JP2003081876A - Method for mixing medicine - Google Patents

Method for mixing medicine

Info

Publication number
JP2003081876A
JP2003081876A JP2001273359A JP2001273359A JP2003081876A JP 2003081876 A JP2003081876 A JP 2003081876A JP 2001273359 A JP2001273359 A JP 2001273359A JP 2001273359 A JP2001273359 A JP 2001273359A JP 2003081876 A JP2003081876 A JP 2003081876A
Authority
JP
Japan
Prior art keywords
drug
mixing
mixed
variation
lactose
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.)
Granted
Application number
JP2001273359A
Other languages
Japanese (ja)
Other versions
JP4925526B2 (en
Inventor
Etsuo Kamata
悦雄 鎌田
Masayuki Kakizawa
眞幸 垣澤
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.)
Asahi Kasei Corp
Original Assignee
Asahi Kasei Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Asahi Kasei Corp filed Critical Asahi Kasei Corp
Priority to JP2001273359A priority Critical patent/JP4925526B2/en
Publication of JP2003081876A publication Critical patent/JP2003081876A/en
Application granted granted Critical
Publication of JP4925526B2 publication Critical patent/JP4925526B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Medicinal Preparation (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a mixing method by which a speed of mixing a low dose medicinal agent with additives is increased and the homogeneity of the contents of the agent is increased when the low dose medicinal agent is mixed with the additives through a powder mixing process. SOLUTION: The mixing method for increasing the homogeneity of the content of the medicinal agent comprises mixing the agent with a fluidizing modifier (talc, light anhydrous silicic acid or the like) in advance, and subsequently mixing the mixed powder further with other additives.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、薬物と添加剤の混
合方法に関する。
TECHNICAL FIELD The present invention relates to a method for mixing a drug and an additive.

【0002】[0002]

【従来の技術】従来、薬物と添加剤を粉体のまま混合し
て、混合粉体を打錠する直接打錠法において、あるいは
混合粉体をカプセル充填する場合において、あるいは混
合粉体を散剤とする場合などにおいて、従来の粉体混合
方法では、凝集性が高い薬物の場合、特に薬物含有濃度
が低いときには、薬物と添加剤の混合速度が遅く、薬物
の含量均一性が向上しにくい傾向があることが知られて
いる。そのため、このような場合には、薬物と添加物を
湿式造粒する方法をとられることが多かった。しかし、
湿式造粒法では、多くの工程を経るため、コストが高
く、バリデーションが難しく、また、水分、熱に弱い薬
物では薬効が低下するという問題がある。薬物と添加剤
を湿式造粒ではなく、粉体状態のままで混合する方法で
薬物の含量均一性を高める検討例はあるが、長時間の混
合を必要とする、あるいは経時的な含量ばらつきが大き
いなど十分な結果は得られていない。
2. Description of the Related Art Conventionally, in the direct tableting method in which a drug and an additive are mixed in powder form and the mixed powder is tableted, or when the mixed powder is filled in capsules, or the mixed powder is powdered. In the conventional powder mixing method, when the drug has high cohesiveness, especially when the drug content concentration is low, the mixing speed of the drug and the additive is slow, and it is difficult to improve the drug content uniformity. It is known that there is. Therefore, in such a case, a method of wet granulating the drug and the additive was often used. But,
In the wet granulation method, there are problems that the cost is high and the validation is difficult because many steps are required, and the drug efficacy is lowered for a drug sensitive to moisture and heat. There is an example of study to improve the drug content uniformity by mixing the drug and additives in a powder state, not by wet granulation, but it requires a long time of mixing, or the content variation over time Not enough results have been obtained, such as being large.

【0003】[0003]

【発明が解決しようとする課題】本発明は、直接打錠法
により得られる錠剤、あるいは粉体を充填するカプセル
剤、あるいは粉体からなる散剤、などを製造する前工程
としての、薬物と所定の種々の添加剤を粉体混合する場
合において、特に最終製剤中における薬物含有量が20
重量%以下と低い場合において、薬物と添加剤の混合速
度を速め、薬物の含量均一性を高めるための混合方法を
提供することを目的とする。
DISCLOSURE OF THE INVENTION The present invention provides a drug and a predetermined amount as a pre-process for producing a tablet obtained by a direct compression method, a capsule filled with powder, a powder made of powder, or the like. In the case of powder-mixing various additives, the drug content in the final preparation is 20
An object of the present invention is to provide a mixing method for increasing the mixing speed of a drug and an additive and enhancing the content uniformity of the drug when the content is as low as less than or equal to wt%.

【0004】[0004]

【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意研究を重ねた結果、薬物と添加剤
を混合する前に、予め薬物と流動改質剤と混合した後、
その混合粉体とその他の添加剤とをさらに混合すること
によって、薬物の混合速度を速め、薬物の含量均一性を
高めること、すなわち薬物含量の変動係数が5%以下の
薬物含有混合粉体とできることを見出し、本発明を完成
するに至った。
Means for Solving the Problems As a result of intensive studies to solve the above problems, the present inventors have found that before mixing a drug and an additive, after mixing the drug and a flow modifier in advance. ,
By further mixing the mixed powder with other additives, the mixing speed of the drug is increased and the uniformity of the drug content is improved, that is, the drug-containing mixed powder having a coefficient of variation of the drug content of 5% or less. They have found that they can do so and have completed the present invention.

【0005】すなわち、本発明は、 1)薬物と添加剤の混合において、薬物と流動改質剤を
混合した後、該混合粉体とその他の添加剤とを混合する
ことを特徴とする薬物の混合方法; 2)流動改質剤がタルク、軽質無水ケイ酸、含水二酸化
ケイ素、ステアリン酸塩よりなる群から選ばれる1種ま
たは2種以上であることを特徴とする請求項1の混合方
法; 3)その他の添加剤がセルロース類、及び/または乳糖
類を含有することを特徴とする請求項1又は2の何れか
の薬物の混合方法;である。
That is, the present invention is: 1) In mixing a drug and an additive, the drug and the flow modifier are mixed, and then the mixed powder and other additives are mixed. Mixing method: 2) The flow modifier is one kind or two or more kinds selected from the group consisting of talc, light anhydrous silicic acid, hydrous silicon dioxide, and stearate; 3) The method for mixing a drug according to claim 1 or 2, wherein the other additive contains cellulose and / or lactose.

【0006】[0006]

【発明の実施の形態】以下に本発明を詳細に説明する。
本発明で用いられる薬物としては、有効成分として製剤
化されるものであれば特に制限はないが、微粉状で、凝
集性の高い薬物に適用すると、本発明の効果が顕著であ
り、好ましい。薬物の平均粒径は凝集性の観点から、画
像解析で求める平均粒径が40μm以下であることが好
ましい。より好ましくは30μm以下である。さらに好
ましくは20μm以下である。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention is described in detail below.
The drug used in the present invention is not particularly limited as long as it is formulated as an active ingredient, but when applied to a drug in the form of fine powder having a high cohesive property, the effect of the present invention is remarkable, which is preferable. The average particle size of the drug is preferably 40 μm or less, which is obtained by image analysis from the viewpoint of cohesiveness. It is more preferably 30 μm or less. More preferably, it is 20 μm or less.

