JPH0256935B2 - - Google Patents
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- Publication number
- JPH0256935B2 JPH0256935B2 JP57085384A JP8538482A JPH0256935B2 JP H0256935 B2 JPH0256935 B2 JP H0256935B2 JP 57085384 A JP57085384 A JP 57085384A JP 8538482 A JP8538482 A JP 8538482A JP H0256935 B2 JPH0256935 B2 JP H0256935B2
- Authority
- JP
- Japan
- Prior art keywords
- container
- powder
- rotary plate
- plate
- granulation
- 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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- Formation And Processing Of Food Products (AREA)
- Medical Preparation Storing Or Oral Administration Devices (AREA)
- Glanulating (AREA)
- Confectionery (AREA)
Description
【発明の詳細な説明】
本発明は粉粒体の造粒ならびにコーチング装置
に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a granulation and coating device for powder and granules.
一般に、たとえば錠剤、細粒剤、顆粒剤、カプ
セル剤等の医薬、チヨコレート等の食品、粉末治
金、触媒、フエライト、セラミツクス、洗剤、化
粧品、染料、顔料等に用いられる粉粒体の造粒な
らびにコーチングには、幾つかの型式の機械装置
が使用されている。その中には、たとえばパンま
たはドラム型の転動造粒・コーチング機、撹拌翼
の付いた撹拌造粒機、さらには、粉粒体を空気で
流動分散させた上、結合液またはコーチング液を
スプレーして粉粒体を凝集させたり、コーチング
したりする。いわゆる流動造粒・コーチング機等
がある。 Generally, granulation of powders and granules used for medicines such as tablets, fine granules, granules, capsules, foods such as thiokolate, powder metallurgy, catalysts, ferrites, ceramics, detergents, cosmetics, dyes, pigments, etc. Several types of mechanical equipment are used for coating as well. Some of them include, for example, pan- or drum-type rolling granulation/coating machines, agitation granulation machines with stirring blades, and furthermore, systems that fluidize and disperse powder and granules with air, and then apply a binding liquid or coating liquid. Spray to agglomerate or coat powder. There are so-called fluid granulation/coating machines.
ところで、たとえば医薬、食品を中心とした分
野の造粒ならびにコーチングにおいては、粒度分
布の揃つた粒とか、球形度の良い粒とか、微粉、
団粒の少ない粒、あるいは重質性の粒等の製造を
要求されたり、またコーチングむらのない、粒破
壊の少ない、付着団粒の発生の少ないコーチング
操作が要求される。 By the way, for example, in granulation and coating in fields centered on pharmaceuticals and foods, it is necessary to produce particles with uniform particle size distribution, particles with good sphericity, fine powder,
It is required to produce grains with few aggregates or heavy grains, and there is also a requirement for a coating operation with no uneven coating, less destruction of grains, and less generation of adhering aggregates.
これらの要求に対し、従来の転動造粒・コーチ
ング機では、重力を利用したカスケード流を用い
るため局所的に強い力を粒に加えることはない
が、その混合性が悪いことにより、造粒において
は粒度分布の広い不均一な粒しか得られず、コー
チングにおいては団粒が発生し易いという欠点が
ある。 In response to these demands, conventional rolling granulation/coating machines use a cascade flow using gravity, so they do not apply strong local force to the grains, but due to poor mixing properties, granulation In this method, only non-uniform grains with a wide particle size distribution can be obtained, and in coating, agglomerates are likely to occur.
一方、撹拌造粒機では、局所的な力による撹拌
によつて粒の破壊と造粒とが併せて進行するの
で、造粒では粒度分布が広くなり、コーチングで
は被膜が不完全になり易いという欠点がある。 On the other hand, in a stirring granulator, particle destruction and granulation proceed at the same time due to stirring caused by local forces, so granulation tends to result in a broader particle size distribution, while coating tends to result in incomplete coatings. There are drawbacks.
また、流動造粒・コーチング機では、粉粒体の
混合分散作用があるが、転動作用がないため、重
質の粒が作りにくいという難点を有している。 In addition, although the fluidized granulation/coating machine has a mixing and dispersing action for powder and granules, it does not have a rolling action, so it has the disadvantage that it is difficult to produce heavy grains.
