JPS60175538A - Preparation of microcapsule - Google Patents

Preparation of microcapsule

Info

Publication number
JPS60175538A
JPS60175538A JP3191884A JP3191884A JPS60175538A JP S60175538 A JPS60175538 A JP S60175538A JP 3191884 A JP3191884 A JP 3191884A JP 3191884 A JP3191884 A JP 3191884A JP S60175538 A JPS60175538 A JP S60175538A
Authority
JP
Japan
Prior art keywords
substance
core material
core
temp
wall
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
JP3191884A
Other languages
Japanese (ja)
Inventor
Masumi Koishi
真純 小石
Tomohiko Sada
佐田 友彦
Masayuki Taniguchi
正幸 谷口
Tetsuya Kimijima
哲也 君島
Yasuhiko Satomi
里見 泰彦
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.)
Japan Oxygen Co Ltd
Nippon Sanso Corp
Original Assignee
Japan Oxygen Co Ltd
Nippon Sanso 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 Japan Oxygen Co Ltd, Nippon Sanso Corp filed Critical Japan Oxygen Co Ltd
Priority to JP3191884A priority Critical patent/JPS60175538A/en
Publication of JPS60175538A publication Critical patent/JPS60175538A/en
Pending 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Preparation (AREA)
  • Manufacturing Of Micro-Capsules (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Abstract

PURPOSE:To simply microencapsulate a substance solid at an ambient temp., by a method wherein a core substance solid at an ambient temp. is ground at a temp. lower than said ambient temp. and the ground core substance is mixed with a wall substance under stirring at the grinding temp. to coat the core substance with said wall substance. CONSTITUTION:A substance solid at an ambient temp. (e.g., camphor) is used as a core substance and this core substance is ground at a temp. lower than the ambient temp. and, subsequently, the ground core substance is mixed with a wall substance (e.g., stearyl alcohol) under stirring at the grinding temp. to coat the core substance with said wall substance. That is, the substance solid at an ambient temp., especially, a substance easily generating chemical or physical change at an ambient temp. can be simply and safely microencapsulated in high yield.

Description

【発明の詳細な説明】 a、技術分野 本発明は、常温で固体状態にあるwJ質を芯物質とし、
これをマイクロカプセル化する方法に係り。
[Detailed Description of the Invention] a. Technical field The present invention uses wJ quality, which is in a solid state at room temperature, as a core material,
This concerns a method of microencapsulating this.

特に芯物質が常温で化学変化または物理変化を起こし易
い物質である場合に有効なマイクロカプセルの製造法に
関するものである。
The present invention relates to a method for producing microcapsules that is particularly effective when the core substance is a substance that easily undergoes chemical or physical changes at room temperature.

b、従来技術及びその問題点 周知のようにマイクロカプセルは、感圧複写紙をはじめ
、医薬、農薬、香料などに広く利用されている。
b. Prior art and its problems As is well known, microcapsules are widely used in pressure-sensitive copying paper, medicines, agricultural chemicals, fragrances, and the like.

従来の代表的なマイクロカプセルの製造法としては、コ
アセルベーション法、界面重合法% 1nsitu重合
法、液中乾燥法%融解分散冷却法、オリフィス法、スプ
レードライング法、気中懸濁被稜法、無機質壁マイクロ
カプセル化法などがある。
Typical conventional microcapsule manufacturing methods include coacervation method, interfacial polymerization method, in-situ polymerization method, submerged drying method, melt dispersion cooling method, orifice method, spray drying method, and air suspension ridge method. , inorganic wall microencapsulation method, etc.

