JPS62180743A - Production of microcapsule encapsulating aqueous liquid - Google Patents

Production of microcapsule encapsulating aqueous liquid

Info

Publication number
JPS62180743A
JPS62180743A JP61020527A JP2052786A JPS62180743A JP S62180743 A JPS62180743 A JP S62180743A JP 61020527 A JP61020527 A JP 61020527A JP 2052786 A JP2052786 A JP 2052786A JP S62180743 A JPS62180743 A JP S62180743A
Authority
JP
Japan
Prior art keywords
org
aqueous liquid
liq
water
modified clay
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
JP61020527A
Other languages
Japanese (ja)
Other versions
JPH0468019B2 (en
Inventor
Akira Noda
章 野田
Michihiro Yamaguchi
山口 道広
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.)
Shiseido Co Ltd
Original Assignee
Shiseido 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 Shiseido Co Ltd filed Critical Shiseido Co Ltd
Priority to JP61020527A priority Critical patent/JPS62180743A/en
Publication of JPS62180743A publication Critical patent/JPS62180743A/en
Publication of JPH0468019B2 publication Critical patent/JPH0468019B2/ja
Granted 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
    • B01J13/06Making microcapsules or microballoons by phase separation
    • B01J13/14Polymerisation; cross-linking
    • B01J13/16Interfacial polymerisation

Abstract

PURPOSE:To increase the strength of the membrane of the titled microcapsule by adding an aq. liq. and an org. modified clay material as an emulsifier into an org. medium immiscible with water, emulsifying the medium, and then producing the microcapsule. CONSTITUTION:Natural and/or synthetic clay material are modified with a quaternary ammonium salt-type org. cation to prepare the org. modified clay mineral as the emulsifier for an aq. liq. The aq. liq. as the core substance and the org. modified clay mineral are added into an org. medium immiscible with water such as ethylene chloride, carbon tetrachloride, and cyclohexane to prepare a liq. emulsifier, and then the microcapsule encapsulating the aq. liq. is produced. Polycarbonate, polyurethane, etc., are appropriately used s the core substance, and the amt. of the org. modified clay mineral to be mixed is controlled to 0.1-5wt%, based on the hydrophobic medium.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は水性液体を内包するマ・イクロカプセルの装造
法に関するもので、特に水と混和しない有(幾媒体中に
水性液体を乳化分散する工程を経てマイクロカプセルを
製造する方法において、水性液体の乳化分、散剤として
有機変性粘土鉱物を使用することにより、製造工程の箭
略化を図り、工業上利用価値の高いマイクロカプセルを
得ることのできる製造法に関するものである。・ [従来の技術] 従来、水性液体を内包する球形カプセルの一般的製法と
しては、(1)界面重合法;水溶性モノマーを含む水溶
液を、油性モノマーを含む水と非混和性の有機溶剤から
なる油相中に乳化分散せしめ、水/油の界面で重合させ
カプセル化する方法、(2)In 5itu重合法:上
記(1)の方法において水溶性モノマー又は油性モノマ
ーのみを用い、これを水粒子表面上で重合させカプセル
化する方法、(3)液中乾燥法:水と非混和性の有機溶
剤と製膜物質と・からなる油相に水を乳化分ji女せし
めた後有機溶剤を除去する方法、などが知られている。
Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a method for packaging microcapsules containing an aqueous liquid, and in particular, the present invention relates to a method for manufacturing microcapsules containing an aqueous liquid. To simplify the manufacturing process and obtain microcapsules with high industrial utility value by using an organically modified clay mineral as an emulsifying component of an aqueous liquid and a powder in a method of manufacturing microcapsules through a process of This relates to a manufacturing method that allows for the production of spherical capsules containing an aqueous liquid.- [Prior Art] Conventionally, the general methods for manufacturing spherical capsules containing an aqueous liquid include (1) interfacial polymerization method; A method in which the monomer is emulsified and dispersed in an oil phase consisting of an organic solvent immiscible with water, and polymerized at the water/oil interface for encapsulation. (2) In-5-itu polymerization method: In the method (1) above, the water-soluble monomer or (3) In-liquid drying method: Emulsification of water in an oil phase consisting of an organic solvent that is immiscible with water and a film-forming substance. A method of removing an organic solvent after sex is known.

