JPH0367737B2 - - Google Patents
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- Publication number
- JPH0367737B2 JPH0367737B2 JP57155539A JP15553982A JPH0367737B2 JP H0367737 B2 JPH0367737 B2 JP H0367737B2 JP 57155539 A JP57155539 A JP 57155539A JP 15553982 A JP15553982 A JP 15553982A JP H0367737 B2 JPH0367737 B2 JP H0367737B2
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- JP
- Japan
- Prior art keywords
- powder
- core material
- core
- microcapsules
- substance
- 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 - Lifetime
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Formation And Processing Of Food Products (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Grain Derivatives (AREA)
- Dispersion Chemistry (AREA)
- Adhesive Tapes (AREA)
- Paints Or Removers (AREA)
- Inks, Pencil-Leads, Or Crayons (AREA)
- Color Printing (AREA)
- Dairy Products (AREA)
- General Preparation And Processing Of Foods (AREA)
- Jellies, Jams, And Syrups (AREA)
- Manufacturing Of Micro-Capsules (AREA)
Description
【発明の詳細な説明】
この発明は、特に常温付近で液体または粘着性
を有する物質または軟質物質をマイクロカプセル
化する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention particularly relates to a method for microencapsulating a substance or a soft substance that is liquid or sticky at room temperature.
マイクロカプセルは感圧複写紙をはじめ、医
療、農薬、香料などに広く利用されている。 Microcapsules are widely used in pressure-sensitive copying paper, medicine, agricultural chemicals, fragrances, and other applications.
従来の代表的なマイクロカプセルの製造法とし
ては、1、コアセルベーシヨン法、2、界面重合
法、3、in situ重合法、4、液中乾燥法、5、
融解分散冷却法、6、オリフイス法、7、スプレ
ードライング法、8、気中懸濁被覆法、9、無機
質壁マイクロカプセル化法などがある。ところが
このような製造法を用いて、水、有機溶剤、水あ
め、糊粘着剤、接着剤などの常温では液体または
粘着性を有する物質もしくは軟質物質をマイクロ
カプセル化する場合には次のような欠点がある。
すなわち、1〜5の方法では分散媒中に上記物質
よりなる芯物質を分散させる際、芯物質が粘着性
を有する場合には芯物質粒子が付着しあつて集塊
化する。また、芯物質と高分子溶液とのぬれおよ
び比重の調整が必要となり、作業が面倒でしかも
仕上つたカプセルの特性もよくない。また、6の
方法はミクロンオーダーのカプセルを作りにく
く、生産効率も低い。さらに、5、7、8の方法
はトナーのカプセル化に使用されているが均一な
膜厚、完全被覆のカプセルを作りにくいうえにト
ナーより粘着性の強い物質の場合には集塊化を招
く。また、1〜8の方法は水や有機溶剤を使用す
るので、水や有機溶剤に浸されたり、反応する芯
物質をカプセル化することができないうえ、有機
溶剤の後処理が面倒であり、カプセルを粉体とし
て取り出すためには乾燥が必要であり、火災、爆
発の危険性がある。さらに、9の方法は芯物質は
軟質物質の場合は芯物質内部に多量の壁物質が混
入し、カプセルというよりはむしろ混合物になり
やすい。 Typical conventional methods for producing microcapsules include: 1. Coacervation method, 2. Interfacial polymerization method, 3. In situ polymerization method, 4. In-liquid drying method, 5.
Examples include the melting and dispersion cooling method, 6. the orifice method, 7. the spray drying method, 8. the air suspension coating method, and 9. the inorganic wall microencapsulation method. However, when using this production method to microcapsule substances that are liquid or sticky at room temperature, such as water, organic solvents, starch syrup, adhesives, adhesives, or soft substances, there are the following drawbacks: There is.
That is, in methods 1 to 5, when a core material made of the above-mentioned material is dispersed in a dispersion medium, if the core material has adhesive properties, the core material particles adhere to each other and form agglomerates. In addition, it is necessary to adjust the wetting of the core material and the polymer solution and the specific gravity, which makes the work laborious and the properties of the finished capsules are also poor. Furthermore, method 6 is difficult to produce micron-order capsules and has low production efficiency. Furthermore, although methods 5, 7, and 8 are used to encapsulate toner, it is difficult to produce capsules with a uniform film thickness and complete coverage, and they also lead to agglomeration if the substance is more adhesive than the toner. . In addition, since methods 1 to 8 use water or organic solvents, it is not possible to encapsulate the core substance that is immersed or reacts in water or organic solvents, and post-treatment of the organic solvent is troublesome. Drying is required to extract it as a powder, which poses the risk of fire and explosion. Furthermore, in method 9, when the core material is a soft material, a large amount of wall material is mixed into the core material, which tends to result in a mixture rather than a capsule.
