JPS6365945A - Preparation of microcapsule - Google Patents

Preparation of microcapsule

Info

Publication number
JPS6365945A
JPS6365945A JP20798886A JP20798886A JPS6365945A JP S6365945 A JPS6365945 A JP S6365945A JP 20798886 A JP20798886 A JP 20798886A JP 20798886 A JP20798886 A JP 20798886A JP S6365945 A JPS6365945 A JP S6365945A
Authority
JP
Japan
Prior art keywords
water
phase separation
microcapsules
producing microcapsules
soluble
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
JP20798886A
Other languages
Japanese (ja)
Inventor
Masayoshi Kasai
笠井 正義
Takayuki Owaki
孝行 大脇
Mitsuru Tanaka
充 田中
Yasuo Miyake
康夫 三宅
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.)
Eisai Co Ltd
Original Assignee
Eisai 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 Eisai Co Ltd filed Critical Eisai Co Ltd
Priority to JP20798886A priority Critical patent/JPS6365945A/en
Publication of JPS6365945A publication Critical patent/JPS6365945A/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
    • B01J13/06Making microcapsules or microballoons by phase separation

Landscapes

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

Abstract

PURPOSE:To prepare a microcapsule within a short time by simple operation, by coating a hardly water-soluble substance with sugar fatty acid ester or lecithin and subsequently adding an inducing agent for phase separation to the coated one. CONSTITUTION:After a hardly water-soluble substance is preliminarily coated with sugar fatty acid ester or lecithin, an inducing agent for phase separation is added to the coated one to prepare the microcapsule of the hardly water-soluble substance by the phase separation of a film forming polymer composition. As the film forming polymer composition, there are gelatin, dextrane and a nonionic cellulose derivative etc. As the inducing agent for phase separation, there are Meglumine(R), alginine, lysine, hystidine, leucine, a water-soluble dye, etc., and, as the water-soluble dye, erythrosine, Tartrazine, Sunset Yellow, Brilliant Blue, etc., are pref.

Description

【発明の詳細な説明】 (1)産業上の利用分野 本発明は水難溶性物質を芯物質とするマイクロカプセル
の製造方法に関する。従って本発明は医薬品9食品、製
紙、写真用フィルムの各分野において利用することがで
きるが、とりわけ油状物質の粉末化、不安定物質の経時
的安定化、物質の味。
DETAILED DESCRIPTION OF THE INVENTION (1) Field of Industrial Application The present invention relates to a method for producing microcapsules whose core material is a poorly water-soluble substance. Therefore, the present invention can be used in the fields of pharmaceuticals, foods, paper manufacturing, and photographic films, but is particularly applicable to the pulverization of oily substances, the stabilization of unstable substances over time, and the taste of substances.

臭の隠蔽化に有効であり、かつ生体に対し安全性の高い
物質のみを使用するので、医薬品の分野において特に利
用される。
It is particularly useful in the pharmaceutical field because it is effective in masking odors and uses only substances that are highly safe for living organisms.

(2)従来技術と問題点 マイクロカプセルの製造については、従来から多数の方
法が提供されてきた。最も多用されてきた方法はいわゆ
る相分離法であり1例えばマイクロカプセルの皮膜とな
る物質を無機塩類やエタノールの添加あるいはpH調整
により芯物質のまわりに相分離させる方法がしばしば採
用されてきた。
(2) Prior Art and Problems Many methods have been proposed for the production of microcapsules. The most commonly used method is the so-called phase separation method.1 For example, a method in which a material that forms the film of a microcapsule is phase-separated around a core material by adding inorganic salts or ethanol or by adjusting the pH has often been adopted.

