JP2649796B2 - Method for producing sustained-release microcapsules - Google Patents

Method for producing sustained-release microcapsules

Info

Publication number
JP2649796B2
JP2649796B2 JP61313729A JP31372986A JP2649796B2 JP 2649796 B2 JP2649796 B2 JP 2649796B2 JP 61313729 A JP61313729 A JP 61313729A JP 31372986 A JP31372986 A JP 31372986A JP 2649796 B2 JP2649796 B2 JP 2649796B2
Authority
JP
Japan
Prior art keywords
substance
wall film
microcapsules
core substance
core
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
Application number
JP61313729A
Other languages
Japanese (ja)
Other versions
JPS63166429A (en
Inventor
雅史 森脇
桂 江藤
浩之 関原
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.)
TOTSUPAN MUUA KK
Original Assignee
TOTSUPAN MUUA KK
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 TOTSUPAN MUUA KK filed Critical TOTSUPAN MUUA KK
Priority to JP61313729A priority Critical patent/JP2649796B2/en
Publication of JPS63166429A publication Critical patent/JPS63166429A/en
Application granted granted Critical
Publication of JP2649796B2 publication Critical patent/JP2649796B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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
    • B01J13/20After-treatment of capsule walls, e.g. hardening

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、マイクロカプセルの芯物質放出量制御方法
に関するものである。
Description: TECHNICAL FIELD The present invention relates to a method for controlling the amount of core substance released from microcapsules.

従来の技術 マイクロカプセルは、芯物質の周囲を壁膜で被覆した
構造をもつ微小体であって、感圧複写紙の塗被剤、医薬
品、農薬、香料、接着剤、酵素、顔料、染料、溶剤など
の封入材として広く応用されている。
2. Description of the Related Art Microcapsules are microscopic bodies having a structure in which a core material is covered with a wall film, and are used as coating materials for pressure-sensitive copying paper, pharmaceuticals, agricultural chemicals, fragrances, adhesives, enzymes, pigments, dyes, It is widely applied as an encapsulant for solvents and the like.

このマイクロカプセルの製造方法としては、疎水性モ
ノマーを含有する非水混和性溶媒を、親水性モノマーを
含有する水中に微細分散させて、非水混和性溶媒と水と
の界面で重合反応させることにより壁膜を形成させる、
いわゆる界面重合法、疎水性ポリマー溶液を、凝固液中
に微細分散状態で導入し硬化させて壁膜を形成させる、
いわゆる液中硬化被覆法、芯物質を媒体中に微分分散状
態で導入し、芯物質又は媒体のいずれか一方に含有させ
たモノマーを重合させて壁膜を形成させる、いわゆるイ
ンサイチュ(insitu)重合法、芯物質を微細分散させた
水溶性ポリマーの水溶液に、水と混和性のポリマーの非
溶媒を加え、芯物質の表面にポリマー被覆を形成させ
る、いわゆるコアセルベーション法などが知られてい
る。
As a method for producing this microcapsule, a non-water-miscible solvent containing a hydrophobic monomer is finely dispersed in water containing a hydrophilic monomer, and a polymerization reaction is performed at an interface between the non-water-miscible solvent and water. To form a wall film,
A so-called interfacial polymerization method, a hydrophobic polymer solution is introduced in a finely dispersed state into a coagulating liquid and cured to form a wall film,
A so-called in-situ polymerization method in which a core material is introduced into a medium in a differentially dispersed state, and a monomer contained in either the core material or the medium is polymerized to form a wall film. A so-called coacervation method is known in which a non-solvent of a water-miscible polymer is added to an aqueous solution of a water-soluble polymer in which a core substance is finely dispersed to form a polymer coating on the surface of the core substance.