このように1〜9の従来のマイクロカプセル化
方法では、いずれの場合も粉状とした場合、常温
では液体になるか集塊化する物質を満足のゆく状
態でマイクロカプセルを製造することができなか
つた。 As described above, in any of the conventional microencapsulation methods 1 to 9, microcapsules cannot be manufactured in a satisfactory state from substances that become liquid or agglomerate at room temperature when powdered. Nakatsuta.
この発明は、上記事情に鑑みてなされたもの
で、常温で液体または粘着性を有する物質もしく
は軟質物質あるいは水や有機溶剤に浸されるかこ
れと反応する物質等を簡単に高収率で、かつ安全
にマイクロカプセル化できしかも上記物質の変
質、変性が生じることがないマイクロカプセルの
製造法を提供することを目的とするものである。 This invention was made in view of the above circumstances, and it is possible to easily and efficiently prepare substances that are liquid or sticky at room temperature, or soft substances, or substances that are immersed in or react with water or organic solvents, in a high yield. Another object of the present invention is to provide a method for producing microcapsules that can be safely microencapsulated without causing any alteration or denaturation of the above-mentioned substances.
以下、この発明を詳しく説明する。 This invention will be explained in detail below.
この発明の製造法に用いられる芯物質として
は、水溶液、水分散液、粘着剤、接着剤、塗料、
有機溶剤などの、粉状とした場合に常温付近(0
℃〜50℃)では液体となるかあるいは集塊化を起
し、粉状を維持できない物質が用いられる。 Core substances used in the production method of this invention include aqueous solutions, aqueous dispersions, pressure-sensitive adhesives, adhesives, paints,
Organic solvents, etc., when made into powder, are kept at room temperature (0
The material used is a substance that becomes liquid or agglomerates at temperatures between 50°C and 50°C, and cannot maintain its powder form.
また、この芯物質を被覆する微粉としては、シ
リカ微粉、各種ベントナイト、酸化アルミニウ
ム、カーボンブラツク、炭酸カルシウム、タル
ク、カオリン、炭酸マグネシウム、酸化チタン、
酸化亜鉛、アルミニウム粉末、セラミツク微粉、
ポリエチレン、ナイロン、メタアクリレートなど
のプラスチツク微粉、フイチン酸およびその金属
塩、でん粉ならびにこれら微粉を表面改質した微
粉が挙げられるが、芯物質との親和性の無いもの
が選択される。特に芯物質が100センチポイズ程
度の粘度を有する液体の場合には、絶対にこれと
親和性のある微粉は避けなければならない。すな
わち、芯物質が親水性であれば疎水性微粉を、芯
物質が疎水性である場合には親水性微粉を選択す
る必要がある。また、芯物質を凍結粉砕して得ら
れる粉末の粒径よりも小さい粒径、好ましくは
1/10以下の粒径の微粉が用いられる。 In addition, the fine powder that coats this core substance includes fine silica powder, various bentonites, aluminum oxide, carbon black, calcium carbonate, talc, kaolin, magnesium carbonate, titanium oxide,
Zinc oxide, aluminum powder, ceramic fine powder,
Examples include plastic fine powders such as polyethylene, nylon, and methacrylate, phytic acid and its metal salts, starch, and surface-modified fine powders of these fine powders, but those having no affinity with the core substance are selected. Particularly when the core substance is a liquid with a viscosity of about 100 centipoise, fine powders that have an affinity for it must be avoided. That is, if the core substance is hydrophilic, it is necessary to select a hydrophobic fine powder, and if the core substance is hydrophobic, it is necessary to select a hydrophilic fine powder. Further, a fine powder having a particle size smaller than the particle size of the powder obtained by freeze-pulverizing the core material, preferably 1/10 or less is used.
