JP3354172B2 - Heavy granulation of high drug content powder - Google Patents

Heavy granulation of high drug content powder

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Publication number
JP3354172B2
JP3354172B2 JP19031792A JP19031792A JP3354172B2 JP 3354172 B2 JP3354172 B2 JP 3354172B2 JP 19031792 A JP19031792 A JP 19031792A JP 19031792 A JP19031792 A JP 19031792A JP 3354172 B2 JP3354172 B2 JP 3354172B2
Authority
JP
Japan
Prior art keywords
powder
granulation
raw material
granulated
fluidized
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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JP19031792A
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Japanese (ja)
Other versions
JPH0630975A (en
Inventor
浩 坂本
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Powrex KK
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Powrex KK
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Publication of JPH0630975A publication Critical patent/JPH0630975A/en
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、製薬等粉体を処理す
る造粒、コーティング等の粒子加工操作に関するもの
で、薬物の含有割合の高い粉体の重質造粒に適した造粒
方法を提供する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a particle processing operation such as granulation and coating for treating powders such as pharmaceuticals, and a granulation method suitable for heavy granulation of powders having a high drug content. I will provide a.

【0002】[0002]

【従来の技術】カプセル用、コーティング用顆粒として
従来はグラニュー糖等を核(シード)に用いてその表面
に薬物を層状に被覆造粒する方法が多く採用されている
が、薬物の含有割合の高い処方(たとえば薬物が80%
以上)では造粒物が大きくなるためカプセルを大きくし
なければならない。また、流動層造粒で得られる造粒物
は嵩高くカプセルに充填するのに不適当であった。この
ような状況からシードを用いないで重質な造粒物を調製
する技法の要請が増加してきた。
2. Description of the Related Art Conventionally, as a granule for capsules and coatings, a method of coating and granulating a drug in a layer on the surface thereof using granulated sugar or the like as a nucleus (seed) has been widely used. High prescription (eg 80% drug
In the above), the granules are large, so the capsules must be large. Further, the granulated product obtained by fluidized bed granulation was bulky and was unsuitable for filling in capsules. Under such circumstances, the demand for techniques for preparing heavy granules without using seeds has increased.

【0003】[0003]

【発明が解決しようとする課題】製薬等で造粒される原
料粉末の性質において、静電気に起因する性質および粉
体そのものの性質による付着・凝集性の高い微粉末の湿
式造粒には下記の問題点があった。
Among the properties of raw material powders to be granulated in pharmaceuticals, etc., the following wet granulation of fine powders having high adhesion and cohesion due to the properties due to static electricity and the properties of the powders themselves are as follows. There was a problem.

【0004】流動造粒法による場合、その性質のために
装置壁面への付着および吹抜け等の流動不良が生じて満
足のいく造粒操作ができなかった。そこで、これを改善
するためにその性質を緩和する粉末助剤を多量に添加し
ていた。
[0004] In the case of the fluidized-granulation method, due to its properties, poor flow such as adhesion to the apparatus wall and blow-through occurred, and a satisfactory granulation operation could not be performed. Therefore, in order to improve this, a large amount of a powder auxiliary agent for relaxing the property has been added.

【0005】押出し造粒の場合、強い混練装置で混練し
てから押出し造粒を行ない、乾燥工程を経て整粒する、
というように複数の装置および操作が必要であった。ま
た、できた造粒物は強い混練のために硬い造粒物とな
り、溶解・崩壊が悪い等の難点があり、これを改善する
ためその性質を緩和する助剤の添加が必要であった。
In the case of extrusion granulation, the mixture is kneaded with a strong kneading device, extruded and granulated, and subjected to a drying process to form a granulated product.
Thus, multiple devices and operations were required. In addition, the formed granules are hard granules due to strong kneading, and have problems such as poor dissolution and disintegration. To improve this, it is necessary to add an auxiliary agent for relaxing the properties.

