JP2679233B2 - Method for manufacturing capsule body - Google Patents

Method for manufacturing capsule body

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Publication number
JP2679233B2
JP2679233B2 JP1084642A JP8464289A JP2679233B2 JP 2679233 B2 JP2679233 B2 JP 2679233B2 JP 1084642 A JP1084642 A JP 1084642A JP 8464289 A JP8464289 A JP 8464289A JP 2679233 B2 JP2679233 B2 JP 2679233B2
Authority
JP
Japan
Prior art keywords
water
capsule body
film
hydrophobic solvent
hydrophobic
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
Application number
JP1084642A
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Japanese (ja)
Other versions
JPH02265642A (en
Inventor
安司 磯部
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.)
Toagosei Co Ltd
Original Assignee
Toagosei Co Ltd
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Filing date
Publication date
Application filed by Toagosei Co Ltd filed Critical Toagosei Co Ltd
Priority to JP1084642A priority Critical patent/JP2679233B2/en
Publication of JPH02265642A publication Critical patent/JPH02265642A/en
Application granted granted Critical
Publication of JP2679233B2 publication Critical patent/JP2679233B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Building Environments (AREA)
  • Investigating Or Analyzing Materials Using Thermal Means (AREA)
  • Formation And Processing Of Food Products (AREA)
  • Cosmetics (AREA)
  • Manufacturing Of Micro-Capsules (AREA)

Description

【発明の詳細な説明】 (イ)発明の目的 〔産業上の利用分野〕 本発明はフィルム形成性重合体を壁膜とするカプセル
体の製造方法に関するものであり、特に内包物の含有率
の高いカプセルを工業的に極めて有利に製造する方法を
提供するものである。
DETAILED DESCRIPTION OF THE INVENTION (a) Purpose of the invention [Industrial field of application] The present invention relates to a method for producing a capsule body having a film-forming polymer as a wall film, and particularly to It is intended to provide a method for industrially extremely advantageously producing high capsules.

本発明により得られたカプセル体は次のような用途に
利用可能である。
The capsule body obtained by the present invention can be used for the following purposes.

例えば本発明で得られる水を芯物質とするカプセル体
は、繊維の内面の風合いを高める調湿剤として、又水を
含む不燃化剤を芯物質とするカプセル体は、建材ボード
中に含ませて火災等の際に、カプセル体が破壊して内包
物が蒸発することにより熱を奪う、所謂耐熱性建材ボー
ドとして利用できる。
For example, the capsule body having water as a core substance obtained in the present invention is used as a humidity control agent for enhancing the texture of the inner surface of the fiber, and the capsule body having a non-combustible agent containing water as a core substance is not contained in the building material board. In the case of a fire or the like, it can be used as a so-called heat-resistant building material board, in which the capsule body is destroyed and the contents are evaporated to take heat.

更に本発明で得られる水性インキを芯物質とするカプ
セル体は、凍結によりカプセルが破壊されるため、冷凍
後の冷凍食品が一度でも解凍された場合に該インキの滲
み出しによる色彩表示により解凍履歴を示す、所謂冷凍
食品向けの解凍履歴表示インジゲーターとして、又水性
インキの代わりに芳香剤水溶液を内包して冷凍中は芳香
を発せず、解凍後に周囲に芳香を放す芳香付与剤として
利用できる。
Furthermore, the capsule body having the aqueous ink as a core substance obtained in the present invention is broken by freezing, so that even if the frozen food after freezing is thawed even once, it is thawed by the color display by the exudation of the ink. Can be used as a so-called thawing history display indicator for frozen foods, or as an aroma-imparting agent that does not emit a fragrance during freezing by containing an aqueous fragrance agent instead of an aqueous ink and releases an aroma to the surroundings after thawing.

更に又本発明で得られるグリセリンや微粉末状炭水化
物或いはこの誘導体を芯物質としたカプセル体は、湿潤
保持性化粧品や酸素除去剤として利用できる。
Furthermore, the capsule body obtained by the present invention containing glycerin, a finely powdered carbohydrate, or a derivative thereof as a core substance can be used as a moisture-retaining cosmetic product or an oxygen scavenger.