本発明の目的は、前記従来技術の欠点を解消
し、均一性の良い造粒ならびにコーチングを行な
うことのできる装置を提供することにある。 SUMMARY OF THE INVENTION An object of the present invention is to provide an apparatus capable of eliminating the drawbacks of the prior art and performing granulation and coating with good uniformity.
この目的を達成するため、本発明は、水平断面
が実質的に円形状をなす容器の中心に設けた回転
軸に、その1個所以上に、該回転軸から外周縁ま
で連続的に延びるほぼ半径方向の切欠きを有する
回転板を、前記容器の底部に沿うよう設け、前記
回転板の面積は容器底面のほぼ全面を蔽い、前記
回転板の切欠き部の回転板回転方向の前縁部を容
器底面に近づけるように形成し、さらに前記容器
の底部領域に、該容器内の粉粒体を流動させるた
めの気体を該容器内に導入する気体導入手段を設
けたものである。 To achieve this object, the present invention provides a container having a substantially circular horizontal cross section with a substantially circular radius extending continuously from the axis of rotation to the outer periphery at one or more points on the axis of rotation provided at the center of a container having a substantially circular horizontal cross section. A rotary plate having a notch in the direction is provided along the bottom of the container, the area of the rotary plate covers almost the entire bottom surface of the container, and the front edge of the notch of the rotary plate in the rotation direction of the rotary plate is provided. is formed so as to be close to the bottom surface of the container, and gas introducing means is provided in the bottom region of the container for introducing gas into the container to cause the powder and granular material in the container to flow.
すなわち、造粒およびコーチングには、本質的
に、できるだけ均一な剪断を粉粒体層に加えるこ
とによつて、滞溜域のない均一な混合作用と適度
の転動作用を粒子に与えることが必要である。こ
のような条件を満足させるために、撹拌造粒機の
撹拌翼に代えて、粉粒体層に適度の転動作用を与
えるための平面状または皿状の回転板を容器底部
に沿つて実質的に水平方向に設ける。この回転板
は、粉粒体層に十分な渦巻状の流動作用を発生さ
せるのに必要な遠心力を与えるためには、容器底
面の少なくとも1/2以上を蔽う大きさにするのが
よい。また、回転板と容器底面との間に入り込む
粉粒体の量をできるだけ少なくするため、回転板
は容器底面にできるだけ近づくよう該容器底面に
沿つて配設するのがよい。さらに、回転板の下方
に入り込んだ粉粒体を回転板上に持ち上げるた
め、回転板の1個所以上を半径方向に切り欠くの
がよく、その切欠部における回転板の回転方向前
縁部は容器底面により接近するようにするのが好
ましい。このような構造により、回転板の回転に
伴なつて回転板下の粉粒体を回転板上にすくい上
げることができる。また、回転板の下側に、該回
転板と容器底面との間に空気を供給する空気ノズ
ルを設けることにより、回転板下の粉粒体を吹き
上げ、切欠部における回転板の回転方向前縁部に
より回転板下の粉粒体をすくい上げ易くすること
ができる。その結果、容器底部の回転板下におけ
る粉粒体の滞溜域はなくなる。さらに、容器の底
壁および(または)側壁にも空気ノズルを設け、
回転板の回転による遠心力によつて容器側壁に達
した粉粒体を該容器側壁に沿つて空気で流動分散
させながら浮かし上げ、粉粒体の渦巻状の循環混
合作用を助長させることできる。 That is, granulation and coating essentially involve applying as uniform a shear to the powder bed as possible to give the particles a uniform mixing action without stagnation areas and a moderate rolling action. is necessary. In order to satisfy these conditions, instead of the stirring blades of the stirring granulator, a flat or dish-shaped rotary plate is installed along the bottom of the container to provide appropriate rolling motion to the powder layer. horizontally. In order to apply the centrifugal force necessary to generate a sufficient spiral flow effect on the powder layer, the rotating plate should have a size that covers at least 1/2 or more of the bottom surface of the container. Furthermore, in order to minimize the amount of powder that enters between the rotating plate and the bottom of the container, the rotating plate is preferably arranged along the bottom of the container so as to be as close as possible to the bottom of the container. Furthermore, in order to lift the powder particles that have entered the lower part of the rotary plate onto the rotary plate, it is preferable to cut out one or more parts of the rotary plate in the radial direction, and the front edge of the rotary plate in the rotational direction at the notch is Preferably it is closer to the bottom surface. With such a structure, as the rotary plate rotates, the powder and granular material under the rotary plate can be scooped up onto the rotary plate. In addition, by providing an air nozzle on the underside of the rotary plate to supply air between the rotary plate and the bottom of the container, the powder and granules under the rotary plate are blown up, and the front edge of the rotary plate in the rotation direction at the notch part is This makes it easier to scoop up the powder and granules under the rotary plate. As a result, there is no stagnation area for powder and granular material under the rotary plate at the bottom of the container. Furthermore, the bottom wall and/or side wall of the container is also provided with air nozzles,
Due to the centrifugal force generated by the rotation of the rotary plate, the powder particles that have reached the side wall of the container are floated along the container side wall while being flowed and dispersed by air, thereby promoting the swirling circulation mixing action of the powder particles.