ところが、このような製造法は、常温で固体状態であり
、かつ常温で化学変化または物理変化を起こし易い物質
(以下、反応性固体物質と称す)をマイクロカプセル化
する場合には%通用が困難であった。すなわち、上記従
来の方法では、Iy7.応性固体物質はマイクロカプセ
ル化の過程で微砕化に伴い表面値が壇太し、上記の変化
が進行し易くなり、その微粒子表面を壁物質で被覆する
以前に化学変化または物理変化が相尚に進んで目的とす
るマイクロカプセルが得られない。また、常温において
バルキーな固体状態では化学反応によりその表面のみに
極く薄い反応生成物質の膜を生じる物質(例えばアルミ
ニウム)においても、微粉化して比表面積を増大させる
と、得られる微粉中の反応生成物の割合が大きくなって
好ましくない場合がある。
However, this manufacturing method is difficult to apply when microcapsulating substances that are solid at room temperature and are susceptible to chemical or physical changes at room temperature (hereinafter referred to as reactive solid substances). Met. That is, in the above conventional method, Iy7. In the process of microencapsulation, the surface value of a reactive solid substance increases as it becomes finer, making it easier for the above changes to occur, and chemical or physical changes occur frequently before the surface of the fine particles is covered with a wall material. However, the desired microcapsules cannot be obtained. In addition, even for substances (such as aluminum) that form a very thin film of reaction products only on the surface due to chemical reactions in a bulky solid state at room temperature, when the specific surface area is increased by pulverization, the reaction in the resulting fine powder This may result in an undesirable increase in the proportion of the product.

C0発明の目的 本発明は、上記事情に鑑みてなされたもので、常温で固
体である物質、特に常温で化学変化または物理変化を起
こし易い物質を簡単に高収率で、かつ安全にマイクロカ
プセル化することができる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。
C0 Purpose of the Invention The present invention has been made in view of the above circumstances, and it is possible to easily microcapsulate substances that are solid at room temperature, especially substances that easily undergo chemical or physical changes at room temperature, in a high yield and safely. The purpose of the present invention is to provide a method for producing microcapsules that can be used to produce microcapsules.

d1発明の構成 以下、本発明の詳細な説明する。d1 Structure of the invention The present invention will be explained in detail below.

本発明のマイクロカプセルの製造法は、常温で固体であ
る物質を芯物質としてマイクロカプセル化するにあたっ
て、前記芯物質を常温より低温度で粉砕し、次いでこの
温度において前記芯物質を壁物質とともに混合攪拌して
前記芯**を前記壁物質で被覆するようにしたことを4
9Itkとし、また、上記の製造法において、前記芯物
質が常温下で化学変化または物理変化を生じる物質であ
り、この芯物質の粉砕及び前記壁物質との混合攪拌を、
前記芯物質の化学変化または物理変化が起こらない温度
もしくは実質的に起こらないと見なせる温度で行なうこ
とを特徴とする。
In the method for producing microcapsules of the present invention, when a substance that is solid at room temperature is microencapsulated as a core material, the core material is pulverized at a temperature lower than room temperature, and then the core material is mixed with a wall material at this temperature. 4. Stirring to coat the core** with the wall material.
9Itk, and in the above manufacturing method, the core substance is a substance that undergoes a chemical or physical change at room temperature, and the pulverization of the core substance and mixing and stirring with the wall substance are
It is characterized in that it is carried out at a temperature at which no chemical or physical change of the core substance occurs or at a temperature at which it can be considered that substantially no chemical change or physical change occurs.

まず、この発明の製造法に用いられる芯物質としては、
アミノ酸類等の臭気性物質、水酸化カリウム、塩化マグ
ネシウム、塩化カルシウム、水酸化ナトリウム等の潮解
性物質、ナフタリン、樟脳等の昇華性物質など、常温下
で酸化反応等の化学変化や昇華等の物理変化を起こし易
い種々の物質をあげることができる。ただし、常温以下
の適宜の低温度で、上記の変化が抑止されるか、やるい
は変化の速度が充分に遅くなり、実質的に抑止される物
質であることが必俄である。
First, the core material used in the manufacturing method of this invention is as follows:
Odorous substances such as amino acids, deliquescent substances such as potassium hydroxide, magnesium chloride, calcium chloride, sodium hydroxide, sublimable substances such as naphthalene and camphor, etc., are subject to chemical changes such as oxidation reactions and sublimation at room temperature. Various substances that easily undergo physical changes can be mentioned. However, it is necessary that the above-mentioned change is suppressed or the rate of change is sufficiently slowed to be substantially suppressed at an appropriate low temperature below room temperature.