〔従来の技術〕[Conventional technology]

従来、水系液体の微小滴をカプセル化する技術として
は、疎水性溶剤とフイルム形成性重合体からなる溶液中
に、芯物質とする水系液体を直接懸濁させ、得られた懸
濁液を水媒体中に微小滴状に分散させ、次にこの分散液
を必要に応じて減圧下で、当該疎水性溶剤の沸点以上に
加熱したり或いは該分散液に溶解しない気体を吹き込む
方法により、当該疎水性溶剤を除去する、所謂水中乾燥
法が知られている。
Conventionally, as a technique for encapsulating microdroplets of an aqueous liquid, an aqueous liquid as a core substance is directly suspended in a solution composed of a hydrophobic solvent and a film-forming polymer, and the resulting suspension is treated with water. It is dispersed in a medium in the form of microdroplets, and then the dispersion is heated under reduced pressure, if necessary, to a temperature not lower than the boiling point of the hydrophobic solvent, or by blowing a gas insoluble in the dispersion, A so-called in-water drying method for removing the organic solvent is known.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

しかし高い含有率で芯物質を内包するカプセル体を製
造するには、疎水性溶剤の初期の蒸発速度を大きくとら
ねばならないが、この方法では液面にフィルム形成性重
合体の皮膜が絶えず形成し、溶剤の蒸発が困難になると
共に、溶剤の蒸発により、仕込んだ分散液全体の体積が
減少して撹拌状態が一定に保持できなくなり、均一な粒
径を有するカプセル体の生成が困難になるという欠点を
有していた。
However, in order to produce a capsule body containing a core substance at a high content rate, the initial evaporation rate of the hydrophobic solvent must be high, but this method constantly forms a film of the film-forming polymer on the liquid surface. In addition, it becomes difficult to evaporate the solvent, and due to the evaporation of the solvent, the volume of the entire dispersion liquid charged is reduced and the stirring state cannot be kept constant, which makes it difficult to form a capsule body having a uniform particle size. It had drawbacks.

更に、この方法では疎水性溶剤の蒸発時に発泡が起
き、蒸発槽上部での均一な撹拌が困難となり、凝集した
カプセル体が生成したり、カプセル体の収率が低下する
という欠点も有していた。
Furthermore, this method also has the drawback that foaming occurs during evaporation of the hydrophobic solvent, making it difficult to uniformly stir in the upper part of the evaporation tank, producing aggregated capsule bodies, and lowering the yield of capsule bodies. It was

これらの現象は特に蒸発槽をスケールアップした場合
に著しく、該方法が未だ工業的に利用されていない原因
となっている。
These phenomena are particularly remarkable when the evaporation tank is scaled up, which is the cause of the method not being industrially used.

(ロ)発明の構成 〔課題を解決するための手段〕 前記課題を解決するために、本発明者は鋭意検討した
結果、疎水性溶剤の蒸発面に水を散布することにより、
上記問題点がことごとく解決されることを見出し、本発
明を完成するに至った。
(B) Configuration of the Invention [Means for Solving the Problems] In order to solve the above problems, the present inventors have made diligent studies, and as a result, by spraying water on the evaporation surface of the hydrophobic solvent,
The inventors have found that all the above problems can be solved, and have completed the present invention.

即ち本発明は、フィルム形成性重合体を疎水性溶剤に
溶解してなる疎水性溶液中に、芯物質となる物質を懸濁
させ、得られた懸濁液を水又は水を主体とする媒体中に
微小滴状に分散させることにより前記芯物質を内包する
疎水性溶液微小粒子を形成させ、次いで常圧又は減圧下
で加熱操作及び/又は気体の吹き込み操作行うことによ
り、前記分散液中において、前記微小粒子の疎水性溶液
層から前記疎水性溶剤を除去することによって、前記フ
ィルム形成性重合体壁膜を前記芯物質の周囲に形成させ
ることにより、前記芯物質を内包するカプセル体を製造
する方法において、前記疎水性溶剤を除去する際に、液
面に散水することを特徴とするカプセル体の製造方法に
関するものである。
That is, the present invention is to suspend a substance to be a core substance in a hydrophobic solution prepared by dissolving a film-forming polymer in a hydrophobic solvent, and to obtain a suspension containing water or a medium containing water as a main component. In the dispersion liquid, by forming a hydrophobic solution microparticles encapsulating the core substance by dispersing it in the form of microdroplets, and then performing heating operation and / or gas blowing operation under normal pressure or reduced pressure, Producing a capsule body containing the core substance by forming the film-forming polymer wall film around the core substance by removing the hydrophobic solvent from the hydrophobic solution layer of the fine particles. In the method described above, water is sprayed on the liquid surface when the hydrophobic solvent is removed.