また低沸点溶媒に水不溶性高分子を溶解しておき加熱蒸
発によって芯物質表面に強制的に析出させるとか、ある
いは温度を変化調節して溶解度を減少させ、芯物質表面
に析出させ、それぞれ皮膜化させる方法もあり2時には
採用されてきた。しかしこれらの従来方法にはそれぞれ
に困雑な問題点が知られている。最も大きな問題点は操
作が複雑で熟練を要することである。例えば、従来の相
分離法では相分離を長時間をかけて徐々に完成させる必
要があり、その成否は操作者の熟練に負う所が大きく1
条件設定の不備によりカプセル同志が粘着凝集する失敗
に至る。また皮膜を硬化させるためにホルムアルデヒド
等を添加しなければならないが、完成品から余剰のホル
ムアルデヒドを完全に除去することが困難であり、特に
相分離マイクロカプセルを医薬品や食品の分野で利用す
る場合に問題点となる。これはジクロロエタンやシクロ
ヘキサン等の低沸点溶媒を使用する方法の場合にも同様
の問題点として起る。すなわち加熱による溶媒除去や冷
却による溶解度低下の操作自体が複雑で時間のかかる操
作であり、操作者の高度の熟練を必要とするが、同時に
残留溶媒を完全に除去することは困難であり、医薬品や
食品の分野では大きな問題点となる。
Alternatively, a water-insoluble polymer can be dissolved in a low-boiling point solvent and forced to precipitate on the surface of the core material by heating and evaporating, or the solubility can be decreased by adjusting the temperature and precipitated on the surface of the core material, forming a film. There is also a method of setting the clock to 2:00, which has been used. However, each of these conventional methods is known to have its own troublesome problems. The biggest problem is that the operation is complicated and requires skill. For example, in conventional phase separation methods, it is necessary to gradually complete phase separation over a long period of time, and its success or failure largely depends on the skill of the operator.
Inadequate setting of conditions led to a failure in which the capsules adhered to each other and agglomerated together. In addition, formaldehyde must be added to harden the film, but it is difficult to completely remove excess formaldehyde from the finished product, especially when phase-separated microcapsules are used in the pharmaceutical and food fields. This becomes a problem. This problem also occurs in methods using low boiling point solvents such as dichloroethane and cyclohexane. In other words, the operations of removing solvent by heating and reducing solubility by cooling are complex and time-consuming operations that require a high level of skill on the part of the operator. This is a major problem in the food and food industries.

(3)問題点を解決するための手段 上記した問題点にかんがみ9本発明者は特別な熟練も必
要とせずに単純簡便な操作によって相分離マイクロカプ
セルを瞬時に調製することのできる技術の開発を目的と
して種々の検討を行った。
(3) Means for Solving the Problems In view of the above-mentioned problems9, the present inventors have developed a technique that allows phase-separated microcapsules to be instantly prepared by simple and convenient operations without requiring any special skill. Various studies were conducted with this aim.

その結果、意外にも芯物質である水難溶性物質をあらか
じめショ糖脂肪酸エステルあるいはレシチンによって被
覆しておくだけで所期の目的が達成されることを見出し
2本発明を完成するに至っ總以下に本発明の詳細な説明
する。
As a result, they unexpectedly discovered that the intended purpose could be achieved simply by coating the core substance, which is a poorly water-soluble substance, with sucrose fatty acid ester or lecithin in advance.2 This led to the completion of the present invention. The present invention will be described in detail.

本発明が解決しようとする対象は水難溶性物質の相分離
マイクロカプセルである。水1溶性物質とは水に任意の
割合で混和しない、あるいは溶解しない物質を言い、固
体状、半固体状、液体状のいづれであってもよく1例え
ばビタミンA、 D、 E。
The object to be solved by the present invention is phase-separated microcapsules for poorly water-soluble substances. A water-soluble substance refers to a substance that does not mix or dissolve in water in any proportion, and may be in solid, semi-solid, or liquid form, such as vitamins A, D, and E.

K等の脂溶性ビタミン類、水難溶性ビタミン類。Fat-soluble vitamins such as K, poorly water-soluble vitamins.

動物油、植物油、鉱物油2合成油などをあげることがで
きる。
Examples include animal oil, vegetable oil, mineral oil, 2 synthetic oils, etc.

相分離とは高分子溶液やコロイド電解質溶液のごとき親
液コロイド溶液が条件の変化によりコロイドに富む液相
とコロイドに乏しい液相との二つの液相に分離する現象
を言い、いわゆるコアセルベーションとも言われ、マイ
クロカプセルを製造するための一つの手段として利用さ
れる。本発明における相分離は本発明に係る皮膜形成性
高分子組成物のコロイド溶液が誘起剤の添加によりコロ
イドに富む液相とコロイドに乏しい液相とに分離する現
象を言い、相分離後コロイドに富む液相(コアセルベー
ト)は水難溶性物質の周囲に堆漬し2次第に水分を失っ
て皮膜となり、マイクロカプセルを形成するに至る。本
発明においてマイクロカプセルは平均直径が50〜10
0ミクロンの球形または紡錐形の粒子として得られるが
、平均直径は任意に調節することができる。
Phase separation is a phenomenon in which a lyophilic colloid solution such as a polymer solution or a colloidal electrolyte solution separates into two liquid phases, a colloid-rich liquid phase and a colloid-poor liquid phase, due to changes in conditions, and is called coacervation. Also called microcapsules, it is used as a means for manufacturing microcapsules. Phase separation in the present invention refers to a phenomenon in which a colloidal solution of the film-forming polymer composition according to the present invention separates into a colloid-rich liquid phase and a colloid-poor liquid phase by the addition of an inducing agent. The rich liquid phase (coacervate) is deposited around the poorly water-soluble substance and gradually loses water to form a film, leading to the formation of microcapsules. In the present invention, the microcapsules have an average diameter of 50 to 10
It is obtained as spherical or cone-shaped particles of 0 micron, but the average diameter can be adjusted arbitrarily.