また、この芯物質を被覆する壁物質としては、芯物質と
の相互間係によって決められるが、一般には次のような
物質が用いられる。まず、ラウリ7に、ミリスチン酸、
ステアリン酸、オレイン酸、などの高級脂肪酸、ラウリ
ルアルコール、パルミチルアルコール、ステアリルアル
コールナトの高級アルコール、パルミチン酸アミド、ス
テアリン敵アミド、オレイン酸アミドなどの高級脂肪1
投アミド、グリセリン脂肪酸エステルなどの高級脂肪酸
エステル、ステアリン斌アルミニウム、ステアリン酸亜
鉛、ステアリン酸カルシウム、オレイン酸鉛、オレイン
酸亜鉛、パルミチン酸銅などの高級脂肪酸金セ4塩、カ
ルナウバワックス、パラフィンワックス、ビーズワック
ス、木ロウ、牛脂ワックス、カルデラワックス、ポリエ
チレンワックス、酸化パラフィンワックスなどの天然お
よび石油系ワックス、ロジン系側脂、テルペン系樹脂な
ど天然および合成樹脂、牛脂などの固形拙脂、ゼラチン
ゼリー、バター、メルトタイプチーズなどの食品、ウッ
ド合金、ニュートン合金などの易融合金などが挙げられ
る。そして、これら壁物質は、常温付近では固形であり
、さらに後述するように低掲度での芯物質との混合攪拌
の際、その温度で芯物質より微粒化し、さらに混合攪拌
の際に生ずる粒子間の摩擦等によって粒子面に発生する
局所熱の温度における壁物質の粘度が芯物質の粘度より
低いことが必要である。なおこれらの粘度の比較は壁物
質の融点又は軟化点付近の温度で行なわれ、そして本発
明の方法での壁物質は発生する局所熱と関連して融点又
は軟化点が約200℃以下である物質を1吏用して行な
うことが好ましい。
The wall material covering the core material is determined depending on the relationship with the core material, but the following materials are generally used. First, lauri 7, myristic acid,
Higher fatty acids such as stearic acid and oleic acid, higher alcohols such as lauryl alcohol, palmityl alcohol, and stearyl alcohol, higher fats such as palmitic acid amide, stearic acid amide, and oleic acid amide1
Higher fatty acid esters such as amide, glycerin fatty acid ester, higher fatty acid gold salts such as aluminum stearate, zinc stearate, calcium stearate, lead oleate, zinc oleate, copper palmitate, carnauba wax, paraffin wax, Natural and petroleum waxes such as beeswax, wood wax, tallow wax, caldera wax, polyethylene wax, and oxidized paraffin wax; natural and synthetic resins such as rosin fat and terpene resin; solid fat such as beef tallow; gelatin jelly; Examples include foods such as butter and melt-type cheese, and easily meltable metals such as Wood alloys and Newtonian alloys. These wall materials are solid at around room temperature, and as will be described later, when mixed with the core material at a low temperature, they become finer than the core material at that temperature, and the particles generated during the mixing and stirring. It is necessary that the viscosity of the wall material be lower than the viscosity of the core material at the temperature of local heat generated on the particle surface due to friction between particles. It should be noted that these viscosity comparisons are made at temperatures near the melting or softening point of the wall material, and the wall material in the method of the present invention has a melting or softening point of about 200° C. or less in relation to the local heat generated. Preferably, one dose of the substance is used.

更に、上記芯物質に対して組み合わされる壁物質を選択
するにあたっては、常温下で芯物質に接 触させた場合
に界面で化学変化を起こさない物質を選ぶことが必要で
ある。
Furthermore, when selecting a wall material to be combined with the core material, it is necessary to select a material that does not cause chemical changes at the interface when brought into contact with the core material at room temperature.

次ニ、マイクロカプセル化についてg明する。Next, microencapsulation will be explained.

まず、芯物質を額体霊素などの冷熱を利用して冷却し、
この状態で粉末化する。この時の温度は、芯物質の性)
ML(化学的または物理的性yi)によって異なり、芯
物質の化学変化または物理変化が起こらないか、あるい
は変化速度が充分に遅くなって実質的に変化が起こらな
いと見なせる温度もしくは望囲気とすることが必要であ
る。
First, the core substance is cooled using cold energy such as the forehead spirit element,
Powder it in this state. The temperature at this time is the property of the core material)
Depending on the ML (chemical or physical property yi), the temperature or desired ambient atmosphere is such that no chemical or physical change in the core substance occurs, or the rate of change is sufficiently slow that it can be considered that no change occurs substantially. It is necessary.