このようにして、本発明者は、転動造粒コーチ
ングに付随した混合性の不良を改善し、撹拌造粒
機にみられる局所的な過大剪断力による粒破壊を
防止し、また流動造粒・コーチング機にない転動
作用を粒子に与えることに成功した。 In this way, the present inventors have improved the poor mixability associated with rolling granulation coating, prevented grain breakage due to localized excessive shearing forces seen in agitated granulators, and・Succeeded in giving particles a rolling action that is not available in coaching machines.
さらに、本発明の造粒ならびにコーチング装置
は、本来の造粒・コーチング作用上に長所に加え
て、近年、医薬・食品工業界で重要視されている
GMP(Good Manufacturing Practice)の見地
からも看過できない特徴を有している。 Furthermore, the granulation and coating device of the present invention has been gaining importance in the pharmaceutical and food industries in recent years, in addition to its inherent advantages in granulation and coating functions.
It has characteristics that cannot be overlooked from the standpoint of GMP (Good Manufacturing Practice).
すなわち、本発明に一見類似している装置とし
て、流動層造粒コーチング機に転動作用を付加す
るために流動層底部に回転円板を設けた装置、お
よび流動層空気分散板上に回転円板を設けた装置
があるが、前者は回転円板下に粉粒体が落下し、
その粉粒体がその後に連続して処理されるバツチ
に混入し、品質を低下させたり、一連の操作の後
の完全な洗浄を困難にしてしまう。一方、後者
は、それに加えて、回転円板と空気分散板との間
にも粉粒体が入り込んでしまうという問題があ
る。したがつて、前記両者従来装置のいずれも
GMPの点で問題を含むものである。 That is, as devices that are seemingly similar to the present invention, there is a device in which a rotating disk is provided at the bottom of the fluidized bed to add rolling action to a fluidized bed granulation coating machine, and a device in which a rotating disk is provided on the fluidized bed air distribution plate. There is a device equipped with a plate, but in the former, powder and granules fall under the rotating disk,
The powder or granules may contaminate batches that are subsequently processed, reducing quality or making it difficult to clean thoroughly after a series of operations. On the other hand, in the latter case, in addition to this, there is a problem in that powder particles also enter between the rotating disk and the air dispersion plate. Therefore, both of the above conventional devices
This is problematic in terms of GMP.
これに対して、本発明の装置は前記従来の流動
層式のものと違つて空気分散板や、粒体の落下し
易い間隙がないので、粉粒体が完全に容器内に保
持され、粉粒体を容器から排出した後、洗浄時に
回転板を少し持ち上げるだけで完全な洗浄が可能
である。したがつて、本発明の装置は造粒やコー
チングの機能が優れている他に、GMPの上から
も非常に良好なものである。 On the other hand, unlike the conventional fluidized bed type device, the device of the present invention does not have an air dispersion plate or a gap where the granules can easily fall, so the granules are completely retained in the container and the powder is After discharging the granules from the container, complete cleaning is possible by simply lifting the rotary plate slightly during cleaning. Therefore, the apparatus of the present invention not only has excellent granulation and coating functions, but also is very good in terms of GMP.
また、別の従来技術として、造粒槽の底壁に沿
う回転円板を設け、この回転円板上で粒子をころ
がり流動させて造粒するという方式も提案されて
いる。しかし、この従来方式では、造粒槽の底壁
面と回転円板との間に粉粒体が入り込んで滞溜ゾ
ーンが形成されてしまうという問題があり、
GMP的に全く問題がないわけではない。 In addition, as another conventional technique, a method has been proposed in which a rotating disk is provided along the bottom wall of the granulation tank, and particles are granulated by rolling and flowing on the rotating disk. However, with this conventional method, there is a problem in that powder and granules enter between the bottom wall surface of the granulation tank and the rotating disk, forming a stagnation zone.