【0006】このように、従来は造粒操作に助剤が必要
なためその分だけ量が増加して錠剤の大きさが大きくな
り、大型カプセルにしなければ充填できない。ところ
が、大きな錠剤、大きなカプセルは呑込みが困難である
など老人や乳幼児の服用には難点がある。服用しやすく
するため錠剤を破砕して投与することもある。しかし、
最近の錠剤等は錠剤表面に薬物放出を制御するコーティ
ング等を施して腸溶性、徐放性等を付与しているが、錠
剤を破砕するとそのような薬物放出制御ができなくなる
という問題がある。
[0006] As described above, conventionally, an auxiliary agent is required for the granulation operation, so that the amount is increased by that amount and the size of the tablet is increased. However, it is difficult for elderly people and infants to take large tablets and capsules. Tablets may be disintegrated for easier administration. But,
In recent tablets and the like, a coating or the like for controlling drug release is provided on the tablet surface to impart enteric properties, sustained release properties, and the like. However, when the tablet is crushed, such a drug release control cannot be performed.

【0007】そこで、この発明の目的は、付着・凝集性
の高い粉体でも、助剤の添加量を可及的に少なくするこ
とのできる造粒方法を提供することにある。
Accordingly, an object of the present invention is to provide a granulation method capable of minimizing the amount of an auxiliary agent added to powder having high adhesion and cohesion.

【0008】[0008]

【課題を解決するための手段】この発明は、付着・凝集
性の高い微粉末よりなる原料粉末を造粒するにあたり、
適当温度に調節した気体により原料粉末を流動させる流
動層造粒装置の容器内底部に垂直回転軸を中心として回
転する攪拌部材を具備した転動流動装置を用い、原料粉
末の付着・凝集性等その性質を改善するための粉末助剤
を原料粉末に対し0乃至15%添加して、装置内で転動
流動させ、粉体の濡れ・溶解性に応じて流動層内部の粉
末の水分をあらかじめ設定した値に制御しながら結合剤
をスプレーして造粒し、得られた造粒物に結合剤をスプ
レーし、当該造粒物の表面に同一粉末もしくは他の粉末
を被覆し重質造粒するものである。
SUMMARY OF THE INVENTION The present invention relates to a method for granulating a raw material powder comprising a fine powder having high adhesion and cohesion.
Adhesion and agglomeration of the raw material powder, etc., using a rolling fluidizing device equipped with a stirring member that rotates around a vertical rotation axis at the bottom of the vessel of the fluidized bed granulator that flows the raw material powder with the gas adjusted to an appropriate temperature A powder auxiliary for improving the properties is added to the raw material powder in an amount of 0 to 15%, and the powder is tumbled and fluidized in the apparatus. According to the wettability and solubility of the powder, the water content of the powder in the fluidized bed is previously determined. The binder is sprayed and granulated while controlling to the set value, and the obtained granulated material is sprayed with the binder, and the same powder or another powder is coated on the surface of the granulated material to perform heavy granulation. Is what you do.

【0009】[0009]

【作用】流動層装置の底部に攪拌部材を具備した転動流
動装置を用いることにより粉末の流動不良が解消し、ま
た、原料粉体の濡れ・溶解性に応じて流動する原料粉体
の流動層内水分をあらかじめ計算もしくは計測した値に
なるように制御しながら結合剤をスプレー等により添加
し造粒することにより壁面に付着した微粉末も造粒の進
行と共に造粒物がかき落とすので、原料粉体の付着・凝
集性等といった性質を改善するための粉末助剤が0から
15%程度以内の少ない添加率でも造粒が可能となる。
さらに重質顆粒を得る方法として、上記操作で得られた
造粒物(一次造粒)に結合剤をスプレー等して表面を湿
潤させ、ここに同一物質を粉末添加して修飾造粒(粉末
で被覆する)することにより一次造粒物粒子表面の谷間
に粉末で充填する操作を行ない、重質で球形な表面の滑
らかな造粒物が得られる。
By using a tumbling fluidizing device equipped with a stirring member at the bottom of the fluidized bed device, poor flow of the powder is eliminated, and the flow of the raw material powder flowing according to the wettability and solubility of the raw material powder is improved. By adding the binder by spraying and granulating while controlling the moisture in the layer to be a value calculated or measured in advance, the fine powder attached to the wall also scrapes off the granulated material as the granulation progresses, Granulation is possible even with a small addition ratio of a powder auxiliary agent for improving properties such as adhesion and cohesion of the raw material powder within a range of about 0 to 15%.
Further, as a method for obtaining heavy granules, the granulated material (primary granules) obtained by the above operation is wetted by spraying a binder or the like, and the same substance is added thereto in a powder form to modify the granules (powder). ) To perform the operation of filling with powder in the valleys on the surface of the primary granulated particles, whereby a heavy, spherical, smooth granulated product having a spherical surface can be obtained.

