JP3130058B2 - Masked granules - Google Patents
Masked granulesInfo
- Publication number
- JP3130058B2 JP3130058B2 JP03021966A JP2196691A JP3130058B2 JP 3130058 B2 JP3130058 B2 JP 3130058B2 JP 03021966 A JP03021966 A JP 03021966A JP 2196691 A JP2196691 A JP 2196691A JP 3130058 B2 JP3130058 B2 JP 3130058B2
- Authority
- JP
- Japan
- Prior art keywords
- particle size
- low
- water
- drug
- melting point
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- Medicinal Preparation (AREA)
- Glanulating (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は薬物の不快な味などがマ
スクされた粒状物に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a granular substance which is masked for an unpleasant taste of a drug.
【0002】[0002]
【従来の技術】医薬品における錠剤、カプセル剤など種
々の剤型にあって、顆粒剤あるいは細粒剤などの粒状製
剤の果たす役割は、特に小児や老齢者の服用性及びコン
プライアンスの向上において極めて重要である。そして
近年、患者の高齢化が急速に進む中で益々その需要は高
まってきている。しかしながら粒状製剤であっても苦味
や酸味あるいは刺激性などの不快な味を有する薬物が含
まれている場合においては、必ずしも服用しやすい製剤
とはなり得ない。2. Description of the Related Art The role of granular preparations such as granules and fine granules in various dosage forms such as tablets and capsules in pharmaceuticals is extremely important, especially in improving the ingestibility and compliance of children and the elderly. It is. And, in recent years, as the aging of patients has progressed rapidly, the demand has been increasing more and more. However, even in the case of a granular preparation, when a drug having an unpleasant taste such as bitterness, acidity or irritation is contained, the preparation is not necessarily easy to take.
【0003】このため、一般に不快な味を有する粒状製
剤には、不快な味をマスキングするための製剤的工夫が
なされるのが通例である。一般に最も多く用いられる製
剤手法としては、ワックスや水不溶性高分子など口中で
溶解しないコーティング剤を粒状物表面にコーティング
する方法がある。この場合、従来ではコーティング剤を
有機溶媒に溶かすか、または水に懸濁させてスプレーコ
ーティングを施す方法が用いられていた。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い。こ
のため最近ではコーティング剤を可塑剤とともに水に分
散させてコーティングを施す方法が見いだされ、広く用
いられるようになった。しかしこの方法もまた、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ィング液に溶けやすいた
め、コーティング時の粒状物同士の付着による凝集物の
発生や被膜形成不良等の欠点を有する。また、スプレー
コーティングの場合、コーティング速度や温度など製造
条件の変動要因が多いため、常に一定品質の製剤を得る
ための精度の高い条件管理が必要となる。特に、粒状製
剤のマスキングにおいては、水不溶性のコーティング剤
を用いるため、条件変動による被膜形成性のバラツキや
被膜量のわずかな変動により品質上重要となる薬物の溶
出特性に大きな影響を及ぼすことを注意しなければなら
ない。[0003] For this reason, generally, granular preparations having an unpleasant taste are usually devised with a formulation for masking the unpleasant taste. The most commonly used formulation technique is to coat the surface of the granular material with a coating agent that does not dissolve in the mouth, such as a wax or a water-insoluble polymer. In this case, conventionally, a method of dissolving the coating agent in an organic solvent or suspending the coating agent in water to perform spray coating has been used. However, the use of the organic solvent has many problems such as adverse effects on hygiene to workers, environmental pollution, and residues in the preparation. For this reason, recently, a method of applying a coating by dispersing a coating agent in water together with a plasticizer has been found, and has been widely used. However, this method is also unsuitable for water-unstable drugs, and when applied to a water-soluble drug, the drug is easily dissolved in the coating solution. It has drawbacks such as generation of substances and poor film formation. Further, in the case of spray coating, since there are many fluctuation factors of manufacturing conditions such as coating speed and temperature, it is necessary to control conditions with high accuracy to always obtain a preparation of constant quality. In particular, since water-insoluble coating agents are used in the masking of granular preparations, it is important to note that variations in film formation due to changes in conditions and slight fluctuations in the amount of films have a significant effect on the elution characteristics of drugs that are important in quality. You have to be careful.
【0004】[0004]
【発明が解決しようとする課題】本発明は薬物のにがみ
などを効果的にマスクした粒状物を提供することを目的
とする。SUMMARY OF THE INVENTION It is an object of the present invention to provide a granular material which effectively masks drug blemishes and the like.