This does not mean that there are no problems in terms of GMP.
これに対し、本発明の装置は、回転板に半径方
向の切欠き部を形成することにより、かつ容器底
面と回転板との間に空気を導入することにより、
容器底面と回転板との間に粉粒体が滞溜すること
を防止でき、造粒作用は勿論のこと、GMP的に
も非常に良好なものである。 In contrast, the device of the present invention has a radial notch formed in the rotary plate and introduces air between the bottom of the container and the rotary plate.
It is possible to prevent the powder from accumulating between the bottom of the container and the rotary plate, and it is very good not only in terms of granulation effect but also in terms of GMP.
以下、本発明を図面に示す実施例にしたがつて
詳細に説明する。 Hereinafter, the present invention will be explained in detail according to embodiments shown in the drawings.
第1図は本発明による造粒ならびにコーチング
装置の一実施例を示す略断面図である。 FIG. 1 is a schematic cross-sectional view showing one embodiment of the granulation and coating apparatus according to the present invention.
本実施例において、造粒ならびにコーチングを
行なうための容器1は水平断面が円形の形状を有
し、上部にはカバー2が設けられ、該カバー2に
は、原料粉末を定量供給する粉末供給管3、容器
1内を排気する排気管4、容器1内を所望の真空
状態にする真空吸引管5、および造粒ならびにコ
ーチング用の液を供給するスプレーノズル6が設
けられている。 In this example, a container 1 for performing granulation and coating has a circular horizontal cross section, and a cover 2 is provided on the top, and the cover 2 has a powder supply pipe for supplying a fixed amount of raw material powder. 3. An exhaust pipe 4 for evacuating the inside of the container 1, a vacuum suction pipe 5 for bringing the inside of the container 1 into a desired vacuum state, and a spray nozzle 6 for supplying liquid for granulation and coating are provided.
一方、前記容器1の底部中央には、図示しない
駆動源から回転駆動される回転軸7が垂直方向に
突設されている。この回転軸7の上端には、容器
1の底壁面に沿うよう水平方向に配置された円板
状の回転板8がボルト9で固定され、該回転板8
の中心部の円錐台形部8aは容器1内に突出し、
その外周側は容器底面に沿う平板部8bとなつて
いる。 On the other hand, at the center of the bottom of the container 1, a rotating shaft 7 that is rotatably driven by a drive source (not shown) is vertically protruded. A disc-shaped rotating plate 8 horizontally arranged along the bottom wall surface of the container 1 is fixed to the upper end of the rotating shaft 7 with bolts 9.
A truncated conical portion 8a at the center of the container 1 protrudes into the container 1,
Its outer peripheral side forms a flat plate portion 8b along the bottom surface of the container.
前記回転板8は容器1内に投入された粉粒体1
0を該回転板8の平板部8b上に載せて回転する
ことにより粉粒体10に対して適度の転動作用を
与えるものである。この回転板8は粉粒体10に
対して十分な渦巻状の流動作用を生起させるのに
必要な遠心力を与えるためには、容器1の底面の
1/2以上、好ましくはほぼ全面を蔽う面積を持つ
のが好ましい。 The rotary plate 8 rotates the powder 1 charged into the container 1.
0 is placed on the flat plate portion 8b of the rotary plate 8 and rotated, thereby imparting an appropriate rolling action to the granular material 10. In order to apply the centrifugal force necessary to generate a sufficient spiral flow action on the powder and granular material 10, this rotary plate 8 should cover more than 1/2 of the bottom surface of the container 1, preferably almost the entire surface. It is preferable to have an area.