上記水性液体を内包するカプセルの上記いずれの製造法
においても、カプセル化の前段階で有機溶剤中へ水性液
体を良好に乳化分散することが必要であり、この際これ
よでは乳化分散剤としてソルビクン脂肪酸エステル、グ
リセリン脂肪酸エステル、ポリグリセリン脂肪酸エステ
ル、プロピレングリコール脂肪酸エステル、ざらにはH
L B (liが10以下の酸化エチレン付加型非イオ
ン界面活性剤等のようなW10型界面活性剤が使用され
ていた。
In any of the above manufacturing methods for capsules containing the aqueous liquid, it is necessary to emulsify and disperse the aqueous liquid well into an organic solvent in the step prior to encapsulation. Fatty acid ester, glycerin fatty acid ester, polyglycerin fatty acid ester, propylene glycol fatty acid ester, Zarani H
A W10 type surfactant such as an ethylene oxide-added nonionic surfactant with LB (li of 10 or less) was used.

[発明が解決しようとする問題点] しかし、前記界面活性剤を用いる従来のマイクロカプセ
ル製造法の(1)と(2)の方法においては、水/油界
面で重合か起こる際、しばしば水性液体の粒子か凝集、
′F1着、ざらには合一してしまい、カプセルとして個
々の形で完全に回収することが不可能であるという困難
が生じていた。また(3)の方法においては、再乳化の
工程でW10型エマルションが破壊され易く、分散した
油滴中に水が保持きれる割合は極めて低くなるという欠
点を有していた。ざらに上記(1)〜(3)のカプセル
化方法においては、膜物質中ないし膜表面に残留した界
面活性剤の除去が困難であるため洗浄時等に多大のコス
トを要し、また芯物質の溶出や膜の緻密性の低下等のカ
プセルの品質自体にも問題があった。
[Problems to be Solved by the Invention] However, in the conventional microcapsule manufacturing methods (1) and (2) using the surfactants, when polymerization occurs at the water/oil interface, the aqueous liquid often particles or agglomerates,
'F1, the particles coalesced together, making it impossible to completely collect them as individual capsules. In addition, method (3) had the disadvantage that the W10 type emulsion was easily destroyed during the re-emulsification step, and the proportion of water that could be retained in the dispersed oil droplets was extremely low. In general, in the encapsulation methods (1) to (3) above, it is difficult to remove the surfactant remaining in the membrane material or on the membrane surface, which requires a great deal of cost during cleaning, and the core material There were also problems with the quality of the capsules themselves, such as the elution of water and a decrease in the density of the membrane.

本発明者等はかかる欠点を解決すべく鋭意検討を重ねた
結果、上記従来法における界面活性剤の代わりに有機変
性粘土鉱物を乳化分散剤として用いることにより、水性
液体粒子の凝集、店着及び合一か全く見られず、形成さ
れたW10型エマルションが非常に安定で、また生成し
たカプセルの分離、洗浄が容易であり、ざらには膜強度
が極めて高いマイクロカプセルが製造できることを見出
し、本発明を完成するに至った。
The present inventors have made extensive studies to solve these drawbacks, and have found that by using an organically modified clay mineral as an emulsifying dispersant instead of the surfactant in the conventional method, the agglomeration of aqueous liquid particles, We discovered that the W10 type emulsion that was formed was extremely stable, with no coalescence observed, and that the capsules formed were easy to separate and wash, making it possible to produce microcapsules with extremely high membrane strength. The invention was completed.

[問題を解決するための手段] すなわち本発明は、水と混和しない有機媒体中に水性液
体を乳化分散する工程を経てマイクロカプセルを製造す
る方法において、水性液体の乳化分散剤として有機変性
粘土鉱物を使用することを特徴とする、水性液体を内包
するマイクロカブビルの製造法である。
[Means for Solving the Problem] That is, the present invention provides a method for producing microcapsules through a step of emulsifying and dispersing an aqueous liquid in an organic medium that is immiscible with water, using an organically modified clay mineral as an emulsifying and dispersing agent for the aqueous liquid. This is a method for producing microcabuvil containing an aqueous liquid, which is characterized by using.