以下、工程の順序に従って本発明を詳細に説明する。 Hereinafter, the present invention will be described in detail in the order of steps.

(1) フィルム形成性重合体を疎水性溶剤に溶解して
なる疎水性溶剤: 混合槽にフィルム形成性重合体と疎水性溶剤を仕込
み、常温又は加温下において、撹拌を行って溶液とす
る。
(1) Hydrophobic solvent prepared by dissolving the film-forming polymer in a hydrophobic solvent: The film-forming polymer and the hydrophobic solvent are charged into a mixing tank and stirred at room temperature or under heating to form a solution. .

フィルム形成性重合体は、疎水性溶剤に溶け均一な溶
液状の組成物とさせる必要があるので、両者は相互に一
対となって選択される。
Since the film-forming polymer needs to be dissolved in a hydrophobic solvent to form a uniform solution composition, both are selected as a pair with each other.

例えば、塩化メチレン、塩化ビニリデン、メチルクロ
ロホルム或いは塩化ビニル等の塩素系溶剤に対しては、
ポリスチレン;スチレン並びにアクリル酸、アクリル酸
エステル、メタクリル酸、メタクリル酸エステル、ブタ
ジエン又はアクレロニトリルとの共重合体;低分子量の
ポリエチレン;塩化ゴム;低分子量の塩化ビニリデン及
び塩化ビニルの共重合体;メチルメタクリレート樹脂;
結晶度の低いポリエステル又はナイロン共重合体が挙げ
られる。
For example, for chlorine-based solvents such as methylene chloride, vinylidene chloride, methyl chloroform or vinyl chloride,
Polystyrene; Copolymer with styrene and acrylic acid, acrylic acid ester, methacrylic acid, methacrylic acid ester, butadiene or acrylonitrile; Low molecular weight polyethylene; Chlorinated rubber; Low molecular weight vinylidene chloride and vinyl chloride copolymers; Methyl methacrylate resin;
A polyester or a nylon copolymer having a low crystallinity can be used.

ベンゼン、トルエン或いはキシレン等の芳香族炭化水
素に対しては、上述と重合体のうち、結晶度の低いポリ
エステル及びナイロン共重合体を除いたものが用いられ
る。
For aromatic hydrocarbons such as benzene, toluene, and xylene, the above-mentioned polymers except those having low crystallinity polyester and nylon copolymer are used.

酢酸エチル、酢酸n−プロピル、酢酸イソプロピル、
プロピオン酸メチル、プロピオン酸エチル又は酪酸メチ
ル等の脂肪酸エステル類に対しては、ニトロセルロー
ス、エチルセルロースエステルガム、クマロン樹脂又は
ロジン等が好ましく用いられる。
Ethyl acetate, n-propyl acetate, isopropyl acetate,
For fatty acid esters such as methyl propionate, ethyl propionate or methyl butyrate, nitrocellulose, ethyl cellulose ester gum, coumarone resin, rosin and the like are preferably used.

これらの内、塩化メチレン又は塩化ビニリデンと、ポ
リスチレン樹脂又はメチルメタクリレート樹脂の組み合
わせ;ベンゼンとエチルセルロースの組み合わせが相溶
性が良く好ましい。
Among these, a combination of methylene chloride or vinylidene chloride and a polystyrene resin or a methyl methacrylate resin; a combination of benzene and ethyl cellulose is preferable because of good compatibility.

疎水性溶剤とフィルム形成性重合体との配合割合は、
疎水性溶剤100重量部当り、フィルム形成性重合体1〜1
0重量部が好ましい。
The mixing ratio of the hydrophobic solvent and the film-forming polymer is
Film-forming polymer 1 to 1 per 100 parts by weight of hydrophobic solvent
0 parts by weight is preferred.

1重量部未満では生成したカプセル体の皮膜が薄すぎ
て破壊し易く、又10重量部を超えると皮膜が厚すぎるた
め次の工程で得られる懸濁液の粘度が高すぎて好ましく
ない。
If it is less than 1 part by weight, the film of the formed capsule body is too thin and is easily broken, and if it exceeds 10 parts by weight, the film obtained is too thick and the viscosity of the suspension obtained in the next step is too high, which is not preferable.

