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JPH0529204B2 - - Google Patents
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JPH0529204B2 - - Google Patents

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Publication number
JPH0529204B2
JPH0529204B2 JP29568985A JP29568985A JPH0529204B2 JP H0529204 B2 JPH0529204 B2 JP H0529204B2 JP 29568985 A JP29568985 A JP 29568985A JP 29568985 A JP29568985 A JP 29568985A JP H0529204 B2 JPH0529204 B2 JP H0529204B2
Authority
JP
Japan
Prior art keywords
granules
coating
substance
melting point
coated
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
JP29568985A
Other languages
Japanese (ja)
Other versions
JPS62153213A (en
Inventor
Chikao Haramiishi
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.)
Daiichi Pharmaceutical Co Ltd
Original Assignee
Daiichi Pharmaceutical 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 Daiichi Pharmaceutical Co Ltd filed Critical Daiichi Pharmaceutical Co Ltd
Priority to JP29568985A priority Critical patent/JPS62153213A/en
Publication of JPS62153213A publication Critical patent/JPS62153213A/en
Publication of JPH0529204B2 publication Critical patent/JPH0529204B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

<産業上の利用分野> 本発明は粉粒状の低融点物質を核として造粒さ
れた粒状物に微粉状の腸溶性コーテイング基剤を
付着させた粒状物に関する。 <従来の技術> 医薬品における腸溶性コーテイングは胃液によ
つて分解する薬物を胃液から保護すること、或は
胃よりも腸での吸収の方が好ましい薬物などでは
その薬効を効率よく発揮させることを目的に、ま
た場合によつては薬物を持続化させるためなどの
製剤的手法としてしばしば用いられる。 一般に腸溶性製剤を得るためのコーテイング方
法としては、腸溶性コーテイング基剤を有機溶媒
に溶解するかもしくは水に分解させて粒状物表面
にスプレーコーテイングを行ない、腸溶性被膜を
施す方法がとられる。しかしながら、有機溶媒を
用いることは、作業者への衛生上の悪影響、環境
汚染及び製剤中への残留など問題点が多く、又エ
タノール等人体にそれほど害のない溶媒を用いる
場合でも防災の面から防爆設備にする必要があ
り、多大の設備費を要する。このため最近では腸
溶性物質を可塑剤とともに水に分散させコーテイ
ングを施す方法が見出され、広く用いられるよう
になつた。しかし、この方法でも水に不安定な薬
物には不適当であり、更には水易溶性の薬物に適
用した場合では薬物がコーテイング液に溶けやす
いためコーテイング時の粒状物同士の付着による
被膜形成不良等の欠点を有する。 一方、腸溶性製剤では、その品質上重要となる
耐胃液性を確保するために多くの被膜剤が必要と
なり又、ピンホールやきれつ等の無いようなち密
な被膜形成性が要求され、これらにともない多大
のコーテイング時間を費やさなければならない。
これが顆粒剤のような粒状物ともなると更に被膜
量は増加し、精密なコーテイング操作が要求され
る。また粒状物では表面の粗さがコーテイング性
に大きな影響を与えるため、コーテイングに適し
た球形で滑らかな表面を持つものが望ましく粒状
物の球形化のための煩雑な操作が必要となる。 <発明が解決しようとする問題点> 本発明者は上記問題点を解決すべく鋭意検討し
た結果、本発明を完成した。 <発明の構成> 本発明は粉粒状の低融点物質を核として造粒さ
れた粒状物に微粉状の腸溶性コーテイング基剤を
付着させた粒状物に関する。 本発明において粉粒状の低融点物質を核として
造粒された粒状物(以下、被コーテイング粒状物
と称す)とは、特開昭58−214333号(以下、引例
と称す)に開示された粒状物、即ち目的とする薬
物の粉体、通常は100μm以下のものと粉粒状の低
融点物質の混合物を流動下加熱し低融点物質の溶
融過程で薬物粉体を低融点物質に付着させて得ら
れる粒状物を意味し、その大きさは一般に20〜40
メツシユのものが使用される。該粒状物は効率よ
く被膜を施すために球状であることが望ましい
が、引例の造粒方法によれば核となる低融点物質
を予め球状にしておけば球状のものを製すること
ができる。 低融点物質としては、その融点が30〜100℃、
好適には50〜80℃であればいかなるものでもよく
例えば、パラフイン、マイクロクリスタリンワツ
クス、セレシンなどの炭化水素類、硬化油、木ロ
ウ、カカオ脂などの油脂類、ミリスチン酸、パル
ミチン酸、ステアリン酸などの脂肪酸類、セタノ
ール、ステアリルアルコールなどの高級アルコー
ル類、マクロゴール6000、マクロゴール4000、バ
チルアルコールなどの多価アルコール類、カルナ
ウバロウ、ミツロウなどのロウ類、パルミチン酸
ヘキサデシル、ステアリン酸オクタデシルなどの
エステル類、ソルビタンモノステアレート、グリ
セリンモノステアレート、アセチル化グリセリン
モノステアレート、プルロニツクF68などの界面
活性剤類もしくはこれらの混合物などが挙げら
れ、又比較的高い融点を有する物質でも二種以上
を混合することにより見掛の融点降下を起し融点
を30〜100℃にしたもの、あるいはイブプロフエ
ン、トリメタジオンなどのように医薬品であつて
もそれ自身が低融点物質であるものは前記の低融
点物質を用いることなく被コーテイング粒状物の
核として利用できる。 次に、腸溶性コーテイング基剤としてはメタア
クリル酸アクリル酸エチルコポリマー、メチルア
クリレートメタアクリル酸コポリマーなどのアク
リル酸系高分子、セルロースアセテートフタレー
ト、カルボキシメチルエチルセルロースなどのセ
ルロース系高分子等をあげることができる。該基
剤の大きさは一般に0.5〜20μm、好ましくは1〜
5μmのものが用いられ、又その使用量は被コーテ
イング粒状物1重量部に対し通常0.05〜0.3重量
部である。 本発明の粒状物は以下の方法により製造するこ
とができる。まず、粒状の低融点物質(球状もし
くは球状にしたものが好ましい)を用いて目的と
する薬物の粉体と、場合によつては適当な賦形剤
とともに流動下、低融点物質の融点以上の温度に
加熱しながら造粒することにより被コーテイング
粒状物を得ることができる。得られた被コーテイ
ング粒状物及び微粉状腸溶性コーテイング基剤
を、場合によつては可塑剤等とともに回転混合機
あるいは糖衣パンに入れ、用いた低融点物質の融
点以上の温度に保持させながら転動させ低融点物
質の溶融過程で被コーテイング粒状物に微粉状腸
溶性コーテイング基剤を付着させたのち、これを
冷却することにより目的とする粒状物を製造する
ことができる。転動速度は一般に1分間あたり30
〜40回転であり、転動時間は通常10〜20分間であ
る。 被コーテイング粒状物に微粉状腸溶性コーテイ
ング基剤を付着させる際に、水に不溶な微粉状物
質例えばステアリン酸カルシウム、ステアリン酸
マグネシウム、タルク、軽質無水ケイ酸、メタケ
イ酸アルミン酸マグネシウム、乳酸カルシウム等
を添加して加温及び転動を行なうと一層スムーズ
に微粉状腸溶性コーテイング基剤を付着させるこ
とができ、かつ製された粒状物の被膜はピンホー
ル及びきれつ等の無いち密なものとなる。添加さ
れる微粉状物質の大きさは一般に0.05〜10μmの
ものが使用される。又、該微粉状物質は微粉状腸
溶性コーテイング基剤1重量部に対し、通常0.01
〜10重量部使用される。 本発明の腸溶性粒状物において腸溶性コーテイ
ング基剤は通常5〜30%(w/w)配合され又、
微粉状物質が添加された場合には該物質は通常1
〜50%(w/w)配合されることが望ましい。 <発明の効果> 本発明の粒状物は、耐胃液性、外観、強度、安
定性等腸溶性製剤として優れた品質を有する。ま
た、その他にも強めて有用な以下の利点を有す
る。 (1) 一般の腸溶性コーテイングに比べて、コーテ
イング液を調整する必要がない上、コーテイン
グ時間が大幅に短縮でき、また複雑な条件設定
を必要とせずしかも簡単な装置によつて収率よ
く製造できるため、低コストで作業効率が極め
た良好である。 (2) 溶媒を用いる必要がないため、安全面、衛生
面、公害面、製剤中への残留などの危険性がな
く、更に主薬の安定性も向上させることができ
る。 (3) 被コーテイング粒状物の製造に使用する低融
点物質として水不溶性のステアリン酸やセタノ