次に本発明の構成について述べる。Next, the configuration of the present invention will be described.

本発明に用いる有機変性粘土鉱物は、天然及び/又は合
成の粘土鉱物を第4級アンモニウム塩型有機カチオンで
変性化せしめたものである。
The organically modified clay mineral used in the present invention is a natural and/or synthetic clay mineral modified with a quaternary ammonium salt type organic cation.

上記天然及び/又は合成の粘土鉱物は、三層構造を有す
るコロイド性含水ケイ酸アルミニウムの一種で、一般に
下記一般式 %式% で表わされる。具体的には、モンモリロナイト、ザボナ
イIJおよびヘクトライト等の天然及び/又は合成(こ
の場合、式中の(0旧基がフッ素で置換されたもの)の
モンモリロナイト′j1およびナトリウムシリシックマ
イカやナトリウム又はリチウムテニオライトの名で知ら
れる合成雲′@(市販品ではダイナモイト;トビーエ業
(株)等がある)等が例示される。
The above-mentioned natural and/or synthetic clay mineral is a type of colloidal hydrous aluminum silicate having a three-layer structure, and is generally expressed by the following general formula %. Specifically, natural and/or synthetic montmorillonite, zabonai IJ, hectorite, etc. (in this case, montmorillonite 'j1 in the formula (0 old group is substituted with fluorine), sodium silicic mica, sodium or Examples include synthetic clouds known as lithium taeniolite (commercially available products include Dynamoite; available from Tobie Gyo Co., Ltd.).

:(以下余白)、・ また、上記第4級アンモニウム塩型有機カチオンは、下
記一般式 (式中、R1は炭素数10〜22なアルキル基またはベ
ンジル基、R2はメチル基または炭素数lO〜22のア
ルキル基、R3とR4は炭素数1〜3のアルキル基また
はヒドロキシアルキル基、Xはハロゲン原子またはメチ
ルサルフェート残基を表わす。)で表わされる。
: (blank space below),・ In addition, the above-mentioned quaternary ammonium salt type organic cation has the following general formula (wherein, R1 is an alkyl group having 10 to 22 carbon atoms or a benzyl group, and R2 is a methyl group or a carbon number 10 to 10). 22 alkyl groups, R3 and R4 are alkyl groups or hydroxyalkyl groups having 1 to 3 carbon atoms, and X represents a halogen atom or a methyl sulfate residue.

本発明で水性液体の乳化分散剤として用いられる有機変
性粘土鉱物は、上記天然及び/叉は合成の粘土鉱物を上
記第4級アンモニウム塩型有機カチオンで変性したもの
であり、市販品としては、ベントン−27、ベントン−
38の商品名で米国ナショナル・リード・インダストリ
ー(National Lead T?+dustri
es)から市販されているものがある。
The organically modified clay mineral used as an emulsifying and dispersing agent for aqueous liquids in the present invention is obtained by modifying the above-mentioned natural and/or synthetic clay minerals with the above-mentioned quaternary ammonium salt type organic cation, and commercially available products include: Benton-27, Benton-
38 product names by National Lead Industry (National Lead T?+dustri)
There are commercially available products from es).

本発明の実施にあたっては、これらの有機変性粘土鉱物
のうちから1種または2種以上が任意に選択される。
In carrying out the present invention, one or more kinds of these organically modified clay minerals are arbitrarily selected.

本発明において、かかる有機変性粘土鉱物の配合量は疎
水性媒体中に0.1〜5重量%であり、更に好ましくは
0.2〜4重量%である。配合量が0.1重量%より少
ない量では、水性物質の乳化、分散が不十分となり、マ
イクロカプセルの膜強度等の品質が低下する可能性があ
る。また、5重量%を越えると、系の粘度が高すぎる等
の恐れが生じ実用には適さない。
In the present invention, the amount of organically modified clay mineral blended in the hydrophobic medium is 0.1 to 5% by weight, more preferably 0.2 to 4% by weight. If the blending amount is less than 0.1% by weight, the emulsification and dispersion of the aqueous substance will be insufficient, and the quality of the microcapsules, such as membrane strength, may deteriorate. Moreover, if it exceeds 5% by weight, the viscosity of the system may become too high, making it unsuitable for practical use.