【0005】[0005]
【課題を解決するための手段】本発明は不快な味を有す
る薬物の粉体、粉粒状の崩壊剤及び粉粒状の水不溶性低
融点物質とを溶融造粒し、得られた造粒物を当該低融点
物質の融点以上の温度で微粉状添加剤と溶融造粒すると
不快な味が効果的にマスキングできるとの知見に基づい
てなされたのである。DISCLOSURE OF THE INVENTION The present invention provides a method of melting and granulating a powder of a drug having an unpleasant taste, a granular disintegrant, and a granular water-insoluble low-melting substance. It was made based on the finding that an unpleasant taste can be effectively masked by melt granulation with a fine powder additive at a temperature equal to or higher than the melting point of the low melting point substance.
【0006】すなわち、本発明は、粉粒状の水不溶性低
融点物質、粉粒状の崩壊剤及び薬物の粉体とを溶融造粒
して得た粒状物を該低融点物質の融点以上の温度で微粉
状添加剤と流動下で溶融して得た粒状物に関し、該粒状
物の表面には水不溶性低融点物質及び上記添加剤からな
る皮膜が形成されていることを特徴とする。[0006] That is, the present invention provides a granulated material obtained by melting and granulating a powdery water-insoluble low-melting substance, a powdered disintegrant and a drug powder at a temperature not lower than the melting point of the low-melting substance. The present invention relates to a granular material obtained by melting under the flow of a fine powdery additive, characterized in that a film comprising a water-insoluble low-melting substance and the above additive is formed on the surface of the granular material.
【0007】本発明において水不溶性低融点物質を用い
て造粒された溶融造粒物(以下、被コーティング粒状物
と称す)としては、特開昭58−214333号に開示
された粒状物、即ち不快な味を有する薬物粉体、粉粒状
の水不溶性低融点物質及び粉粒状の崩壊剤とを該低融点
物質の融点以上の温度で流動混合下、加熱し該低融点物
質の溶融過程で薬物粉体を該低融点物質に付着させて得
られる造粒物があげられ、その大きさは一般に150〜
1400μm のものが使用される。該被コーティング粒
状物は効率よく被覆を施すために滑らかな表面であるこ
とが望ましいが、上記公開公報の造粒方法によればほぼ
球状で滑らかな表面をもつ被コーティング粒状物を製す
ることができる。[0007] In the present invention, as a molten granulated product using a water-insoluble low melting point substance (hereinafter, referred to as a coated granular material), a granular material disclosed in JP-A-58-214333, that is, A drug powder having an unpleasant taste, a powdery water-insoluble low-melting substance and a powdery disintegrant are heated under fluid mixing at a temperature equal to or higher than the melting point of the low-melting substance, and the drug is melted in the melting process of the low-melting substance. Granules obtained by adhering powder to the low-melting substance are mentioned.
1400 μm is used. It is desirable that the coated granules have a smooth surface for efficient coating, but according to the granulation method disclosed in the above publication, it is possible to produce coated granules having an almost spherical and smooth surface. it can.
【0008】本発明で用いる水不溶性低融点物質として
は、その融点が40〜90℃、好適には50〜80℃の
ものが望ましく、例えば、ステアリン酸、パルミチン
酸、ミリスチ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、硬化油、木ロウ
等の油脂類、グリセリン脂肪酸エステルなどの界面活性
剤、パラフィン、マイクロクリスタリンワックスなどの
炭化水素類、もしくはこれらの混合物が挙げられる。ま
た、上記水不溶性の低融点物質であっても、マクロゴー
ル類などの水溶性低融点物質と共融して得られる混合物
も使用することができる。又、粉粒状のものを使用する
のが好ましく、その粒径は目的とする粒状物の粒径に応
じて決定すればよく、通常100〜840μm の範囲の
ものを用いるのがよい。The water-insoluble low melting point substance used in the present invention preferably has a melting point of 40 to 90 ° C., preferably 50 to 80 ° C., for example, fatty acids such as stearic acid, palmitic acid and myristic acid; Examples include higher alcohols such as cetanol and stearyl alcohol, oils and fats such as hardened oil and wood wax, surfactants such as glycerin fatty acid ester, hydrocarbons such as paraffin and microcrystalline wax, and mixtures thereof. Further, even the above-mentioned water-insoluble low-melting point substance, a mixture obtained by eutectic with a water-soluble low-melting point substance such as macrogol can be used. It is preferable to use a powdery and granular material, and the particle size may be determined according to the particle size of the target granular material, and it is generally preferable to use a particle size in the range of 100 to 840 μm.