【0007】薬物の濃度は薬物の有効投与量と関係する
ため、一概には言えないが、実用に用いられる濃度であ
れば特に制限はない。ただ、使用する薬剤の濃度が低い
場合において、本発明の効果がより顕著であるため、最
終製剤中で20重量%以下である場合が好ましく、より
好ましくは10重量%以下、特に好ましくは5重量%以
下、更に好ましくは2重量%以下である。薬物濃度の下
限については特に制限はないが、0.01重量%以上程
度である。薬物は必要に応じて2種以上をのものを併用
してもかまわない。
Since the concentration of the drug is related to the effective dose of the drug, it cannot be generally stated, but there is no particular limitation as long as it is a concentration which is practically used. However, since the effect of the present invention is more remarkable when the concentration of the drug used is low, it is preferably 20% by weight or less, more preferably 10% by weight or less, particularly preferably 5% by weight in the final preparation. % Or less, more preferably 2% by weight or less. The lower limit of the drug concentration is not particularly limited, but is about 0.01% by weight or more. If necessary, two or more drugs may be used in combination.

【0008】流動改質剤としては、「医薬品添加物事典
2000」(薬業時報社(株)発行)において、流動化
剤、滑沢剤に分類される添加剤が挙げられる。流動化剤
としては、タルク、軽質無水ケイ酸、含水二酸化ケイ
素、酸化チタンなどである。滑沢剤としては、ステアリ
ン酸マグネシウム、ステアリン酸カルシウム、ステアリ
ン酸などのステアリン酸塩、含水無晶形酸化ケイ素、ケ
イ酸マグネシウム、ケイ酸カルシウム、炭酸マグネシウ
ムなどが挙げられる。好ましくはタルク、軽質無水ケイ
酸、含水二酸化ケイ素、ステアリン酸塩である。流動改
質剤は1種を使用しても良いし、2種以上を併用しても
かまわない。
Examples of the flow modifier include additives classified into fluidizers and lubricants in "Pharmaceutical Additives Encyclopedia 2000" (published by Yakuhin Jikho Co., Ltd.). Examples of the fluidizing agent include talc, light anhydrous silicic acid, hydrous silicon dioxide, titanium oxide and the like. Examples of the lubricant include magnesium stearate, calcium stearate, stearates such as stearic acid, hydrous amorphous silicon oxide, magnesium silicate, calcium silicate, and magnesium carbonate. Preferred are talc, light anhydrous silicic acid, hydrous silicon dioxide and stearate. The flow modifier may be used alone or in combination of two or more kinds.

【0009】本発明の薬物の混合法では、薬物を所定の
添加剤と混合する前に、上記流動改質剤と混合すること
が必要である。このような手法をとることにより、混合
紛体より得られる最終製剤中の薬物含有量が20重量%
以下と低い場合であっても、その薬物含量バラツキが小
さく、後述する薬物含量変動係数が5%以下の、いわゆ
る含量均一性に優れた錠剤を得ることができる。
In the method of mixing a drug of the present invention, it is necessary to mix the drug with the above-mentioned flow modifier before mixing it with a predetermined additive. By taking such a method, the drug content in the final preparation obtained from the mixed powder is 20% by weight.
Even when it is as low as below, the variation in the drug content is small, and a tablet having a so-called drug content variation coefficient of 5% or less, which will be described later, excellent in so-called content uniformity can be obtained.

【0010】薬物に添加する流動改質剤の比率について
は、改質剤および薬剤の種類にもよるが、概略、薬物に
対して、0.1重量%〜200重量%程度が好ましい。
0.1重量%未満であると流動改質剤による、薬物の凝
集を解く効果が小さいため、本発明の効果が得られにく
い場合がある。200重量%を超えると流動改質剤の飛
散性、付着性が発現し、作業性が悪くなるため、本発明
の効果が得られにくい。厳密には流動改質剤の添加量
は、その種類により異なる。タルクの場合、好ましくは
薬物に対して、5重量%〜200重量%程度である。さ
らに好ましくは、20重量%〜100重量%程度であ
る。軽質無水ケイ酸、含水二酸化ケイ素、ステアリン酸
塩の場合は好ましくは薬物に対して、0.1重量%〜2
0重量%程度である。さらに好ましくは、0.5重量%
〜10重量%である。
The ratio of the flow modifier added to the drug depends on the type of the modifier and the drug, but is preferably about 0.1 to 200% by weight based on the drug.
If the amount is less than 0.1% by weight, the effect of releasing the aggregation of the drug by the flow modifier is small, so that the effect of the present invention may be difficult to obtain. If it exceeds 200% by weight, the flowability and the adhesion of the flow modifier will be exhibited and the workability will be deteriorated, so that the effects of the present invention will be difficult to obtain. Strictly speaking, the addition amount of the flow modifier differs depending on its type. In the case of talc, it is preferably about 5% by weight to 200% by weight with respect to the drug. More preferably, it is about 20% to 100% by weight. In the case of light anhydrous silicic acid, hydrous silicon dioxide and stearate, preferably 0.1% by weight to 2 based on the drug.
It is about 0% by weight. More preferably, 0.5% by weight
10 to 10% by weight.

【0011】薬物と流動改質剤を混合する時、本発明の
効果を失わない程度に、他の添加剤の一部をここで添加
してもかまわない。その際の流動改質剤の添加量は、薬
物及び同時に添加する添加剤の合計に対して、上記の添
加量が目安となる。薬物と流動改質剤の混合方法として
は、通常行われる粉体の混合方法であれば特に制限はな
い。V型、W型、ダブルコーン型、コンテナタンク型混
合機などの容器回転式混合機、あるいは高速撹拌型、万
能撹拌型、リボン型、ナウター型混合機などの撹拌式混
合機を使用することができる。また、粉体量が少ない場
合は、ポリエチレン袋に粉体を入れ、手で振とうする方
法をとることもできる。
When the drug and the flow modifier are mixed, a part of the other additives may be added here to the extent that the effects of the present invention are not lost. The amount of the flow modifier added at that time is based on the total amount of the drug and the additives added at the same time as a guide. The mixing method of the drug and the flow modifier is not particularly limited as long as it is a commonly used powder mixing method. V-type, W-type, double-cone type, container-tank type mixers and other container-rotating type mixers, or high-speed stirring type, universal stirring type, ribbon type, Nauta-type mixers and other stirring type mixers can be used. it can. When the amount of powder is small, it is possible to put the powder in a polyethylene bag and shake it by hand.

【0012】混合時間はおのおのの混合方法に適した時
間を設定することができる。一般に、容器回転式混合機
の場合は1〜60分間程度の混合が好ましい。これより
時間が短いと、薬物と流動改質剤の種類によっては、本
発明の効果が発揮できない場合がある。これより長時間
やってもかまわないが、効果がさらに上がることは少な
いので、労力の無駄となる場合が多い。3〜20分程度
がさらに好ましい。撹拌式混合機の場合は0.1〜10
分程度の混合が好ましく、0.5〜3分程度がさらに好
ましい。手で振とうする場合は、0.2〜20分程度の
混合が好ましく、0.5〜5分程度がさらに好ましい。
The mixing time can be set to a time suitable for each mixing method. Generally, in the case of a container rotary type mixer, mixing for about 1 to 60 minutes is preferable. If the time is shorter than this, the effect of the present invention may not be exhibited depending on the type of drug and flow modifier. It may be used for a longer time than this, but since the effect does not increase further, it is often a waste of labor. About 3 to 20 minutes is more preferable. 0.1-10 for agitated mixers
Mixing for about a minute is preferable, and about 0.5 to 3 minutes is more preferable. When shaking by hand, mixing for about 0.2 to 20 minutes is preferable, and about 0.5 to 5 minutes is more preferable.