有は変性粘土鉱物を含有きせる有機媒体としては、エチ
レンクロライド、メチレンクロライド、四塩化炭素、塩
弗素化エチレン、クロロホルム等のハ1コ□ゲン化炭化
水素やエーテル類、またはノルマルヘキサン、シクロヘ
キサン、デカン、ベンゼン、□キシレン、1−ルエン等
の炭化水素、酢酸エチル、酢酸ブチル等の酢酸エステル
を単独にまたは混合して用いろことができる。
Examples of organic media containing modified clay minerals include ethylene chloride, methylene chloride, carbon tetrachloride, chlorofluorinated ethylene, chloroform, and other hydrogenated hydrocarbons and ethers, or normal hexane, cyclohexane, and decane. , benzene, xylene, 1-luene, and acetate esters such as ethyl acetate and butyl acetate may be used alone or in combination.

本発明に係Jツる有機変性粘土鉱物を含有した上記有機
媒体と芯物質の水性液体との混合比率は、乳化、分散の
し易ざや系の安定性の点から、1:2から100:1の
範囲か適当であり、より打上しくは1:1から50=1
の範囲である。
The mixing ratio of the organic medium containing the organically modified clay mineral according to the present invention and the aqueous core liquid is from 1:2 to 100: from the viewpoint of ease of emulsification and dispersion and stability of the system. 1 range or appropriate, more preferably 1:1 to 50=1
is within the range of

本発明のマーでクロカプセルに内包きれる水性(1に体
としては、純水の他、メタノール、エタノール、イソプ
ロパツールなどの低級アルコール類やエチレングリコー
ル、プロピレングリコール、グリセリン、1,3ブヂレ
ングリコール、ソルビット、ブドウ糖などの多価アルコ
ール類からiHばれる1種又は2種以上の単独または水
との組合ゼ;塩化ナトリウム、炭酸ナトリ1クム、メタ
リン酸ナトリrクム、リン酸二水素ナトリウム、rtC
酸すトリウムなどの無機塩類、塩酸、リン酸、酢酸など
の酸、水酸化ナトリウム、水酸化カルシウム、アンモニ
ア水などの塩基、ビタミンC,Hなどのビタミンやカラ
ターゼ、ウレアーゼ、リパーゼなどの酵素等の水溶性薬
効成分に代表される水に可溶性の物質の水溶液;油分、
香料及びビタミンA、B2、D、E等の脂溶性物質の0
 ’/ W ’m乳化物や懸濁液などが挙げられるが、
特□に限定されるものではなく、種々の目的に応じて選
択□ざJする。当然のことながら上記成分は目的に応じ
て適当に組合せて用いら□れても□よい。
The aqueous substances that can be encapsulated in macrocapsules using the mer of the present invention include pure water, lower alcohols such as methanol, ethanol, and isopropanol, ethylene glycol, propylene glycol, glycerin, and 1,3-butylene. One or more types of iH derived from polyhydric alcohols such as glycol, sorbitol, and glucose, alone or in combination with water; sodium chloride, 1 cum sodium carbonate, sodium cum phosphate, sodium dihydrogen phosphate, rtC
Inorganic salts such as thorium acid, acids such as hydrochloric acid, phosphoric acid, and acetic acid, bases such as sodium hydroxide, calcium hydroxide, and aqueous ammonia, vitamins such as vitamins C and H, and enzymes such as calatase, urease, and lipase. Aqueous solutions of water-soluble substances such as water-soluble medicinal ingredients; oils,
0 of fat-soluble substances such as fragrances and vitamins A, B2, D, and E
' / W 'm emulsions and suspensions, etc.
It is not limited to any particular □, and can be selected according to various purposes. Naturally, the above components may be used in appropriate combinations depending on the purpose.