【0009】上記水溶性低融点物質を用いて溶融造粒さ
れる薬物としては、不快な味を有する薬物である塩酸セ
トラキサート、オフロキサシン、インドメタシン、アス
ピリンなどをあげることができる。これらは通常低融点
物質1重量部に対し8重量部以下で、好ましくは0.5〜
5重量部使用するのがよい。本発明にかかわる崩壊剤と
しては、クロスカメロースナトリウム、カルボキシメチ
ルセルロースカルシウム、カルボキシメチルセルロー
ス、低置換度ヒドロキシプロピロセルロース、結晶セル
ロース、カルボキシメチルスターチナトリウム、架橋化
ポリビニルピロリドンなどがあげられる。崩壊剤は被コ
ーティング粒状物1重量部に対して0.01〜0.2重量部
とするのが好ましく、通常150μm 以下、好ましくは
100μm以下の粒径のものを使用するのが望ましい。
上記溶融造粒物は水不溶性低融点物質、薬物及び崩壊剤
のみで形成することができるが、賦形剤としてとうもろ
こしデンプン、乳糖等を使用することができ、その使用
量は低融点物質1重量部に対し通常0.05〜4重量部と
するのがよい。賦形剤としては粒径が通常1〜150μ
m のものを使用するのがよい。[0009] Drugs that are melt-granulated using the water-soluble low-melting substance include cetraxate hydrochloride, ofloxacin, indomethacin, aspirin and the like, which have unpleasant tastes. These are usually 8 parts by weight or less, preferably 0.5 to 1 part by weight of the low-melting substance.
It is preferred to use 5 parts by weight. Examples of the disintegrant according to the present invention include croscarmellose sodium, carboxymethylcellulose calcium, carboxymethylcellulose, low-substituted hydroxypropyl cellulose, crystalline cellulose, sodium carboxymethyl starch, crosslinked polyvinylpyrrolidone, and the like. The disintegrant is preferably used in an amount of 0.01 to 0.2 part by weight per 1 part by weight of the granular material to be coated, and usually has a particle size of 150 μm or less, preferably 100 μm or less.
The above-mentioned molten granules can be formed only with a water-insoluble low-melting substance, a drug and a disintegrant, but corn starch, lactose, etc. can be used as an excipient, and the amount of the low-melting substance is 1 weight. The amount is usually 0.05 to 4 parts by weight per part by weight. Excipients usually have a particle size of 1 to 150μ
It is better to use m.
【0010】上記被コーティング粒状物の表面に被覆す
る微粉状添加剤としては、例えば、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、ステアリン
酸カルシウム、ステアリン酸マグネシウム、酸化チタ
ン、合成ケイ酸アルミニウムあるいはこれらの混合物な
どが挙げられる。これらのうち無機粉体を使用するのが
好ましい。その大きさは任意とすることができるが、2
0μm 以下のものを使用するのが好ましい。その使用量
は、被コーティング粒状物1重量部に対して通常0.05
〜0.5重量部とするのがよい。[0010] Examples of the fine powdery additives to be coated on the surface of the above-mentioned granular material to be coated include talc, light anhydrous silicic acid, magnesium aluminate metasilicate, calcium stearate, magnesium stearate, titanium oxide, synthetic aluminum silicate or the like. These mixtures and the like can be mentioned. Of these, inorganic powders are preferably used. Its size can be arbitrary, but 2
It is preferable to use one having a size of 0 μm or less. The amount to be used is usually 0.05 to 1 part by weight of the granular material to be coated.
The content is preferably 0.5 parts by weight.
【0011】本発明の粒状物は、例えば、以下の方法に
より製造することができる。まず、粉粒状の水不溶性低
融点物質を用いて通常0.1〜150μm粒径の不快な味を有
する薬物粉体と粉粒状の崩壊剤、場合によっては適当な
賦形剤とともに流動混合下、低融点物質の融点以上の温
度に通常5〜30分間加熱しながら造粒することにより被
コーティング粒状物を得る。得られた被コーティング粒
状物及び微粉状添加剤、所望によっては被コーティング
粒状物1重量部に対し通常0.1重量部以下の上記の如き
賦形剤とともに回転混合機あるいは流動乾燥機に入れ、
用いた低融点物質の融点以上の温度に保持しながら流動
混合させることにより被コーティング粒状物に微粉状添
加剤を付着させて水不溶性低融点物質及び前記添加剤か
らなる皮膜を形成させることができ、こののち、混合操
作を停止することなく冷却させることにより、目的とす
る粒状物を製造することができる。The granular material of the present invention can be produced, for example, by the following method. First, a powdery, water-insoluble low-melting substance is used to give an unpleasant taste, usually with a particle size of 0.1 to 150 μm.