つぎにマイクロカプセル化について説明する。
まず、芯物質を液体窒素などの冷熱を利用して凍
結し、この状態で粉末化する。この時の温度は、
芯物質の種類によつて異り、水溶液、水分散液な
どでは−20℃程度であり、粘着剤、接着剤などの
ように粘着性あるいは易集塊性のものでは−50〜
−80℃程度である。そして、粉砕機の回転数(粉
砕速度)や粉砕温度を適宜調節して平均粒径1〜
100μmの粉末とする。 Next, microencapsulation will be explained.
First, the core material is frozen using cold heat such as liquid nitrogen, and in this state is turned into powder. The temperature at this time is
The temperature varies depending on the type of core material; for aqueous solutions and dispersions, the temperature is around -20°C, and for sticky or easily agglomerated materials such as adhesives and adhesives, the temperature is -50°C or more.
The temperature is around -80℃. Then, by adjusting the rotation speed (grinding speed) and grinding temperature of the grinder as appropriate, the average particle size is 1 to 1.
Make a powder of 100μm.
ついで、この粉末を低温度に保つて集塊化ある
いは融解を起さないように維持しつつ、上記微粉
を加えて混合撹拌してマイクロカプセル化する。
この混合撹拌には、液化窒素冷却ジヤケツトを装
備したカツター付高速撹拌機を用いることが好ま
しく、撹拌条件は撹拌速度5000〜2000rpm、撹拌
時間5〜60秒である。特に、このタイプの撹拌機
を用いた場合上記凍結粉砕もこの装置内で行え、
工程上有利となる。その他、混合撹拌にはボール
ミル、カツター付撹拌機、アトライターなども用
いることができる。撹拌時の温度は上記凍結粉砕
時の温度と同程度であり、摩擦熱による温度上昇
を防止するために、撹拌機には液化窒素等の冷却
剤を通じ冷却を行いつづける必要がある。また、
芯物質の粉末と微粉との混合比は、芯物質の粉末
の形状によつても左右され、粉末が球状の場合に
は微粉は少量で済むが通常は芯物質の粉末100重
量部に対して微粉0.5〜20重量部とされる。さら
に、得られるマイクロカプセルの粒径は芯物質の
粉末の粒径と微粉による膜厚によつて決められる
ため、凍結粉砕の条件、芯物質と微粉との混合量
比、混合撹拌の条件によつて任意に調節でき、平
均粒径1〜1500μmのマイクロカプセルが良好に
得られる。 Next, while maintaining this powder at a low temperature to prevent agglomeration or melting, the fine powder is added and mixed and stirred to form microcapsules.
For this mixing and stirring, it is preferable to use a high-speed stirrer with a cutter equipped with a liquefied nitrogen cooling jacket, and the stirring conditions are a stirring speed of 5000 to 2000 rpm and a stirring time of 5 to 60 seconds. In particular, when this type of stirrer is used, the above-mentioned freeze-pulverization can also be performed within this device.
It is advantageous in terms of process. In addition, a ball mill, a stirrer with a cutter, an attritor, etc. can also be used for mixing and stirring. The temperature during stirring is about the same as the temperature during the above-mentioned freezing and pulverization, and in order to prevent temperature rise due to frictional heat, it is necessary to continue cooling the stirrer by passing a coolant such as liquefied nitrogen. Also,
The mixing ratio of core material powder and fine powder also depends on the shape of the core material powder.If the powder is spherical, a small amount of fine powder is required, but usually it is mixed per 100 parts by weight of core material powder. The fine powder is 0.5 to 20 parts by weight. Furthermore, the particle size of the resulting microcapsules is determined by the particle size of the core material powder and the film thickness of the fine powder, so it also depends on the freeze-grinding conditions, the mixing ratio of the core material and the fine powder, and the mixing and stirring conditions. The particle size can be adjusted as desired, and microcapsules with an average particle size of 1 to 1,500 μm can be obtained satisfactorily.
このようにして得られたマイクロカプセルは、
芯物質の粉末が微粉で完全に被覆され常温になつ
てもサラサラした流動性の良い粉末となる。 The microcapsules obtained in this way are
The core material powder is completely covered with fine powder, resulting in a smooth and fluid powder even at room temperature.