また、これらの方法で形成される壁膜の材料として
は、例えばゼラチン、アラビアゴム、ポリアミド、ポリ
ウレタン、ポリエステル、ポリスルホンアミド、ポリ尿
素、ポリスルホネート、ポリカーボネート、エポキシ樹
脂、尿素−ホルムアルデヒド樹脂、メラミン−ホルムア
ルデヒド樹脂などがある。
Examples of the material of the wall film formed by these methods include gelatin, gum arabic, polyamide, polyurethane, polyester, polysulfonamide, polyurea, polysulfonate, polycarbonate, epoxy resin, urea-formaldehyde resin, melamine-formaldehyde. There are resins and the like.

ところで、近年、マイクロカプセルの利用分野が広が
るとともに、その要求特性が高くなってきたが、その1
つとして、マイクロカプセル内の芯物質が徐々に放出さ
れて、所要の効果を持続的に発揮する性質、いわゆる徐
放性がある。
By the way, in recent years, as the use field of microcapsules has expanded, the required characteristics have been increasing.
For example, there is a property that the core substance in the microcapsule is gradually released and the required effect is continuously exhibited, that is, a so-called sustained release property.

しかしながら、これまで、壁膜に徐放性を付与する方
法は知られていないため、徐放性のマイクロカプセルと
するには、溶解性の異なる壁膜をもつマイクロカプセル
や壁膜の厚さの異なるマイクロカプセルを複数種類調製
し、混合して使用しなければならなかったが、これには
多大の労力と経費を要し、とうてい工業的に実施しうる
ものではなかった。
However, there has been no known method for imparting sustained-release properties to the wall membrane. Thus, in order to obtain a sustained-release microcapsule, a microcapsule having a wall membrane having a different solubility or a thickness of the wall membrane is not considered. A plurality of different microcapsules had to be prepared and mixed and used, but this required a great deal of labor and expense and was not practically feasible.

発明が解決しようとする課題 本発明は、使用目的に応じ、マイクロカプセルの芯物
質の放出量を制御する方法を提供することを目的として
なされたものである。
DISCLOSURE OF THE INVENTION An object of the present invention is to provide a method for controlling the release amount of a core substance of a microcapsule according to the purpose of use.

課題を解決するための手段 本発明者らは、マイクロカプセルの芯物質放出量制御
方法を開発するために種々研究を重ねた結果、あらかじ
め疎水性芯物質中に、それと水性媒体の両方に対して相
溶性を示す液状物質を含有させ、かつその含有量及び疎
水性芯物質に対する分配率及び壁膜形成のための反応条
件を変えるという簡単な方法により、壁膜のち密性を調
節して生成マイクロカプセルの芯物質放出量を制御しう
ることを見出し、この知見に基づいて本発明を完成する
に至った。
Means for Solving the Problems The present inventors have conducted various studies in order to develop a method for controlling the amount of core substance released from microcapsules. A simple method of containing a compatible liquid material, and changing the content, distribution ratio to the hydrophobic core material, and reaction conditions for forming the wall film, adjusts the tightness of the wall film to form the microparticles. They found that the amount of core substance released from the capsule could be controlled, and based on this finding, completed the present invention.

すなわち、本発明は、水性媒体中に疎水性芯物質を分
散させたのち、この芯物質の周囲に壁膜を形成させてマ
イクロカプセルを製造するに当り、あらかじめ該疎水性
芯物質中に、水性媒体及び疎水性芯物質の両方に対して
相溶性を示す液状物質を含有させ、その含有量を疎水性
芯物質100重量部に対して0.1〜20重量部の範囲で変える
とともに、その疎水性芯物質に対する分配率及び壁膜形
成のための反応条件を変えることにより壁膜のち密性を
調節することを特徴とする生成マイクロカプセルの芯物
質放出量制御方法を提供するものである。
That is, the present invention disperses a hydrophobic core material in an aqueous medium, and then forms a wall film around the core material to produce microcapsules. A liquid material that is compatible with both the medium and the hydrophobic core material is contained, and the content is changed in the range of 0.1 to 20 parts by weight with respect to 100 parts by weight of the hydrophobic core material, and the hydrophobic core is changed. It is an object of the present invention to provide a method for controlling a core substance release amount of produced microcapsules, characterized in that the density of a wall film is adjusted by changing a distribution ratio to a substance and a reaction condition for forming a wall film.