Granules to be coated by granulating while heating at a temperature not lower than the melting point of the low-melting substance, usually for 5 to 30 minutes, under fluid mixing with a drug powder and a powdered disintegrant, and in some cases suitable excipients Get. The obtained granules to be coated and the fine powdery additives, if necessary, are usually put into a rotary mixer or a fluidized dryer together with the excipients described above, usually 0.1 parts by weight or less per 1 part by weight of the granules to be coated,
It is possible to form a film composed of the water-insoluble low-melting substance and the above-mentioned additive by adhering the finely powdered additive to the coated granular material by fluid-mixing while maintaining the temperature at or above the melting point of the used low-melting substance. Thereafter, by cooling the mixture without stopping the mixing operation, the target granular material can be produced.
【0012】加熱操作は通常温水または熱風により行わ
れその温度は一般に、用いる水不溶性低融点物質の融点
より5〜30℃高い温度で操作するのが好ましく、その
時間は用いる原材料の種類や製造スケールによって異な
るが、通常1〜10Kg程度のスケールにおいては10〜
20分である。The heating operation is usually performed with hot water or hot air, and the temperature is generally preferably 5 to 30 ° C. higher than the melting point of the water-insoluble low-melting substance to be used. Depends on the scale, but usually on a scale of about 1 to 10 kg
20 minutes.
【0013】[0013]
【発明の効果】本発明の粒状物は、口中における味のマ
スキング性、溶出性、外観、強度安定性等粒状製剤とし
て優れた品質を有する。また、その他にも極めて有用な
以下の利点を有する。 (1) 一般のマスキングのためのコーティングに比べて、
コーティング液を調製する必要がない上、コーティング
時間が大幅に短縮でき、また複雑な条件設定を必要とせ
ず簡単な装置によって一定品質の製品を収率よく製造で
きる。 (2) 溶媒を用いる必要がないため、安全面、衛生面、公
害面、製品中への残留などの危険性がなく、更に薬物の
安定性も損なうことがない。 (3) 水不溶性低融点物質の粒度を変えることにより、容
易に製品の粒度をコントロールすることができる。例え
ば、造粒時150〜250μm の水不溶性低融点物質を
用いると、粒径250〜500μm の細粒剤が得られ、
300〜850μm の水溶性低融点物質を用いると、粒
径500〜1400μm の顆粒剤を得ることができる。 (4) 水不溶性低融点物質、崩壊剤及び微粉末状添加剤の
種類や量を調節することにより口中におけるマスキング
の程度及び体内での溶出性を自由にコントロールするこ
とができる。EFFECTS OF THE INVENTION The granules of the present invention have excellent quality as granular preparations, such as taste masking properties in the mouth, dissolution properties, appearance, and strength stability. In addition, it has the following very useful advantages. (1) Compared to coating for general masking,
There is no need to prepare a coating solution, the coating time can be greatly reduced, and a product of constant quality can be produced with a simple apparatus at a high yield without the need for complicated conditions. (2) Since there is no need to use a solvent, there is no danger such as safety, hygiene, pollution, or residue in the product, and the stability of the drug is not impaired. (3) The particle size of the product can be easily controlled by changing the particle size of the water-insoluble low-melting substance. For example, when a water-insoluble low-melting substance having a particle size of 150 to 250 μm is used during granulation, a fine granule having a particle size of 250 to 500 μm can be obtained.
When a water-soluble low melting point substance having a particle size of 300 to 850 µm is used, a granule having a particle size of 500 to 1400 µm can be obtained. (4) The degree of masking in the mouth and dissolution in the body can be freely controlled by adjusting the type and amount of the water-insoluble low-melting substance, disintegrant and fine powder additive.
【0014】次に実施例をあげて本発明を具体的に説明
する。Next, the present invention will be specifically described with reference to examples.