本発明のマー1″□クロカプセル中の前記水性液体の内
包量は、カプセル全体に対して10〜95重量%であり
、更(ご好まルくは40〜95重景%である。内包量が
10重■%より少ないとカプセルを化粧料等の中に配置
台した場合水性液体の量カー少ないため、内容物の□持
□つ有用性を十分発揮す杷ことが困難になり、一方、9
5′!″量%を越えるとカプセル皮膜の強度が著しく低
下し、弱い外力により容易にカプセル破壊′#τ生じる
可能性らあることから実用には適さない。   □ 本発明のマイクロカプセルの壁膜となる物質としては、
前記免面重合法、In 5itu重合法、液中乾燥法に
使用できるものならば良く、例えば、ポリカニボネート
、ポリスルボネート、ポリエステル、ポリウレタン、ポ
リアミド、ポリイソシアネート、ポリ原素等の縮合系1
合体、オレフィン、メチレンJ酢酸ビニル、塩化ビニル
、塩化ビニリデン、ビ□ニルエステル、ビ丑ルエーテル
、アクリル酸エステル、メタクリル酸エステル等やアク
リロニトリル、メタアクリロニトリルおよびこれらの誘
導体等、更に天然ゴム、塩花ゴム、ヒルロース誘導体等
□の天然高分□子又はその加工物などが上げられる。 
  □ 本発明のマイクロカプセルの粒子径は、凡そ2μm〜4
mmのものが好ましい。カプセル粒子径が2μmより小
ざいと、マイクロカプセル自体は形成し得るが内包量が
少なくなるため、使用時に内包物本来の有□用性が十誉
発揮できないことになり、士な4mmより大きいとマイ
ク旧カプセル膜の形成が困難になったり、形成きれたと
しても非常に微弱なものとなる恐れが大きい。
The amount of the aqueous liquid contained in the capsule of the present invention is 10 to 95% by weight, preferably 40 to 95% by weight, based on the entire capsule. If the amount is less than 10% by weight, when the capsule is placed in a cosmetic product, the amount of aqueous liquid will be small, making it difficult to retain the contents and fully utilize the usefulness. 9
5′! If the amount exceeds 1%, the strength of the capsule film will decrease significantly and the capsule may easily break due to weak external force, so it is not suitable for practical use. □ Substance that forms the wall of the microcapsule of the present invention as,
Any material can be used as long as it can be used in the above-mentioned surface polymerization method, in-5itu polymerization method, and submerged drying method, such as condensation systems 1 such as polycanibonate, polysulfonate, polyester, polyurethane, polyamide, polyisocyanate, polyelement, etc.
Coalescence, olefin, methylene J vinyl acetate, vinyl chloride, vinylidene chloride, vinyl ester, vinyl ether, acrylic ester, methacrylic ester, etc., acrylonitrile, methacrylonitrile and derivatives thereof, etc., as well as natural rubber, salt flower rubber, Examples include natural polymers such as hillulose derivatives, and processed products thereof.
□ The particle size of the microcapsules of the present invention is approximately 2 μm to 4 μm.
mm is preferable. If the capsule particle size is smaller than 2 μm, the microcapsule itself can be formed, but the amount of encapsulation will be small, and the inherent usefulness of the encapsulated material will not be fully demonstrated during use. There is a great possibility that it will be difficult to form the old microphone capsule membrane, or that even if it is formed, it will be extremely weak.

[発明の効果]     ′ 本発明の製造□法に紅いては、□乳化分散剤として機能
する有機変性粘土鉱物が粉末であることから、水性液体
粒子あ集合、量着及び合一が全く見られず、また生成し
たカプセルの分離、洗;)が極めて容易であり□、ざら
に緻蕾な壁膜を形成することから熱的にも機械的にも安
定性が高いという利点を有しており、一般のマイクロカ
プセルの製造法として工業上有用性の高いものである。
[Effects of the invention] ′ In the manufacturing method of the present invention, since the organically modified clay mineral that functions as an emulsifying and dispersing agent is in the form of powder, aggregation, deposition, and coalescence of aqueous liquid particles are not observed at all. It also has the advantage of being extremely easy to separate and wash the capsules produced, and that it is highly stable both thermally and mechanically as it forms a rough and dense wall film. This method is highly useful industrially as a general method for producing microcapsules.