また、得られるマイクロカプセルの芯物質の密
閉効果およびカプセルの強度を高めたい場合に
は、このようにして得られたマイクロカプセルを
さらに、ポリマーフイルムで被覆してもよい。す
なわち、芯物質の粉末を比較的少量の微粉で被覆
したのち、従来のマイクロカプセル化法によつて
ポリマーフイルムを被覆する。この場合、カプセ
ルとポリマーフイルムおよびポリマーフイルム溶
液との親和性を考慮に入れておく必要がある。親
水性微粉で被覆されたマイクロカプセルに対して
は水溶性ポリマーによるマイクロカプセル化が適
し、具体的にはゼラチンによるコアセルベーシヨ
ン法などが利用できる。また、疎水性微粉で被覆
されたマイクロカプセルに対しては有機溶媒液か
らのコアセルベーシヨン法等の疎水性高分子によ
るマイクロカプセル化法が適している。 Furthermore, if it is desired to enhance the sealing effect of the core material of the microcapsules obtained and the strength of the capsules, the microcapsules thus obtained may be further coated with a polymer film. That is, the core material powder is coated with a relatively small amount of fine powder, and then a polymer film is coated by a conventional microencapsulation method. In this case, it is necessary to take into account the compatibility of the capsule with the polymer film and the polymer film solution. For microcapsules coated with hydrophilic fine powder, microencapsulation using a water-soluble polymer is suitable, and specifically, a coacervation method using gelatin can be used. Furthermore, for microcapsules coated with hydrophobic fine powder, a microencapsulation method using a hydrophobic polymer such as a coacervation method using an organic solvent solution is suitable.
なお、芯物質はその粘度が高い程マイクロカプ
セルの形状保持力がすぐれて安定性がよいので、
低粘度の芯物質の場合にはこれに充填剤、増粘
剤、ゲル化剤などを加えて増粘もしくはゲル化さ
せておくことが好ましい。 In addition, the higher the viscosity of the core substance, the better the ability to maintain the shape of the microcapsules and the better the stability.
In the case of a low-viscosity core material, it is preferable to add a filler, thickener, gelling agent, etc. to the core material to thicken or gel it.
このようなマイクロカプセルの製造法によれ
ば、芯物質を凍結粉砕して粉末化し、これに微粉
を加えて低温度下で混合撹拌するものであるの
で、芯物質への微粉の混入が少なく、そのために
極めて少量の微粉で芯物質を効率よく被覆し得
て、微粉によつてマイクロカプセル芯物質の性能
の低下を最小限にとどめる。又、製造途中で芯物
質および微粉のロスが全くなく、収率100%でマ
イクロカプセル化でき、工程が簡単で短時間で製
造でき、製造装置も撹拌機のみでよくしたがつて
製造コストが著るしく低いものとなる。また、す
べての工程が低温下で行われるので、芯物質およ
び微粉の変性変質がなく不安定な芯物質をもマイ
クロカプセル化できる。さらに、水や有機溶剤を
使用する従来法に比べて乾燥工程や排液処理が不
要となり、かつ作業の安定性も高い。マイクロカ
プセルの粒径の調整が任意にかつ容易に行えるの
で、目的に応じた粒度のマイクロカプセルを簡単
に用意できる。 According to this method of manufacturing microcapsules, the core material is freeze-pulverized and powdered, and fine powder is added to this and mixed and stirred at low temperature, so that there is less fine powder mixed into the core material. Therefore, the core material can be efficiently coated with a very small amount of fine powder, and the deterioration of the performance of the microcapsule core material due to the fine powder can be kept to a minimum. In addition, there is no loss of core material or fine powder during production, and microcapsules can be produced with a 100% yield.The process is simple and can be produced in a short time, and the production equipment requires only a stirrer, so the production cost is significant. It becomes very low. Furthermore, since all steps are carried out at low temperatures, there is no denaturation or alteration of the core material or fine powder, and even unstable core materials can be microencapsulated. Furthermore, compared to conventional methods that use water or organic solvents, there is no need for a drying process or wastewater treatment, and the process is highly stable. Since the particle size of the microcapsules can be arbitrarily and easily adjusted, microcapsules with a particle size suitable for the purpose can be easily prepared.
以下、実施例を示して具体的に説明する。 Hereinafter, a specific explanation will be given by showing examples.
