JP2007091688A - Method for producing fine powder for coating of solid preparation - Google Patents

Method for producing fine powder for coating of solid preparation Download PDF

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JP2007091688A
JP2007091688A JP2005286543A JP2005286543A JP2007091688A JP 2007091688 A JP2007091688 A JP 2007091688A JP 2005286543 A JP2005286543 A JP 2005286543A JP 2005286543 A JP2005286543 A JP 2005286543A JP 2007091688 A JP2007091688 A JP 2007091688A
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fine powder
coating
polymer
powder
solid preparation
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Shinji Fujimoto
信司 藤本
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Kurimoto Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an industrial method for the mass-production of fine powder for the coating of a solid preparation to enable dense coating even by a dry process. <P>SOLUTION: Agglomerated particles of fine polymer powder produced massively by spray drying and having an average particle diameter of ≤1μm is disintegrated and classified by a jet mill furnished with an air stream classifier. The fine powder for the coating of a solid preparation, having an average particle diameter of ≤1μm and enabling dense coating even by a dry process can be produced in a mass on an industrial scale by efficiently disintegrating the agglomerated particles of fine polymer powder producible in a mass by spray drying. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、固形製剤をコーティングする固形製剤コーティング用微粉末の製造方法に関する。   The present invention relates to a method for producing a fine powder for coating a solid preparation for coating a solid preparation.

固形製剤には、その薬物の効くタイミングや速度を調節したり、薬物から特定の部位を保護したりする等の目的に応じて、各種の基剤がコーティングされる。このコーティング基剤には、セルロース系、アクリル系、生体内分解性等の高分子粉末が多く用いられ、湿式法または乾式法のコーティングによって固形製剤にコーティングされる。湿式法では、コーティング基剤を溶解または懸濁させた液を固形製剤に噴霧したのち、液体を蒸発させるコーティング方法が一般的であり、乾式法では、コーティング基剤と結合剤を固形製剤と一緒に撹拌し、コーティング基剤を結合剤によって固形製剤に付着させるコーティング方法が一般的である。   The solid preparation is coated with various bases in accordance with the purpose of adjusting the timing and speed at which the drug works or protecting a specific site from the drug. As the coating base, a polymer powder such as cellulose, acrylic or biodegradable is often used, and is coated on a solid preparation by a wet method or a dry method. In the wet method, a coating method in which a liquid in which a coating base is dissolved or suspended is sprayed on a solid preparation and then the liquid is evaporated is generally used. In the dry method, the coating base and the binder are combined with the solid preparation. In general, a coating method is used in which the coating base is adhered to a solid preparation by a binder.

前記コーティング基剤としての高分子粉末は、緻密なコーティングを行うために、平均粒子径が1μm以下の高分子微粉末であることが望ましい。このような平均粒子径が1μm以下の高分子微粉末のコーティング基剤を製造する方法としては、セルロース系高分子を、水と任意の割合で混合できる有機溶剤を含んだ溶媒に溶解して高分子溶液とし、この高分子溶液を水と混合したあとに有機溶剤を除去した濃縮液を噴霧乾燥する方法が提案されている(例えば、特許文献1参照)。特許文献1には、噴霧乾燥では平均粒子径が10μm程度の高分子粉末が得られ、この高分子粉末を水に再投入して分散させて得られた分散液中の高分子微粉末の平均粒子径が1μm以下であったと記載されている。すなわち、この噴霧乾燥で得られた10μm程度の高分子粉末は、平均粒子径が1μm以下の高分子微粉末の結合粒体となっている。   The polymer powder as the coating base is desirably a polymer fine powder having an average particle diameter of 1 μm or less in order to perform dense coating. As a method for producing such a coating base of a polymer fine powder having an average particle diameter of 1 μm or less, a cellulose polymer is dissolved in a solvent containing an organic solvent that can be mixed with water at an arbitrary ratio. There has been proposed a method of spray-drying a concentrated solution obtained by forming a molecular solution and mixing the polymer solution with water and then removing the organic solvent (see, for example, Patent Document 1). In Patent Document 1, a polymer powder having an average particle size of about 10 μm is obtained by spray drying, and the average of the polymer fine powder in the dispersion obtained by re-injecting the polymer powder into water and dispersing it. It is described that the particle diameter was 1 μm or less. That is, the polymer powder of about 10 μm obtained by this spray drying is a bonded particle of polymer fine powder having an average particle size of 1 μm or less.