【0013】本発明では、このようにして得られた薬物
と流動改質剤との混合紛体を、その他の添加剤と混合す
る。その他の添加剤としては、例えば、賦形剤、崩壊
剤、結合剤、着色料、甘味料、着香料、湿潤剤などが挙
げられる。また、再び、流動化剤、滑沢剤を添加するこ
とも自由である。ここで滑沢剤を添加する場合は、薬物
と流動改質剤との混合粉体、その他の添加剤を混合した
後、さらに滑沢剤を添加して短時間混合することが錠剤
成形上好ましい。また、混合時の含量均一性に問題のな
い薬物の場合であれば、ここでその他の添加剤とともに
該薬物を混合することもできる。
In the present invention, the mixed powder of the drug thus obtained and the flow modifier is mixed with other additives. Examples of other additives include excipients, disintegrants, binders, colorants, sweeteners, flavoring agents, wetting agents and the like. Further, it is also free to add a fluidizing agent and a lubricant again. In the case of adding a lubricant here, it is preferable in terms of tablet molding that after the powder mixture of the drug and the flow modifier and other additives are mixed, the lubricant is further added and mixed for a short time. . In the case of a drug having no problem in content uniformity during mixing, the drug can be mixed with other additives here.

【0014】賦形剤としては、結晶セルロース、粉末セ
ルロースなどのセルロース類、結晶乳糖、造粒乳糖など
の乳糖類、セルロース類と乳糖類を複合化物類、D−マ
ンニトール、白糖、エリスリトール、トレハロースなど
の糖類及び糖アルコール類、トウモロコシデンプン、バ
レイショデンプン、部分アルファー化デンプン等のデン
プン類、リン酸水素カルシウム、無水リン酸水素カルシ
ウム、ケイ酸アルミニウム、メタケイ酸アルミン酸マグ
ネシウムなどの無機物質類、などがある。
As the excipient, celluloses such as crystalline cellulose and powdered cellulose, lactose such as crystalline lactose and granulated lactose, complex compounds of cellulose and lactose, D-mannitol, sucrose, erythritol, trehalose, etc. Sugars and sugar alcohols, corn starch, potato starch, starches such as partially pregelatinized starch, inorganic substances such as calcium hydrogen phosphate, anhydrous calcium hydrogen phosphate, aluminum silicate, and magnesium aluminometasilicate. is there.

【0015】これらのうち、セルロース類を用いる場
合、賦形剤中の結晶セルロースの配合率は、通常使用さ
れる配合率であれば特に制限はないが、一般的には最終
製剤中で1重量%〜95重量%が好ましい。より好まし
くは5重量%〜70重量%、さらに好ましくは10重量
%〜50重量%である。崩壊剤としては、カルメロース
カルシウム、低置換度ヒドロキシプロピルセルロース、
クロスカルメロースナトリウムなどのセルロース誘導体
類、トウモロコシデンプン、カルボキシメチルスターチ
ナトリウム、ヒドロキシプロピルスターチ、部分アルフ
ァー化デンプンなどのデンプン及びデンプン誘導体類、
クロスポビドンなどの合成高分子類、などがある。結合
剤としては、ヒドロキシプロピルセルロース、ヒドロキ
シプロピルメチルセルロース、カルメロースナトリウ
ム、メチルセルロース等のセルロース誘導体類、ポビド
ンなどの合成高分子類などがある。
Of these, when celluloses are used, the compounding ratio of crystalline cellulose in the excipient is not particularly limited as long as it is a commonly used compounding ratio, but generally 1% by weight in the final preparation. % To 95% by weight is preferred. It is more preferably 5% by weight to 70% by weight, and further preferably 10% by weight to 50% by weight. As a disintegrant, carmellose calcium, low-substituted hydroxypropyl cellulose,
Cellulose derivatives such as croscarmellose sodium, corn starch, sodium carboxymethyl starch, hydroxypropyl starch, starch and starch derivatives such as partially pregelatinized starch,
There are synthetic polymers such as crospovidone. Examples of the binder include cellulose derivatives such as hydroxypropylcellulose, hydroxypropylmethylcellulose, carmellose sodium and methylcellulose, and synthetic polymers such as povidone.

【0016】上記添加剤の中でも、セルロース類、及び
乳糖類、およびそれらの複合化物類が、混合速度、含量
均一性を向上させる点において優れている。特に、セル
ロース類の中では結晶セルロースが、乳糖類の中では造
粒乳糖が優れている。両者とも比較的、粒子表面が粗で
あるため、分散された薬物を表面に捕らえて、薬物が再
凝集するのを抑制するためと推定している。ここで使用
する混合機としては、薬物と流動改質剤との混合で用い
た混合機と同様、通常用いられている装置を使用すれば
良い。
Among the above additives, celluloses, lactose, and their composites are excellent in improving mixing speed and content uniformity. Particularly, crystalline cellulose is excellent among celluloses, and granulated lactose is excellent among lactose. It is presumed that both of them have a relatively rough particle surface, so that the dispersed drug is trapped on the surface and the reaggregation of the drug is suppressed. As the mixer used here, an apparatus which is normally used may be used, like the mixer used for mixing the drug and the flow modifier.

【0017】混合時間はおのおのの混合方法に適した時
間を設定することができる。一般に、容器回転式混合機
の場合は3〜60分間程度の混合が好ましい。これより
時間が短いと効果が出にくい。これより長時間やっても
かまわないが、効果がさらに上がることは少ないので、
労力の無駄となる。5〜30分程度がさらに好ましい。
撹拌式混合機の場合は0.5〜10分程度の混合が好ま
しく、1〜5分程度がさらに好ましい。
The mixing time can be set to a time suitable for each mixing method. Generally, in the case of a container rotary type mixer, mixing for about 3 to 60 minutes is preferable. If the time is shorter than this, the effect is difficult to obtain. It doesn't matter if you do it longer than this, but since the effect is less likely to increase further,
It is a waste of labor. About 5 to 30 minutes is more preferable.
In the case of a stirring mixer, mixing for about 0.5 to 10 minutes is preferable, and about 1 to 5 minutes is more preferable.

【0018】本発明の方法で得られる、薬物含量の変動
係数が小さい薬物含有混合粉体は、必要に応じて、流動
化剤あるいは滑沢剤を添加した後、そのままカプセルに
充填して、カプセル剤としても良いし、散剤としても良
い。本発明の方法で得られる薬物含有混合粉体には、通
常用いられる錠剤製造法が適用できる。特に従来、薬物
含量が低い場合には、最終製剤中の薬物含量均一性に劣
るとして、敬遠されていた直接打錠法も、本発明におい
ては、その操作の簡便さのゆえに特に好ましく用いられ
る方法である。
The drug-containing mixed powder having a small coefficient of variation of drug content obtained by the method of the present invention may be added with a fluidizing agent or a lubricant, if necessary, and then filled into capsules as they are, to give capsules. It may be used as an agent or a powder. A commonly used tablet manufacturing method can be applied to the drug-containing mixed powder obtained by the method of the present invention. Particularly, when the drug content is low, the direct tableting method, which has been shunned as being inferior in the uniformity of the drug content in the final preparation, is particularly preferably used in the present invention because of its simple operation. Is.

