JPS61252202A - Production of uniform spherical polymer - Google Patents

Production of uniform spherical polymer

Info

Publication number
JPS61252202A
JPS61252202A JP9405085A JP9405085A JPS61252202A JP S61252202 A JPS61252202 A JP S61252202A JP 9405085 A JP9405085 A JP 9405085A JP 9405085 A JP9405085 A JP 9405085A JP S61252202 A JPS61252202 A JP S61252202A
Authority
JP
Japan
Prior art keywords
monomer
film
solution
capsule
polymer
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.)
Pending
Application number
JP9405085A
Other languages
Japanese (ja)
Inventor
Shiro Matsumoto
松本 史朗
Misao Hoshino
星野 美佐男
Hidehiko Kobayashi
秀彦 小林
Yoichi Takashima
洋一 高島
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.)
Freund Corp
Original Assignee
Freund Corp
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 Freund Corp filed Critical Freund Corp
Priority to JP9405085A priority Critical patent/JPS61252202A/en
Publication of JPS61252202A publication Critical patent/JPS61252202A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02Making microcapsules or microballoons
    • B01J13/06Making microcapsules or microballoons by phase separation
    • B01J13/14Polymerisation; cross-linking

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Polymerisation Methods In General (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Manufacturing Of Micro-Capsules (AREA)

Abstract

PURPOSE:To obtain the titled polymer having a uniform particle diameter and a high purity in good efficiency, by enveloping a specified amount of a monomer (solution) in a film to form a capsule, polymerizing the monomer (solution) in the capsule and removing the film therefrom. CONSTITUTION:A given amount of a monomer (solution) 5 comprising at least one functional group-containing monomer (e.g., styrene) and, optionally, a solvent (e.g., isooctane) and a polymerization initiator (e.g., benzoyl peroxide) is enveloped in a solution 6 (e.g., water) containing a film-forming agent (e.g., sodium alginate) immiscible with the monomer (solution) to form a concentric two-phase liquid drop 7 of a uniform diameter. A curing agent (e.g., CaCl2) is added to solution 6 to coagulate the film-forming agent into a film 8 and thereby form a capsule 9. This capsule 9 is heated to polymerize the monomer and obtain a polymer particle 10 enveloped in film 8. The film 8 is removed to obtain a spherical polymer comprising a polymer particle 10 and having a given particle diameter.

Description

【発明の詳細な説明】 〔技術分野〕 本発明は球状重合体の製造技術に関し、特に均一粒度の
球状重合体の製造に適用して有効な技術に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a technology for producing spherical polymers, and particularly to a technology that is effective when applied to the production of spherical polymers with uniform particle size.

〔背景技術〕[Background technology]

球状重合体は、その内部構造が均質であっても、また多
孔質であっても実用上重要である。たとえば、多孔質重
合体はイオン交換樹脂の母体やクロマトグラフィ用ゲル
であるカラム充填物として、また触媒用または吸着材用
の担体として利用される。これらは、通常、単官能モノ
マおよび所望量の多官能モノマを共重合させた二次元網
目構造をもつ多孔質重合体で形成されている。これらの
球状多孔質重合体はその粒度がそろっていることがこれ
らを利用する上で極めて重要であるとされている。
Spherical polymers are of practical importance whether their internal structure is homogeneous or porous. For example, porous polymers are used as base materials for ion exchange resins, column packings such as gels for chromatography, and as carriers for catalysts or adsorbents. These are usually formed from a porous polymer having a two-dimensional network structure obtained by copolymerizing a monofunctional monomer and a desired amount of a polyfunctional monomer. It is said that it is extremely important for these spherical porous polymers to have uniform particle sizes in order to utilize them.

球状重合体の製造方法としては、一般的にはモノマを水
中に分散させて重合を行う懸濁重合法や、該重合法に乳
化剤を併用して行う乳化重合法がある。
Methods for producing spherical polymers generally include a suspension polymerization method in which monomers are dispersed in water and polymerized, and an emulsion polymerization method in which an emulsifier is used in combination with the polymerization method.