【0010】[0010]

【実施例】まず、図1(a)に例示したこの発明の造粒
方法に使用する転動流動装置について説明すると、流動
層装置(1)の容器内底部に、垂直回転軸を中心にして
回転可能に拌羽根付き回転円板(3)を設け、この回転
円板(3)の下部中心から外周を通り流動室(2)に、
適当な温度に調節した気体を通気する。この場合、攪拌
羽根付き回転円板(3)が攪拌部材を構成して粒子に強
い転動作用を与える。攪拌羽根の構造は、たとえば、円
周方向に交互に現われるように配置した傾斜平面部と水
平面部を回転円板(3)の上面に一体的に形成させる。
なお、そのような攪拌羽根を有しない回転円板であって
も粉体粒子に攪拌転動作用を与えることができるため、
攪拌部材というときは攪拌羽根を有しない回転円板をも
含むものとする。また、通気構造としては、回転円板
(3’)にスリットを形成したり(図1(b))、回転円
板(3”)の一部に金網あるいは多孔板のような通気性
材料を使用することもできる(図1(c))。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, a rolling fluidizing device used in the granulating method of the present invention illustrated in FIG. 1 (a) will be described. A rotatable disk (3) with stirring blades is provided rotatably, and from the lower center of the rotary disk (3) to the fluid chamber (2) through the outer periphery.
The gas adjusted to an appropriate temperature is vented. In this case, the rotating disk (3) with stirring blades constitutes a stirring member and gives the particles a strong rolling operation. In the structure of the stirring blade, for example, an inclined plane part and a horizontal plane part arranged so as to appear alternately in the circumferential direction are integrally formed on the upper surface of the rotating disk (3).
It should be noted that even a rotating disk having no such stirring blades can provide the powder particles with a stirring rotation operation,
The term "stirring member" includes a rotating disk having no stirring blade. As the ventilation structure, a slit is formed in the rotating disk (3 ') (FIG. 1 (b)), or a part of the rotating disk (3 ") is made of a permeable material such as a wire mesh or a perforated plate. It can also be used (FIG. 1 (c)).

【0011】原料粉末の付着・凝集性等その性質を改善
するために添加する乳糖、澱粉等の粉末助剤は、原料粉
末に対し0乃至15%の範囲とする。
The amount of powder auxiliary such as lactose or starch added to improve the properties such as adhesion and cohesion of the raw material powder is in the range of 0 to 15% based on the raw material powder.

【0012】粉体の濡れ・溶解性に応じて流動層内部の
粉末の水分をあらかじめ設定した値に制御しながら結合
剤をスプレーする。ノズル位置は図示を省略してある
が、目的に応じてトップスプレー、下部接線スプレー、
中間部接線スプレーなどが可能である。トップスプレー
は粉末からの造粒に適し、回転円板の作用により流動不
良が生じないため大風量の必要性が少ない。このためノ
ズル上に浮遊する微粉末の割合が少なく、したがってス
プレーミストに接触し造粒される割合が高い。また、回
転円板の転動・分散作用により流動層に比較して粗大粒
子の生成が少なく、粒度分布はシャープになる。接線ス
プレーは修飾造粒およびコーティングに適したスプレー
方式で、修飾造粒はスプレーノズルと同軸で粉末の供給
も可能な構造である。鞘付きノズルはスプレーされたミ
ストが分散したところで粒子と接触するように工夫した
もので、流動する粒子層の中に挿入してもノズル先端
(ミストが霧状にならない領域)に粒子が進入しないよ
うに二次空気を通気しスプレーゾーンを確保してある。
この結果ノズルの汚れ(粉末付着)はほとんどない。
The binder is sprayed while controlling the water content of the powder inside the fluidized bed to a predetermined value according to the wettability and solubility of the powder. Although the nozzle position is not shown, top spray, lower tangential spray,
Intermediate tangential spraying is possible. Top spray is suitable for granulation from powder, and there is no need for a large air volume because flow action does not occur due to the action of the rotating disk. For this reason, the ratio of the fine powder floating on the nozzle is small, and therefore, the ratio of contact with the spray mist and granulation is high. In addition, due to the rolling and dispersing action of the rotating disk, the generation of coarse particles is smaller than in the fluidized bed, and the particle size distribution becomes sharp. The tangential spray is a spray method suitable for modified granulation and coating, and the modified granulation has a structure capable of supplying powder coaxially with a spray nozzle. The sheathed nozzle is designed so that the sprayed mist comes into contact with the particles when it is dispersed. Even when inserted into the flowing particle layer, the particles do not enter the nozzle tip (the area where the mist does not become mist) The secondary air is ventilated to ensure a spray zone.
As a result, the nozzle is hardly stained (powdered powder).