ールなどを用いると腸溶性でしかも放出速度が
コントロールされた粒状物を得ることができ
る。又、微粉状腸溶性物質の選択により溶出の
PHコントロールも可能な粒状物が得られる。 (4) 本発明の粒状物は、そのまま顆粒剤としても
よく、また適宜賦形剤、滑沢剤、崩壊剤等を加
えて打錠すれば錠剤とすることができる。更に
必要により滑沢剤を加えて硬カプセルに充填す
ればカプセル剤とすることもできる。次に、実
施例を挙げて本発明を具体的に説明する。 実施例 1 流動層造粒機(グラツドWSG−5型)に100メ
ツシユ篩で篩下したアデノシン三リン酸二ナトリ
ウム1.0Kg、乳糖2.75Kg及び球状ステアリン酸
(20〜40メツシユ)1.25Kgを入れ、90℃で加熱流
動させながら造粒したのち、12及び40メツシユの
ふるいにて整粒し、被コーテイング粒状物(以
下、素顆粒と称す)を得た。次に目製したジヤケ
ツト付き二重円錐型混合機に該素顆粒2Kgと微粉
砕したオイドラギツトL100(20μm以下Po¨hm
Pharm社製)以下0.3Kg及びタルク0.3Kgを入れ、
75℃の温水をジヤケツト内に循環させながら回転
させ、10分後循環水を冷水に切り替えてステアリ
ン酸の融点以下の温度に冷却し、顆粒を得た。 実施例 2 実施例1と同様にして製したアデノシン三リン
酸二ナトリウム含有素顆粒2Kgと微粉砕したセル
ロースアセテートフタレート0.15Kg及びタルク
0.4Kgを自製したジヤケツト付き二重円錐型混合
機に入れ、実施例1と同様に操作して顆粒を得
た。 実施例 3 流動層造粒機に食用色素青色1号0.05Kg、乳糖
3.0Kg、トウモロコシデンプン0.7Kg及び球状のマ
クロゴール6000(20〜40メツシユ)1.25Kgを入れ、
80℃で加熱流動させながら造粒したのち12及び40
メツシユのふるいにて整粒し、素顆粒を得た。次
に糖衣パンに該素顆粒3Kgと微粉砕したオイドラ
ギツトL100 0.5Kg及びタルク0.25Kgを入れパン側
面に80℃の熱風を当てて試料を加熱させながら
30r.p.mで回転させ、20分後熱風を冷風に冷り替
えマクコロゴール6000の融点以下の温度に冷却
し、顆粒を得た。 試験例 実施例1、2及び3で得られた顆粒について耐
胃液性及び溶出性を検討した。 測定は日局一般試験法の溶出試験法第1法によ
り定められた溶出試験器を用い、第1液にて2時
間の試験を行ない、1時間後及び2時間後に試験
液をサンプリングし、溶出したアデノシン三リン
酸二ナトリウム又は食用色素青色1号の吸光度を
測定し、溶出率を算出した(耐胃液性試験)。次
に試験液を第2液に代えて同一試料について2時
間までの試験を行ない、一定時間毎に試験液をサ
ンプリングし、それぞれの吸光度を測定して溶出
率を算出した(溶出試験)。結果を表−1に示し
た。
<Industrial Application Field> The present invention relates to a granular material in which a finely powdered enteric coating base is adhered to a granular material granulated using a powdery low melting point substance as a core. <Prior art> Enteric coating for pharmaceuticals is used to protect drugs that are degraded by gastric juices from gastric juices, or to efficiently exert their medicinal effects for drugs that are better absorbed in the intestine than in the stomach. It is often used for pharmaceutical purposes, and in some cases as a pharmaceutical technique, such as to prolong the duration of drugs. Generally, the coating method for obtaining enteric-coated preparations involves dissolving an enteric coating base in an organic solvent or decomposing it in water and spray coating the surface of the granular material to form an enteric coating. However, the use of organic solvents has many problems, such as adverse health effects on workers, environmental pollution, and residues in formulations, and even when using solvents that are not harmful to the human body, such as ethanol, there are concerns from the perspective of disaster prevention. Explosion-proof equipment is required, which requires a large amount of equipment cost. For this reason, a method has recently been discovered in which a coating is applied by dispersing an enteric substance together with a plasticizer in water, and this method has become widely used. However, even this method is unsuitable for drugs that are unstable in water, and furthermore, when applied to easily water-soluble drugs, the drug easily dissolves in the coating liquid, resulting in poor film formation due to adhesion of particulates during coating. It has the following disadvantages. On the other hand, enteric-coated preparations require a large amount of coating agent to ensure gastric juice resistance, which is important for quality, and also require the ability to form a dense coating without pinholes or cracks. Therefore, a large amount of coating time must be spent.
When this becomes a particulate material such as granules, the amount of coating increases further, and a precise coating operation is required. In addition, since the surface roughness of granular materials has a great effect on coating properties, it is desirable to have a spherical shape suitable for coating with a smooth surface, but complicated operations are required to make the granular material spherical. <Problems to be Solved by the Invention> The present inventor has completed the present invention as a result of intensive studies to solve the above problems. <Structure of the Invention> The present invention relates to a granular material in which a finely powdered enteric coating base is adhered to a granular material granulated using a powdery low melting point substance as a core. In the present invention, the granules granulated using a powder-like low melting point substance as cores (hereinafter referred to as coated granules) refer to the granules disclosed in JP-A-58-214333 (hereinafter referred to as the reference). The product is obtained by heating a mixture of a target drug powder, usually less than 100 μm, and a granular low-melting substance under flowing conditions so that the drug powder adheres to the low-melting substance during the process of melting the low-melting substance. refers to granular matter that is generally sized 20 to 40