ところが上記2法によっては、球状重合体を所望の均一
の粒度に制御することが非常に困難であり、一定の粒度
の球状重合体を得るためにはふるい分けを必要とするた
め、所望の粒度の球状重合体の収率は小さくならざるを
得ない。
However, with the above two methods, it is very difficult to control the spherical polymer to the desired uniform particle size, and sieving is required to obtain the spherical polymer with a constant particle size. The yield of spherical polymers must be low.

また、前者においては液体中に分散させた液滴は互いに
、付着する傾向があることから、凝集防止剤で付着防止
の工夫を必要とする。しかし、完全な付着防止は掻めて
困難である。
In addition, in the former case, droplets dispersed in a liquid tend to stick to each other, so it is necessary to take measures to prevent adhesion using an anti-aggregation agent. However, complete prevention of adhesion is extremely difficult.

さらに、後者については、乳化剤の影響およびその乳化
剤の処理が問題となる。
Furthermore, regarding the latter, the influence of the emulsifier and the treatment of the emulsifier are problematic.

即ち、従来法では均一でかつ効率よく所望の粒度の球状
重合体を製造することは不可能であり、所望の均一粒度
の球状重合体の製造方法の開発が強く要望されている。
That is, it is impossible to uniformly and efficiently produce a spherical polymer with a desired particle size using conventional methods, and there is a strong demand for the development of a method for producing a spherical polymer with a desired uniform particle size.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、所望の均一な粒度からなる純度の高い
球状重合体を効率よく製造できる技術を提供することに
ある。
An object of the present invention is to provide a technique that can efficiently produce a highly pure spherical polymer having a desired uniform particle size.

〔発明の概要〕 本発明者は前記目的を達成すべ(研究を重ねて、本発明
を成すに至った。
[Summary of the Invention] The inventor of the present invention has accomplished the above-mentioned object (through repeated research).

すなわち、必要な場合には重合開始剤を含む、一または
二種以上のモノマまたはそのモノマと溶媒との混合溶液
の一定量を、該モノマまたは混合溶液に不溶の材料から
なる皮膜で覆いカプセルを形成し、次いで該カプセルを
所定の条件で処理することにより該皮膜内に封入されて
いるモノマを重合させ、その後カプセル材料の皮膜を除
去することにより、粒度のそろった高純度の球状重合体
を容易に製造することができ、前記目的が達成されるも
のである。
That is, a certain amount of a mixed solution of one or more monomers or a solvent containing one or more monomers and a solvent, including a polymerization initiator if necessary, is covered with a film made of a material that is insoluble in the monomers or the mixed solution to form a capsule. The capsule is then treated under predetermined conditions to polymerize the monomer encapsulated within the film, and then the film of the capsule material is removed to produce a highly pure spherical polymer with uniform particle size. It can be easily manufactured and the above object can be achieved.

本発明の一つの特徴は、モノマまたはその溶液の一定量
をカプセルに封入して均一な球状重合体を製造すること
にある。
One feature of the present invention is that a uniform spherical polymer is produced by encapsulating a certain amount of the monomer or its solution.

このカプセル形成の有効な方法としては、たとえば特開
昭57−19032号公報または特開昭59−1185
9号公報に詳細に説明されており、この方法に準じて行
うことが生産能率が高く有利であると考えられる。
As an effective method for forming this capsule, for example, Japanese Patent Application Laid-Open No. 57-19032 or Japanese Patent Application Laid-Open No. 59-1185
This method is explained in detail in Japanese Patent No. 9, and it is considered to be advantageous to carry out the process according to this method because of high production efficiency.

次に、上記方法の概略を説明する。すなわち、特開昭5
7−19032号公報に開示された技術によって、同心
二重ノズルの内心ノズルからは、必要な場合には重合開
始剤を含む、−もしくは二種以上のモノマまたは該モノ
マと溶媒との混合溶液(以下、モノマ溶液ともいう、)
を、外心ノズルからは前記モノマまたはモノマ溶液には
溶解しない皮膜形成材を含む溶液を、該同心二重ノズル
に振動を与えながら、流出させて均一な同心二相液滴を
生成せしめる。次いで、特開昭59〜11859号公報
に開示された技術によって前記同心二相液滴を該皮膜形
成材の硬化剤を含む微小液滴よりなるミスト層中を落下
せしめることによってカプセル化させるものである。
Next, an outline of the above method will be explained. In other words, Japanese Patent Publication No. 5
According to the technique disclosed in Japanese Patent No. 7-19032, from the inner nozzle of the concentric double nozzle, a mixed solution of two or more monomers or the monomers and a solvent containing a polymerization initiator if necessary ( (hereinafter also referred to as monomer solution)
A solution containing the monomer or a film-forming material that is not dissolved in the monomer solution is caused to flow out from the circumcenter nozzle while applying vibration to the concentric double nozzle to generate uniform concentric two-phase droplets. Next, the concentric two-phase droplets are encapsulated by falling through a mist layer made up of micro droplets containing a hardening agent for the film forming material using the technique disclosed in JP-A-59-11859. be.