【0019】上記、錠剤製造にあたっては、従来よく用
いられている他の手法を併用することができる。例え
ば、崩壊剤を適切に使用することで、薬物含量の変動が
小さい口腔内崩壊錠を製造することも自由である。ま
た、その他の添加剤として、ヒドロキシプロピルメチル
セルロースのようなゲル形成物質を添加することで、徐
放性錠剤にすることもできるし、更に、錠剤に苦味マス
キングを施したり、徐放性コーティングあるいは腸溶性
コーティングを施したりすることも自由である。
In the above-mentioned tablet production, it is possible to use other techniques which have been often used conventionally. For example, by appropriately using a disintegrant, it is also free to produce an orally disintegrating tablet with a small variation in drug content. In addition, a sustained-release tablet can be prepared by adding a gel-forming substance such as hydroxypropylmethylcellulose as another additive, and further, the tablet may be masked with a bitter taste, or the sustained-release coating or intestine may be added. It is also free to apply a soluble coating.

【0020】[0020]

【実施例】以下、実施例により本発明を詳細に発明する
が、本発明の技術範囲および実施態様をこれらにより制
限されるものではない。なお、実施例、比較例における
物性評価に関する手法は以下の通りである。 [薬物の平均粒径]デジタルマイクロスコープ((株)
キーエンス、VH−7000)あるいは電子顕微鏡
((株)日立製作所、)で撮影した画像を、画像処理解
析ソフトを使用して求めた。 [薬物混合粉体のサンプリング方法]薬物と流動改質剤
との混合粉体を、その他の添加剤と混合する工程におい
て、粉体試料採取器(筒井理化学(株)製。サンプル容
量0.8ml)を使用し、混合機としてV型ブレンダー
の場合、混合5分後、15分後、30分後に混合機を停
止して、各時点で所定の3箇所から3点ずつ、計9点サ
ンプリングを行う。混合機として高速撹拌混合機の場合
は、混合5分後のみについて測定を行う。
EXAMPLES The present invention will be described in detail below with reference to examples, but the technical scope and embodiments of the present invention are not limited thereto. In addition, the method regarding physical property evaluation in Examples and Comparative Examples is as follows. [Average particle size of drug] Digital microscope (Co., Ltd.)
Images taken with KEYENCE, VH-7000) or an electron microscope (Hitachi, Ltd.) were obtained using image processing analysis software. [Damping method of drug mixed powder] In the step of mixing the powder mixed with the drug and the flow modifier with other additives, a powder sampler (manufactured by Tsutsui Rikagaku Co., Ltd., sample volume 0.8 ml) In the case of a V-type blender as a mixer, the mixer is stopped after 5 minutes, 15 minutes, and 30 minutes of mixing, and 3 points are sampled from 3 predetermined points at each time point, and a total of 9 points are sampled. To do. When the mixer is a high-speed stirring mixer, the measurement is performed only after 5 minutes of mixing.

【0021】[打錠方法]ロータリー打錠機(クリーン
プレスコレクト12HUK、菊水製作所(株)製)を用
いて、所定の方法により、ターンテーブル回転数50r
pmで、径8mm、200mgの錠剤に成形した。 [薬物の定量方法]サンプリングした粉体から200m
gを精秤し、100mlメスフラスコに入れて、純水で
100mlにメスアップする。樹脂フィルタにより水溶
液中の不溶分を濾過した後、濾液中の薬物濃度を分光光
度計(日本分光(株)製)を用いて吸光度から定量し
た。錠剤の場合は、錠剤一個約200mgを精秤した
後、同様に操作し、定量した。
[Tabletting method] A rotary tabletting machine (Clean Press Collect 12HUK, manufactured by Kikusui Seisakusho Co., Ltd.) was used and a turntable rotation speed of 50r was obtained by a predetermined method.
It was formed into a tablet having a diameter of 8 mm and a diameter of 200 mg. [Determination method of drug] 200m from sampled powder
g is precisely weighed, put in a 100 ml measuring flask, and made up to 100 ml with pure water. After filtering the insoluble matter in the aqueous solution with a resin filter, the drug concentration in the filtrate was quantified from the absorbance using a spectrophotometer (manufactured by JASCO Corporation). In the case of tablets, about 200 mg of each tablet was precisely weighed, and then the same operation was performed to quantify.

【0022】[含量均一性の評価方法]薬物混合粉体を
評価する場合、上記、混合粉体サンプリング法により採
取した9個の試料各々の薬物濃度を測定し、錠剤を評価
する場合は、上記打錠法により得られた調剤を10個を
任意にサンプリングしたものの各々の重量並びに薬物濃
度を測定し、それら測定値の標準偏差および平均値よ
り、(標準偏差/平均値)*100で定義される変動係
数(%)から含量均一性を評価した。変動係数が低いほ
ど含量均一性が高い。
[Evaluation Method of Content Uniformity] In the case of evaluating a drug mixed powder, the drug concentration of each of the nine samples collected by the mixed powder sampling method is measured, and in the case of evaluating a tablet, the above method is used. The weight and drug concentration of each of 10 arbitrarily prepared preparations obtained by the tableting method were measured, and defined as (standard deviation / average value) * 100 from the standard deviation and average value of those measured values. Content uniformity was evaluated from the coefficient of variation (%). The lower the coefficient of variation, the higher the content uniformity.

【0023】[0023]

【実施例1】アセトアミノフェン(吉富ファインケミカ
ル(株)製の粉末タイプを小型粉砕機で粉砕して使用。
平均粒径16μm。)30g、タルク(和光純薬(株)
製)15gをポリエチレン袋に入れて、手動にて3分間
振とうして混合した後、その混合粉体30g、結晶セル
ロース「アビセル」PH−101(旭化成(株)製)4
00g、100メッシュ乳糖(DMV社製)1570g
を秤り取り(混合比率;結晶セルロース/乳糖/アセト
アミノフェン/タルク=20/78.5/1/0.
5)、容量5リットルのV型混合機(ダルトン社製)に
投入し(充填率を約65%に設定)、30分間混合し
た。薬物濃度の変動係数を表1に示す。
[Example 1] Acetaminophen (a powder type manufactured by Yoshitomi Fine Chemical Co., Ltd.) was crushed and used by a small crusher.
Average particle size 16 μm. ) 30 g, talc (Wako Pure Chemical Industries, Ltd.)
15 g in a polyethylene bag and shaken by hand for 3 minutes to mix, and then 30 g of the mixed powder, crystalline cellulose "Avicel" PH-101 (manufactured by Asahi Kasei Co., Ltd.) 4
00g, 100 mesh lactose (manufactured by DMV) 1570g
Were weighed (mixing ratio; crystalline cellulose / lactose / acetaminophen / talc = 20 / 78.5 / 1/0.
5) The mixture was put into a V-type mixer (manufactured by Dalton) having a capacity of 5 liters (filling rate was set to about 65%) and mixed for 30 minutes. The coefficient of variation of drug concentration is shown in Table 1.

【0024】[0024]

【実施例2】実施例1で使用したアセトアミノフェン3
0g、軽質無水ケイ酸「アエロジル200」(日本アエ
ロジル(株)製)3gをポリエチレン袋に入れて、3分
間手動で振とうし混合した後、その混合粉体22g、
「アビセル」PH−101を400g、100メッシュ
乳糖1578gを秤り取り(混合比率;結晶セルロース
/乳糖/アセトアミノフェン/軽質無水ケイ酸=20/
78.9/1/0.1)、実施例1と同様にV型混合機
で混合した。薬物濃度の変動係数を表1に示す。
Example 2 Acetaminophen 3 used in Example 1
0 g of light anhydrous silicic acid "Aerosil 200" (manufactured by Nippon Aerosil Co., Ltd.) was placed in a polyethylene bag and shaken by hand for 3 minutes to mix, and then 22 g of the mixed powder,
400 g of "Avicel" PH-101 and 1578 g of 100 mesh lactose were weighed (mixing ratio; crystalline cellulose / lactose / acetaminophen / light anhydrous silicic acid = 20 /
78.9 / 1 / 0.1) and mixed with a V-type mixer in the same manner as in Example 1. The coefficient of variation of drug concentration is shown in Table 1.