【0013】次に、図1(a)に示した構造を有する多機
能型転動流動装置(商品名「マルチプレックス」)にア
セトアミノフェン粉末を仕込み、助剤を全く添加するこ
となく転動流動造粒を行ない(一次造粒)、この造粒物
にアセトアミノフェンを粉末添加し修飾造粒した場合の
造粒物の粒度分布を図2に示す。なお、実験条件は表1
のとおりである。
Next, acetaminophen powder was charged into a multifunctional tumbling and fluidizing device (trade name “Multiplex”) having the structure shown in FIG. 1A, and tumbling was performed without adding any auxiliary agent. FIG. 2 shows the particle size distribution of the granulated product obtained by performing fluidized granulation (primary granulation), adding acetaminophen to the granulated product, and subjecting the granulated product to modified granulation. Table 1 shows the experimental conditions.
It is as follows.

【0014】[0014]

【表1】 [Table 1]

【0015】図2に示されるように、粒度分布がシャー
プで重質な造粒が、特別なシードを用いなくても容易な
操作で可能となった。
As shown in FIG. 2, a heavy granulation having a sharp particle size distribution can be achieved by an easy operation without using a special seed.

【0016】処方は、造粒操作が困難な難溶性薬物とし
てアセトアミノフェンを用いたが、結晶性の粉末である
ため造粒物の表面状態はやや粗くなった。水溶性の高い
薬物では滑らかな表面状態になり易い。特にアセトアミ
ノフェンは流動層造粒法では壁面付着が多く、また吹抜
け現象のため円滑な流動状態の保持が困難であるが、転
動流動造粒ではこのような現象は初期の短時間のみで、
造粒の進行とともに解消され良好な造粒性を示す。
In the formulation, acetaminophen was used as a poorly soluble drug which was difficult to granulate, but the surface state of the granulated material was slightly rough because it was a crystalline powder. A highly water-soluble drug tends to have a smooth surface state. In particular, acetaminophen has a large amount of wall adhesion in the fluidized-bed granulation method, and it is difficult to maintain a smooth fluidized state due to the blow-through phenomenon. ,
It is eliminated with the progress of granulation and shows good granulation properties.

【0017】操作のポイントは過大風量としないこと
で、特に修飾造粒すなわち粉掛けでの大風量は添加した
修飾用粉末の飛散による付着効率の低下につながる。修
飾用粉末が付着し転動作用により圧密された後に流動化
空気と接触し表面乾燥を経て再度、濡れ、粉末付着が繰
り返される回転円板の構造が適当である。
The point of the operation is that the amount of air is not excessively large. In particular, the large amount of air in the modification granulation, that is, powdering, leads to a decrease in the adhesion efficiency due to the scattering of the added modification powder. The structure of the rotating disk, in which the powder for modification is adhered and compacted by the rolling operation, comes into contact with fluidized air, undergoes surface drying, is wetted again, and powder adhesion is repeated, is appropriate.

【0018】造粒操作の末期において造粒の進行は抑制
しながら造粒物の表面に結合剤を添加することで打錠性
の向上がはかれる。
At the end of the granulation operation, tableting properties can be improved by adding a binder to the surface of the granulated product while suppressing the progress of granulation.

【0019】また、強い混練作用はないため造粒物も適
度の硬さで打錠性もよく、造粒物は球形に近く表面も滑
らかなため薬物放出制御のためのコーテイング等の後処
理が容易である。
Further, since there is no strong kneading action, the granulated material has a moderate hardness and good tableting properties. The granulated material is nearly spherical and has a smooth surface, so that post-treatments such as coating for controlling drug release can be performed. Easy.

【0020】添加する粉末の性質によっては結合剤の中
に分散・懸濁してスプレーしても同様な結果が得られ
る。
Depending on the nature of the powder to be added, similar results can be obtained by dispersing and suspending in a binder and spraying.

【0021】また、造粒物の状況によっては修飾造粒を
省略してもよい。
Further, depending on the condition of the granulated material, the modified granulation may be omitted.