特に、液状及びゼリー状の化粧vIとして利用する場合
に、同−剤型内でも芯物質である水性液体の種類を替え
ることにより、様々な感触を付与するマイクロカプセル
を製造でざる点で極めて有益である。
In particular, when used as a liquid or jelly cosmetic VI, it is extremely useful in that microcapsules with various textures can be produced by changing the type of aqueous liquid that is the core substance even within the same dosage form. It is.

[実施例コ 以下に実施例を挙げて本発明を更に具体的に説明するが
、本発明はこれらに限定されるものではない。
[Example] The present invention will be explained in more detail with reference to Examples below, but the present invention is not limited thereto.

実施例1 ジエチレントリアミン30gと炭酸ナトリウム40gを
溶かした水溶液300m1に等hfの水を加えた後、ベ
ントン−38をW10型分11文剤として30g含有し
たクロロホルム−シクロヘキサン混合溶液(体積比で1
 : 3 ) 3000mlに加え、スリーワンモータ
ーで撹拌し1.W2O型の乳化分散物を作った。撹拌力
は分散滴のサイズが0.5〜1mmの大さ・ざになるよ
うに加減し、温度は常に室温で行った。続いて、撹拌を
止めずに上記乳化分散物に、30gのテレフタル酸クロ
リドを溶かしたクロロホルムーシクロノ\キサン混合i
ff ?fりを加えた。この結果、分4B2水滴表面で
テレフタル酸クロリドとジエチレントリアミン間に重縮
合が起こり、ポリジエチレンフタルアミド膜が生成して
水滴がカブビル化された。
Example 1 After adding equal hf of water to 300 ml of an aqueous solution in which 30 g of diethylenetriamine and 40 g of sodium carbonate were dissolved, a chloroform-cyclohexane mixed solution containing 30 g of Bentone-38 as a W10 type part 11 agent (volume ratio: 1
: 3) Add to 3000ml and stir with a three-one motor. A W2O type emulsified dispersion was prepared. The stirring power was adjusted so that the size of the dispersed droplets was 0.5 to 1 mm, and the temperature was always kept at room temperature. Subsequently, without stopping stirring, chloroform-cyclono\xane mixture i in which 30 g of terephthalic acid chloride was dissolved was added to the above emulsified dispersion.
ff? Added f. As a result, polycondensation occurred between terephthalic acid chloride and diethylenetriamine on the surface of the 4B2 water droplet, a polydiethylene phthalamide film was formed, and the water droplet was turned into a cabbage.

このようにして得られたカプセルを遠心分i;f!ff
i IjMで濾過と洗浄を数回性ない、ポリオキシエチ
レンラウリルエーテル(20E O)により水中に移行
しカプセル分散水溶液を得た。
The capsules thus obtained were centrifuged i;f! ff
i Filtered and washed several times with IjM and transferred to water with polyoxyethylene lauryl ether (20E 2 O) to obtain an aqueous capsule dispersion solution.

比較例I W10型分散剤にポリオキシエチレンオレイルエーテル
(2EO)を使用した以外は実施例1と同様の方法でカ
プセルの調製を行ったところ、W10型分散物にテレフ
タル酸クロリド溶液を添加した瞬間に分散水滴が合一し
、単一カプセルとしての回収が不可能であった。
Comparative Example I Capsules were prepared in the same manner as in Example 1 except that polyoxyethylene oleyl ether (2EO) was used as the W10 dispersion. The dispersed water droplets coalesced, making it impossible to collect them as a single capsule.