皮膜形成性高分子組成物とは相分離により皮膜を形成す
るに至る一以上の高分子からなる組成物を8い、該高分
子としては例えば、ゼラチン、カゼイン、フィブリノー
ゲンのごときポリペブタイド、デキストラン、アラビヤ
ゴム、キト酸のごとキ多糖類1  ヒドロキシプロピル
メチルセルロース。
A film-forming polymer composition refers to a composition consisting of one or more polymers that form a film through phase separation, and examples of such polymers include gelatin, casein, polypeptides such as fibrinogen, dextran, and gum arabic. , chitic acid, chipolysaccharide 1, hydroxypropyl methylcellulose.

ヒドロキシプロピルセルロース、メチルセルロースのご
とき非イオン性セルロース誘導体を挙げることができる
。例えばゼラチン、デキストラン。
Nonionic cellulose derivatives such as hydroxypropylcellulose and methylcellulose can be mentioned. For example, gelatin, dextran.

ヒドロキシプロピルメチルセルロースの組合わせは好ま
しい組成物の一つであり、この場合に組成比はゼラチン
1重量部に対しデキストランおよびヒドロキシメチルセ
ルロースはそれぞれ1〜4重量部が適当であり、また相
分離をさせるにあたっての組成物の水溶液中の濃度は2
〜20%W/Vが適当であり、特に4〜1α’N/Vが
好ましい。
The combination of hydroxypropyl methylcellulose is one of the preferred compositions, and in this case, the appropriate composition ratio is 1 to 4 parts by weight each of dextran and hydroxymethylcellulose to 1 part by weight of gelatin. The concentration of the composition in an aqueous solution is 2
~20% W/V is appropriate, and 4-1α'N/V is particularly preferred.

しかし本発明はこれらの組成比および濃度に限定される
ことはな(2選択した高分子の種類によって適宜に決定
すればよい。
However, the present invention is not limited to these composition ratios and concentrations (2) They may be appropriately determined depending on the type of selected polymer.

組成物水溶液の調製は組成物を構成する各高分子を個別
に水に溶解してから混合すればよいが。
The composition aqueous solution may be prepared by individually dissolving each polymer constituting the composition in water and then mixing them.

これに限定されない。It is not limited to this.

本発明の特徴は水難溶性物質をショ糖脂肪酸エステルま
たはレシチンによって被覆してから、相分離のための誘
起剤を添加することにある。ここでショ糖脂肪酸エステ
ルは一般にシュガーエステルの名称で市販されているも
のを入手して使用すればよい。シュガーエステルの種類
については特に限定はないが2例えばシュガーエステル
S−970(リョウトウ産業)が好ましい。レシチンに
ついても特に限定はな(、大豆レシチン、卵黄レシチン
およびそれらの水添レシチンを適宜に選択して使用すれ
ばよい。ショ糖脂肪酸エステルおよびレシチンを組合せ
て使用してもよい。使用量は水難溶性物質1重量部に対
して0.1〜1重量部が適当であるが、目的とするマイ
クロカプセルの粒径あるいは水難溶性物質が固体、半固
体、液体のいづれの状態であるかに応じて、要は水難溶
性物質が(まなく被覆されるのに必要な量を決定すれば
よく9本発明はこの使用量によって限定されない。
A feature of the present invention is that a poorly water-soluble substance is coated with sucrose fatty acid ester or lecithin, and then an inducer for phase separation is added. Here, as the sucrose fatty acid ester, those commercially available under the name of sugar ester may be obtained and used. The type of sugar ester is not particularly limited, but for example, Sugar Ester S-970 (Ryoto Sangyo) is preferred. There are no particular limitations on lecithin (soybean lecithin, egg yolk lecithin, and their hydrogenated lecithins may be selected and used as appropriate. Sucrose fatty acid esters and lecithin may be used in combination. The amount used is determined by water standards. The appropriate amount is 0.1 to 1 part by weight per 1 part by weight of the soluble substance, but it depends on the particle size of the target microcapsules or whether the poorly water-soluble substance is in a solid, semi-solid, or liquid state. In short, it is only necessary to determine the amount necessary to completely coat the poorly water-soluble substance (9) The present invention is not limited by this amount.