以下、本発明を詳細に説明する。 Hereinafter, the present invention will be described in detail.

本発明方法におけるマイクロカプサルの形成方法には
特に制限はなく、従来行われている界面重合法、液中硬
化被覆法、インサイチュ重合法、コアセルベーション法
などの中から任意に選択して使用することができる。こ
の場合、芯物質としては、疎水性物質を、また芯物質を
微細分散させる媒体としては水性媒体をそれぞれ用いる
ことが必要である。このような芯物質の例としては、非
水混和性溶剤、油性インキ、非水溶性医薬成分、非水溶
性農薬成分、非水溶性接着剤などを挙げることができ
る。またマイクロカプセルの壁膜を構成する材料として
は、例えばゼラチン、アラビアゴム、ポリアミド、ポリ
ウレタン、ポリエステル、ポリスルホンアミド、ポリ尿
素、ポリスルホネート、ポリカーボネート、エポキシ樹
脂、尿素・ホルムアルデヒド樹脂、メラミン−ホルムア
ルデヒド樹脂などが用いられるが、特にスチレン−無水
マレイン酸共重合体のアルカリによる部分加水分解物と
メチロール化メラミン又はスチロール化尿素との反応生
成物が好適である。
The method for forming microcapsules in the method of the present invention is not particularly limited, and may be arbitrarily selected from conventional methods such as interfacial polymerization, in-liquid curing coating, in-situ polymerization, and coacervation. can do. In this case, it is necessary to use a hydrophobic substance as the core substance and an aqueous medium as a medium for finely dispersing the core substance. Examples of such core materials include non-water-miscible solvents, oil-based inks, water-insoluble pharmaceutical ingredients, water-insoluble pesticide ingredients, water-insoluble adhesives, and the like. Examples of the material constituting the wall film of the microcapsule include gelatin, gum arabic, polyamide, polyurethane, polyester, polysulfonamide, polyurea, polysulfonate, polycarbonate, epoxy resin, urea-formaldehyde resin, melamine-formaldehyde resin, and the like. Among them, a reaction product of a partially hydrolyzed styrene-maleic anhydride copolymer with an alkali and a methylolated melamine or a styreneolated urea is particularly preferred.

本発明方法においては、マイクロカプセルの形成時
に、芯物質中に、この芯物質とこれを微細分散させる水
性媒体の両方に対して相溶性を示す液状物質を含有させ
ておくことが必要である。
In the method of the present invention, it is necessary to include a liquid material that is compatible with both the core material and the aqueous medium in which the core material is finely dispersed in the core material when forming the microcapsules.

この液状物質は、疎水性芯物質の周囲に壁膜を形成さ
せる際に、該芯物質から水性媒体中に溶出して、壁膜の
ち密性を調節する。
When a liquid film is formed around the hydrophobic core material, the liquid material elutes from the core material into the aqueous medium to regulate the tightness of the wall film.

このような液状物質としては、例えば多価アルコー
ル、ポリエチレングリコールやポリプロピレングリコー
ルのようなポリアルキレングリコール、水溶性エポキシ
化合物などを挙げることができる。
Examples of such liquid substances include polyhydric alcohols, polyalkylene glycols such as polyethylene glycol and polypropylene glycol, and water-soluble epoxy compounds.

本発明方法においては、この液状物質について、その
含有量を、疎水性芯物質100重量部に対して0.1〜20重量
部の範囲で変えるとともに、その疎水性芯物質に対する
分配率を変えることが重要であり、また壁膜形成のため
の反応条件を変えることが重要である。
In the method of the present invention, it is important to change the content of the liquid substance in the range of 0.1 to 20 parts by weight with respect to 100 parts by weight of the hydrophobic core substance, and to change the distribution ratio to the hydrophobic core substance. It is important to change the reaction conditions for forming the wall film.