実施例2 モンモリロナイトと塩化ジステアリルジメチルアンモニ
ウムとの反応により生成した有機変性粘度鉱物の0.5
gとエピコート828のLogを含んだキシレン100
mp’pに、10gテトラエチレンペンタアミン及び0
.1gビタミンCを溶かした水溶液40m1を添加し、
ホモミキサーにより5000rpmで10分間乳化して
W10型エマルションを得た。次いで液温を30℃に調
整してスリーワンモーターの800rpmで30分間撹
拌し、ざらに60℃で6時間撹拌して重合反応を終了さ
せた後、生成したカプセルの洗浄を行った。この結果、
ビタミンC水溶液を内包する平均粒径25μm、のエポ
キシ樹脂カプセルを得た。
Example 2 0.5 of an organically modified clay mineral produced by the reaction of montmorillonite and distearyldimethylammonium chloride
xylene 100 containing the Log of g and Epicote 828
mp'p, 10 g tetraethylenepentamine and 0
.. Add 40ml of an aqueous solution containing 1g of vitamin C,
The mixture was emulsified using a homomixer at 5000 rpm for 10 minutes to obtain a W10 type emulsion. Next, the liquid temperature was adjusted to 30° C., and the mixture was stirred for 30 minutes at 800 rpm using a three-one motor, and roughly stirred at 60° C. for 6 hours to complete the polymerization reaction, and then the produced capsules were washed. As a result,
Epoxy resin capsules containing an aqueous vitamin C solution and having an average particle size of 25 μm were obtained.

実施例3、比較例2 4gのポリスチレンと1gのベントン−27を含有した
40m1のメチレンクロライド中に、1gのグルコース
を含む12m1の水溶液をホモミキサーにより5000
rpmで10分間乳化してW2O型の第一次エマルショ
ンを得た。次にこの第一次エマルシコンをポリオギシエ
ヂレンソルビタンモノラウレ−!・(201EC))の
0.2%水溶ifR300ml中に添加し、スリーワン
モーターの500rpmで5分間乳化した。続いて弱い
撹拌を行ないながら系の温度を40℃に上昇し、2時間
その温度に維持してメヂレンクロライドを蒸発除去した
後、濾過して白色物質を得、た(実施例3)。また、上
記の実施例におけるベントン−27に代えてソルビタン
モノオレー1・を用い、同様の方法で調製して白色物質
を得た(比較例2)。
Example 3, Comparative Example 2 12 ml of an aqueous solution containing 1 g of glucose was added to 40 ml of methylene chloride containing 4 g of polystyrene and 1 g of bentone-27 using a homomixer for 5,000 g.
The mixture was emulsified at rpm for 10 minutes to obtain a W2O type primary emulsion. Next, use this primary emulsion as polyoxyethylene sorbitan monolaure! (201EC)) was added to 300 ml of 0.2% aqueous ifR, and emulsified for 5 minutes at 500 rpm using a three-one motor. Subsequently, the temperature of the system was raised to 40° C. with weak stirring and maintained at that temperature for 2 hours to evaporate and remove methylene chloride, followed by filtration to obtain a white substance (Example 3). Further, a white material was obtained by using sorbitan monoole 1 in place of bentone-27 in the above example and preparing in the same manner (Comparative Example 2).

各々の生成物を光学顕微鏡下で観察したところ、いずれ
も粒径が60〜100μmの球状粒子が観察された。一
方、各々の生成物を濾過した際の濾液中に含まれるグル
コース量をアントロン−硫酸法により定量し、その結果
からカプセル化されたグルコースの割合(=カプセル化
されたグルコースffi/配合した全グルコース営)を
3回の繰返し実験を行ない調べたところ、実施例3では
いずれも95%以上であるのに対し、比較例2では70
%程度であり、ベントン−27を使用することで内包量
を非常に高くすることかで苧た。比較例2でグルコース
のカプセル化比率が低いのは、再乳化の際W10型エマ
ルションが破壊し、中空のポリスチレン球やポリスチレ
ンだけの球になるためであリ、これは光学顕微鏡下で球
状粒子をガラス板で挾み押しつぶした際、内包水溶液の
届出が見られなかったことから確認すれた。
When each product was observed under an optical microscope, spherical particles with a particle size of 60 to 100 μm were observed. On the other hand, the amount of glucose contained in the filtrate when each product was filtered was determined by the anthrone-sulfuric acid method, and from the results, the ratio of encapsulated glucose (= encapsulated glucose ffi/total glucose blended) was determined. As a result of repeating the experiment three times, it was found that in Example 3, the percentage was 95% or more, whereas in Comparative Example 2, the percentage was 70% or more.
%, and by using Bentone-27, it was possible to increase the amount of encapsulation to a very high level. The reason why the glucose encapsulation ratio in Comparative Example 2 is low is that the W10 type emulsion is destroyed during re-emulsification, resulting in hollow polystyrene spheres or spheres made only of polystyrene. This was confirmed because no report of the encapsulated aqueous solution was found when the sample was crushed between glass plates.