実施例 1
メチレンブルーで着色した水を冷却固化したの
ち、カツター付撹拌機によつて粉砕し、平均粒径
50μmの凍結粉末とし、この粉末100重量部を、
溶解することのない低温である−20℃に保持しつ
つ、疎水性シリカ微粉(日本アエロジル(株)製商品
名アエロジルR972、平均粒径16mμ)5重量部
とともにカツター付高速撹拌機内で混合撹拌し
た。撹拌速度20000rpmで10秒間撹拌したところ、
着色水粉末の表面が疎水性シリカ微粉で被覆され
たマイクロカプセルが得られた。なお、混合撹拌
終了後の温度は−10℃であつた。このマイクロカ
プセルは常温においても流動性にすぐれ、サラサ
ラの状態であつた。また、このマイクロカプセル
を紙の上に散布し、加圧したところマイクロカプ
セルから、青色の水が放出され、紙が青く染色さ
れた。Example 1 After cooling and solidifying water colored with methylene blue, it was pulverized with a stirrer equipped with a cutter, and the average particle size was
50μm frozen powder, 100 parts by weight of this powder,
The mixture was mixed and stirred with 5 parts by weight of hydrophobic silica fine powder (trade name Aerosil R972, average particle size 16 mm, manufactured by Nippon Aerosil Co., Ltd.) in a high-speed stirrer equipped with a cutter while maintaining the temperature at -20°C, which is a low temperature at which it will not dissolve. . When stirred for 10 seconds at a stirring speed of 20,000 rpm,
Microcapsules were obtained in which the surface of colored water powder was coated with hydrophobic silica fine powder. The temperature after the mixing and stirring was -10°C. This microcapsule had excellent fluidity and remained smooth even at room temperature. When the microcapsules were spread on paper and pressurized, blue water was released from the microcapsules, staining the paper blue.
実施例 2
市販のでん粉糊(商品名ヤマト糊)を芯物質と
して、実施例1と全く同様にしてマイクロカプセ
ルを製造したところ、常温においても流動性に優
れ、サラサラの粉末が得られた。このマイクロカ
プセル粉末を紙上に散布したのち、別の紙をあて
加圧し乾燥したところ、二枚の紙はよく接着し
た。Example 2 Microcapsules were produced in exactly the same manner as in Example 1 using commercially available starch paste (trade name Yamato paste) as the core material, and a smooth powder with excellent fluidity even at room temperature was obtained. After scattering this microcapsule powder onto a piece of paper, another piece of paper was applied to it and dried under pressure, and the two pieces of paper adhered well.
実施例 3
バターを液化窒素で−60℃に冷却凍結し、カツ
ター付撹拌機で粉砕して平均粒径50μmの凍結粉
末とした。この粉末100重量部を、集塊化するこ
とのない温度である−50℃に保持しつつ、シリカ
微粉(商品名アエロジル200、平均粒径16mμ)
5重量部とともにカツター付撹拌機にて撹拌速度
20000rpmで10秒間混合撹拌したところ、バター
のシリカ微粉カプセルを収率100%で得た。この
ものは常温においてもサラサラで流動性の良い粉
末であつた。Example 3 Butter was cooled and frozen at −60° C. with liquid nitrogen, and ground into frozen powder with an average particle size of 50 μm using a stirrer equipped with a cutter. Fine silica powder (trade name Aerosil 200, average particle size 16 mμ) was added to 100 parts by weight of this powder while maintaining it at -50°C, a temperature that does not cause agglomeration.
Stir with 5 parts by weight using a stirrer with a cutter at a stirring speed.
When mixed and stirred at 20,000 rpm for 10 seconds, butter silica fine powder capsules were obtained with a yield of 100%. This powder was smooth and had good fluidity even at room temperature.
実施例 4
アクリレート系粘着剤(綜研化学(株)製、商品名
SKダイン1504)を充分な粘着力が生じるまで、
架橋および脱溶剤した。このものを液化窒素で凍
結したのちカツター付撹拌機によつて平均50μm
の粉末とした。この粉末100重量部を、集塊化す
ることのない温度である−60℃に保持しつつ、シ
リカ微粉(商品名アエロジル200)10重量部とと
もにカツター付撹拌機にて撹拌速度20000rpmで
30秒間混合撹拌したところ、粘着剤のシリカ微粉
カプセルが得られた。Example 4 Acrylate adhesive (manufactured by Soken Kagaku Co., Ltd., trade name
SK Dyne 1504) until it has sufficient adhesive strength.