疎水性溶剤は、好ましくは内包物とする物質100重量
部に対して、70〜300重量使用されるが、この混合割合
において、内包物となる物質と実質的に相溶しない状
態、即ち均一な単一相を形成とないことが必要である。
The hydrophobic solvent is preferably used in an amount of 70 to 300 parts by weight with respect to 100 parts by weight of the substance to be encapsulated, but in this mixing ratio, it is substantially incompatible with the substance to be encapsulated, that is, uniform. It is necessary not to form a single phase.

又、疎水性溶剤の沸点は、水との共沸が期待されるの
で特に定められないが、30〜100℃の範囲にあると溶剤
の除去がし易く好ましい。
The boiling point of the hydrophobic solvent is not particularly limited because it is expected to be azeotropic with water, but it is preferably in the range of 30 to 100 ° C. because the solvent can be easily removed.

(2) 芯物質となる物質を(1)の疎水性溶液中に懸
濁させる工程: (1)の疎水性溶液に芯物質とする物質を加え、高撹
拌下で十分に混合すれば、懸濁液を得ることができる。
(2) Step of suspending the substance to be the core substance in the hydrophobic solution of (1): If the substance to be the core substance is added to the hydrophobic solution of (1) and sufficiently mixed under high stirring, A suspension can be obtained.

この場合予め、当該溶液中に油溶性界面活性剤又は親
水性懸濁剤の水溶液を少量存在させれば、更に容易に安
定な懸濁液を得ることができるが、多量に使用すると疎
水性溶剤を蒸発させる工程で発泡が著しくなり好ましく
ない。
In this case, if a small amount of an aqueous solution of an oil-soluble surfactant or a hydrophilic suspending agent is previously present in the solution, a stable suspension can be obtained more easily, but if a large amount is used, a hydrophobic solvent is used. In the step of evaporating, the foaming becomes remarkable, which is not preferable.

芯物質とする物質は、用途に応じて選択される水、水
溶液、水分散液、ゲル状物又は微粉末状物質で、例え
ば、純水、水を含む不燃化剤、インキ水溶液、芳香剤水
溶液、グリセリンと水との混合液、酵素水溶液、化粧
品、微粉末状炭水化物或いはL−アスコルビン酸等が挙
げられる。
The substance used as the core substance is water, an aqueous solution, an aqueous dispersion, a gel-like substance or a fine powdery substance selected according to the use, and for example, pure water, an incombustible agent containing water, an aqueous ink solution, an aromatic water solution. , A mixed solution of glycerin and water, an enzyme aqueous solution, cosmetics, finely powdered carbohydrates or L-ascorbic acid.

(3) (2)で得た懸濁液を水又は水を主体とする媒
体中に微小滴状に分散させる工程: (2)で得た懸濁液を疎水性溶剤の蒸気圧を超える圧
力下で、微小滴発生装置、例えば遠心散布型のアドマイ
ザーを使用して、直接微小滴化することができるが、よ
り均一な粒径を得るには、該懸濁液を、水又は水を主体
とする媒体中に、比較的強い撹拌下で分散させる方法が
好ましい。
(3) A step of dispersing the suspension obtained in (2) in the form of microdroplets in water or a water-based medium: a pressure exceeding the vapor pressure of the hydrophobic solvent in the suspension obtained in (2). Below, a microdroplet generator, for example, an atomizer of the centrifugal spraying type, can be used to directly make microdroplets, but in order to obtain a more uniform particle size, the suspension is water or water-based. It is preferable to disperse the medium in the medium under relatively strong stirring.

この際、該媒体中にゼラチン、部分ケン化ポリビニル
アルコール又はスチレン−無水マレイン酸共重合体等の
分散剤を予め溶解しておくと、当該懸濁液を容易に微小
滴状に分散させることができる。
At this time, if a dispersant such as gelatin, partially saponified polyvinyl alcohol or styrene-maleic anhydride copolymer is previously dissolved in the medium, the suspension can be easily dispersed in the form of microdroplets. it can.

この工程によって、芯物質を内包し疎水性溶液を壁層
とする微小粒子が形成される。
By this step, fine particles containing the core substance and having the hydrophobic solution as the wall layer are formed.