前記噴霧乾燥による造粒法は高温気流中に液体を分散させて乾燥する方法であり、液体の比表面積を著しく増加させることにより、秒単位で乾燥して大量の粉末を得ることができる。この噴霧乾燥造粒法は、微粒化、熱風と液滴の接触、水分蒸発、熱風からの製品の分離回収の4段階から成る(例えば、非特許文献1参照)。また、熱風と液滴の接触方法には、並流、向流、混合流の3方式があり、並流方式では液滴が水含有量の多い段階で熱風と接触し、乾燥が進むにつれて周囲の温度が低下するので、熱に弱い物質の乾燥に適している。   The granulation method by spray drying is a method in which a liquid is dispersed in a high-temperature air stream and dried, and by greatly increasing the specific surface area of the liquid, it can be dried in seconds to obtain a large amount of powder. This spray drying granulation method is composed of four stages of atomization, contact between hot air and droplets, evaporation of moisture, and separation and recovery of products from the hot air (for example, see Non-Patent Document 1). In addition, there are three methods of contact between hot air and droplets: cocurrent, countercurrent, and mixed flow. In the cocurrent flow method, the droplet contacts the hot air at a stage where the water content is high, and as the drying proceeds, This is suitable for drying heat-sensitive materials.

特開平8−109124号公報JP-A-8-109124 「造粒ハンドブック」,社団法人日本粉体工業技術協会編,オーム社,1991年,p.249〜254“Granulation Handbook”, edited by Japan Powder Industrial Technology Association, Ohm, 1991, p. 249-254

特許文献1に記載された噴霧乾燥によってコーティング基剤としての高分子粉末を製造する方法は、噴霧乾燥のままでは得られる高分子粉末の平均粒子径が10μm程度であり、コーティング基剤を乾式法でコーティングする場合は、緻密なコーティングができない問題がある。また、コーティング基剤を湿式法でコーティングする場合は、コーティング基剤を液中で溶解または懸濁させて、この10μm程度の高分子粉末を平均粒子径が1μm以下の高分子微粉末として分散液中に分散させることができるが、分散が不十分であると平均粒子径が1μmを越えて、コーティングの緻密性が損なわれる恐れがある。   In the method for producing a polymer powder as a coating base by spray drying described in Patent Document 1, the average particle size of the polymer powder obtained by spray drying is about 10 μm. When coating with, there is a problem that a dense coating cannot be performed. When the coating base is coated by a wet method, the coating base is dissolved or suspended in the liquid, and the polymer powder of about 10 μm is dispersed as a polymer fine powder having an average particle diameter of 1 μm or less. However, if the dispersion is insufficient, the average particle diameter may exceed 1 μm and the denseness of the coating may be impaired.

前記噴霧乾燥で得られる10μm程度の高分子粉末を、乾式法でも緻密なコーティングができるようにするためには、高分子微粉末の結合粒体である高分子粉末を、乳鉢等で解砕することが考えられるが、噴霧乾燥で大量に得られる高分子粉末を処理しきれず、需要が多く工業的規模での大量生産が望まれるコーティング基剤の製造には十分に対応できない。   In order to be able to coat the polymer powder of about 10 μm obtained by spray drying with a dry method, the polymer powder, which is a bonded particle of polymer fine powder, is crushed with a mortar or the like. However, the polymer powder obtained in a large amount by spray drying cannot be fully processed, and cannot sufficiently cope with the production of a coating base that is in great demand and is desired to be mass-produced on an industrial scale.