被覆には例えば次のような方法が推奨される。まず少量
の水またはエタノールにショ糖脂肪酸エステルまたはレ
シチンを加温溶解し、この中に水難溶性物質を分散また
は溶解してお(。次に水を激しく撹拌しながら、この水
中に上記によってあらかじめ調製しておいた液を徐々に
投入する。これにより水難溶性物質の分散粒の周囲にシ
ョ糖脂肪酸エステルまたはレシチンの被覆が完成する。
For example, the following methods are recommended for coating. First, warm and dissolve sucrose fatty acid ester or lecithin in a small amount of water or ethanol, and disperse or dissolve the poorly water-soluble substance therein.Next, while vigorously stirring the water, add the previously prepared Gradually pour in the solution that has been prepared.This completes the coating of the sucrose fatty acid ester or lecithin around the dispersed particles of the poorly water-soluble substance.

従って例えば皮膜形成性高分子組成物の水溶液を激しく
撹拌しながら、この中にあらかじめ調製しておいた液を
徐々に投入すればよい。しかしこれは本発明の好ましい
態様例を示したにすぎない。次に相分離のための誘起剤
はコロイドの凝結剤、沈澱剤として一般に公知の物質を
入手して使用すればよいが2本発明においては例えばメ
グルミン。
Therefore, for example, while vigorously stirring an aqueous solution of a film-forming polymer composition, a previously prepared solution may be gradually poured into the solution. However, this is merely an example of a preferred embodiment of the invention. Next, as an inducer for phase separation, any substance generally known as a coagulant or precipitant for colloids may be obtained and used. In the present invention, for example, meglumine is used.

アルギニン、リジン、ヒスチジン、ロイシン、イソロイ
シン、バリンを挙げることができる。また意外にもエリ
スロシン、タートラジン、サンセットイエロー、ブリリ
アントブルーのごとき水溶性色素も本発明の誘起剤とし
て機能することが判った。さらにこの場合にはこれら色
素による遮光性着色マイクロカプセルが得られる。誘起
剤の添加量は少量でよく、具体的には誘起剤の水溶液を
あらかじめ用意しておき、すでにショ糖脂肪酸エステル
またはレシチンの被覆が完成している液をゆる(撹拌し
ながら、この中に徐々に滴下し、顕微鏡で相分離の進行
を観察しながら、所定の相分離が完成するのに必要な量
を加えればよい。従って誘起剤の添加量および添加方法
は状況に応じて適宜に定めて行なえばよい。多(の場合
に相分離は5〜15分程度の短時間で完成し、操作は単
純簡便で特別の熟練を要しない。なお相分離が完成した
直後の段階で液温を20〜30℃に保ち2例えばヒドロ
キシプロピルメチルセルロースフタレートやアルミニウ
ムレーキ色素を微粉末のまま、あるいは水懸濁液として
投入すると、これらの物質が直ちにコアセルベート表面
に付着し、さらに内部にとりこまれる。この結果、ヒド
ロキシプロピルメチルセルロースフタレートによる腸溶
性マイクロカプセルやアルミニウムレーキ色素による遮
光性着色マイクロカプセルが得られる。これらは本発明
に付加された技術であり、これによって本発明は限定さ
れない。
Mention may be made of arginine, lysine, histidine, leucine, isoleucine, and valine. It has also surprisingly been found that water-soluble dyes such as erythrosine, tartrazine, sunset yellow, and brilliant blue also function as inducers in the present invention. Furthermore, in this case, light-shielding colored microcapsules can be obtained using these dyes. The amount of the inducing agent to be added can be small. Specifically, prepare an aqueous solution of the inducing agent in advance, and add the solution already coated with sucrose fatty acid ester or lecithin (with stirring) into the solution. While gradually dropping the inducer and observing the progress of phase separation using a microscope, add the amount necessary to complete the desired phase separation.Therefore, the amount and method of addition of the inducer should be determined as appropriate depending on the situation. Phase separation can be completed in a short time of about 5 to 15 minutes in the case of multi-phase separation, and the operation is simple and easy and does not require any special skill. When the temperature is maintained at 20 to 30°C and 2, for example, hydroxypropyl methyl cellulose phthalate or aluminum lake pigment is introduced as a fine powder or as a water suspension, these substances immediately adhere to the coacervate surface and are further incorporated into the interior. Enteric-coated microcapsules made of hydroxypropyl methylcellulose phthalate and light-shielding colored microcapsules made of aluminum lake dye are obtained.These are techniques added to the present invention, and the present invention is not limited thereby.