【0022】[0022]

【発明の効果】この発明によれば、粉末の流動不良が解
消し、原料粉体の付着・凝集性等といった性質を改善す
るための粉末助剤が0から15%程度以内の少ない添加
率でも造粒が可能である。したがって、従来の流動層造
粒による場合のように造粒物が大きくならず、かつ、粒
度分布のシャープな造粒が可能で、この造粒物をシード
に同種の薬物による修飾造粒、もしくは多成分の粉末を
多層被覆しフイルムコーティングを行なう等の操作が可
能となったものである。これらの造粒物は流動層造粒に
比較してカプセル充填及びコーティング用顆粒として良
好であり、また多層の修飾造粒により多様化した要望に
対応できる。
According to the present invention, the poor flow of the powder is eliminated, and the powder auxiliary agent for improving the properties such as the adhesion and cohesion of the raw material powder is added even at a small addition rate of about 0 to 15%. Granulation is possible. Therefore, as in the case of conventional fluidized bed granulation, the granulated material does not become large, and granulation with a sharp particle size distribution is possible, and the granulated material is modified and granulated with the same drug as a seed, or It is possible to perform operations such as multi-layer coating of multi-component powder and film coating. These granulated products are better as granules for capsule filling and coating than fluidized bed granulation, and can respond to diversified demands by multi-layer modified granulation.

【図面の簡単な説明】[Brief description of the drawings]

【図1】転動流動装置を例示する縦断面略図である。FIG. 1 is a schematic longitudinal sectional view illustrating a tumbling flow device.

【図2】粒度分布図である。FIG. 2 is a particle size distribution diagram.

【符号の説明】[Explanation of symbols]

1 流動層装置 2 流動室 3 回転円板 DESCRIPTION OF SYMBOLS 1 Fluid bed apparatus 2 Fluid chamber 3 Rotating disk

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 付着・凝集性の高い微粉末よりなる原料
粉末を造粒するにあたり、適当温度に調節した気体によ
り原料粉末を流動させる流動層造粒装置の容器内底部に
垂直回転軸を中心として回転する攪拌部材を具備した転
動流動装置を用い、原料粉末の付着・凝集性等その性質
を改善するための粉末助剤を原料粉末に対し0乃至15
%添加して、装置内で転動流動させ、粉体の濡れ・溶解
性に応じて流動層内部の粉末の水分をあらかじめ設定し
た値に制御しながら結合剤をスプレーして造粒し、得ら
れた造粒物に結合剤をスプレーし、当該造粒物の表面に
同一粉末もしくは他の粉末を被覆し重質造粒することを
特徴とする高薬物含量粉体の重質造粒法。
When granulating a raw material powder comprising a fine powder having high adhesion and cohesion, a vertical rotation axis is centered on the bottom inside a vessel of a fluidized-bed granulator for flowing the raw material powder with a gas adjusted to an appropriate temperature. And a powder auxiliary agent for improving the properties such as adhesion and cohesion of the raw material powder is added to the raw material powder in an amount of from 0 to 15%.
%, And tumbled and fluidized in the apparatus. The binder was sprayed and granulated while controlling the water content of the powder in the fluidized bed to a preset value according to the wettability and solubility of the powder. A heavy granulation method for a high drug content powder, comprising spraying a binder onto the obtained granules, coating the surface of the granules with the same powder or another powder, and performing heavy granulation.
JP19031792A 1992-07-17 1992-07-17 Heavy granulation of high drug content powder Expired - Lifetime JP3354172B2 (en)

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JP19031792A JP3354172B2 (en) 1992-07-17 1992-07-17 Heavy granulation of high drug content powder

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Cited By (1)

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CN108261396A (en) * 2016-12-30 2018-07-10 北京化工大学 A kind of method of granulating

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JPWO2015046383A1 (en) * 2013-09-30 2017-03-09 富士フイルム株式会社 Process for producing drug substance-containing nucleus, drug substance-containing nucleus, pharmaceutical composition, and orally disintegrating tablet
JP5897196B1 (en) * 2015-10-05 2016-03-30 大同化成工業株式会社 Compound granulated product containing sugar or sugar alcohol, swelling binder, disintegrant and superabsorbent excipient, and production method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108261396A (en) * 2016-12-30 2018-07-10 北京化工大学 A kind of method of granulating

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