Crosslinked and solvent removed. After freezing this material with liquefied nitrogen, it was frozen to an average size of 50 μm using a stirrer with a cutter.
powder. While maintaining 100 parts by weight of this powder at -60°C, which is a temperature that does not cause agglomeration, it was stirred with 10 parts by weight of silica fine powder (trade name Aerosil 200) using a stirrer with a cutter at a speed of 20,000 rpm.
After mixing and stirring for 30 seconds, fine silica powder capsules of the adhesive were obtained.
実施例 5
実施例4で得られたマイクロカプセル粉末10g
を10%ゼラチン温水溶液30g中に分散した後、10
%アラビアゴム水溶液30gと混合し、撹拌しなが
ら40℃の水140mlを加え、さらに10%酢酸を滴下
してPH4.2に調整し、コアセルベート滴で上記粉
末を包含させた。この分散液をさらに5℃に冷却
したのち30%ホルマリン1mlを加えさらに10%
NaOH水溶液を加えてPH9とし、ついで1℃/
分の昇温速度で50℃まで加温したところ、上記マ
イクロカプセルの表面がゼラチンで被覆された二
重マイクロカプセルができた。この二重マイクロ
カプセルを噴霧乾燥したところ形状保持力および
流動性のよいマイクロカプセル粉末が得られた。Example 5 10g of microcapsule powder obtained in Example 4
After dispersing in 30g of 10% gelatin warm water solution, 10
% aqueous gum arabic solution, 140 ml of water at 40° C. was added with stirring, and 10% acetic acid was added dropwise to adjust the pH to 4.2, and the above powder was encapsulated with coacervate droplets. After further cooling this dispersion to 5°C, 1 ml of 30% formalin was added and an additional 10%
Add NaOH aqueous solution to adjust the pH to 9, then 1℃/
When the mixture was heated to 50° C. at a temperature increase rate of 10 minutes, double microcapsules were formed in which the surfaces of the microcapsules were coated with gelatin. When this double microcapsule was spray-dried, a microcapsule powder with good shape retention and fluidity was obtained.
以上説明したようにこの発明のマイクロカプセ
ルの製造法は、粉状とした場合に常温付近では液
体となるかあるいは集塊化を起し、粉状を維持で
きない物質よりなる芯物質を、その粉末が融解ま
たは集塊化を起すことのない低温度で凍結粉砕
し、ついでこの温度において、微粉と混合撹拌す
るものであるので、常温付近で液体または粘着性
を有する物質もしくは軟質物質あるいは水や有機
溶剤に侵されるかもしくはこれらと反応する物質
を芯物質とすることができ、これら芯物質を極め
て簡単な工程操作で、短時間に、収率100%でマ
イクロカプセルとすることができ、粘着剤、接着
剤、塗料をはじめとしてトナーなどの電子写真材
料、医薬品、食品等に利用でき応用範囲が非常に
広範囲となる。また、従来法に比べて、製造に際
し、水や有機溶剤を全く使用しないので乾燥工程
や排液処理が不要となり、作業安定性も高い。さ
らに、任意の粒径のマイクロカプセルを容易に製
造することができ、目的に応じた多様性に富むマ
イクロカプセルを製造できるなどの利点を有す
る。 As explained above, the method for producing microcapsules of the present invention is to remove the core material, which is made of a material that becomes liquid or agglomerates at room temperature when it is made into powder and cannot maintain its powder state, into powder. The material is freeze-pulverized at a low temperature that will not cause melting or agglomeration, and then mixed and stirred with fine powder at this temperature. Substances that are eroded by solvents or react with them can be used as core substances, and these core substances can be made into microcapsules in a short period of time with 100% yield through extremely simple process operations, and can be used as adhesives. It can be used in a wide range of applications, including adhesives, paints, electrophotographic materials such as toner, medicines, and foods. Furthermore, compared to conventional methods, since no water or organic solvents are used during production, there is no need for a drying process or drainage treatment, and the process is highly stable. Further, it has the advantage that microcapsules of any particle size can be easily produced, and microcapsules with a wide variety of purposes can be produced.