前記カプセル化法は重合開始剤を含む−もしくは二種以
上のモノマまたはモノマ溶液を、所望の一定容量のカプ
セル内に封入した状態で重合できるので、重合中に付着
を起こすことがないばかりではなく、重合後の球状重合
体は均一粒径のものが得られる。したがって、本発明に
よれば、従来法の付着防止剤または乳化剤等は全く不用
であり、分級という労力のかかる操作も全く必要としな
い。
The encapsulation method allows polymerization of monomers or monomer solutions containing a polymerization initiator while encapsulating them in capsules with a desired fixed volume, and therefore not only does not cause adhesion during polymerization. After polymerization, a spherical polymer having a uniform particle size can be obtained. Therefore, according to the present invention, there is no need for conventional anti-adhesive agents or emulsifiers, and there is no need for the labor-intensive operation of classification.

本発明は、一または二種以上の官能基を有する種々のモ
ノマを利用することができ、またそれらモノマの混合物
であってもよい。具体的には、たとえばモノビニル化合
物、ジビニル化合物等の多官能ビニル化合物がある。
The present invention can utilize various monomers having one or more types of functional groups, and may also be a mixture of these monomers. Specifically, there are polyfunctional vinyl compounds such as monovinyl compounds and divinyl compounds.

モノビニル化合物としては、たとえばスチレン系化合物
またはアクリル系化合物等があり、ジビニル化合物とし
てはジビニルベンゼン誘導体等が、トリビニル化合物と
してはトリメタクリル酸エステル等がある。
Examples of monovinyl compounds include styrene compounds and acrylic compounds, examples of divinyl compounds include divinylbenzene derivatives, and examples of trivinyl compounds include trimethacrylic acid esters.

前記のモノマと溶媒との混合溶液は、上記一または二種
以上のモノマを、必要な場合には重合開始剤とともに溶
媒に溶解することにより調整される。
The above-mentioned mixed solution of monomer and solvent is prepared by dissolving the above-mentioned one or more monomers together with a polymerization initiator, if necessary, in a solvent.

重合開始剤としては、たとえば過酸化ベンゾイル、アゾ
イソブチロニトリルまたはt−ブチルヒドロキシパーオ
キサイド等が使用できる。また、溶媒はモノマに対する
溶解性が高い親油性のものが通しており、たとえばイソ
オクタン、ペブタン等の脂肪族系またはトルエン等の芳
香族系の溶媒のいずれも利用できる。
As the polymerization initiator, for example, benzoyl peroxide, azoisobutyronitrile or t-butylhydroxyperoxide can be used. Further, the solvent is a lipophilic one that has high solubility for the monomer, and for example, an aliphatic solvent such as isooctane or pebtan, or an aromatic solvent such as toluene can be used.

前記モノマ混合液等を封入した同心二相液滴を形成させ
るための被覆液としては、このモノマ混合液等と混ざり
合わない皮膜形成剤を含む水溶液を用いることができる
。その皮膜形成剤としては、たとえばアルギン酸ナトリ
ウム、カルボキシメチルセルロース等がある。
As the coating liquid for forming concentric two-phase droplets enclosing the monomer mixture etc., an aqueous solution containing a film forming agent that does not mix with the monomer mixture etc. can be used. Examples of the film forming agent include sodium alginate and carboxymethyl cellulose.