ついで、この粉末を低温度に保って化学変化あるいは物
理変化を起さないように維持しつつ、上記壁物質を加え
て混合攪拌し、マイクロカプセル化する。この混合攪拌
には、液化窒素冷却ジャケットを装備したカッター刊高
速撹拌機を用いることが好ましく、撹拌条件は攪拌速度
5,000〜30.00Orpm、攪拌時間数秒〜10
分である。特に、このタイプの(・6:神様を用いた場
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、混合攪拌にはボールミル、カッター付攪拌機
、アトライターなども用いることができる。攪拌時の温
度は、上記凍結粉砕時の温度と同根1屍であり%摩擦熱
による温度上昇を防止するために、攪拌機には液化窒素
等の冷却剤を通じ、冷却を行いつづける必要がある。ま
た、芯物質の粉末と壁物質との混合比は、芯物質の粉末
の形状によっても左右され、粉末が球状の場合には壁物
質は少量で済むが、通常は芯物質の粉末100重量部に
対して壁物質0.5〜50重量都とされる。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
と壁物質による膜厚によって決められるため、粉砕の条
件、芯物質と壁物質との混合量比、混合撹拌の条件によ
って任意に、114s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。この混合攪拌操
作中、壁物質の粉末はこの攪拌時の温度において、上述
のように芯物讐よりも微粒化されやすいので、この芯物
質と壁物質の両者が衝突した際、芯物質の表面により微
粒化した壁物質が物理的に付着した後更に両者の衝突表
面が局部的に摩擦熱が発生し加熱され、壁物質の粘度が
芯物質の粘度より低いことにより壁物質が流動して芯物
質の粉末の表面に塗りつけられ、これによって芯物質の
粉末は壁物質で被覆されることになる。
Next, while maintaining this powder at a low temperature to prevent chemical or physical changes, the above-mentioned wall material is added and mixed and stirred to form microcapsules. For this mixing and stirring, it is preferable to use a Cutter high-speed stirrer equipped with a liquefied nitrogen cooling jacket, and the stirring conditions are a stirring speed of 5,000 to 30.00 rpm, and a stirring time of several seconds to 1000 rpm.
It's a minute. In particular, when using this type of (・6: God), the above-mentioned freezing and pulverization can also be performed within this device, which is advantageous in terms of the process.In addition, ball mills, stirrers with cutters, attritors, etc. can also be used for mixing and stirring. The temperature during stirring is the same as the temperature during freeze-grinding, and in order to prevent temperature rise due to frictional heat, the stirrer must be continuously cooled by passing a coolant such as liquefied nitrogen. The mixing ratio of the core material powder and the wall material also depends on the shape of the core material powder; if the powder is spherical, a small amount of wall material is required, but usually 100 parts by weight of the core material powder is used. In addition, the particle size of the microcapsules obtained is determined by the particle size of the core material powder and the film thickness of the wall material. 114 seconds can be set arbitrarily depending on the mixing ratio of the material and wall material and the mixing and stirring conditions, and the average particle size is 1 to 1500 μm.
microcapsules can be obtained satisfactorily. During this mixing and stirring operation, the powder of the wall material is more likely to be atomized than the core material at the temperature during stirring, so when the core material and wall material collide, the surface of the core material After the atomized wall material physically adheres to the surface, frictional heat is generated locally on the collision surface of the two, which causes the wall material to flow and become heated due to the viscosity of the wall material being lower than that of the core material. It is smeared onto the surface of the material powder, thereby covering the core material powder with the wall material.

このようにして得られたマイクロカプセ)Vは、芯物質
の粉末が壁物質で完全に被覆され常温になってもサラサ
ラした流動性の良い粉末となる。
In the microcapsules V thus obtained, the core material powder is completely covered with the wall material, and the powder remains smooth and fluid even at room temperature.

なお、上記の工程により得られたマイクロカプセルは、
そのカプセルが芯物質に対して通気性を有する場合があ
るので、必要に応じてより完全なカプセル化を図る場合
には、更に気相法等によりマイクロカプセル表面をポリ
マーにて被覆する処理や、マイクロカプセルの壁物質を
溶解、再凝固させて緻密化を図る処理等を施せばよい。
In addition, the microcapsules obtained by the above steps are
Since the capsule may have air permeability to the core material, if necessary, to achieve more complete encapsulation, the surface of the microcapsule may be coated with a polymer using a vapor phase method, etc. What is necessary is to perform a process such as dissolving and re-solidifying the wall material of the microcapsules to achieve densification.