実施例4 10gのエチルセルロースと0.5gのベントン−38
を含有したベンゼン100m1中に、0.1gのカタラ
ーゼを含有する水溶液20m1をホモミキサーにより 
3000rpmで15分間乳化してW2O型の第一次エ
マルションを得た。次にこの第一次エマルションを、p
116.60℃の1%ゼラヂン水溶液800 ml巾に
添加し、スリーワンモーターの500rpmで5分間乳
化し、続いて弱い撹拌を行ないながら系の温度を80℃
に上昇し、3時間その温度に維持してベンゼンを蒸発除
去してマイクロカプセルを形成させた。次いで、濾過に
よりマイクロカプセルを単離し、水洗して、カタラーゼ
水溶液を含有する平均粒径】50μmのマイクロカプセ
ルを得た。
Example 4 10g ethylcellulose and 0.5g bentone-38
Using a homomixer, 20 ml of an aqueous solution containing 0.1 g of catalase was added to 100 ml of benzene containing
Emulsification was performed at 3000 rpm for 15 minutes to obtain a W2O type primary emulsion. Next, this primary emulsion was
116. Add to 800 ml of 1% aqueous geladine solution at 60°C, emulsify for 5 minutes at 500 rpm using a three-one motor, and then raise the temperature of the system to 80°C with gentle stirring.
and maintained at that temperature for 3 hours to evaporate the benzene and form microcapsules. Next, the microcapsules were isolated by filtration and washed with water to obtain microcapsules containing an aqueous catalase solution with an average particle size of 50 μm.

Claims (1)

【特許請求の範囲】[Claims] 水と混和しない有機媒体中に水性液体を乳化分散する工
程を経てマイクロカプセルを製造する方法において、水
性液体の乳化分散剤として有機変性粘土鉱物を使用する
ことを特徴とする、水性液体を内包するマイクロカプセ
ルの製造法。
A method for manufacturing microcapsules through a step of emulsifying and dispersing an aqueous liquid in an organic medium that is immiscible with water, characterized in that an organically modified clay mineral is used as an emulsifying and dispersing agent for the aqueous liquid, and the aqueous liquid is encapsulated therein. Method for manufacturing microcapsules.
JP61020527A 1986-02-01 1986-02-01 Production of microcapsule encapsulating aqueous liquid Granted JPS62180743A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61020527A JPS62180743A (en) 1986-02-01 1986-02-01 Production of microcapsule encapsulating aqueous liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61020527A JPS62180743A (en) 1986-02-01 1986-02-01 Production of microcapsule encapsulating aqueous liquid

Publications (2)

Publication Number Publication Date
JPS62180743A true JPS62180743A (en) 1987-08-08
JPH0468019B2 JPH0468019B2 (en) 1992-10-30

Family

ID=12029627

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61020527A Granted JPS62180743A (en) 1986-02-01 1986-02-01 Production of microcapsule encapsulating aqueous liquid

Country Status (1)

Country Link
JP (1) JPS62180743A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004538354A (en) * 2001-08-15 2004-12-24 ビーエーエスエフ アクチェンゲゼルシャフト Microcapsule dispersion
FR2930434A1 (en) * 2008-04-25 2009-10-30 Courtage Et De Diffusion Codif Use of organophilic clay as a dispersant in the preparation of self-gelling mask compositions for cosmetic purposes

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004538354A (en) * 2001-08-15 2004-12-24 ビーエーエスエフ アクチェンゲゼルシャフト Microcapsule dispersion
FR2930434A1 (en) * 2008-04-25 2009-10-30 Courtage Et De Diffusion Codif Use of organophilic clay as a dispersant in the preparation of self-gelling mask compositions for cosmetic purposes

Also Published As

Publication number Publication date
JPH0468019B2 (en) 1992-10-30

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