そこで、本発明の課題は、乾式法でも緻密なコーティングができる固形製剤コーティング用微粉末を、工業的規模で大量生産可能とすることである。   Therefore, an object of the present invention is to enable mass production of fine powder for coating a solid preparation that can be densely coated by a dry method on an industrial scale.

上記の課題を解決するために、本発明の固形製剤コーティング用微粉末の製造方法は、平均粒子径が1μm以下の高分子微粉末の分散した分散液を噴霧乾燥させ、この噴霧乾燥で得られた高分子微粉末の結合粒体を気流式分級機を備えたジェットミルで解砕、分級して、固形製剤コーティング用微粉末を製造する方法を採用した。   In order to solve the above problems, the method for producing a fine powder for coating a solid preparation of the present invention is obtained by spray-drying a dispersion of polymer fine powder having an average particle size of 1 μm or less and performing this spray-drying. A method of producing a fine powder for solid formulation coating by pulverizing and classifying the bonded fine particles of the polymer fine powder with a jet mill equipped with an airflow classifier was adopted.

すなわち、噴霧乾燥で得られる平均粒子径が1μm以下の高分子微粉末の結合粒体を、気流式分級機を備えたジェットミルで解砕、分級することにより、噴霧乾燥で大量に得られる高分子微粉末の結合粒体を効率よく解砕して、乾式法でも緻密なコーティングができる平均粒子径が1μm以下の固形製剤コーティング用微粉末を、工業的規模で大量生産可能とした。   That is, a high molecular weight powder obtained by spray drying is obtained by pulverizing and classifying bonded fine particles of polymer fine powder having an average particle size of 1 μm or less obtained by spray drying in a jet mill equipped with an airflow classifier. The fine particles for coating a solid preparation having an average particle size of 1 μm or less that can be finely coated even by a dry method can be mass-produced on an industrial scale.

前記ジェットミルは、複数のジェットノズルを有し、粉砕室の中央部付近で前記高分子微粉末の結合粒体同士を衝突させる流動層式のものが好適である。   The jet mill is preferably a fluidized bed type having a plurality of jet nozzles and causing the bonded fine particles of the polymer fine powder to collide with each other near the center of the crushing chamber.

本発明の固形製剤コーティング用微粉末の製造方法は、噴霧乾燥で得られる平均粒子径が1μm以下の高分子微粉末の結合粒体を、気流式分級機を備えたジェットミルで解砕、分級するようにしたので、噴霧乾燥で大量に得られる高分子微粉末の結合粒体を効率よく解砕して、乾式法でも緻密なコーティングができる平均粒子径が1μm以下の固形製剤コーティング用微粉末を、工業的規模で製造可能とすることができる。   The method for producing a fine powder for coating a solid preparation according to the present invention comprises pulverizing and classifying bonded fine particles of a polymer fine powder having an average particle size of 1 μm or less obtained by spray drying in a jet mill equipped with an airflow classifier. As a result, fine particles for solid pharmaceutical coatings with an average particle size of 1 μm or less that can be efficiently pulverized from fine particles of polymer fine powder obtained in large quantities by spray-drying and can be densely coated by a dry method. Can be made on an industrial scale.

以下、図面に基づき、本発明の実施形態を説明する。図1は、本発明に係る固形製剤コーティング用微粉末の製造方法の製造工程を示す。まず、固形製剤コーティング用の高分子微粉末の分散した分散液を作製し、この分散液を噴霧乾燥する。こののち、噴霧乾燥で得られた高分子粉末を気流式分級機を備えたジェットミルで解砕、分級して、平均粒子径が1μm以下の固形製剤コーティング用微粉末を製造する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 shows a production process of a method for producing a fine powder for coating a solid preparation according to the present invention. First, a dispersion in which fine polymer powder for solid preparation coating is dispersed is prepared, and this dispersion is spray-dried. Thereafter, the polymer powder obtained by spray drying is pulverized and classified with a jet mill equipped with an airflow classifier to produce a fine powder for solid preparation coating having an average particle size of 1 μm or less.