皮膜形成剤を凝固させる硬化剤としては塩化カルシウム
、硫酸ナトリウム等があり、これらを皮膜形成剤の種類
に応じて適当なものを選択し、その水溶液として用いる
ことができる。
Hardening agents for coagulating the film-forming agent include calcium chloride, sodium sulfate, etc., and an appropriate one can be selected depending on the type of film-forming agent and used as an aqueous solution.

重合後のカプセル皮膜を除去するための処理剤としては
ポリアクリル酸ナトリウム水溶液等を用いることができ
る。
As a treatment agent for removing the capsule film after polymerization, an aqueous solution of sodium polyacrylate or the like can be used.

本発明の一例である具体的な製造プロセスをさらに詳細
に説明する。
A specific manufacturing process that is an example of the present invention will be described in more detail.

第1図は製造プロセスの概略を示す工程図であり、第2
図は第1図に示す各工程における粒子の状態を示す断面
図である。
Figure 1 is a process diagram showing an outline of the manufacturing process;
The figure is a cross-sectional view showing the state of particles in each step shown in FIG. 1.

工程lはモノマまたはモノマと溶媒との混合溶液の所定
量を含む液滴を形式する工程、工程2はその所定量のモ
ノマ等の表面に皮膜を形成する工程であり、カプセル形
成工程はこの両工程からなるものである。このカプセル
形成工程としては、工程1で第2図(alに示すような
前記の−もしくは二種以上のモノマまたは該モノマ溶液
5を、これらに溶解しない皮膜形成剤を含む溶液6で包
み込んだ均一な粒径の同心二相液滴7を形成させた後、
工程2で第2図山)に示すように外側液相の皮膜形成剤
を凝固させて皮膜8を形成することによりカプセル9の
形成を行うことができる。
Step 1 is a step of forming droplets containing a predetermined amount of a monomer or a mixed solution of a monomer and a solvent, and step 2 is a step of forming a film on the surface of the predetermined amount of monomer, etc. The capsule forming step is a step of forming a droplet containing a predetermined amount of a monomer or a mixed solution of a monomer and a solvent. It consists of processes. In this capsule forming step, in Step 1, the above-mentioned monomer or two or more monomers or the monomer solution 5 as shown in FIG. After forming concentric two-phase droplets 7 with a particle size of
In step 2, capsules 9 can be formed by coagulating the film-forming agent in the outer liquid phase to form a film 8, as shown in FIG.

上記二相液滴7は、たとえば前記特開昭57−1903
2号公報に詳述されている方法により形成でき、形成さ
れる二相液滴7の各液相の径は、同心二重ノズルの径、
各法のそれぞれの流速、同心二重ノズルに与える振動数
および各法の物性によって決り、最適な条件は実験によ
って定められる。振動数は200〜数Klbの範囲、各
法の流速はそれぞれ0.5〜5+wl/secが目安と
なる。その後の皮膜形成も前述の特開昭59−1185
9号公報に記載する方法に準じて行えば完全なカプセル
化が可能である。
The two-phase droplet 7 is, for example,
It can be formed by the method detailed in Publication No. 2, and the diameter of each liquid phase of the two-phase droplet 7 to be formed is the diameter of the concentric double nozzle,
The optimum conditions are determined by the flow rate of each method, the frequency of vibration applied to the concentric double nozzle, and the physical properties of each method, and are determined by experiment. The vibration frequency ranges from 200 to several Klb, and the flow rate for each method is approximately 0.5 to 5+wl/sec. The subsequent film formation was also described in the above-mentioned Japanese Patent Application Laid-Open No. 59-1185.
Complete encapsulation is possible by following the method described in Publication No. 9.

工程3は重合工程であり、モノマまたはモノマ溶液を封
入したカプセルを、たとえば80℃〜90℃程度の温水
浴で適当な時間攪拌しながら加温すれば封入されている
モノマは重合し、皮膜8で覆われたポリマ粒子10とな
る。
Step 3 is a polymerization step, in which the monomer or monomer solution is heated in a hot water bath for an appropriate time while stirring in a hot water bath at about 80°C to 90°C, and the encapsulated monomer is polymerized to form a film 8. This results in polymer particles 10 covered with.