(4) 疎水性溶剤の除去: 上記で得た分散液を常圧又は減圧下で、加熱及び/又
は該媒体に不溶性の気体を吹き込むことにより、該分散
液中の微小粒子の疎水性溶液からなる壁層より、疎水性
溶剤を除去する。
(4) Removal of Hydrophobic Solvent: From the hydrophobic solution of fine particles in the dispersion liquid, by heating the dispersion liquid obtained above under normal pressure or reduced pressure and / or blowing an insoluble gas into the medium. The hydrophobic solvent is removed from the resulting wall layer.

本発明はこの際に、蒸発面に散水することを特徴とす
るものである。
At this time, the present invention is characterized in that water is sprinkled on the evaporation surface.

この操作に好適な装置について添付の図面に基づいて
詳細に説明する。
An apparatus suitable for this operation will be described in detail with reference to the accompanying drawings.

図1における1は、上部が開放され、撹拌機2を付帯
している蒸発槽であり、必要に応じて加熱するためのジ
ャケット5が付帯される。
Reference numeral 1 in FIG. 1 denotes an evaporation tank having an open upper portion and an agitator 2 attached thereto, and a jacket 5 for heating is attached as necessary.

この槽の内部には(1)〜(3)の工程を経て得られ
た分散液が仕込まれている。。
The dispersion obtained through the steps (1) to (3) is charged in the tank. .

3は、微細なノズルを多数有するリング状の散水器
で、加圧型貯水槽4を付帯している。
Reference numeral 3 is a ring-shaped water sprinkler having a large number of fine nozzles, and is provided with a pressurization type water storage tank 4.

このノズルより水を前記分散液の液面に微滴状に散水
することができる。
Water can be sprayed in the form of fine droplets from the nozzle onto the liquid surface of the dispersion liquid.

散水速度は、該分散液から蒸発する疎水性溶剤の蒸発
速度と同程度とし、又散水量は、最終的に蒸発する疎水
性溶剤の量と同程度にすると、該分散液の量が常に概ね
一定となり、撹拌状態が常に一定に保たれるので好まし
い。
If the water sprinkling rate is set to the same level as the evaporation rate of the hydrophobic solvent that evaporates from the dispersion, and the water sprinkling amount is set to the same level as the amount of the hydrophobic solvent that finally evaporates, the amount of the dispersion is always approximately It is preferable because it becomes constant and the stirring state is always kept constant.

なお、分散液量を一定に保つ方法としては、散水量の
調整以外に、別の方法で蒸発槽に水を補給してもよい。
As a method for keeping the amount of the dispersion liquid constant, water may be supplied to the evaporation tank by another method other than the adjustment of the amount of water sprayed.

散水は、特に疎水性溶剤の蒸発が著しい初期の間に行
うとカプセル体の収率が良く好ましい。
It is preferable that the water sprinkling is performed during the initial period when the evaporation of the hydrophobic solvent is remarkable, because the yield of the capsule is good.

この工程により、溶剤を含まない重合体壁膜で被覆さ
れたカプセル体をスラリー状で得ることができ、更に真
空濾過機又は遠心分離機により脱水することによりケー
キ状のものとして回収される。
By this step, a capsule body coated with a polymer wall film containing no solvent can be obtained in the form of a slurry, and is further dehydrated by a vacuum filter or a centrifuge to be recovered as a cake.

得られたカプセル体はこのまま他の物質と混合して使
用も可能であるが、必要に応じて気流乾燥機又は流動乾
燥機を通してカプセル体の表面を乾燥してから使用する
こともできる。
The obtained capsule body can be used as it is by mixing it with other substances, but if necessary, it can be used after drying the surface of the capsule body through an airflow dryer or a fluid dryer.

得られるカプセル体中の内包物の量は、カプセル体全
体の重量を100とした場合に20〜90であることが好まし
い。
The amount of the inclusions in the obtained capsule body is preferably 20 to 90 when the weight of the entire capsule body is 100.

90を超える場合は膜厚が薄過ぎてカプセルが破壊し易
く、又20未満では皮膜が厚すぎてカプセル体としての性
能が十分に発揮されなく各々好ましくない。
When it exceeds 90, the film thickness is too thin and the capsule is easily broken, and when it is less than 20, the film is too thick and the performance as a capsule body is not sufficiently exhibited, which is not preferable.

〔作用〕[Action]

本発明において疎水性溶剤を蒸発除去する際に、蒸発
面に散水することにより、カプセル体を高い収率で製造
することができる。
In the present invention, when the hydrophobic solvent is removed by evaporation, water can be sprayed on the evaporation surface to produce a capsule body with a high yield.