【0025】[0025]

【実施例3】実施例1で使用したアセトアミノフェン3
0g、タルク15gをポリエチレン袋に入れて、3分間
手動で振とうし混合した後、その混合粉体25.3g、
「アビセル」PH−101を675.6g、100メッ
シュ乳糖988.1gを秤り取り(混合比率;結晶セル
ロース/乳糖/アセトアミノフェン/タルク=40/5
8.5/1/0.5)、実施例1と同様にV型混合機で
混合した。薬物濃度の変動係数を表1に示す。
Example 3 Acetaminophen 3 used in Example 1
0 g and 15 g of talc were placed in a polyethylene bag and shaken by hand for 3 minutes to mix, and then 25.3 g of the mixed powder,
675.6 g of "Avicel" PH-101 and 988.1 g of 100 mesh lactose were weighed (mixing ratio; crystalline cellulose / lactose / acetaminophen / talc = 40/5).
8.5 / 1 / 0.5) and mixed with a V-type mixer in the same manner as in Example 1. The coefficient of variation of drug concentration is shown in Table 1.

【0026】[0026]

【実施例4】実施例1で使用したアセトアミノフェン3
0g、タルク15gをポリエチレン袋に入れて、3分間
手動で振とうし混合した後、その混合粉体27.1g、
結晶セルロース「セオラス」KG−802(旭化成
(株)製)を361.9g、100メッシュ乳糖142
9.4gを秤り取り(混合比率;結晶セルロース/乳糖
/アセトアミノフェン/タルク=20/78.5/1/
0.5)、実施例1と同様にV型混合機で混合した。薬
物濃度の変動係数を表1に示す。
Example 4 Acetaminophen 3 used in Example 1
0 g and talc 15 g were put in a polyethylene bag and shaken by hand for 3 minutes to mix, then 27.1 g of the mixed powder,
361.9 g of crystalline cellulose "Ceorus" KG-802 (manufactured by Asahi Kasei Corporation), 100 mesh lactose 142
9.4 g was weighed (mixing ratio; crystalline cellulose / lactose / acetaminophen / talc = 20 / 78.5 / 1 /
0.5) and mixed with a V-type mixer in the same manner as in Example 1. The coefficient of variation of drug concentration is shown in Table 1.

【0027】[0027]

【実施例5】実施例1で使用したアセトアミノフェン3
0g、ステアリン酸マグネシウム2.1gをポリエチレ
ン袋に入れて、3分間手動で振とうし混合した後、その
混合粉体14.8g、「セオラス」KG−802を55
2.5g、100メッシュ乳糖813.9gを秤り取り
(混合比率;結晶セルロース/乳糖/アセトアミノフェ
ン/ステアリン酸マグネシウム=40/58.93/1
/0.07)、実施例1と同様にV型混合機で混合し
た。薬物濃度の変動係数を表1に示す。
Example 5 Acetaminophen 3 used in Example 1
0 g and 2.1 g of magnesium stearate were put in a polyethylene bag and shaken by hand for 3 minutes to mix, and then 14.8 g of the mixed powder, 55 of "Ceorus" KG-802.
2.5 g and 813.9 g of 100 mesh lactose were weighed (mixing ratio; crystalline cellulose / lactose / acetaminophen / magnesium stearate = 40 / 58.93 / 1)
/0.07) and mixed with a V-type mixer in the same manner as in Example 1. The coefficient of variation of drug concentration is shown in Table 1.

【0028】[0028]

【実施例6】実施例1で使用したアセトアミノフェン3
0g、タルク15gをポリエチレン袋に入れて、3分間
手動で振とうし混合した後、その混合粉体31.2g、
造粒乳糖「Super−Tab」(ラクトース・ニュー
ジーランド社製)2050gを秤り取り(混合比率;乳
糖/アセトアミノフェン/タルク=98.5/1/0.
5)、実施例1と同様にV型混合機で混合した。薬物濃
度の変動係数を表1に示す。
Example 6 Acetaminophen 3 used in Example 1
0 g and talc 15 g were put in a polyethylene bag and shaken by hand for 3 minutes to mix, and then 31.2 g of the mixed powder,
2050 g of granulated lactose “Super-Tab” (Lactose New Zealand) was weighed (mixing ratio; lactose / acetaminophen / talc = 98.5 / 1/0.
5) and mixing with a V-type mixer as in Example 1. The coefficient of variation of drug concentration is shown in Table 1.

【0029】[0029]

【実施例7】実施例1で使用したアセトアミノフェン
1.9g、タルク1.9g、「アビセル」PH−101
/19gをポリエチレン袋に入れて、3分間手動で振と
うし混合した後、その混合粉体の全量、及び「アビセ
ル」PH−101/361g、「Super−Tab」
1516.2gを秤り取り(混合比率;結晶セルロース
/乳糖/アセトアミノフェン/タルク=20/79.8
/0.1/0.1)、実施例1と同様にV型混合機で混
合した。薬物濃度の変動係数を表1に示す。
Example 7 1.9 g of acetaminophen used in Example 1, 1.9 g of talc, "Avicel" PH-101
/ 19g was put in a polyethylene bag and shaken by hand for 3 minutes to mix, and then the total amount of the mixed powder and "Avicel" PH-101 / 361g, "Super-Tab"
Weigh 1516.2 g (mixing ratio; crystalline cellulose / lactose / acetaminophen / talc = 20 / 79.8)
/0.1/0.1) and mixed with a V-type mixer in the same manner as in Example 1. The coefficient of variation of drug concentration is shown in Table 1.

【0030】[0030]

【実施例8】エテンザミド(吉富ファインケミカル
(株)製Pタイプを小型粉砕機で粉砕して使用。平均粒
径は24μm。)800g、タルク160gを高速撹拌
混合機(パウレック(株)製、VG10型)に仕込み、
インペラ回転数400rpm、クロススクリュー150
0rpmで撹拌し、2分間混合した。続いて、その混合
粉体102g、及び「アビセル」PH−302/102
0g、マンニット(東和化成工業(株)製)578gを
秤り取り(混合比率;結晶セルロース/マンニット/エ
テンザミド/タルク=60/34/5/1)、実施例1
と同様にV型混合機で混合した。薬物濃度の変動係数を
表1に示す。
[Embodiment 8] 800 g of ethenzamid (P type manufactured by Yoshitomi Fine Chemical Co., Ltd. is crushed and used by a small crusher. The average particle size is 24 μm) and 160 g of talc are a high speed stirring mixer (manufactured by Paulec Co., VG10 type). ),
Impeller rotation speed 400 rpm, cross screw 150
Stir at 0 rpm and mix for 2 minutes. Then, 102 g of the mixed powder, and "Avicel" PH-302 / 102
0 g and 578 g of Mannitol (manufactured by Towa Kasei Co., Ltd.) were weighed (mixing ratio; crystalline cellulose / mannite / ethenzamid / talc = 60/34/5/1), Example 1
And mixed with a V-type mixer in the same manner. The coefficient of variation of drug concentration is shown in Table 1.