Methushi's is used. It is desirable that the granules be spherical in order to efficiently apply the coating, but according to the cited granulation method, spherical particles can be produced by making the core low-melting substance spherical in advance. As a low melting point substance, its melting point is 30~100℃,
Suitably, any material may be used as long as the temperature is 50 to 80°C, such as paraffin, microcrystalline wax, hydrocarbons such as ceresin, hydrogenated oil, wood wax, fats and oils such as cacao butter, myristic acid, palmitic acid, and stearin. Fatty acids such as acids, higher alcohols such as cetanol and stearyl alcohol, polyhydric alcohols such as macrogol 6000, macrogol 4000, and batyl alcohol, waxes such as carnauba wax and beeswax, hexadecyl palmitate, octadecyl stearate, etc. Examples include esters, surfactants such as sorbitan monostearate, glycerin monostearate, acetylated glycerin monostearate, Pluronic F68, and mixtures thereof, and even substances with a relatively high melting point may contain two or more types. Substances that have an apparent melting point drop of 30 to 100°C by mixing, or drugs that themselves are low melting point substances, such as ibuprofen and trimethadione, are considered low melting point substances. It can be used as the core of the granular material to be coated without using. Next, examples of enteric coating bases include acrylic acid polymers such as methacrylic acid ethyl acrylate copolymer, methyl acrylate methacrylic acid copolymer, cellulose polymers such as cellulose acetate phthalate, and carboxymethyl ethyl cellulose. can. The size of the base is generally 0.5 to 20 μm, preferably 1 to 20 μm.
5 μm is used, and the amount used is usually 0.05 to 0.3 parts by weight per 1 part by weight of the granules to be coated. The granules of the present invention can be produced by the following method. First, a granular low melting point substance (preferably spherical or spherical) is used to mix the target drug powder and, if necessary, with an appropriate excipient under flowing conditions at a temperature higher than the melting point of the low melting point substance. Granules to be coated can be obtained by granulation while heating to a certain temperature. The obtained granules to be coated and the finely powdered enteric coating base are placed in a rotary mixer or a sugar-coating pan together with a plasticizer as the case may be, and rolled while maintaining the temperature at a temperature higher than the melting point of the low-melting substance used. After the finely powdered enteric coating base is adhered to the granular material to be coated during the melting process of the low melting point substance by moving the granular material, the target granular material can be produced by cooling it. The rolling speed is generally 30 per minute.
~40 revolutions, and rolling time is typically 10-20 minutes. When attaching the finely divided enteric coating base to the granules to be coated, water-insoluble finely divided substances such as calcium stearate, magnesium stearate, talc, light anhydrous silicic acid, magnesium aluminate metasilicate, calcium lactate, etc. When added, heated and rolled, the fine powder enteric coating base can be applied even more smoothly, and the resulting granular coating becomes dense without pinholes or cracks. . The size of the added fine powder substance is generally 0.05 to 10 μm. Further, the fine powder substance is usually used in an amount of 0.01 part by weight per part by weight of the fine powder enteric coating base.
~10 parts by weight are used. In the enteric coated granules of the present invention, the enteric coating base is usually blended in an amount of 5 to 30% (w/w), and
If a finely divided substance is added, the substance will usually be 1