本発明方法の好適な実施態様に従えば、疎水性芯物質
に、前記の液状物質を加え、この混合物を水性媒体中に
適宜微細分散させ、芯物質の周囲に壁膜を形成させる。
この際疎水性芯物質中の液状物質は、水性媒体に可溶な
ため、微細分散状態の芯物質中から水性媒体中に拡散放
出され、形成される壁膜のち密性が調節される。したが
って、該液状物質の種類や添加量を適当に選ぶことによ
り芯物質からの溶出量をコントロールすることができ、
壁膜の特性を制御することができる。
According to a preferred embodiment of the method of the present invention, the aforementioned liquid substance is added to the hydrophobic core substance, and this mixture is finely dispersed in an aqueous medium as appropriate to form a wall film around the core substance.
At this time, since the liquid substance in the hydrophobic core substance is soluble in the aqueous medium, the liquid substance is diffused and released from the finely dispersed core substance into the aqueous medium, and the tightness of the formed wall film is adjusted. Therefore, the amount of elution from the core substance can be controlled by appropriately selecting the type and amount of the liquid substance,
The properties of the wall membrane can be controlled.

次に本発明の好適な実施態様を、壁材がスチレン−無
水マレイン酸共重合体のアルカリによる部分加水分解物
とメチロール化メラミン又はメチロール化尿素との反応
生成物である場合を例に挙げて説明すると、まず水性媒
体中にスチレン−無水マレイン酸共重合体を分散し、こ
れに所望量のアルカリを加え20〜100℃の温度に保っ
て、所望の加水分解率になるまで加水分解したのち、こ
の部分加水分解の水溶液を0.5〜20重量%の濃度に調整
する。次いで、この中に、所要量の液状物質を溶解した
疎水性芯物質を加え、所要時間高速かきまぜあるいは超
音波などにより乳化又は分散させる。この際の芯物質の
量は、重量に基づきスチレン−無水マレイン酸共重合体
の部分加水分解物の5〜50倍程度が適当であり、また、
該疎水性芯物質を乳化又は分散させるのに要する時間
は、該液状物質の水性媒体及び疎水性芯物質に対する分
配率や、所望する壁膜の特性などを考慮し、通常1〜30
分の範囲で適宜選ばれる。
Next, a preferred embodiment of the present invention will be described by taking, as an example, a case where the wall material is a reaction product of a partially hydrolyzed styrene-maleic anhydride copolymer with an alkali and a methylolated melamine or a methylolated urea. To explain, first, a styrene-maleic anhydride copolymer is dispersed in an aqueous medium, a desired amount of alkali is added thereto, and the mixture is maintained at a temperature of 20 to 100 ° C. and hydrolyzed until a desired hydrolysis rate is reached. The aqueous solution of this partial hydrolysis is adjusted to a concentration of 0.5 to 20% by weight. Next, a hydrophobic core substance in which a required amount of a liquid substance is dissolved is added thereto, and the mixture is emulsified or dispersed by high-speed stirring or ultrasonic waves for a required time. The amount of the core substance at this time is suitably about 5 to 50 times the partial hydrolyzate of the styrene-maleic anhydride copolymer based on the weight, and
The time required for emulsifying or dispersing the hydrophobic core material is usually 1 to 30 in consideration of the partition ratio of the liquid material to the aqueous medium and the hydrophobic core material, the desired properties of the wall film, and the like.
In the range of minutes.