前記回転板8の下面は容器1の底面に対してで
きるだけ接近し、両面間に粉粒体10が入り込ん
で滞溜するのを極力抑制するのが望ましいが、本
実施例においては回転板8の下面と容器1の底面
との間に入り込む粉粒体を該回転板8の平板部8
b上にすくい上げて回転板8の下方に粉粒体の滞
溜域が形成されないようにするため、回転板8の
平板部8bの1個所に半径方向への切欠部11が
形成されている。この切欠部11は平面で見て半
径方向内側から外側に行くにつれてやや末広がり
状に形成され、またその断面形状は第3図に示す
ように回転板8の回転方向前縁部11aが上方か
ら下方前縁に向けて斜めに切り取られ、回転板8
の下方の粉粒体を該回転板8の上にすくい上げ易
いよう構成されている。 It is desirable that the lower surface of the rotary plate 8 be as close to the bottom surface of the container 1 as possible to prevent the powder and granular material 10 from entering and accumulating between both surfaces as much as possible. The powder and granules that enter between the lower surface and the bottom surface of the container 1 are removed from the flat plate portion 8 of the rotary plate 8.
A notch 11 in the radial direction is formed at one location in the flat plate portion 8b of the rotary plate 8 in order to prevent the formation of a stagnation area of powder and granules below the rotary plate 8 by scooping the powder onto the rotary plate 8. This notch 11 is formed in a shape that becomes slightly wider as it goes from the inner side to the outer side in the radial direction when viewed in plan, and its cross-sectional shape is such that the front edge 11a in the rotational direction of the rotary plate 8 extends from the upper side to the lower side. The rotating plate 8 is cut diagonally toward the leading edge.
It is constructed so that the powder and granular material below can be easily scooped up onto the rotary plate 8.
また、本実施例においては、回転板8の下面と
容器1の底面との間に入り込んだ粉粒体を容器1
の周囲方向に吹き上げて切欠部11で回転板8上
にすくい上げ易くするため、回転軸7の中を通つ
て回転板8の下面と容器1の底面との間に外側方
向に空気を噴出する空気供給路12が設けられて
いる。この空気供給路12の空気噴出ノズル開口
は回転軸7の半径方向でもよいが、該回転軸7の
接線方向に形成すればより良好な粉粒体吹上げ除
去効果が得られ、また該ノズル開口の個数は1個
に限定されるものではない。また、前記回転軸7
の上部周囲にはベアリング13が容器底壁の下側
位置において設けられている。 In addition, in this embodiment, the powder and granules that have entered between the lower surface of the rotary plate 8 and the bottom surface of the container 1 are removed from the container 1.
Air is blown outwardly between the lower surface of the rotary plate 8 and the bottom surface of the container 1 through the rotary shaft 7 in order to blow it up in the circumferential direction and easily scoop it up onto the rotary plate 8 at the notch 11. A supply path 12 is provided. The air jet nozzle opening of this air supply path 12 may be formed in the radial direction of the rotating shaft 7, but if it is formed in the tangential direction of the rotating shaft 7, a better effect of blowing up and removing powder particles can be obtained, and the nozzle opening The number of objects is not limited to one. Further, the rotating shaft 7
A bearing 13 is provided around the top of the container at a position below the bottom wall of the container.
さらに、本実施例の容器1の側壁下部、すなわ
ち、回転板8の平板部8bのやや上方の位置と対
応する位置には、回転板8の回転による遠心力で
容器1の側壁に達した粉粒体10を該側壁に沿つ
て空気の力で流動分散させながら浮かし上げ、粉
粒体10の渦巻状の循環混合作用を助長するため
の空気ノズル14が配設されている。この空気ノ
ズル14は容器1の半径方向に空気を導入するよ
う開口させてもよいが、粉粒体10の循環混合作
用をより良好に行なうためには空気ノズル14を
容器1に対して接線方向に開口させるのが好まし
い。空気ノズル14の個数も何ら1個に限定され
ず、複数個設けてもよく、また容器1の底壁に設
けてもよい。 Furthermore, powder that has reached the side wall of the container 1 due to the centrifugal force caused by the rotation of the rotary plate 8 is located at the lower part of the side wall of the container 1 of this embodiment, that is, at a position corresponding to a position slightly above the flat plate portion 8b of the rotary plate 8. An air nozzle 14 is provided to float the granules 10 along the side wall while being fluidized and dispersed by the force of the air, and to promote the swirling circulation mixing action of the granules 10. The air nozzle 14 may be opened to introduce air in the radial direction of the container 1, but in order to better circulate and mix the powder and granular material 10, the air nozzle 14 may be opened in a tangential direction to the container 1. It is preferable to open the opening. The number of air nozzles 14 is not limited to one at all, and a plurality of air nozzles 14 may be provided, or may be provided on the bottom wall of the container 1.