また、得られるマイクロカプセルの流!l4JJ性を一
層高めたい場合あるいは壁物質による被覆をより完全に
するために上記混合撹拌時に次のような平均粒径約10
0μm以下の微粉末を少祉加えることもできる。微粉末
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、カーボンブラック、炭酸カルシウム、タルク、
カオリン%酸化チタン、セラミック粉末、フィチン酸お
よびその金に1塩、ポリエチレン、ナイロン、メタアク
リレートなどの合成樹脂微粉末、でん粉ならびにこれら
粉末を表面処理した微粉末が挙げられる。この微粉末の
添加量は、芯物質の粉末100重量部に対して0.5〜
5重を部で十分である。
Also, the flow of microcapsules obtained! 14 If you want to further improve the JJ properties or to make the wall material more completely coated, use the following average particle size of about 10 during the above mixing and stirring process.
A small amount of fine powder of 0 μm or less can also be added. Fine powders include silica fine powder, various bentonites, aluminum oxide, carbon black, calcium carbonate, talc,
Examples include kaolin% titanium oxide, ceramic powder, phytic acid and its gold salt, fine powder of synthetic resin such as polyethylene, nylon, methacrylate, starch, and fine powder obtained by surface treatment of these powders. The amount of this fine powder added is 0.5 to 100 parts by weight of the core material powder.
5 parts is enough.

このようなマイクロカプセルの製造法によれば。According to this method of manufacturing microcapsules.

芯物質を凍結粉砕して粉末化し、これに壁?I質を加え
て低温度下で混合攪拌するものであるので、製造途中で
芯物質の化学変化または物理変化が災質的に抑止され、
芯物質のロスが全く無<、高収率でマイクロカプセル化
でき、しかも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<、シたがって製造コストが著しく低
いものとなる。また、すべての工程が芯物質の変化を抑
え得る低温度下で行なわれるので、芯物質に加えて壁物
質の変性変質も抑えられる。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、かつ作業の安全性も高い。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。
Freeze and crush the core material and turn it into powder, and add this to the wall? Since the material is added and mixed and stirred at low temperature, chemical or physical changes in the core material during production are dramatically suppressed.
There is no loss of core material, microcapsules can be produced at high yields, 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 extremely low. . Furthermore, since all processes are carried out at low temperatures that can suppress changes in the core material, degeneration and alteration of the wall material as well as the core material can be suppressed. Furthermore, compared to conventional methods that use water or organic solvents, there is no need for a drying process or wastewater treatment, and the work is highly safe. 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.

また、上述のごとく本発明の方法は、常温で活性の高い
芯物質に対して非常にM効であるが、無活性物質を芯物
質に用いた場合にも効果がある。
Furthermore, as described above, the method of the present invention is highly effective for core substances that are highly active at room temperature, but is also effective when an inactive substance is used as the core substance.

すなわち、芯物質を低温下で凍結粉砕することに′より
、微粉砕化が容易となって芯vIJ賀の総表面積を大き
くすることが可能となり、良好なマイクロカプセルが得
られる。
That is, by freezing and pulverizing the core material at low temperatures, fine pulverization becomes easy and the total surface area of the core material can be increased, resulting in good microcapsules.

e、実施例 以下、実施例を示して本発明を具体的に説明する。e. Example Hereinafter, the present invention will be specifically explained with reference to Examples.

〔実施例1〕 芯物質として樟脳76重量部、壁物質としてステアリル
アルコール20京−献部、微量添加剤として疎水性シリ
カ微粉(商品名アエロジル)Atist部を用いてマイ
クロカプセルを製造した。
[Example 1] Microcapsules were manufactured using 76 parts by weight of camphor as a core material, 20 quintillion parts by weight of stearyl alcohol as a wall material, and Atist part of hydrophobic silica fine powder (trade name: Aerosil) as a trace additive.

まず、カッター付攪拌機の中に芯物質を入れ、これを液
体窒素を用いて一80υ以下に冷却した。
First, a core material was placed in a stirrer equipped with a cutter, and the core material was cooled to below -80 υ using liquid nitrogen.