It is desirable that the content is ~50% (w/w). <Effects of the Invention> The granular material of the present invention has excellent qualities as an enteric-coated preparation, such as gastric juice resistance, appearance, strength, and stability. In addition, it has the following extremely useful advantages. (1) Compared to general enteric coating, there is no need to adjust the coating solution, the coating time can be significantly shortened, and there is no need to set complicated conditions, and it can be manufactured with high yield using simple equipment. Because of this, it is low cost and extremely efficient. (2) Since there is no need to use a solvent, there is no risk of safety, hygiene, pollution, or residue in the formulation, and the stability of the active ingredient can also be improved. (3) By using water-insoluble stearic acid, cetanol, or the like as a low-melting substance used in the production of coated granules, it is possible to obtain enteric-coated granules with a controlled release rate. In addition, the elution rate can be reduced by selecting the fine powder enteric substance.
A granular material with PH control can be obtained. (4) The granules of the present invention may be made into granules as they are, or may be made into tablets by adding appropriate excipients, lubricants, disintegrating agents, etc. Furthermore, if necessary, a lubricant may be added and the mixture may be filled into hard capsules to form capsules. Next, the present invention will be specifically explained with reference to Examples. Example 1 1.0 kg of adenosine triphosphate disodium sieved through a 100 mesh sieve, 2.75 kg of lactose, and 1.25 kg of spherical stearic acid (20 to 40 mesh) were placed in a fluidized bed granulator (Grad WSG-5 type). After granulation while heating and fluidizing at 90°C, the particles were sized using 12 and 40 mesh sieves to obtain coated granules (hereinafter referred to as elementary granules). Next, 2 kg of the elementary granules and finely ground Eudragit L100 (Po¨hm of 20 μm or less) were placed in a double conical mixer with a jacket.
Pharm) and 0.3Kg of talc below,
The jacket was rotated while circulating hot water at 75°C inside the jacket, and after 10 minutes, the circulating water was switched to cold water to cool the jacket to a temperature below the melting point of stearic acid to obtain granules. Example 2 2 kg of elementary granules containing disodium adenosine triphosphate produced in the same manner as in Example 1, 0.15 kg of finely ground cellulose acetate phthalate, and talc.
0.4 kg was placed in a self-made double cone mixer with a jacket and operated in the same manner as in Example 1 to obtain granules. Example 3 Food coloring blue No. 1 0.05Kg and lactose were added to a fluidized bed granulator.
3.0Kg, corn starch 0.7Kg and spherical macrogol 6000 (20-40 mesh) 1.25Kg,
12 and 40 after granulation while heating and fluidizing at 80℃
The particles were sized using a mesh sieve to obtain elementary granules. Next, put 3 kg of the raw granules, 0.5 kg of finely ground Eudragit L100, and 0.25 kg of talc into a sugar-coated bread, and heat the sample by blowing hot air at 80°C on the side of the pan.
It was rotated at 30 rpm, and after 20 minutes, the hot air was replaced with cold air to cool it to a temperature below the melting point of Makkorogol 6000 to obtain granules. Test Example The gastric fluid resistance and dissolution properties of the granules obtained in Examples 1, 2, and 3 were examined. The measurement is carried out using a dissolution tester specified in the Dissolution Test Method 1 of the Japanese Pharmacopoeia General Testing Method, and a 2-hour test is carried out using the first solution.After 1 hour and 2 hours, the test solution is sampled to determine the dissolution. The absorbance of disodium adenosine triphosphate or food coloring blue No. 1 was measured, and the dissolution rate was calculated (gastric juice resistance test). Next, the test solution was replaced with a second solution and a test was conducted on the same sample for up to 2 hours, and the test solution was sampled at regular intervals and the absorbance of each sample was measured to calculate the dissolution rate (dissolution test). The results are shown in Table-1.