前記高分子微粉末の分散した分散液は公知の方法で作製することができる。例えば、高分子素材を有機溶媒を含んだ溶媒に溶解して高分子溶液とし、この高分子溶液を水と混合した後に有機溶媒を除去して分散液を作製することができる。また、この方法以外にも、アクリル系高分子溶液の作製方法として知られている乳化重合法等で作製することができる。   The dispersion in which the polymer fine powder is dispersed can be prepared by a known method. For example, a polymer material can be dissolved in a solvent containing an organic solvent to form a polymer solution, and the polymer solution is mixed with water, and then the organic solvent is removed to prepare a dispersion. In addition to this method, it can be prepared by an emulsion polymerization method known as a method for preparing an acrylic polymer solution.

図2は、前記噴霧乾燥に用いた噴霧乾燥造粒装置を示す。この噴霧乾燥造粒装置は、高分子微粉末の分散した分散液Aと熱風Bを乾燥室1の頂部から同方向に噴出する並流式のものであり、分散液Aは微粒化器2で撹拌されて溶液中の高分子が微粒化されたのち、乾燥室1内に噴射されるようになっている。熱風Bとの接触で乾燥された高分子粉末Cは、捕集機3で熱風Bと分離されて回収される。   FIG. 2 shows the spray drying granulator used for the spray drying. This spray-drying granulator is a co-current type in which a dispersion A and hot air B in which polymer fine powder is dispersed are jetted from the top of the drying chamber 1 in the same direction. After being agitated and the polymer in the solution is atomized, it is sprayed into the drying chamber 1. The polymer powder C dried by contact with the hot air B is separated from the hot air B by the collector 3 and collected.

図3は、前記高分子粉末Cの解砕、分級に用いたジェットミルを示す。このジェットミルは、竪型筒状のケーシング11に複数のジェットノズル12を設け、供給管13から供給される高分子粉末Cを、ケーシング11の中央部付近で互いに衝突させる流動層式のものであり、この衝突で解砕された高分子微粉末Dは、ケーシング11の上部に設けられた気流式分級機14の高速回転する分級ロータ14aで分級され、その排出管14bから捕集機15に送られる。分級されて捕集機15で捕集された高分子微粉末Dは、回収容器16に固形製剤コーティング用微粉末Eの製品として回収される。   FIG. 3 shows a jet mill used for crushing and classifying the polymer powder C. This jet mill is a fluidized bed type in which a plurality of jet nozzles 12 are provided in a vertical cylindrical casing 11 and polymer powder C supplied from a supply pipe 13 collides with each other near the center of the casing 11. The polymer fine powder D crushed by this collision is classified by a classifying rotor 14a that rotates at high speed of an airflow classifier 14 provided on the upper portion of the casing 11, and is collected from the discharge pipe 14b to the collector 15. Sent. The polymer fine powder D that has been classified and collected by the collector 15 is collected in the collection container 16 as a product of the fine powder E for solid formulation coating.

図4(a)、(b)は、前記噴霧乾燥造粒装置での噴霧乾燥で得られた高分子粉末Cの電子顕微鏡写真を示す。図4(a)は倍率が800倍のものであり、高分子粉末Cの粒子径は10〜数10μmになっている。図4(b)は倍率を10000倍に拡大したものであり、高分子粉末Cは粒子径が1μm以下の多数の微粉末の結合粒体であることがわかる。   4A and 4B show electron micrographs of the polymer powder C obtained by spray drying using the spray drying granulator. In FIG. 4A, the magnification is 800 times, and the particle diameter of the polymer powder C is 10 to several tens of μm. FIG. 4 (b) shows an enlargement of the magnification to 10,000 times, and it can be seen that the polymer powder C is a large number of fine particles of bonded particles having a particle diameter of 1 μm or less.