工程4は皮膜の除去工程であり、適当な処理剤1を含む
処理槽の中で重合後のカプセルを攪拌することにより皮
膜8を除去することができ、上記ポリマ粒子10からな
る所望の粒径の球状重合体が製造されるものである。
Step 4 is a film removal step, in which the film 8 can be removed by stirring the capsules after polymerization in a treatment tank containing an appropriate treatment agent 1, and the desired particle size made of the polymer particles 10 can be removed. A spherical polymer is produced.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、モノマまたはモノマ溶液の一定量をカ
プセルに封入することにより、該カプセル内で重合を行
わせることができるものであり、その後カプセル皮膜を
除去することにより、均一粒径の球状重合体を容易に製
造できるものである。
According to the present invention, by enclosing a certain amount of a monomer or a monomer solution into a capsule, polymerization can be carried out within the capsule, and by subsequently removing the capsule film, spherical particles with a uniform diameter can be formed. The polymer can be easily produced.

また、この方法によれば、従来の乳化重合法または懸濁
重合法とのような添加剤を使用する必要がないため粒度
がそろっており、かつ純度の高い球状重合体を高収率で
製造できるものである。
In addition, this method does not require the use of additives as in conventional emulsion polymerization or suspension polymerization methods, so it is possible to produce spherical polymers with uniform particle size and high purity at a high yield. It is possible.

さらに、多官能性モノマを含むモノマ溶液をカプセル化
することにより、均一粒度の多孔質球状重合体を同様に
製造できる。
Furthermore, by encapsulating a monomer solution containing a polyfunctional monomer, porous spherical polymers with uniform particle size can be similarly produced.

このように、本発明は工業的に極めて有益な技術に関す
るものである。
As described above, the present invention relates to an industrially extremely useful technology.

次に、本発明による実施例を説明する。Next, embodiments according to the present invention will be described.

(実施例1〕 内径1.2fi、外径1.8 wnaのノズルを内径2
.9Hのノズルの内側に同心になるように配した二重ノ
ズルの外側にアルギン酸ナトリウムの0.8重量パーセ
ント水溶液を、内側ノズルにステレフ36体積%、ジビ
ニルベンゼン24体積%°、イソオクタン39.4体積
%、過酸化ベンゾイル0.6体積%のモノマ混合溶液を
、それぞれ42ml/win 、 106m1/win
の速度で供給する。そして、このモノマ混合溶液を供給
しながら、該二重ノズルを振巾100μ鴎、振動数40
0Hz”i:振動させて同心二相液滴の外径4.0鶴の
均一粒径の液滴を毎秒400個発生させる。別に超音波
方式のミスト発生機を用いて脩温の塩化カルシウム30
重量%水溶液から微細なミストを発生させ、極めて弱い
空気流中にただよりせ、そのミスト層の中心部を上記同
心二相液滴を落下せしめる。このミスト層を通過中に液
滴表面ではアルギン酸ナトリウムと塩化カルシウムの反
応が起こり水不溶性のアルギン酸カルシウムとなり皮膜
が形成される。このカプセル粒子を念のため該塩化カル
シウム水溶液中に落下させてカプセル化を完了せしめる
0次に該カプセル粒子を90℃の温水浴中にてゆっくり
撹拌させながら、アルギン酸カルシウムで被覆されてい
るポリマ粒子を得る。その後、ポリリン酸ナトリウム1
0重量%水溶液中に移し、化学的に処理してアルギン酸
カルシウム皮膜を除去し、直径2.3館の均一なポリマ
粒子を得た。
(Example 1) A nozzle with an inner diameter of 1.2 fi and an outer diameter of 1.8 wna was
.. A 0.8% by weight aqueous solution of sodium alginate was placed on the outside of a double nozzle placed concentrically inside the 9H nozzle, and 36% by volume of Stereph, 24% by volume of divinylbenzene, and 39.4% by volume of isooctane were placed in the inside nozzle. % and benzoyl peroxide 0.6 volume % monomer mixed solution at 42 ml/win and 106 ml/win, respectively.
supply at a rate of Then, while supplying this monomer mixed solution, the double nozzle was heated at a vibration width of 100 μm and a vibration frequency of 40 μm.
0Hz"i: Vibrate to generate 400 concentric two-phase droplets with an outer diameter of 4.0 mm and a uniform particle size per second. Separately, an ultrasonic mist generator is used to generate calcium chloride at a temperature of 30 Hz.
A fine mist is generated from a wt % aqueous solution, suspended in an extremely weak air flow, and the concentric two-phase droplets fall from the center of the mist layer. While passing through this mist layer, a reaction between sodium alginate and calcium chloride occurs on the surface of the droplet to form water-insoluble calcium alginate, forming a film. The capsule particles are dropped into the calcium chloride aqueous solution to complete the encapsulation.Next, the capsule particles are slowly stirred in a 90°C hot water bath while the polymer particles coated with calcium alginate are poured into the calcium chloride aqueous solution. get. Then, sodium polyphosphate 1
The particles were transferred into a 0% by weight aqueous solution and chemically treated to remove the calcium alginate film to obtain uniform polymer particles with a diameter of 2.3 cm.