【表】 表−1から明らかなように、本発明の粒状物は
耐胃液性を十分に確保し、しかも第2液中におい
て優れた溶出性を示した。
[Table] As is clear from Table 1, the granules of the present invention had sufficient gastric juice resistance and also exhibited excellent dissolution properties in the second liquid.

【特許請求の範囲】[Claims]

1 昇華および/または再結晶し易い活性物質を
含有する速やかに分散し得る核が、やはり速やか
に分散し得る、そして a 架橋したポリビニルピロリドン b 架橋したカルボキシメチルセルロースナトリ
ウム c デンプングリコール酸ナトリウム d イオン交換樹脂 e 微結晶セルロース f 圧縮し得るデンプン g デンプンおよび変性デンプン h アルギン酸およびその誘導体 i ホルムアルデヒド−カゼイン より選ばれた一種以上の崩壊剤を含有する圧縮コ
ーテイング層によつて被覆されており、分散錠全
体が水中20℃において3分以内に0.71mm以下の粒
子寸法を有する均質な飲用可能な分散液に崩壊す
ることができることを特徴とする錠剤。 2 崩壊剤が架橋したポリビニルピロリドンであ
1 a rapidly dispersible core containing an active substance susceptible to sublimation and/or recrystallization, which is also rapidly dispersible, and a crosslinked polyvinylpyrrolidone b crosslinked sodium carboxymethyl cellulose c sodium starch glycolate d ion exchange resin e microcrystalline cellulose f compressible starch g starch and modified starch h alginic acid and its derivatives i formaldehyde-casein is coated with a compression coating layer containing one or more disintegrants selected from A tablet characterized in that it is capable of disintegrating in water at 20° C. within 3 minutes into a homogeneous drinkable dispersion with a particle size of 0.71 mm or less. 2 The disintegrant is cross-linked polyvinylpyrrolidone.