次に、メチロール化メラミン又はメチロール化尿素の
水溶液を、前記のスチレン−無水マレイン酸共重合体の
部分加水分解物と芯物質とを含む水溶液に加え、pH3〜
7、40〜90℃の条件下で、30〜180分間かきまぜながら
反応させる。この際のpH調整に、必要ならば、酸例えば
クエン酸を用いることができる。また、メチロール化メ
ラミン又はメチロール化尿素の量は、スチレン−無水マ
レイン酸共重合体の部分加水分解物100重量部当り10〜1
00重量部の範囲内で選ばれる。
Next, an aqueous solution of methylolated melamine or methylolated urea was added to the aqueous solution containing the partial hydrolyzate of the styrene-maleic anhydride copolymer and the core substance, and had a pH of 3 to
7. React with stirring at 40-90 ° C for 30-180 minutes. In this case, an acid such as citric acid can be used for pH adjustment, if necessary. The amount of methylolated melamine or methylolated urea is 10 to 1 per 100 parts by weight of the partially hydrolyzed styrene-maleic anhydride copolymer.
It is selected within the range of 00 parts by weight.

この反応により、芯物質の周囲にスチレン−無水マレ
イン酸共重合体の部分加水分解物と、メチロール化メラ
ミン又はメチロール化尿素との反応生成物から成る壁膜
が形成され、しかもこの壁膜は、該液状物質によりち密
性が調節され、芯物買からの溶出量をコントロールする
ことができる。
By this reaction, a wall film composed of a reaction product of a partial hydrolyzate of a styrene-maleic anhydride copolymer and a methylolated melamine or a methylolated urea is formed around the core substance. The tightness is controlled by the liquid substance, and the amount of elution from the core material can be controlled.

発明の効果 本発明方法によれば、カプセル中の芯物質(有効成
分)の放出量、放出時間、タイミングなどを所望どおり
にコントロールしうるように、壁膜の特性を任意に調節
することができ、例えば徐放性マイクロカプセルを容易
に製造しうる。
Effect of the Invention According to the method of the present invention, the characteristics of the wall membrane can be arbitrarily adjusted so that the release amount, release time, timing, etc. of the core substance (active ingredient) in the capsule can be controlled as desired. For example, sustained-release microcapsules can be easily produced.

実施例 次に実施例により本発明をさらに詳細に説明するが、
本発明はこれらの例によってなんら制限されるものでは
ない。
Examples Next, the present invention will be described in more detail with reference to Examples.
The invention is not limited in any way by these examples.

なお、この例においては、マイクロカプセルの壁膜の
ち密性を耐溶剤性により評価したが、このマイクロカプ
セルの耐溶剤性は次のようにして求めた。
In this example, the tightness of the wall film of the microcapsules was evaluated by solvent resistance. The solvent resistance of the microcapsules was determined as follows.

すなわち、ドライカプセル0.5gに溶剤20ccを加え、超
音波洗浄器(25℃)で30時間処理したのち、該溶剤中に
抽出された芯物質量を液体クロマトグラフィーで定量
し、耐溶剤性を芯物質全量に対する%で示した。数値の
小さいものほど耐溶剤性が優れている。
That is, after adding 20 cc of a solvent to 0.5 g of the dry capsule and treating it in an ultrasonic cleaner (25 ° C.) for 30 hours, the amount of the core substance extracted in the solvent is quantified by liquid chromatography, and the solvent resistance is determined. It was shown as% of the total amount of the substance. The smaller the value, the better the solvent resistance.

なお、溶剤としてエタノール及びテトラヒドロフラン
の2種類を用いた。
Note that two types of solvents, ethanol and tetrahydrofuran, were used.

