemical Industries, Ltd. | Process for producing spherical compound hardened melamine resin particles |
JP4658989B2 (en) * | 2007-03-30 | 2011-03-23 | 株式会社日本触媒 | Amino resin particles, method for producing the same, and use thereof |
JP5476145B2 (en) * | 2010-02-01 | 2014-04-23 | 旭有機材工業株式会社 | Method for producing spherical furan-aldehyde resin particles |
US9632081B2 (en) | 2012-03-28 | 2017-04-25 | Konica Minolta, Inc. | Detection method for biological substance |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5815523A (en) * | 1981-07-23 | 1983-01-28 | Nippon Oil & Fats Co Ltd | Production of alkyl-etherified amino resin |
-
1985
- 1985-09-20 JP JP60206608A patent/JPH0717723B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007186721A (en) * | 2002-07-19 | 2007-07-26 | Nippon Shokubai Co Ltd | Method for producing crosslinked amino-resin particle |
Also Published As
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JPS6268811A (en) | 1987-03-28 |
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