Claims (1)
した場合集塊化を起こし粉状を維持できない物質
よりなる芯物質を、その融点又はガラス転移温度
以下の低温度にして凍結粉砕し、ついでこの低温
度を保持して前記凍結粉砕した芯物質に該芯物質
の水親和性と相反する水親和性を有する物質を前
記粉砕した芯物質の粒径より小さい粒径の微粉末
として加えて混合撹拌して、芯物質を微粉末で被
覆したことを特徴とするマイクロカプセルの製造
法。 2 常温付近で液体であつたり、あるいは粉状と
した場合集塊化をおこし粉状を維持できない物質
よりなる芯物質を、その融点又はガラス転移温度
以下の低温度にして凍結粉砕し、ついでこの低温
度を保持して前記凍結粉砕した芯物質に、該芯物
質の水親和性と相反する水親和性を有する物質を
前記粉砕した芯物質粒径より小さい粒径の微粉末
として加えて混合撹拌して、芯物質を微粉末で被
覆した後、更にこれをポリマーフイルムで被覆す
ることを特徴とするマイクロカプセルの製造法。[Claims] 1. A core material made of a material that is liquid at around room temperature or that cannot maintain its powder form due to agglomeration when made into a powder is heated to a low temperature below its melting point or glass transition temperature. freeze-mill, and then maintain this low temperature to infuse the freeze-milled core material with a substance having a water affinity that is opposite to that of the core material, with a particle size smaller than that of the milled core material. A method for producing microcapsules, characterized in that a core substance is coated with fine powder by adding it as a powder and mixing and stirring. 2 The core material, which is a liquid at room temperature or is made of a material that cannot maintain its powder form due to agglomeration when made into a powder, is freeze-pulverized at a low temperature below its melting point or glass transition temperature, and then this material is A substance having a water affinity that is contrary to the water affinity of the core material is added to the freeze-pulverized core material while maintaining a low temperature as a fine powder having a particle size smaller than the particle size of the crushed core material, and the mixture is stirred. A method for producing microcapsules, which comprises coating a core substance with a fine powder, and then coating the core substance with a polymer film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57155539A JPS5946125A (en) | 1982-09-07 | 1982-09-07 | Preparation of microcapsule |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57155539A JPS5946125A (en) | 1982-09-07 | 1982-09-07 | Preparation of microcapsule |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5946125A JPS5946125A (en) | 1984-03-15 |
| JPH0367737B2 true JPH0367737B2 (en) | 1991-10-24 |
Family
ID=15608266
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57155539A Granted JPS5946125A (en) | 1982-09-07 | 1982-09-07 | Preparation of microcapsule |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5946125A (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61136458A (en) * | 1984-12-08 | 1986-06-24 | Nippon Tansan Gas Kk | Viscous agent injection device |
| JPS6128386U (en) * | 1984-07-27 | 1986-02-20 | 日本葉緑素株式会社 | dye pack |
| JPS61136433A (en) * | 1984-12-07 | 1986-06-24 | Kikusui Kagaku Kogyo Kk | Microencapsulated powder emulsion |
| JPS6463035A (en) * | 1987-09-02 | 1989-03-09 | Soken Kagaku Kk | Powdery body having compound structure and production thereof |
| JP4514902B2 (en) * | 1999-08-24 | 2010-07-28 | 株式会社コーセー | Water-containing powder composition, process for producing the same, and cosmetics containing the powder composition |
| KR100468051B1 (en) * | 2002-01-26 | 2005-01-24 | 한국화학연구원 | Process for silica microcapsule by sol-gel reation |
| JP6525188B2 (en) * | 2015-02-17 | 2019-06-05 | 国立研究開発法人産業技術総合研究所 | Adhesive-encapsulated silica microcapsule, method for producing the same, adhesive material and adhesive material applicator |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS535694A (en) * | 1976-07-03 | 1978-01-19 | Kiyuugo Tanaka | Platinum wire used in combustible gas concentration measurements |
| JPS5855813B2 (en) * | 1978-02-04 | 1983-12-12 | ぺんてる株式会社 | Microcapsules and their manufacturing method |
| JPS57155538A (en) * | 1981-03-20 | 1982-09-25 | Konishiroku Photo Ind Co Ltd | Formation of color photographic silver halide image |
-
1982
- 1982-09-07 JP JP57155539A patent/JPS5946125A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5946125A (en) | 1984-03-15 |
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