比較例1 スクリプセット520[商品名、モンサント社製、スチ
レン−無水マレイン酸共重合体(モル比1:1)]100gと
水酸化ナトリウム0.17モルとを水中で加熱し、スチレン
−無水マレイン酸共重合体の部分加水分解物の5重量%
水溶液300gにフタル酸ジメチル300gを2分間乳化分散し
たのち、60℃のウォーターバスでかきまぜながら保温し
ている乳化分散液中に、メラミン樹脂(Sumirog Resin
607 Syrup,住友化学社製)120gを添加し、2時間反
応してカプセルスラリーを得た。
Comparative Example 1 100 g of a script set 520 [trade name, manufactured by Monsanto Co., styrene-maleic anhydride copolymer (molar ratio 1: 1)] and 0.17 mol of sodium hydroxide were heated in water to form a styrene-maleic anhydride copolymer. 5% by weight of partial hydrolyzate of polymer
After emulsifying and dispersing 300 g of dimethyl phthalate in 300 g of the aqueous solution for 2 minutes, stir the mixture in a water bath at 60 ° C and keep the temperature in the emulsified dispersion to add melamine resin (Sumirog Resin).
(607 Syrup, manufactured by Sumitomo Chemical Co., Ltd.) was added and reacted for 2 hours to obtain a capsule slurry.

このカプセルを取り出し、耐溶剤性を求め、その結果
を第1表に示した。
The capsules were taken out and the solvent resistance was determined. The results are shown in Table 1.

比較例2 イソプロピルナフタレン(呉羽化学社製、KMC−113)
120gにテレフタル酸クロライド13gを溶解した溶液を、
2重量%ポリビニルアルコール水溶液300g中で2分間乳
化処理した。次いで、この乳化液中にかきまぜながら、
水80gに炭酸ナトリウム4gとジエチレントリアミン8gと
を溶解した水溶液を徐々に加え、24時間反応してカプセ
ルを得た。
Comparative Example 2 Isopropyl naphthalene (KMC-113, manufactured by Kureha Chemical Co., Ltd.)
A solution of terephthalic acid chloride 13 g dissolved in 120 g,
The emulsion was emulsified in 300 g of a 2% by weight aqueous solution of polyvinyl alcohol for 2 minutes. Then, while stirring into this emulsion,
An aqueous solution in which 4 g of sodium carbonate and 8 g of diethylenetriamine were dissolved in 80 g of water was gradually added, and the mixture was reacted for 24 hours to obtain a capsule.

このカプセルを取り出し、耐溶剤性を求め、その結果
を第2表に示した。
The capsule was taken out and the solvent resistance was determined. The results are shown in Table 2.

実施例1,2 比較例1において、フタル酸ジメチルに、水溶性エポ
キシ化合物(ナガセ化成工業社製、デナコールEX 61
1)1gを溶解したものを芯物質として用い、かつ乳化処
理時間を5分間(実施例1)及び10分間(実施例2)と
した以外は、比較例1と同様に処理し、カプセルを得
た。これらのカプセルの耐溶剤性を求め、その結果を第
1表に示した。
Examples 1 and 2 In Comparative Example 1, dimethyl phthalate was added to a water-soluble epoxy compound (Denacol EX 61, manufactured by Nagase Kasei Kogyo Co., Ltd.).
1) A capsule was obtained by treating in the same manner as in Comparative Example 1 except that 1 g was dissolved as a core substance and the emulsification time was 5 minutes (Example 1) and 10 minutes (Example 2). Was. The solvent resistance of these capsules was determined, and the results are shown in Table 1.