最後にマイクロカプセル化の終了した分散液を冷却し、
マイクロカプセルを分離し、水H50、’0エタノール
水、無水エタノールの順序で洗浄し、冷風乾燥してマイ
クロカプセルを単離する。あるいは冷却後にマイクロカ
プセルを含有したまま噴霧乾燥や流動層造粒乾燥にかけ
てマイクロカプセルを取り出してもよい。
Finally, the microencapsulated dispersion is cooled,
The microcapsules are separated, washed with H50 water, '0 ethanol water, and absolute ethanol in this order, and dried with cold air to isolate the microcapsules. Alternatively, after cooling, the microcapsules may be taken out by spray drying or fluidized bed granulation drying while still containing the microcapsules.

(4)作用 従来技術に比べ2本発明方法によれば短時間で。(4) Effect Compared to the prior art, the method of the present invention takes a shorter time.

単純簡便な操作により、特別の熟練を要せずにマイクロ
カプセルを製造することができ、得られたマイクロカプ
セルはマイクロカプセルが一般的に有している諸作用2
例えば油状物質の粉末化、不安定物質の経時的安定化、
物質の味、臭の隠蔽化の諸作用を有する。また本発明方
法においては生体に対して安全性の高い物質のみを使用
し2例えばボルムアルデヒドのごとき毒性のある架橋剤
を使用しないので、医薬品の分野において有利に使用す
ることができる。また本発明方法によって得られるマイ
クロカプセルは相分離のための誘起剤として水溶性色素
を使用することにより、あるいは相分離が完成した直後
の段階でアルミニウムレーキ色素を添加することによっ
て、それぞれ容易に遮光性着色マイクロカプセルとする
ことができ。
Microcapsules can be produced by simple and easy operations without requiring special skill, and the resulting microcapsules have various functions that microcapsules generally have.
For example, turning oily substances into powder, stabilizing unstable substances over time,
It has the effect of masking the taste and odor of substances. Furthermore, the method of the present invention uses only substances that are highly safe for living organisms and does not use toxic crosslinking agents such as bomaldehyde, so it can be advantageously used in the pharmaceutical field. Furthermore, the microcapsules obtained by the method of the present invention can be easily shielded from light by using a water-soluble dye as an inducer for phase separation, or by adding an aluminum lake dye immediately after phase separation is completed. Can be colored microcapsules.

光に対し不安定な物質を安定化することができる。It can stabilize substances that are unstable to light.

(5)実施例 以下に記載する実施例によって本発明を具体的に説明す
る。
(5) Examples The present invention will be specifically explained by the examples described below.

実施例1 エタノール5rnlにシュガーエステルS−970(リ
ョウトウ産業)0.5#およびビタミンEアセテート2
.51Iを50℃で溶解させた。他方、水9Q miに
ヒドロキシプロピルメチルセルロース5.1よびデキス
トラン(分子i 40000 ) 5.9を溶解した溶
液と水20 mlにゼラチン2gを溶解した溶液とを混
合し。
Example 1 Sugar ester S-970 (Ryoto Sangyo) 0.5 # and vitamin E acetate 2 in 5 rnl of ethanol
.. 51I was dissolved at 50°C. On the other hand, a solution of 5.1 hydroxypropyl methyl cellulose and 5.9 of dextran (molecules i 40000) dissolved in 9 Q mi of water was mixed with a solution of 2 g of gelatin dissolved in 20 ml of water.

40℃に保持しながら激しく撹拌した。ここに前記ビタ
ミンEアセテート液を徐々に滴下した。山内状態となり
1〜50ミクロンの油滴の表面をシュガーエステルが被
覆している状態が観察された。
The mixture was stirred vigorously while maintaining the temperature at 40°C. The vitamin E acetate solution was gradually dropped therein. It was observed that the surface of oil droplets with a size of 1 to 50 microns was coated with sugar ester.

次にゆるく撹拌しながら5%メグルミン溶液2mlを徐
々に添加し、顕微鏡で相分離の進行を観察した。約10
分で完成し球形ないし紡錐形のマイクロカプセルが形成
した。次に28℃に冷却し、水5 mlにヒドロキシプ
ロピルメチルセルロースフタレート0.5.!i’を懸
濁した液を添加した。7°Cに冷却し、マイクロカプセ
ルを分離して冷水100〃+/ 。
Next, 2 ml of 5% meglumine solution was gradually added while stirring gently, and the progress of phase separation was observed using a microscope. about 10
The process was completed within minutes, and spherical or spindle-shaped microcapsules were formed. Next, it was cooled to 28°C, and 0.5% of hydroxypropyl methyl cellulose phthalate was added to 5 ml of water. ! A suspension of i' was added. Cool to 7°C, separate the microcapsules, and wash with cold water at 100°C.