この理由は散水により液面にフィルム形成性重合体の
皮膜が形成することが防止されるため、疎水性溶剤の除
去速度が増大し、カプセル体周囲の皮膜の形成速度が上
昇し、結果として内包物が内部からカプセル体外へ流出
することを防ぐことができるためと考えられる。
The reason for this is that the film formation polymer film is prevented from being formed on the liquid surface by water sprinkling, so that the removal rate of the hydrophobic solvent is increased and the film formation rate around the capsule body is increased, resulting in inclusion. It is considered that this can prevent the substance from flowing out of the capsule body from the inside.

又本発明で得られるカプセル体の粒度分布幅が狭い
が、これは発泡が少なくかつ液量が一定であるため撹拌
コントロールが十分行われるためと考えられる。
Further, the particle size distribution width of the capsule body obtained in the present invention is narrow, which is considered to be because the stirring is sufficiently controlled because the foaming is small and the liquid amount is constant.

〔実施例及び比較例〕(Examples and Comparative Examples)

以下に実施例及び比較例を挙げて本発明をさらに詳し
く説明する。
Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples.

なお、粒度分布は、湿式の篩分法を用いて測定し、20
メッシュ不通過物(表1において「非粒子状物」と略記
する。)の重量を測定し、ついで通過物の内、100メッ
シュ篩を通過しないものの重量%(表1において「100M
e上」と略記する。)及び280メッシュ篩を通過するもの
の重量%(表1において「280Me下」と略記する。)を
測定した。
The particle size distribution is measured using a wet sieving method,
The weight of the mesh non-passing material (abbreviated as “non-particulate matter” in Table 1) was measured, and then the weight% of the passing material that did not pass through the 100 mesh sieve (“100 M in Table 1”).
"above". ) And the weight percentage of those passing through a 280 mesh sieve (abbreviated as “under 280 Me” in Table 1) were measured.

実施例1 内容積100、内径50cmの上面が開放した混合槽の上
部に、内径10cm、外径45cmで1cm2当り平均20個の直径0.
5mmのノズル穴を有するリング状の散水器を有し、かつ
櫂型撹拌機及び窒素吹き込み用ノズルを付帯した図1に
示す態様の装置を使用した。
Example 1 On the upper part of a mixing tank having an inner volume of 100 and an inner diameter of 50 cm and an open upper surface, an inner diameter of 10 cm and an outer diameter of 45 cm were obtained, with an average of 20 diameters per cm 2 .
An apparatus having an embodiment shown in FIG. 1 having a ring-shaped water sprinkler having a nozzle hole of 5 mm and having a paddle type stirrer and a nozzle for blowing nitrogen was used.

ここにスタイロン679(数平均分子量10万のポリスチ
レン重合体;旭化成工業(株)製)550gと塩化メチレン
15.8kgからなる溶液を仕込み、250rpmの撹拌下で純水1
1.3kgを仕込み2分間撹拌した。
Stylon 679 (polystyrene polymer having a number average molecular weight of 100,000; manufactured by Asahi Chemical Industry Co., Ltd.) 550 g and methylene chloride
A solution consisting of 15.8 kg was charged and pure water was added under stirring at 250 rpm.
1.3 kg was charged and stirred for 2 minutes.

次いで撹拌を200rpmにして、ゼラチン450gを溶解した
水溶液45kgを投入し、液温を18℃から45℃に加温すると
同時に、1.0kg/分の流量で液面に散水しながら20分間撹
拌を行い、更に散水を止めて、45℃で1時間撹拌を続
け、スラリー状物を得た。
Then, stirring was set to 200 rpm, 45 kg of an aqueous solution in which 450 g of gelatin was dissolved was charged, and the temperature of the liquid was heated from 18 ° C to 45 ° C, and at the same time, stirring was performed for 20 minutes while water was sprinkling on the liquid surface at a flow rate of 1.0 kg / min. Further, the sprinkling of water was stopped and stirring was continued at 45 ° C. for 1 hour to obtain a slurry.

これを真空濾過機で濾過した後、2時間通風乾燥機に
通し、水を内包したカプセル体を得、粒度分布を、前述
の方法に従い測定した。この結果を表1に記す。
After filtering this with a vacuum filter, it was passed through an air dryer for 2 hours to obtain a capsule body containing water, and the particle size distribution was measured according to the method described above. The results are shown in Table 1.