実施例3,4 比較例2において、イソプロピルナフタレンに、さら
に水溶性エポキシ化合物(デナコールEX 611)1gを添
加し、かつ乳化処理時間を5分間(実施例3)及び10分
間(実施例4)とした以外は、比較例2と同様に処理
し、カプセルを得た。これらのカプセルの耐溶剤性を求
め、その結果を第2表に示した。
Examples 3 and 4 In Comparative Example 2, 1 g of a water-soluble epoxy compound (Denacol EX 611) was further added to isopropyl naphthalene, and the emulsification time was changed to 5 minutes (Example 3) and 10 minutes (Example 4). A capsule was obtained in the same manner as in Comparative Example 2 except for the above. The solvent resistance of these capsules was determined, and the results are shown in Table 2.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】水性媒体中に疎水性芯物質を分散させたの
ち、この芯物質の周囲に壁膜を形成させてマイクロカプ
セルを製造するに当り、あらかじめ該疎水性芯物質中
に、水性媒体及び疎水性芯物質の両方に対して相溶性を
示す液状物質を含有させ、その含有量を疎水性芯物質10
0重量部に対して0.1〜20重量部の範囲で変えるととも
に、その疎水性芯物質に対する分配率及び壁膜形成のた
めの反応条件を変えることにより壁膜のち密性を調節す
ることを特徴とする生成マイクロカプセルの芯物質放出
量制御方法。
(1) dispersing a hydrophobic core material in an aqueous medium, and then forming a wall film around the core material to manufacture microcapsules; And a liquid substance that is compatible with both the hydrophobic core substance and the content thereof.
It is characterized in that it changes in the range of 0.1 to 20 parts by weight with respect to 0 parts by weight, and that the partitioning ratio of the hydrophobic core substance and the reaction conditions for forming the wall film are changed to adjust the tightness of the wall film. To control the amount of core substance released from the resulting microcapsules.
JP61313729A 1986-12-26 1986-12-26 Method for producing sustained-release microcapsules Expired - Fee Related JP2649796B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61313729A JP2649796B2 (en) 1986-12-26 1986-12-26 Method for producing sustained-release microcapsules

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61313729A JP2649796B2 (en) 1986-12-26 1986-12-26 Method for producing sustained-release microcapsules

Publications (2)

Publication Number Publication Date
JPS63166429A JPS63166429A (en) 1988-07-09
JP2649796B2 true JP2649796B2 (en) 1997-09-03

Family

ID=18044815

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61313729A Expired - Fee Related JP2649796B2 (en) 1986-12-26 1986-12-26 Method for producing sustained-release microcapsules

Country Status (1)

Country Link
JP (1) JP2649796B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02240567A (en) * 1989-03-14 1990-09-25 Sekisui Chem Co Ltd Drug for blood taking tube and blood taking tube using this drug

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5115769A (en) * 1974-06-14 1976-02-07 Aisin Seiki Jidoshaniokeru seidoekiatsuijokoatsuhoshosochi
JPS5441289B2 (en) * 1974-10-18 1979-12-07

Also Published As

Publication number Publication date
JPS63166429A (en) 1988-07-09

Similar Documents

Publication Publication Date Title
US5277979A (en) Process for microencapsulation
JPH09505074A (en) Microcapsules containing suspensions of biologically active compounds
JPH0568300B2 (en)
CZ300099B6 (en) Microcapsule and process for producing thereof
JPS602100B2 (en) Method for manufacturing microcapsules
JPH0620535B2 (en) Microcapsule manufacturing method
JPS63178840A (en) Slowly-releasable microcapsule
US4518547A (en) Microencapsulation process
EP0305212B1 (en) Process for microencapsulation, uses of polymers prepared by said process, and compositions containing polymers prepared by said process
CN108395504A (en) The method that emulsifier-free emulsion polymerization prepares double responsiveness polymer Janus microballoons
GB2177997A (en) Process for producing microcapsules
JPH02293041A (en) Production of microcapsule containing water-soluble material
AU716412B2 (en) Microencapsulation process and product
JPH01194939A (en) Preparation of microcapsule
JP2649796B2 (en) Method for producing sustained-release microcapsules
JP2534691B2 (en) Method for producing high-density microcapsules
JPH028774B2 (en)
JPH0337970B2 (en)
JP3194768B2 (en) Microcapsule and method for producing the same
JPS60216838A (en) Preparation of microcapsule
JPH0379061B2 (en)
JPS60238140A (en) Preparation of microcapsule
JP3186783B2 (en) Manufacturing method of microcapsules
DE10010194A1 (en) Production of micro- and/or nano-capsules used e.g. for encapsulating pharmaceutical and cosmetic active ingredients comprises mixing together the starting materials under laminar conditions and encapsulating in the conventional manner
JP2824309B2 (en) Manufacturing method of microcapsules

Legal Events

Date Code Title Description
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