50 ”6 工9 /−ル水50rnl、無水エタ/ 
−ル5Qmlで洗浄し、冷風乾燥して平均直径50ミク
ロンのマイクロカプセルからなる細粒粉末を得た。
50 ”6 engineering 9/-le water 50rnl, anhydrous eta/
The microcapsules were washed with 5 Q ml of water and dried with cold air to obtain a fine powder consisting of microcapsules with an average diameter of 50 microns.

実施例2 水100 miにシュガーエステルS−970(リョウ
トウ産業)0.5gを80℃で溶解し、ビタミンEアセ
テ−)2.!M/を添加して分散した。以下の操作を実
施例1記載と同様に行ない、平均直径50ミクロンのマ
イクロカプセルからなる細粒粉末を得た。
Example 2 0.5g of Sugar Ester S-970 (Ryoto Sangyo) was dissolved in 100ml of water at 80°C, and vitamin E acetate)2. ! M/ was added and dispersed. The following operations were carried out in the same manner as described in Example 1 to obtain fine powder consisting of microcapsules with an average diameter of 50 microns.

実施例3 ビタミンEアセテートの代わりにビタミンB2を使用し
て実施例1記載と同様に行ない、平均直径20ミクロン
のマイクロカプセルからなる粉末を得た。
Example 3 The same procedure as described in Example 1 was carried out using vitamin B2 instead of vitamin E acetate to obtain a powder consisting of microcapsules with an average diameter of 20 microns.

実施例4 ビタミンEアセテートの代わりにビタミンに、を使用し
て実施例1記載と同様に行ない、平均直径100ミクロ
ンのマイクロカプセルからなる細粒粉末を得た。
Example 4 The same procedure as described in Example 1 was carried out using vitamin E acetate instead of vitamin A to obtain fine powder consisting of microcapsules with an average diameter of 100 microns.

実施例5 実施例1において5%メグルミン溶液2mlの代わりに
596アルギニン溶液2mlを使用した点を除いて実施
例1記載と同様に行ない、平均直径50ミクロンのマイ
クロカプセルからなる細粒粉末を得た。
Example 5 The same procedure as described in Example 1 was carried out except that 2 ml of 596 arginine solution was used instead of 2 ml of 5% meglumine solution in Example 1, to obtain fine powder consisting of microcapsules with an average diameter of 50 microns. .

実施例6 実施例4において5%メグルミン溶液2mトの代わりに
5%タートラジン溶液IQmJを使用した点を除いて実
施例1記載と同様に行ない、平均直径70ミクロンのマ
イクロカプセルからなる細粒粉末を得た。
Example 6 The same procedure as described in Example 1 was carried out except that 5% tartrazine solution IQmJ was used instead of 2 m of 5% meglumine solution in Example 4, and a fine powder consisting of microcapsules with an average diameter of 70 microns was prepared. Obtained.

実施例7 実3m例1においてシュガーエステルS−970の代わ
りに大豆レシチンを使用した点を除いて実施例1記載と
同様に行ない、平均直径50ミクロンのマイクロカプセ
ルからなる細粒粉末を得た。
Example 7 Example 3 The same procedure as described in Example 1 was repeated except that soybean lecithin was used instead of sugar ester S-970 in Example 1 to obtain a fine powder consisting of microcapsules with an average diameter of 50 microns.

実施例8 実施例1においてヒドロキシプロピルメチルセルロース
5gの代わりにメチルセルロース1gを使用した点を除
いて実施例1記載と同様に行ない。
Example 8 The same procedure as described in Example 1 was carried out except that 1 g of methyl cellulose was used instead of 5 g of hydroxypropyl methyl cellulose.

平均直径50ミクロンのマイクロカプセルからなる細粒
粉末を得た。
A fine powder consisting of microcapsules with an average diameter of 50 microns was obtained.

(6)発明の効果 実験例1 実施例1においてシュガーエステルS−970を使用し
ない点を除いて実施例1記載と同様に行った。
(6) Effect of the Invention Experimental Example 1 The same procedure as described in Example 1 was conducted except that sugar ester S-970 was not used in Example 1.

その結果、ビタミンEアセテートの油滴の周囲にコアセ
ルベートが堆積されず、マイクロカプセルが形成されな
かった。実施例1においてはマイクロカプセルが形成さ
れたことと対比すると、あらかじめシュガーエステルS
−970によって被覆することが必須であることが判明
した。
As a result, coacervate was not deposited around the vitamin E acetate oil droplets, and no microcapsules were formed. In contrast to the formation of microcapsules in Example 1, sugar ester S
-970 was found to be essential.