なお、最終的には溶媒であるイソオクタンを除去するこ
とにより粒径のそろった多孔質球状重合体が得られる。
Incidentally, by finally removing the isooctane solvent, a porous spherical polymer having a uniform particle size can be obtained.

〔実施例2〕 実施例1におけるモノマ混合液の希釈剤をイソオクタン
の代わりにヘプタンを用いて実験を行い、実施例1と同
様に直径2.3簡の均一なポリマ粒子を得た。
[Example 2] An experiment was conducted using heptane instead of isooctane as the diluent for the monomer mixture in Example 1, and uniform polymer particles with a diameter of 2.3 pieces were obtained in the same manner as in Example 1.

〔実施例3〕 内径0.9誼のノズルの内側に、内径0.5 m 、外
径0.6鶴のノズルを同心に配した二重ノズルに実施例
1と同様にモノマ混合液および皮膜形成剤を含む溶液を
それぞれ16.7ml/sin 、 15.211/s
inずつ供給し、振動数400 Hzで振動操作するこ
とにより直径1.1(1Mの均一な粒子を得た。
[Example 3] A monomer mixture and a film were applied in the same manner as in Example 1 to a double nozzle in which a nozzle with an inner diameter of 0.5 m and an outer diameter of 0.6 m was arranged concentrically inside a nozzle with an inner diameter of 0.9 mm. 16.7 ml/sin and 15.211/s of the solution containing the forming agent, respectively.
Uniform particles with a diameter of 1.1 (1M) were obtained by supplying the particles at a rate of 1.5 in. and vibrating at a frequency of 400 Hz.

以上、本発明の詳細な説明したが、本発明は前記実施例
に限定されるものでないことはいうまでもない。
Although the present invention has been described in detail above, it goes without saying that the present invention is not limited to the above embodiments.

たとえば、モノマまたはモノマ溶液のカプセル封入を、
特開昭57−19032号公報および同59−1185
9号公報に記載された方法で行うものについて説明した
が1.これに限るものでなく、同様のカプセル形成が可
能な方法であれば如何なる方法によってもよい。
For example, encapsulation of monomers or monomer solutions
JP-A-57-19032 and JP-A-59-1185
The method described in Publication No. 9 was explained, but 1. The present invention is not limited to this, and any method that can form a similar capsule may be used.

また、単官能と二官能の二種類のビニルモノマ、それも
スチレンとジビニルベンゼンとに溶媒を混合せしめた溶
液をカプセル封入する例についてのみ説明したが、無溶
媒系であってもよく、使用するモノマも一種類のみであ
っても三種類以上の混合系であってもよい。
In addition, although we have only described an example in which a solution of two types of vinyl monomers, monofunctional and difunctional, styrene and divinylbenzene, mixed with a solvent is encapsulated, a solvent-free system may also be used, and the monomers used may be encapsulated. It may be one type or a mixture of three or more types.

さらに、重合の種類および方法も実施例に示したものに
限らないことはいうまでもない。
Furthermore, it goes without saying that the type and method of polymerization are not limited to those shown in the Examples.