【0015】実施例1 流動層造粒機(グラットWSG−5型)に塩酸セトラキ
サート2.8Kg(粒径:150μm 以下)、トウモロコシ
デンプン0.5Kg(粒径:10μm 以下)、クロスカルメ
ロースナトリウム0.5Kg(粒径:20〜50μm )及び
モノステアリン酸グリセリン(150〜250μm 、日
本油脂製)1.2Kgを入れ、吸気温度85℃で加熱流動さ
せながら造粒したのち冷却し、500μm のふるいにて
篩過し、被コーティング粒状物を得た(平均粒径約40
0μm )。次にジャケット付きクロスロータリーミキサ
ー(CM−10型)に該被コーティング粒状物2.1Kgと
タルク0.9Kg(粒径:約10μm 以下)を入れ、80℃
の温水をジャケット内に循環させながら1分間に20回
転の速度で回転させ、10分後循環水を水道水に切り替
えて試料温度40℃まで冷却し、マスキング粒状製剤
(細粒剤、平均粒径:約400μm )を得た。EXAMPLE 1 2.8 kg of cetraxate hydrochloride (particle size: 150 μm or less), 0.5 kg of corn starch (particle size: 10 μm or less), croscarmellose sodium 0 in a fluidized bed granulator (Grat WSG-5). 2.5 kg (particle size: 20-50 μm) and 1.2 kg of glyceryl monostearate (150-250 μm, manufactured by NOF Corporation) are granulated while heated and fluidized at an intake temperature of 85 ° C., and then cooled, and then sieved to a 500 μm sieve. To obtain granules to be coated (average particle size of about 40
0 μm). Next, 2.1 kg of the coated granular material and 0.9 kg of talc (particle size: about 10 μm or less) are put into a jacketed cross rotary mixer (CM-10 type), and the mixture is heated to 80 ° C.
Of warm water is circulated in the jacket at a speed of 20 revolutions per minute, and after 10 minutes, the circulating water is switched to tap water and cooled to a sample temperature of 40 ° C., and the masked granular preparation (fine granules, average particle size) : About 400 µm).
【0016】実施例2 実施例1と同様にして得られた被コーティング粒状物4.
2Kgを、びタルク1.56Kg(粒径:約10μm 以下)と
ともに再び流動層造粒機に入れ、吸気温度80℃で加熱
しながら流動させ、粉末がすべて被コーティング粒状物
に付着した(約20分)のち、ダンパー操作により熱風
を室内空気に替え試料温度40℃まで冷却してマスキン
グ粒状製剤(細粒剤、平均粒径:約400μm )を得
た。Example 2 Coated granules obtained in the same manner as in Example 1.
2 kg together with 1.56 kg of talc (particle size: about 10 μm or less) was again put into a fluidized bed granulator, and was made to flow while heating at an intake air temperature of 80 ° C., so that all the powder adhered to the granules to be coated (about 20). After that, the hot air was replaced with room air by a damper operation and cooled to a sample temperature of 40 ° C. to obtain a masked granular preparation (fine granules, average particle size: about 400 μm).
【0017】実施例3 流動層造粒機にオフロキサシン1.4Kg(粒径:10μm
以下)、低置換度ヒドロキシプロピルセルロース0.5Kg
(粒径:20〜50μm )、乳糖1.5Kg(粒径:150
μm 以下)、トウモロコシデンプン0.3Kg(粒径:10
μm 以下)及びステアリン酸(150〜250μm )1.
3Kgを入れ、吸気温度85℃で実施例1と同様にして被
コーティング粒状物を得た(平均粒径:約400μm
)。次にジャケット付きクロスロータリーミキサーに
該被コーティング粒状物2.1Kgとタルク0.8Kg(粒径:
約10μm )を入れ、実施例1と同様にしてマスキング
粒状製剤(細粒剤、平均粒径:約400μm )を得た。Example 3 1.4 kg of ofloxacin (particle size: 10 μm) was added to a fluidized bed granulator.
Below), low-substituted hydroxypropylcellulose 0.5 kg
(Particle size: 20-50 μm), lactose 1.5 kg (particle size: 150
μm or less), 0.3 kg of corn starch (particle size: 10
μm or less) and stearic acid (150-250 μm) 1.
3 kg, and a granular material to be coated was obtained in the same manner as in Example 1 at an intake air temperature of 85 ° C. (average particle size: about 400 μm).