実験例2 試料と方法 表1記載の仕込処方(重量比)による三種類のマイクロ
カプセルを本発明方法によって製造し。
Experimental Example 2 Samples and Methods Three types of microcapsules were produced according to the formulation (weight ratio) shown in Table 1 by the method of the present invention.

試料1〜3として用意した。試料1は非着色マイクロカ
プセル、試料2.試料3は着色マイクロカプセルである
。各試料に1000ルツクスの光を照射し、経日的にビ
タミンに、含意を測定し、残存率を求めた。なお、ビタ
ミンに2の測定はUnisel QC18カラムを用い
る高速液体クロマト法で行ない。
Samples 1 to 3 were prepared. Sample 1 is non-colored microcapsule, sample 2. Sample 3 is a colored microcapsule. Each sample was irradiated with 1000 lux light, and the vitamin content was measured over time to determine the residual rate. Note that the measurement of vitamin 2 was performed by high performance liquid chromatography using a Unisel QC18 column.

吸光波長248 nmでのピークの高さより試料100
=中のビタミンに2含量を求めた。
Sample 100 from the peak height at absorption wavelength 248 nm
= The content of 2 vitamins in it was determined.

表1 試料1 試料2 試料3 ビタミ7に、       1   1   1ゼラチ
ン      2  2  2 シユガーエステル  0.25 0.25  0.25
メグルミン     o、os   −o、osエリス
ロシン     −0,08− 結果 結果を図1に示す。図中・印線、Δ印線、○印線はそれ
ぞれ試料1.試料2.試料3の結果を示す。図1より本
発明方法によって得られるマイクロカプセルは相分離の
ための誘起剤として水溶性色素を使用することにより、
あるいは相分離が完成した直後の段階でアルミニウムレ
ーキ色素を添加することlこよってそれぞれ容易に遮光
性着色マイクロカプセルとすることができ、光に対して
不安定な物質を安定化することができることが判明する
Table 1 Sample 1 Sample 2 Sample 3 Vitamin 7, 1 1 1 Gelatin 2 2 2 Sugar ester 0.25 0.25 0.25
Meglumine o, os -o, os erythrosin -0,08- Results The results are shown in Figure 1. In the figure, the marked lines, Δ marked lines, and ○ marked lines are for sample 1. Sample 2. The results of sample 3 are shown. From Figure 1, the microcapsules obtained by the method of the present invention can be obtained by using a water-soluble dye as an inducer for phase separation.
Alternatively, it is possible to add an aluminum lake dye immediately after phase separation is completed, thereby easily forming light-shielding colored microcapsules and stabilizing substances that are unstable to light. Prove.

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

図1はマイクロカプセルに対する光照射の実験結果であ
り、照射時間と残存率の関係を示すグラフである。
FIG. 1 shows the experimental results of light irradiation on microcapsules, and is a graph showing the relationship between irradiation time and survival rate.

Claims (7)

【特許請求の範囲】[Claims] (1)皮膜形成性高分子組成物の相分離によって水難溶
性物質のマイクロカプセルを製造するにあたり、あらか
じめ当該水難溶性物質をショ糖脂肪酸エステルまたはレ
シチンによって被覆してから、当該相分離のための誘起
剤を添加することを特徴とするマイクロカプセルの製造
方法
(1) When producing microcapsules of a poorly water-soluble substance by phase separation of a film-forming polymer composition, the poorly water-soluble substance is coated in advance with sucrose fatty acid ester or lecithin, and then induced for phase separation. A method for producing microcapsules characterized by adding an agent
(2)皮膜形成性高分子組成物がゼラチンを主成分とす
る組成物である特許請求の範囲第1項記載のマイクロカ
プセルの製造方法
(2) The method for producing microcapsules according to claim 1, wherein the film-forming polymer composition is a composition containing gelatin as a main component.
(3)皮膜形成性高分子組成物がゼラチン、デキストラ
ン、非イオン性セルロース誘導体からなる組成物である
特許請求の範囲第1項記載のマイクロカプセルの製造方
(3) The method for producing microcapsules according to claim 1, wherein the film-forming polymer composition is a composition comprising gelatin, dextran, and a nonionic cellulose derivative.
(4)非イオン性セルロース誘導体がヒドロキシプロピ
ルメチルセルロースまたはメチルセルロースである特許
請求の範囲第3項記載のマイクロカプセルの製造方法
(4) The method for producing microcapsules according to claim 3, wherein the nonionic cellulose derivative is hydroxypropylmethylcellulose or methylcellulose.
(5)誘起剤がメグルミン、アルギニン、リジン、ヒス
チジン、ロイシン、イソロイシン、バリンのいづれかで
ある特許請求の範囲第1項ないし第4項記載のマイクロ
カプセルの製造方法
(5) The method for producing microcapsules according to claims 1 to 4, wherein the inducer is any one of meglumine, arginine, lysine, histidine, leucine, isoleucine, and valine.
(6)誘起剤が水溶性色素である特許請求の範囲第1項
ないし第4項記載のマイクロカプセルの製造方法
(6) The method for producing microcapsules according to claims 1 to 4, wherein the inducing agent is a water-soluble dye.
(7)水溶性色素がエリスロシン、タートラジン、サン
セットイエロー、ブリリアントブルーのいづれかである
特許請求の範囲第6項記載のマイクロカプセルの製造方
(7) The method for producing microcapsules according to claim 6, wherein the water-soluble dye is any one of erythrosine, tartrazine, sunset yellow, and brilliant blue.
JP20798886A 1986-09-05 1986-09-05 Preparation of microcapsule Pending JPS6365945A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20798886A JPS6365945A (en) 1986-09-05 1986-09-05 Preparation of microcapsule