【0031】[0031]

【実施例9】塩酸フェニルプロパノールアミン(アルプ
ス薬品工業(株)製を小型粉砕機で粉砕して使用。平均
粒径は28μm。)50g、タルク25gをポリエチレ
ン袋に入れて、3分間手動で振とうし混合した。その
後、混合粉体57g、及び「アビセル」PH−101/
380g、100メッシュ乳糖703g、部分α化デン
プン「PCS」(旭化成(株)製)380g、マンニッ
ト380gを秤り取り(混合比率;結晶セルロース/乳
糖/部分α化デンプン/マンニット/塩酸フェニルプロ
パノールアミン/タルク=20/37/20/20/2
/1)、実施例1と同様にV型混合機で混合した。薬物
濃度の変動係数を表1に示す。
Example 9 50 g of phenylpropanolamine hydrochloride (manufactured by Alps Chemical Co., Ltd. was used after crushing with a small crusher. Average particle size is 28 μm) and 25 g of talc were placed in a polyethylene bag and shaken manually for 3 minutes. It was mixed. Then, 57 g of mixed powder, and "Avicel" PH-101 /
380 g, 100 mesh lactose 703 g, partially pregelatinized starch "PCS" (manufactured by Asahi Kasei Co., Ltd.) 380 g, and mannitol 380 g were weighed (mixing ratio; crystalline cellulose / lactose / partially pregelatinized starch / mannite / phenylpropanol hydrochloride) Amine / talc = 20/37/20/20/2
/ 1), and mixed with a V-type mixer in the same manner as in Example 1. The coefficient of variation of drug concentration is shown in Table 1.

【0032】[0032]

【実施例10】実施例1で使用したアセトアミノフェン
30g、タルク15gをポリエチレン袋に入れて、3分
間手動で振とうし混合した後、その混合粉体30g、及
び「アビセル」PH−101/400g、100メッシ
ュ乳糖1570gを秤り取り(混合比率;結晶セルロー
ス/乳糖/アセトアミノフェン/タルク=20/78.
5/1/0.5)、高速撹拌混合機に仕込み、インペラ
回転数400rpm、クロススクリュー1500rpm
で撹拌し、5分間混合した。薬物濃度の変動係数を表2
に示す。
[Example 10] 30 g of acetaminophen used in Example 1 and 15 g of talc were placed in a polyethylene bag and shaken by hand for 3 minutes to mix, and then 30 g of the mixed powder, and "Avicel" PH-101 / 400 g, 1570 g of 100 mesh lactose were weighed (mixing ratio; crystalline cellulose / lactose / acetaminophen / talc = 20/78.
5/1 / 0.5), charged into a high speed stirring mixer, impeller rotation speed 400 rpm, cross screw 1500 rpm
Stir and mix for 5 minutes. Table 2 shows the coefficient of variation of drug concentration
Shown in.

【0033】[0033]

【実施例11】V型混合機の混合時間を15分とする以
外は、実施例1と同様に混合を行った後、さらにステア
リン酸マグネシウム(太平化学(株)製)10gをV型
混合機に添加し、5分間混合した。混合後の薬物濃度の
変動係数を表3に示す。薬物含有量のばらつきの小さい
混合粉体が得られた。続いて、得られた全薬物混合粉体
から前述の方法により打錠し、錠剤重量、及び錠剤中の
薬物含有量変動係数を求めた。その結果を表3に示す。
錠剤重量及び薬物含有量のばらつきの小さい錠剤が得ら
れた。
[Embodiment 11] After mixing was carried out in the same manner as in Example 1 except that the mixing time of the V-type mixer was 15 minutes, 10 g of magnesium stearate (manufactured by Taihei Chemical Co., Ltd.) was further added to the V-type mixer. And mixed for 5 minutes. Table 3 shows the coefficient of variation of the drug concentration after mixing. A mixed powder having a small variation in the drug content was obtained. Subsequently, the obtained all-drug mixed powder was tabletted by the above-mentioned method, and the tablet weight and the coefficient of variation of the drug content in the tablet were determined. The results are shown in Table 3.
Tablets with small variations in tablet weight and drug content were obtained.

【0034】[0034]

【実施例12】V型混合機の混合時間を15分とする以
外は、実施例3と同様に混合を行った後、さらにステア
リン酸マグネシウム8.5gをV型混合機に添加し、5
分間混合した。混合後の薬物濃度の変動係数を表3に示
す。薬物含有量のばらつきの小さい混合粉体が得られ
た。続いて、実施例11と同様に操作し、錠剤重量、及
び錠剤中の薬物含有量変動係数を求めた。その結果を表
3に示す。錠剤重量及び薬物含有量のばらつきの小さい
錠剤が得られた。
[Example 12] After mixing was performed in the same manner as in Example 3 except that the mixing time of the V-type mixer was 15 minutes, 8.5 g of magnesium stearate was further added to the V-type mixer, and
Mix for minutes. Table 3 shows the coefficient of variation of the drug concentration after mixing. A mixed powder having a small variation in the drug content was obtained. Then, the same operation as in Example 11 was carried out to determine the tablet weight and the coefficient of variation of the drug content in the tablet. The results are shown in Table 3. Tablets with small variations in tablet weight and drug content were obtained.

【0035】[0035]

【比較例1】アセトアミノフェンとタルクとの前混合を
行わず、アセトアミノフェン20g、タルク10gをそ
のままV型混合機に仕込み、「アビセル」PH−10
1、100メッシュ乳糖との混合を実施例1と同様に実
施した(混合比率は実施例1と同じ)。薬物濃度の変動
係数を表1に示す。
Comparative Example 1 Acetaminophen 20 g and talc 10 g were directly charged into a V-type mixer without pre-mixing acetaminophen and talc, and "Avicel" PH-10
Mixing with 1,100 mesh lactose was performed in the same manner as in Example 1 (mixing ratio is the same as in Example 1). The coefficient of variation of drug concentration is shown in Table 1.

【0036】[0036]

【比較例2】アセトアミノフェンと「アエロジル20
0」との前混合を行わず、アセトアミノフェン20g、
「アエロジル200」2gをそのままV型混合機に仕込
み、「アビセル」PH−101、100メッシュ乳糖と
の混合を実施例2と同様に実施した(混合比率は実施例
2と同じ)。薬物濃度の変動係数を表1に示す。
[Comparative Example 2] Acetaminophen and "Aerosil 20"
0 "without pre-mixing with acetaminophen,
2 g of "Aerosil 200" was charged as it was into a V-type mixer, and mixing with "Avicel" PH-101, 100 mesh lactose was carried out in the same manner as in Example 2 (the mixing ratio is the same as in Example 2). The coefficient of variation of drug concentration is shown in Table 1.

【0037】[0037]

【比較例3】タルクを添加せずに、アセトアミノフェン
16.9g、「アビセル」PH−101/675.6
g、100メッシュ乳糖996.5gとの混合を実施例
3と同様に実施した(混合比率;結晶セルロース/乳糖
/アセトアミノフェン=40/59/1)。薬物濃度の
変動係数を表1に示す。
Comparative Example 3 Acetaminophen 16.9 g, “Avicel” PH-101 / 675.6 without adding talc.
g, 100 mesh lactose 996.5 g were mixed in the same manner as in Example 3 (mixing ratio; crystalline cellulose / lactose / acetaminophen = 40/59/1). The coefficient of variation of drug concentration is shown in Table 1.