). Next, 2.1 kg of the coated granules and 0.8 kg of talc (particle size:
About 10 μm), and a masked granular preparation (fine granules, average particle size: about 400 μm) was obtained in the same manner as in Example 1.
【0018】試験例1 実施例1、2及び3で得られたマスキング粒状製剤につ
き、口中マスキング試験及び溶出試験を実施した。また
比較対象試料として、それぞれの被コーティング粒状物
についても同様の試験を行った。口中マスキング試験
は、試料のそれぞれ0.5gを口に含み苦味あるいは酸味
を感じるまでの時間を測定しマスキング時間とした。な
お試験者は5名とした。Test Example 1 The masked granular preparations obtained in Examples 1, 2 and 3 were subjected to a mouth masking test and a dissolution test. The same test was performed for each of the coated granular materials as comparative samples. In the mouth masking test, 0.5 g of each of the samples was contained in the mouth, and the time until bitterness or sourness was felt was measured and defined as masking time. The number of testers was five.
【0019】溶出試験は、日局一般試験法溶出試験法第
1法により行い、日局第1液を用いて試験開始後5分お
きに30分までの試験液をサンプリングし、塩酸セトラ
キサートまたはオフロキサシンの吸光度を測定しその溶
出率75%に達する時間(T 75%)を計算により求め
た。これらの結果を表1に示す。The dissolution test is performed according to the Japanese Pharmacopoeia General Test
5 minutes after the start of the test using JP
Sample the test solution for up to 30 minutes
Measure the absorbance of xate or ofloxacin and dissolve
Time to reach 75% output rate (T 75%) By calculation
Was. Table 1 shows the results.
【0020】 表1 試験結果 マスキング時間 溶出時間(T75%) 実施例1 被コーティンク゛粒状物 2〜 3秒 2.5 分 マスキンク゛ 粒状物 30〜 60 秒 5.2 分 実施例2 被コーティンク゛粒状物 1〜 2秒 1.5 分 マスキンク゛ 粒状物 20〜 40 秒 3.4 分 実施例3 被コーティンク゛粒状物 3 〜 5秒 4.6 分 マスキンク゛ 粒状物 40〜 60 秒 9.2 分Table 1 Test results Masking time Elution time (T 75 %) Example 1 Coated material (granular material) 2-3 seconds 2.5 minutes Maskinque (granulated material) 30-60 seconds 5.2 minutes Example 2 Coated material (granular material 1) 22 seconds 1.5 minutes Maskinque granules 20-40 seconds 3.4 minutes Example 3 Coated material 3-5 seconds 4.6 minutes Maskinque granules 40-60 seconds 9.2 minutes
【0021】表1から明らかなように、本発明のマスキ
ング粒状物は十分な口中マスキング性を有し、しかも速
やかな溶出特性を示した。As is evident from Table 1, the masked granules of the present invention had sufficient mouth masking properties and exhibited rapid elution characteristics.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭63−27423(JP,A) 特開 昭58−214333(JP,A) 特開 昭62−181214(JP,A) 特公 昭42−17324(JP,B1) 特公 昭39−17168(JP,B1) ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-63-27423 (JP, A) JP-A-58-214333 (JP, A) JP-A-62-181214 (JP, A) JP-B-42 17324 (JP, B1) JP-B 39-17168 (JP, B1)
Claims (3)
崩壊剤及び不快な味を有する薬物の粉体とを溶融造粒し
て得た粒状物を、該低融点物質の融点以上の温度で、微
粉状添加剤と流動下、溶融することを特徴とする前記薬
物の不快な味がマスクされ、かつ速やかな溶出特性を有
する粒状物の製造法。1. A particulate water-insoluble low melting point substance, a granulate and a powder of a drug with a disintegrant and unpleasant taste of the powdered obtained by melt granulation, above the melting point of the low melting point materials At the temperature, the unpleasant taste of the drug, which is characterized by melting with the fine powder additive under flow, is masked and has a rapid dissolution property.
Preparation of granules to be.