実施例2〜8、比較例1 実施例1における疎水性溶剤、フィルム形成性重合体
及び内包物の種類と量、散水の量と期間及び溶剤除去工
程における温度を表1のように変更した以外は実施例1
と同じ条件で、カプセル体を得た。
Examples 2 to 8, Comparative Example 1 Other than changing the types and amounts of the hydrophobic solvent, the film-forming polymer and the inclusions, the amount and period of water spray, and the temperature in the solvent removal step in Example 1 as shown in Table 1. Is Example 1
Under the same conditions as above, a capsule body was obtained.

得られたカプセル体の評価結果を表1に記す。 Table 1 shows the evaluation results of the obtained capsules.

(ハ)発明の効果 本発明の方法により、水中乾燥法によるカプセル体を
高い収率で、かつ狭い粒度分布で得ることが可能となっ
た。
(C) Effect of the Invention According to the method of the present invention, it becomes possible to obtain a capsule body by an in-water drying method with a high yield and a narrow particle size distribution.

【図面の簡単な説明】 図1は、本発明に好適な装置に関する概略図である。 1……蒸発槽、2……撹拌機 3……リング状の散水器 4……加圧型貯水槽、5……ジャケットBRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic view of an apparatus suitable for the present invention. 1 ... Evaporating tank, 2 ... Stirrer, 3 ... Ring sprinkler, 4 ... Pressurized water storage tank, 5 ... Jacket

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 A62C 2/00 A62C 2/00 X G01N 25/00 G01N 25/00 Z 33/02 33/02 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location A62C 2/00 A62C 2/00 X G01N 25/00 G01N 25/00 Z 33/02 33/02

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】フィルム形成性重合体を疎水性溶剤に溶解
してなる疎水性溶液中に、芯物質となる物質を懸濁さ
せ、得られた懸濁液を水又は水を主体とする媒体中に微
小滴状に分散させることにより前記芯物質を内包する疎
水性溶液微小粒子を形成させ、次いで常圧又は減圧下で
加熱操作及び/又は気体の吹き込み操作行うことによ
り、前記分散液中において、前記微小粒子の疎水性溶液
層から前記疎水性溶剤を除去することによって、前記フ
ィルム形成性重合体壁膜を前記芯物質の周囲に形成させ
ることにより、前記芯物質を内包するカプセル体を製造
する方法において、前記疎水性溶剤を除去する際に、液
面に散水することを特徴とするカプセル体の製造方法。
1. A substance which becomes a core substance is suspended in a hydrophobic solution obtained by dissolving a film-forming polymer in a hydrophobic solvent, and the resulting suspension is water or a medium containing water as a main component. In the dispersion liquid, by forming a hydrophobic solution microparticles encapsulating the core substance by dispersing it in the form of microdroplets, and then performing heating operation and / or gas blowing operation under normal pressure or reduced pressure, Producing a capsule body containing the core substance by forming the film-forming polymer wall film around the core substance by removing the hydrophobic solvent from the hydrophobic solution layer of the fine particles. The method for producing a capsule body according to the above method, wherein water is sprayed on the liquid surface when the hydrophobic solvent is removed.
JP1084642A 1989-04-05 1989-04-05 Method for manufacturing capsule body Expired - Lifetime JP2679233B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1084642A JP2679233B2 (en) 1989-04-05 1989-04-05 Method for manufacturing capsule body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1084642A JP2679233B2 (en) 1989-04-05 1989-04-05 Method for manufacturing capsule body

Publications (2)

Publication Number Publication Date
JPH02265642A JPH02265642A (en) 1990-10-30
JP2679233B2 true JP2679233B2 (en) 1997-11-19

Family

ID=13836348

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2679233B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100537952B1 (en) * 2001-04-13 2005-12-21 주식회사 태평양 Hollow type microcapsule made of hydrophobic polymer and preparation method thereof, and cosmetic compositions containing the microcapsule
WO2004058844A1 (en) * 2002-12-25 2004-07-15 E-Tec Co., Ltd. Resin particle, resin microcapsule, and methods for producing them
CN103387691B (en) * 2012-05-08 2015-08-26 中国石油化工股份有限公司 A kind of hollow polystyrene plastic pellet and its preparation method and application
CN102886232A (en) * 2012-10-19 2013-01-23 上海纳米技术及应用国家工程研究中心有限公司 Device for preparing polymer microsphere with controllable grain size and method thereof

Also Published As

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