【0038】[0038]

【比較例4】アセトアミノフェンとステアリン酸マグネ
シウムとの前混合を行わず、アセトアミノフェン13.
8g、ステアリン酸マグネシウム1gをそのままV型混
合機に仕込み、「セオラス」KG−802、100メッ
シュ乳糖との混合を実施例5と同様に実施した(混合比
率は実施例5と同じ)。薬物濃度の変動係数を表1に示
す。
Comparative Example 4 Acetaminophen 13. Acetaminophen was not premixed with magnesium stearate.
8 g and 1 g of magnesium stearate were charged into a V-type mixer as they were, and mixed with "Ceorus" KG-802, 100 mesh lactose in the same manner as in Example 5 (mixing ratio is the same as in Example 5). The coefficient of variation of drug concentration is shown in Table 1.

【0039】[0039]

【比較例5】タルクを添加せずに、アセトアミノフェン
1.9g、「アビセル」PH−101/19gをポリエ
チレン袋に入れて、3分間手動で振とうし混合した後、
その混合粉体の全量、及び「アビセル」PH−101/
361g、「Super−Tab」1518.1gを秤
り取り(混合比率;結晶セルロース/乳糖/アセトアミ
ノフェン=20/79.9/0.1)、実施例7と同様
にV型混合機で混合した。薬物濃度の変動係数を表1に
示す。
Comparative Example 5 1.9 g of acetaminophen and "Avicel" PH-101 / 19 g were put in a polyethylene bag without adding talc, and the mixture was shaken by hand for 3 minutes to mix,
The total amount of the mixed powder, and "Avicel" PH-101 /
361 g and “Super-Tab” 1518.1 g were weighed (mixing ratio; crystalline cellulose / lactose / acetaminophen = 20 / 79.9 / 0.1), and mixed with a V-type mixer in the same manner as in Example 7. did. The coefficient of variation of drug concentration is shown in Table 1.

【0040】[0040]

【比較例6】アセトアミノフェンとタルクとの前混合を
行わず、アセトアミノフェン20g、タルク10gをそ
のまま高速撹拌混合機に仕込み、「アビセル」PH−1
01、100メッシュ乳糖との混合を実施例10と同様
に実施した(混合比率は実施例10と同じ)。薬物濃度
の変動係数を表2に示す。
Comparative Example 6 Without pre-mixing acetaminophen and talc, 20 g of acetaminophen and 10 g of talc were directly charged into a high-speed stirring mixer, and "Avicel" PH-1
Mixing with 01,100 mesh lactose was carried out in the same manner as in Example 10 (mixing ratio is the same as in Example 10). The coefficient of variation of drug concentration is shown in Table 2.

【0041】[0041]

【比較例7】V型混合機の混合時間を15分とする以外
は、比較例1と同様に混合を行った後、さらにステアリ
ン酸マグネシウム10gをV型混合機に添加し、5分間
混合した。混合後の薬物濃度の変動係数を表3に示す。
続いて、実施例11と同様の方法にて得られた、錠剤重
量と錠剤中の薬物含有量の変動係数を表3に示す。
Comparative Example 7 After mixing was carried out in the same manner as in Comparative Example 1 except that the mixing time of the V-type mixer was 15 minutes, 10 g of magnesium stearate was further added to the V-type mixer and mixed for 5 minutes. . Table 3 shows the coefficient of variation of the drug concentration after mixing.
Then, Table 3 shows the coefficient of variation of the tablet weight and the drug content in the tablet, which were obtained in the same manner as in Example 11.

【0042】[0042]

【比較例8】V型混合機の混合時間を15分とする以外
は、比較例3と同様に混合を行った後、実施例12と同
様の方法にて得られた、錠剤重量と錠剤中の薬物含有量
の変動係数を表3に示す。尚、上記実施例、比較例の混
合粉体組成および混合条件の一覧を表4に示す。表中
「量」は、重量%を表す。
[Comparative Example 8] Tablet weight and tablet content obtained in the same manner as in Example 12 after mixing was performed in the same manner as in Comparative Example 3 except that the mixing time of the V-type mixer was 15 minutes. The coefficient of variation of the drug content of is shown in Table 3. Table 4 shows a list of mixed powder compositions and mixing conditions of the above Examples and Comparative Examples. In the table, "amount" represents% by weight.

【0043】[0043]

【表1】 [Table 1]

【0044】[0044]

【表2】 [Table 2]

【0045】[0045]

【表3】 [Table 3]

【0046】[0046]

【表4】 [Table 4]

【0047】[0047]

【発明の効果】本発明の、薬物と流動改質剤を混合した
後、該混合粉体とその他の添加剤を混合する方法を用い
ると、最終製剤に対して薬物含量が20重量%以下と低
含量であっても、極めて短時間で薬物含量の変動係数を
5%以下、好ましくは2.5%以下にすることができ
る。つまり、従来の薬物と流動改質剤とその他の添加剤
を一括で添加する方法と比べて、薬物含量の変動係数を
低く抑えるための混合時間を1/5程度に短縮すること
ができる。また、本発明の方法を用いて薬物の混合を行
えば、短時間で薬物含量の変動が小さい混合粉体が得ら
れるため、薬物含量が低い場合でも、直接打錠法で錠剤
を製造することが容易である。
[Effects of the Invention] When the method of mixing the drug and the flow modifier of the present invention and then mixing the mixed powder with other additives is used, the drug content is 20% by weight or less based on the final preparation. Even with a low content, the coefficient of variation of the drug content can be reduced to 5% or less, preferably 2.5% or less in a very short time. That is, the mixing time for suppressing the coefficient of variation of the drug content to be low can be shortened to about ⅕ as compared with the conventional method in which the drug, the flow modifier and the other additive are added all at once. Further, when the drug is mixed using the method of the present invention, a mixed powder having a small variation in the drug content can be obtained in a short time, and therefore, even when the drug content is low, tablets can be directly produced by the tableting method. Is easy.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 薬物と添加剤の混合において、薬物と流
動改質剤を混合した後、該混合粉体とその他の添加剤と
を混合することを特徴とする薬物の混合方法。
1. A method of mixing a drug, which comprises mixing the drug and a flow modifier, and then mixing the powder mixture and other additives.
【請求項2】 流動改質剤がタルク、軽質無水ケイ酸、
含水二酸化ケイ素、ステアリン酸塩よりなる群から選ば
れる1種または2種以上であることを特徴とする請求項
1の混合方法。
2. The flow modifier is talc, light anhydrous silicic acid,
2. The mixing method according to claim 1, which is one or more selected from the group consisting of hydrous silicon dioxide and stearate.
【請求項3】 その他の添加剤がセルロース類、及び/
または乳糖類を含有することを特徴とする請求項1又は
2の何れかの薬物の混合方法。
3. The other additives are celluloses, and / or
Alternatively, the method for mixing a drug according to claim 1 or 2, further comprising lactose.
JP2001273359A 2001-09-10 2001-09-10 Drug mixing method Expired - Lifetime JP4925526B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001273359A JP4925526B2 (en) 2001-09-10 2001-09-10 Drug mixing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001273359A JP4925526B2 (en) 2001-09-10 2001-09-10 Drug mixing method

Publications (2)

Publication Number Publication Date
JP2003081876A true JP2003081876A (en) 2003-03-19
JP4925526B2 JP4925526B2 (en) 2012-04-25

Family

ID=19098585

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001273359A Expired - Lifetime JP4925526B2 (en) 2001-09-10 2001-09-10 Drug mixing method

Country Status (1)