カルボキシメチルセルロースカルシウム、カルボキシメ
チルセルロース、低置換度ヒドロキシプロピルセルロー
ス、結晶セルロース、カルボキシメチルスターチナトリ
ウム、架橋化ポリビニルピロリドンおよびこれらの混合
物からなる群より選ばれ、かつ、微粉状添加剤がタル
ク、軽質無水ケイ酸、メタケイ酸アルミン酸マグネシウ
ム、ステアリン酸カルシウム、ステアリン酸マグネシウ
ム、酸化チタン、合成ケイ酸アルミニウムおよびこれら
の混合物からなる群から選ばれることを特徴とする、請
求項1に記載の製造法。2. The disintegrant is croscarmellose sodium,
Carboxymethylcellulose calcium, carboxymethylcellulose, low-substituted hydroxypropylcellulose, crystalline cellulose, carboxymethylstarch sodium, cross-linked polyvinylpyrrolidone and mixtures thereof, and the finely powdered additive is talc, light anhydrous silicic acid The method according to claim 1, wherein the method is selected from the group consisting of magnesium aluminate metasilicate, calcium stearate, magnesium stearate, titanium oxide, synthetic aluminum silicate and a mixture thereof.
μmであり、かつ、粉粒状の崩壊剤の粒子径が150μm以
下であり、かつ、不快な味を有する薬物の粉体の粒子径
が0.1〜150μmであり、かつ、微粉状添加剤の粒子径が2
0μm以下であることを特徴とする、請求項2に記載の製
造法。3. The water-insoluble low-melting substance has a particle size of 100 to 840.
μm, and the particle size of the powdery disintegrant is 150 μm or less, and the particle size of the drug powder having an unpleasant taste is 0.1 to 150 μm, and the particle size of the fine powder additive. Is 2
3. The method according to claim 2, wherein the thickness is 0 μm or less.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03021966A JP3130058B2 (en) | 1991-02-15 | 1991-02-15 | Masked granules |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03021966A JP3130058B2 (en) | 1991-02-15 | 1991-02-15 | Masked granules |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0691150A JPH0691150A (en) | 1994-04-05 |
JP3130058B2 true JP3130058B2 (en) | 2001-01-31 |
Family
ID=12069802
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP03021966A Expired - Lifetime JP3130058B2 (en) | 1991-02-15 | 1991-02-15 | Masked granules |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3130058B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2005000312A1 (en) * | 2003-06-27 | 2006-08-03 | 大塚製薬株式会社 | Drug sustained-release particles and process for producing the same |
JP7166510B2 (en) | 2018-07-23 | 2022-11-08 | ジェイ・アイ・サイエンス有限会社 | Taste intensity judgment method |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
PT841062E (en) | 1995-07-21 | 2005-03-31 | Daiichi Seiyaku Co | PROCESS FOR THE PRODUCTION OF A GRANULAR PREPARATION |
JP5042447B2 (en) * | 1995-07-21 | 2012-10-03 | 第一三共株式会社 | Mixed preparation |
US6099865A (en) * | 1998-07-08 | 2000-08-08 | Fmc Corporation | Croscarmellose taste masking |
JP4570725B2 (en) * | 2000-04-05 | 2010-10-27 | 大塚製薬株式会社 | Composition for pharmaceutical preparation |
AU2001290239A1 (en) * | 2000-09-19 | 2002-04-02 | Daiichi Pharmaceutical Co., Ltd. | Medicinal composition |
JP4310605B2 (en) | 2001-05-25 | 2009-08-12 | 大塚製薬株式会社 | Pharmaceutical composition |
CN100528233C (en) * | 2003-10-29 | 2009-08-19 | 盐野义制药株式会社 | Process for producing coated preparation having relieved unpleasantness |
GB0330255D0 (en) * | 2003-12-31 | 2004-02-04 | Vectura Ltd | Multiparticulate formulations for oral delivery |
JP4342426B2 (en) * | 2004-11-24 | 2009-10-14 | 科研製薬株式会社 | Itraconazole formulation for oral administration |
-
1991
- 1991-02-15 JP JP03021966A patent/JP3130058B2/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2005000312A1 (en) * | 2003-06-27 | 2006-08-03 | 大塚製薬株式会社 | Drug sustained-release particles and process for producing the same |
JP4592590B2 (en) * | 2003-06-27 | 2010-12-01 | 大塚製薬株式会社 | Drug sustained-release particles and process for producing the same |
US8734843B2 (en) | 2003-06-27 | 2014-05-27 | Otsuka Pharmaceutical Co., Ltd. | Medicament sustained-release particles and method for preparing the same |
JP7166510B2 (en) | 2018-07-23 | 2022-11-08 | ジェイ・アイ・サイエンス有限会社 | Taste intensity judgment method |
Also Published As
Publication number | Publication date |
---|---|
JPH0691150A (en) | 1994-04-05 |
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