JP29568985A 1985-12-26 1985-12-26 Enteric granular agent Granted JPS62153213A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29568985A JPS62153213A (en) 1985-12-26 1985-12-26 Enteric granular agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29568985A JPS62153213A (en) 1985-12-26 1985-12-26 Enteric granular agent

Publications (2)

Publication Number Publication Date
JPS62153213A JPS62153213A (en) 1987-07-08
JPH0529204B2 true JPH0529204B2 (en) 1993-04-28

Family

ID=17823901

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29568985A Granted JPS62153213A (en) 1985-12-26 1985-12-26 Enteric granular agent

Country Status (1)

Country Link
JP (1) JPS62153213A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2771292B1 (en) * 1997-11-21 2000-02-18 Ethypharm Lab Prod Ethiques TIAGABINE-CONTAINING SPHEROIDS, METHOD OF PREPARATION AND PHARMACEUTICAL COMPOSITIONS
CN1301104C (en) 2002-02-21 2007-02-21 大塚制药株式会社 Sustained release preparations and process for producing the same
ES2221804B1 (en) * 2003-06-18 2006-04-01 Lipofoods, S.L. MICROCAPSULES FOR THE ADMINISTRATION OF ACTIVE INGREDIENTS.
JP4885536B2 (en) * 2005-12-26 2012-02-29 ニッカウヰスキー株式会社 Processing equipment

Also Published As

Publication number Publication date
JPS62153213A (en) 1987-07-08

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