Country Link
JP (1) JP4925526B2 (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005073286A1 (en) 2004-01-30 2005-08-11 Asahi Kasei Chemicals Corporation Porous cellulose aggregate and formed product composition comprising the same
JP2005255617A (en) * 2004-03-11 2005-09-22 Asahi Kasei Chemicals Corp Solid pharmaceutical preparation composition comprising fine particulate active ingredient and porous cellulose aggregate
JP2006063030A (en) * 2004-08-27 2006-03-09 Fuji Pharmaceutical Co Ltd Method for producing tablet with low component content
WO2007066646A1 (en) 2005-12-06 2007-06-14 Asahi Kasei Chemicals Corporation Process for producing tablet by high-speed direct compression
JP2008189634A (en) * 2007-02-08 2008-08-21 Akiyama Jozai Kk Method for producing intraorally quickly disintegrable tablet
JP2010525052A (en) * 2007-04-25 2010-07-22 ザ プロクター アンド ギャンブル カンパニー Pharmaceutical dosage form with improved vitamin D content uniformity
US9132195B2 (en) 2008-05-21 2015-09-15 Asahi Kasei Chemicals Corporation Cellulose powder having excellent segregation preventive effect, and compositions thereof
KR20170015277A (en) 2014-06-10 2017-02-08 라이온 가부시키가이샤 Tablet containing sake yeast
JP2018177800A (en) * 2017-04-19 2018-11-15 日本臓器製薬株式会社 Production method of premix drug substance
KR20190005939A (en) 2016-05-10 2019-01-16 니폰 조키 세야쿠 가부시키가이샤 Method for producing acetaminophen formulations
WO2019093434A1 (en) 2017-11-09 2019-05-16 日本臓器製薬株式会社 Acetaminophen preparation, and method for producing same

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07138189A (en) * 1993-06-23 1995-05-30 Euro Celtique Sa Release control preparation coated with ethyl cellulose aqueous dispersion

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07138189A (en) * 1993-06-23 1995-05-30 Euro Celtique Sa Release control preparation coated with ethyl cellulose aqueous dispersion

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005073286A1 (en) 2004-01-30 2005-08-11 Asahi Kasei Chemicals Corporation Porous cellulose aggregate and formed product composition comprising the same
US8597686B2 (en) 2004-01-30 2013-12-03 Asahi Kasei Chemicals Corporation Porous cellulose aggregate and formed product composition comprising the same
JP2005255617A (en) * 2004-03-11 2005-09-22 Asahi Kasei Chemicals Corp Solid pharmaceutical preparation composition comprising fine particulate active ingredient and porous cellulose aggregate
JP2006063030A (en) * 2004-08-27 2006-03-09 Fuji Pharmaceutical Co Ltd Method for producing tablet with low component content
JP4756153B2 (en) * 2004-08-27 2011-08-24 富士製薬工業株式会社 Method for producing tablets with low content
EP1958619A4 (en) * 2005-12-06 2012-09-19 Asahi Kasei Chemicals Corp Process for producing tablet by high-speed direct compression
WO2007066646A1 (en) 2005-12-06 2007-06-14 Asahi Kasei Chemicals Corporation Process for producing tablet by high-speed direct compression
EP1958619A1 (en) * 2005-12-06 2008-08-20 Asahi Kasei Chemicals Corporation Process for producing tablet by high-speed direct compression
JP4841564B2 (en) * 2005-12-06 2011-12-21 旭化成ケミカルズ株式会社 Tablet production method by high-speed direct tableting
US8106100B2 (en) 2005-12-06 2012-01-31 Asahi Kasei Chemicals Corporation Process for producing tablet by high-speed direct compression
JP2008189634A (en) * 2007-02-08 2008-08-21 Akiyama Jozai Kk Method for producing intraorally quickly disintegrable tablet
JP2010525052A (en) * 2007-04-25 2010-07-22 ザ プロクター アンド ギャンブル カンパニー Pharmaceutical dosage form with improved vitamin D content uniformity
US8703187B2 (en) 2007-04-25 2014-04-22 Warner Chilcott Company, Llc Vitamin D content uniformity in pharmaceutical dosage forms
US9132195B2 (en) 2008-05-21 2015-09-15 Asahi Kasei Chemicals Corporation Cellulose powder having excellent segregation preventive effect, and compositions thereof
KR20170015277A (en) 2014-06-10 2017-02-08 라이온 가부시키가이샤 Tablet containing sake yeast
KR20190005939A (en) 2016-05-10 2019-01-16 니폰 조키 세야쿠 가부시키가이샤 Method for producing acetaminophen formulations
US11033501B2 (en) 2016-05-10 2021-06-15 Nippon Zoki Pharmaceutical Co., Ltd. Method for manufacturing acetaminophen preparation
US11433031B2 (en) 2016-05-10 2022-09-06 Nippon Zoki Pharmaceutical Co., Ltd. Method for manufacturing acetaminophen preparation
JP2018177800A (en) * 2017-04-19 2018-11-15 日本臓器製薬株式会社 Production method of premix drug substance
JP7105473B2 (en) 2017-04-19 2022-07-25 日本臓器製薬株式会社 Manufacturing method of premix drug substance
WO2019093434A1 (en) 2017-11-09 2019-05-16 日本臓器製薬株式会社 Acetaminophen preparation, and method for producing same
US11458102B2 (en) 2017-11-09 2022-10-04 Nippon Zoki Pharmaceutical Co., Ltd. Acetaminophen preparation, and method for producing same

Also Published As

Publication number Publication date
JP4925526B2 (en) 2012-04-25

Similar Documents

Publication Publication Date Title
TWI453203B (en) New solid pharmaceutical formulations comprising bibw 2992
US20210069207A1 (en) Pharmaceutical solid preparation comprising benzazepines and production method thereof
JP2009524658A (en) Levetiracetam preparation and method for producing the same
CA2755274A1 (en) Tablet and granulated powder containing 6-fluoro-3-hydroxy-2-pyrazinecarboxamide
JP6804585B2 (en) Pharmaceutical dosage form
JP2003081876A (en) Method for mixing medicine
JP2002326927A (en) Quick-releasing tablet containing metformin hydrochloride
TWI418370B (en) Dissolution-stable pharmaceutical agent
JP6496084B2 (en) Orally disintegrating tablets
JP4698000B2 (en) Easily water-soluble drug-containing tablets
JP2007314448A (en) Method for producing cetirizine hydrochloride-containing tablet
JPH1121236A (en) Loxoprofen-sodium solid preparation
JP3746062B2 (en) Solid preparation and method for producing the same
JP6321131B2 (en) Dissolution improvement method of amlodipine-containing combination tablets
JP2021098671A (en) Pharmaceutical composition containing levetiracetam
EP2153822A1 (en) Granulation of active pharmaceutical ingredients
WO2022042646A1 (en) Lurasidone hydrochloride composition and preparation method therefor
JP2016117652A (en) Fast disintegrating tablet suitable for administration to children, and simple production method thereof
JP2003160487A (en) Pravastatin sodium-containing tablet and method for producing the same
JP6233911B2 (en) Irbesartan-containing tablets with improved chemical stability
JP2017132724A (en) Orally disintegrating tablet formulation comprising amlodipine-containing coated granulated material
WO2023067522A1 (en) Pharmaceutical compositions

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20080908

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20110906

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20111102

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20111122

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20120117

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20120207

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20120207

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20150217

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 4925526

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

EXPY Cancellation because of completion of term