十分に冷却が進んで芯物質が低温度となった後、回転速
度15000〜25000rpmで2分間粉砕撹拌した
。このとき、微粉同志のMf@やシャフト部分の摩擦に
よる発熱を除くために、液体窒素を絶えず供給して低温
度を維持した。次いで、微粉砕された芯物質に、予冷し
た壁物質とアエロジルを入れ、上記と同一攪拌速度で混
合攪拌した。
After the core material was sufficiently cooled to a low temperature, it was pulverized and stirred for 2 minutes at a rotational speed of 15,000 to 25,000 rpm. At this time, liquid nitrogen was constantly supplied to maintain a low temperature in order to eliminate heat generation due to Mf@ between the fine powders and friction between the shaft portion. Next, the pre-cooled wall material and Aerosil were added to the finely pulverized core material and mixed and stirred at the same stirring speed as above.

上記の操作により樟脳粉末の表面にステアリルアルコー
ルが被覆されたマイクロカプセルが高収率で得られた。
By the above operation, microcapsules in which the surface of camphor powder was coated with stearyl alcohol were obtained in high yield.

このマイクロカプセルと、このマイクロカプセルに用い
た樟脳と同一重量かつ同一粉砕度の樟脳とについて臭気
比較を行なったところ、マイクロカプセルは樟脳臭が少
なく、明確な差が認められた。また、マイクロカプセル
中の樟脳分と純粋な樟脳とについて、経時的な重量減少
を測定したところ、図に示す結果を得て、マイクロカプ
セル化により芯物質とした樟脳の昇華速度が抑制される
ことが認められた。
When comparing the odor of this microcapsule with camphor of the same weight and same degree of crushing as the camphor used in this microcapsule, it was found that the microcapsule had less camphor odor, and a clear difference was observed. In addition, we measured the weight loss over time of the camphor content in the microcapsules and pure camphor, and the results shown in the figure were obtained, indicating that microencapsulation suppresses the sublimation rate of camphor as a core material. was recognized.

〔実施例2〕 芯物質として塩化マグネシウム2水塩80重曽部、壁物
質としてひまし油硬化油17重量部及び疎水性シリカ微
粉3型電部を用いて、実施例1と同様な操作でマイクロ
カプセルをMJ4gし、塩化マグネシウム粉末がひまし
油硬化油で被覆されたマイクロカプセルを得た。このマ
イクロカプセルは、塩化マグネシウムが高い潮解性をも
つ物質であるにもかかわらず、調製後1週間経過後にも
サラサラの粉末状1坂を維持した。
[Example 2] Microcapsules were prepared in the same manner as in Example 1 using 80 parts by weight of magnesium chloride dihydrate as the core material, 17 parts by weight of hydrogenated castor oil as the wall material, and type 3 hydrophobic silica powder. 4 g of MJ was added to obtain microcapsules in which magnesium chloride powder was coated with hydrogenated castor oil. Despite the fact that magnesium chloride is a highly deliquescent substance, the microcapsules maintained a smooth, powdery consistency even after one week had passed since their preparation.

10発明の効果 以上、1#細に説明したように1本発明のマイクロカプ
セルの製造法は、芯物質の粉砕を常温より低温度で行な
うことから、粉砕効率が向上して微粉砕化が容易となり
、粒径の小さいマイクロカプセルを容易に製造すること
ができる。丈な、芯物質として常温での化学的または物
理的活性が高い物質を用いる場合には、芯物質の化学的
または物理的変化を充分抑止できる低温度で芯物質の粉
砕及び壁物質による被糧を行なうから、芯*質の変性、
変化を抑えて従来困罐であった活性の賜い固体物質のマ
イクロカプセル化を高収率で行なうことができる。才だ
製造に際し、水や有機溶剤を全く使用しないので乾燥工
程や排液処理が不滅となり、作業安全性も高い。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
製造できる等の効果を奏する。
10 Effects of the Invention As explained in detail, the method for producing microcapsules of the present invention improves the pulverization efficiency and facilitates pulverization because the core substance is pulverized at a temperature lower than room temperature. Therefore, microcapsules with small particle size can be easily produced. When using a material that is long and has high chemical or physical activity at room temperature as a core material, the core material is pulverized and absorbed by the wall material at a low temperature that sufficiently suppresses chemical or physical changes in the core material. Because of this, the degeneration of the core* quality,
Due to its activity, which has been difficult to achieve in the past, it is possible to microencapsulate solid substances in high yields while suppressing changes. During production, no water or organic solvents are used, so the drying process and wastewater treatment are indestructible, and work safety is high. Furthermore, microcapsules of any particle size can be easily produced, and microcapsules with a wide variety of purposes can be produced.