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

第1図は本発明の一実施例による均一な球状重合体の製
造方法の工程、第2図ial〜(dlは第1図の各工程
における粒子の状態を順次示す断面図である。 1・・・液滴形成工程、 2・・・皮膜形成工程、 3・・・重合工程、 4・・・被膜除去工程、 5・・・モノマ溶液、 6・・・皮膜形成剤を含む溶液、 7・・・同心二相液滴、 8・・・皮膜、 9・・・カプセル、 10・・・ポリマ粒子。
FIG. 1 shows the steps of a method for producing a uniform spherical polymer according to an embodiment of the present invention, and FIG. 2 is a sectional view showing the state of particles in each step in FIG. ... Droplet formation step, 2. Film forming step, 3. Polymerization step, 4. Film removal step, 5. Monomer solution, 6. Solution containing film forming agent, 7. ... Concentric two-phase droplet, 8... Film, 9... Capsule, 10... Polymer particle.

Claims (3)

【特許請求の範囲】[Claims] (1)、モノマまたはモノマと溶媒との混合溶液の一定
量を皮膜で覆いカプセルを形成する工程と、上記皮膜内
に封入されたモノマを重合させる工程と、上記皮膜を除
去する工程とからなる均一な球状重合体の製造方法。
(1) Consists of a step of covering a certain amount of a monomer or a mixed solution of a monomer and a solvent with a film to form a capsule, a step of polymerizing the monomer encapsulated in the film, and a step of removing the film. A method for producing a uniform spherical polymer.
(2)、カプセルを形成する工程が、モノマまたはモノ
マと溶媒との混合溶液の一定量を封入した、均一な同心
多相液滴を形成する工程と、該液滴の外相を皮膜化せし
めカプセル封入する工程とからなることを特徴とする特
許請求の範囲第1項記載の均一な球状重合体の製造方法
(2) The step of forming a capsule includes a step of forming a uniform concentric multiphase droplet enclosing a certain amount of a monomer or a mixed solution of a monomer and a solvent, and a step of forming a film on the outer phase of the droplet to form a capsule. A method for producing a uniform spherical polymer according to claim 1, comprising the step of encapsulating.
(3)、多相液滴が二相液滴であることを特徴とする特
許請求の範囲第2項記載の均一な球状重合体の製造方法
(3) The method for producing a uniform spherical polymer according to claim 2, wherein the multiphase droplets are two-phase droplets.
JP9405085A 1985-05-01 1985-05-01 Production of uniform spherical polymer Pending JPS61252202A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9405085A JPS61252202A (en) 1985-05-01 1985-05-01 Production of uniform spherical polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9405085A JPS61252202A (en) 1985-05-01 1985-05-01 Production of uniform spherical polymer

Publications (1)

Publication Number Publication Date
JPS61252202A true JPS61252202A (en) 1986-11-10

Family

ID=14099723

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9405085A Pending JPS61252202A (en) 1985-05-01 1985-05-01 Production of uniform spherical polymer

Country Status (1)

Country Link
JP (1) JPS61252202A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008502463A (en) * 2004-06-01 2008-01-31 ボストン サイエンティフィック リミテッド Embolization
JP2010505985A (en) * 2006-10-05 2010-02-25 ビーエーエスエフ ソシエタス・ヨーロピア Method for producing water-absorbing polymer particles by polymerization of droplets of a monomer solution
CN109265711A (en) * 2018-09-03 2019-01-25 胡权 A kind of preparation method of polymer particle

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5811505A (en) * 1981-07-15 1983-01-22 Nippon Oil Co Ltd Preparation of water-insoluble polymer having uniform shape
JPS61101504A (en) * 1984-10-22 1986-05-20 Kanegafuchi Chem Ind Co Ltd Production of truly spherical polymer particle

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5811505A (en) * 1981-07-15 1983-01-22 Nippon Oil Co Ltd Preparation of water-insoluble polymer having uniform shape
JPS61101504A (en) * 1984-10-22 1986-05-20 Kanegafuchi Chem Ind Co Ltd Production of truly spherical polymer particle

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008502463A (en) * 2004-06-01 2008-01-31 ボストン サイエンティフィック リミテッド Embolization
JP2010505985A (en) * 2006-10-05 2010-02-25 ビーエーエスエフ ソシエタス・ヨーロピア Method for producing water-absorbing polymer particles by polymerization of droplets of a monomer solution
CN109265711A (en) * 2018-09-03 2019-01-25 胡权 A kind of preparation method of polymer particle
WO2020048435A1 (en) * 2018-09-03 2020-03-12 胡权 Polymer particles preparation method

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