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20798886A JPS6365945A (en) 1986-09-05 1986-09-05 Preparation of microcapsule

Publications (1)

Publication Number Publication Date
JPS6365945A true JPS6365945A (en) 1988-03-24

Family

ID=16548820

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20798886A Pending JPS6365945A (en) 1986-09-05 1986-09-05 Preparation of microcapsule

Country Status (1)

Country Link
JP (1) JPS6365945A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0350246A2 (en) * 1988-07-05 1990-01-10 Takeda Chemical Industries, Ltd. Sustained release microcapsule for water soluble drug
JPH0753356A (en) * 1993-08-16 1995-02-28 Morishita Jintan Kk Seamless capsule containing easily oxidizable oily substance and its production
JPH10502621A (en) * 1994-07-01 1998-03-10 エフ・ホフマン−ラ ロシユ アーゲー Multiple microencapsulation of lipophilic substances
JP2003508195A (en) * 1999-08-27 2003-03-04 メーヌラブ Method for encapsulating active substances by coacervation of polymer in non-chlorinated organic solvents
JP2004075582A (en) * 2002-08-13 2004-03-11 Takeda Chem Ind Ltd Method for stabilizing ingredient other than active ingredient prescribed in solid pharmaceutical composition
JP2013519499A (en) * 2010-02-15 2013-05-30 ネステク ソシエテ アノニム Liquid-filled protein-phosphatidic acid capsule dispersion
JP2013519518A (en) * 2010-02-18 2013-05-30 ネステク ソシエテ アノニム Dispersion of liquid filled chitosan-anionic lipophilic surfactant capsules
KR20160148028A (en) * 2014-05-05 2016-12-23 바스프 에스이 Formulation of fat-soluble vitamin

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5858146A (en) * 1981-10-05 1983-04-06 Tanabe Seiyaku Co Ltd Microcapsule with fast releasability and preparation thereof

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5858146A (en) * 1981-10-05 1983-04-06 Tanabe Seiyaku Co Ltd Microcapsule with fast releasability and preparation thereof

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0350246A2 (en) * 1988-07-05 1990-01-10 Takeda Chemical Industries, Ltd. Sustained release microcapsule for water soluble drug
JPH0753356A (en) * 1993-08-16 1995-02-28 Morishita Jintan Kk Seamless capsule containing easily oxidizable oily substance and its production
JPH10502621A (en) * 1994-07-01 1998-03-10 エフ・ホフマン−ラ ロシユ アーゲー Multiple microencapsulation of lipophilic substances
JP2003508195A (en) * 1999-08-27 2003-03-04 メーヌラブ Method for encapsulating active substances by coacervation of polymer in non-chlorinated organic solvents
JP2004075582A (en) * 2002-08-13 2004-03-11 Takeda Chem Ind Ltd Method for stabilizing ingredient other than active ingredient prescribed in solid pharmaceutical composition
JP2013519499A (en) * 2010-02-15 2013-05-30 ネステク ソシエテ アノニム Liquid-filled protein-phosphatidic acid capsule dispersion
JP2013519518A (en) * 2010-02-18 2013-05-30 ネステク ソシエテ アノニム Dispersion of liquid filled chitosan-anionic lipophilic surfactant capsules
KR20160148028A (en) * 2014-05-05 2016-12-23 바스프 에스이 Formulation of fat-soluble vitamin
JP2017521359A (en) * 2014-05-05 2017-08-03 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se Fat-soluble vitamin preparation
US11090276B2 (en) 2014-05-05 2021-08-17 Basf Se Formulation of fat-soluble vitamin

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