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

図面は、実施例1における経時的な重責変化の測定結果
を示すグラフである。 出願人日本酸素株式会社
The drawing is a graph showing the measurement results of changes in burden over time in Example 1. Applicant Nippon Sanso Co., Ltd.

Claims (1)

【特許請求の範囲】 l)常温では固体である物質よりなる芯物質を常温より
低温度で粉砕し、次いでこの温度において前記芯9勿質
を壁?+質とともに混合攪拌して前記芯物質を壁物質で
被覆するようにしたことを特徴とするマイクロカプセル
の製造法。 2)前記芯物質は、常温下で化学変化または物理的変化
を生じる物質であり、この芯物質の粉砕及び前記壁物質
との混合攪拌は前記芯物質の化学変化または物理的変化
が起こらない温度もしくは前記芯物質の化学変化または
物理的変化が実質的に生じない温度で行なう特許請求の
範囲第1項記載のマイクロカプセルの製造法。 3)前記芯vlJ實と壁物質の粉砕が両者の混合状態で
行なわれる特許請求の範囲第1項または第2項記載のマ
イクロカプセルの製造法。
[Claims] l) A core material made of a substance that is solid at room temperature is pulverized at a temperature lower than room temperature, and then the core material 9 is ground at this temperature. A method for producing microcapsules, characterized in that the core material is covered with a wall material by mixing and stirring the core material with the material. 2) The core material is a material that undergoes chemical or physical changes at room temperature, and the core material is crushed and mixed and stirred with the wall material at a temperature at which chemical or physical changes do not occur in the core material. The method for producing microcapsules according to claim 1, wherein the process is carried out at a temperature at which substantially no chemical or physical changes occur in the core substance. 3) The method for producing microcapsules according to claim 1 or 2, wherein the core material and wall material are crushed in a mixed state.
JP3191884A 1984-02-22 1984-02-22 Preparation of microcapsule Pending JPS60175538A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3191884A JPS60175538A (en) 1984-02-22 1984-02-22 Preparation of microcapsule

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3191884A JPS60175538A (en) 1984-02-22 1984-02-22 Preparation of microcapsule

Publications (1)

Publication Number Publication Date
JPS60175538A true JPS60175538A (en) 1985-09-09

Family

ID=12344352

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3191884A Pending JPS60175538A (en) 1984-02-22 1984-02-22 Preparation of microcapsule

Country Status (1)

Country Link
JP (1) JPS60175538A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5232689A (en) * 1990-12-21 1993-08-03 Dow Corning Corporation Translucent antiperspirant compositions

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50103578A (en) * 1974-01-21 1975-08-15
JPS5362897A (en) * 1976-11-13 1978-06-05 Haruo Tanemura Production of luxury drink utilizing tea as raw mate ria l
JPS55153581A (en) * 1979-05-21 1980-11-29 Osaka Gas Co Ltd Production of processed fishery product
JPS5614344A (en) * 1979-07-13 1981-02-12 Hitachi Ltd Display system for incorporation of lower-level device
JPS58219939A (en) * 1982-06-12 1983-12-21 Masatoshi Yamada Solidification of oily substance

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50103578A (en) * 1974-01-21 1975-08-15
JPS5362897A (en) * 1976-11-13 1978-06-05 Haruo Tanemura Production of luxury drink utilizing tea as raw mate ria l
JPS55153581A (en) * 1979-05-21 1980-11-29 Osaka Gas Co Ltd Production of processed fishery product
JPS5614344A (en) * 1979-07-13 1981-02-12 Hitachi Ltd Display system for incorporation of lower-level device
JPS58219939A (en) * 1982-06-12 1983-12-21 Masatoshi Yamada Solidification of oily substance

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5232689A (en) * 1990-12-21 1993-08-03 Dow Corning Corporation Translucent antiperspirant compositions

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