図5は、前記高分子粉末Cをジェットミルで解砕、分級して得られた高分子微粉末Dの電子顕微鏡写真を示す。この写真の倍率は13000倍であり、高分子微粉末Dは粒子径が0.1〜0.2μm程度の球形の微粉末となっている。この高分子微粉末Dの平均粒子径は、図4(b)に示した解砕前の結合粒体の微粉末の平均粒子径よりも小さくなっている。この理由は明確ではないが、ジェットミルの流動層での高分子微粉末D同士や、高分子微粉末Dと高分子粉末Cとの衝突による研磨作用によることが考えられる。   FIG. 5 shows an electron micrograph of the polymer fine powder D obtained by crushing and classifying the polymer powder C with a jet mill. The magnification of this photograph is 13000 times, and the polymer fine powder D is a spherical fine powder having a particle diameter of about 0.1 to 0.2 μm. The average particle diameter of the polymer fine powder D is smaller than the average particle diameter of the fine powder of the bonded granule before pulverization shown in FIG. The reason for this is not clear, but may be due to the polishing action caused by the collision between the polymer fine powders D in the fluidized bed of the jet mill or between the polymer fine powder D and the polymer powder C.

本発明に係る固形製剤コーティング用微粉末の製造方法の製造工程を示す工程図Process drawing which shows the manufacturing process of the manufacturing method of the fine powder for solid formulation coating which concerns on this invention 図1の噴霧乾燥工程に用いた噴霧乾燥造粒装置を示す概略縦断面図1 is a schematic longitudinal sectional view showing a spray drying granulator used in the spray drying process of FIG. 図1の解砕、分級工程に用いたジェットミルを示す概略縦断面図1 is a schematic longitudinal sectional view showing a jet mill used in the crushing and classification process of FIG. a、bは、それぞれ図2の噴霧乾燥造粒装置で得られた高分子粉末Cの電子顕微鏡写真a and b are electron micrographs of polymer powder C obtained by the spray-drying granulator shown in FIG. 図3のジェットミルで解砕、分級して得られた高分子微粉末Dの電子顕微鏡写真Electron micrograph of fine polymer powder D obtained by crushing and classifying with the jet mill of FIG.

符号の説明Explanation of symbols

1 乾燥室
2 微粒化器
3 捕集機
11 ケーシング
12 ジェットノズル
13 供給管
14 気流式分級機
14a 分級ロータ
14b 排出管
15 捕集機
16 回収容器
DESCRIPTION OF SYMBOLS 1 Drying chamber 2 Atomizer 3 Collector 11 Casing 12 Jet nozzle 13 Supply pipe 14 Airflow classifier 14a Classification rotor 14b Drain pipe 15 Collector 16 Collection container

Claims (2)

平均粒子径が1μm以下の高分子微粉末の分散した分散液を噴霧乾燥させ、この噴霧乾燥で得られた高分子微粉末の結合粒体を気流式分級機を備えたジェットミルで解砕、分級して、固形製剤コーティング用微粉末を製造するようにした固形製剤コーティング用微粉末の製造方法。   The dispersion of polymer fine powder having an average particle size of 1 μm or less is spray-dried, and the polymer fine powder-bound particles obtained by spray drying are crushed with a jet mill equipped with an airflow classifier. A method for producing a fine powder for solid preparation coating, wherein the fine powder for solid preparation coating is produced by classification. 前記ジェットミルを、複数のジェットノズルを有し、粉砕室の中央部付近で前記高分子微粉末の結合粒体同士を衝突させる流動層式のものとした請求項1に記載の固形製剤コーティング用微粉末の製造方法。   2. The solid formulation coating according to claim 1, wherein the jet mill is a fluidized bed type having a plurality of jet nozzles and causing the bonded fine particles of the polymer fine powder to collide with each other in the vicinity of the center of the crushing chamber. Production method of fine powder.
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WO2016002621A1 (en) * 2014-06-30 2016-01-07 株式会社日清製粉グループ本社 Method for concentrating specific component of powder

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