本実施例の容器1の側壁の内側には、粉粒体1
0の混合作用を補助するバツフル板75が設けら
れている。もつとも、このバツフル板15は省略
してもよい。また、容器1の側壁下部には、造粒
あるいはコーチングされた製品を容器1の外部に
取り出すための製品排出部16が形成され、バル
ブ17で開閉される。さらに、本実施例では、造
粒あるいはコーチングされる粉粒体10の中の湿
度、温度等を感知し、スプレーノズル6からの液
体供給量や、図示しない熱風供給源からの熱風供
給量等を制御するのに役立つセンサ18が容器1
内に設置されている。 Inside the side wall of the container 1 of this embodiment, a powder 1
A baffle plate 75 is provided to assist the mixing action of 0. However, this baffle plate 15 may be omitted. Further, a product discharge section 16 for taking out the granulated or coated product to the outside of the container 1 is formed at the lower side wall of the container 1, and is opened and closed by a valve 17. Furthermore, in this embodiment, the humidity, temperature, etc. in the powder 10 to be granulated or coated are sensed, and the amount of liquid supplied from the spray nozzle 6, the amount of hot air supplied from a hot air supply source (not shown), etc. A sensor 18 serves to control the container 1.
is installed inside.
次に、本実施例の作用について説明する。 Next, the operation of this embodiment will be explained.
まず、容器1内に造粒、コーチング用の粉末原
料を図示しないホツパから粉末供給管3を経て所
要量投入する。一方、図示しない駆動源により回
転軸7および回転板8を回転させると、容器1内
の粉末原料は第1図に粉粒体10として示す如く
回転板8の平板部8b上で遠心力を受けて渦巻状
の流動運動を発生すると共に、その粉粒体10は
回転板8の回転に伴なつて均一な混合作用および
転動作用を受ける。 First, a required amount of powder raw material for granulation and coating is introduced into the container 1 through the powder supply pipe 3 from a hopper (not shown). On the other hand, when the rotary shaft 7 and the rotary plate 8 are rotated by a drive source (not shown), the powder raw material in the container 1 is subjected to centrifugal force on the flat plate portion 8b of the rotary plate 8, as shown as powder 10 in FIG. As the rotating plate 8 rotates, the granular material 10 receives a uniform mixing action and a rolling action as the rotating plate 8 rotates.
一方、回転板8の下面と容器1の底面とは接近
しかつ回転板8の平板部8bには半径方向の切欠
部11が形成されているので、回転板8の下側に
入り込んだ粉粒体は切欠部11から回転板8上に
すくい上げられ、回転板8の下方に粉粒体が滞溜
することが防止される。 On the other hand, since the lower surface of the rotary plate 8 and the bottom surface of the container 1 are close to each other and the flat plate part 8b of the rotary plate 8 is formed with a radial notch 11, powder particles that have entered the lower side of the rotary plate 8 The particles are scooped up onto the rotary plate 8 from the notch 11, and the accumulation of powder and granular materials below the rotary plate 8 is prevented.
また、回転軸7に設けた空気供給路12を通つ
て回転板8の下面と容器1の底面との間に空気を
噴出するようにしたので、容器底面上の粉粒体は
この空気により吹き上げられ、切欠部11を通し
て回転板8上にすくい上げ易くなり、回転板8の
下方への粉粒体の滞溜はより確実に防止される。 In addition, since air is ejected between the lower surface of the rotating plate 8 and the bottom surface of the container 1 through the air supply path 12 provided on the rotating shaft 7, the powder and granules on the bottom surface of the container are blown up by this air. This makes it easier to scoop up the powder onto the rotary plate 8 through the notch 11, and the accumulation of powder and granules below the rotary plate 8 is more reliably prevented.
さらに、本実施例においては、容器1の側壁下
部に空気ノズル14が設けられているので、回転
板8の回転による遠心力で容器側壁に達した粉粒
体10は空気ノズル14からの空気により容器側
壁に沿つて流動分散しながら浮かし上げられ、粉
粒体10の渦巻状の循環混合作用が助長される。 Furthermore, in this embodiment, since the air nozzle 14 is provided at the lower part of the side wall of the container 1, the powder 10 that has reached the container side wall due to the centrifugal force caused by the rotation of the rotary plate 8 is blown by air from the air nozzle 14. The particles are floated up while being fluidized and dispersed along the side wall of the container, and the swirling circulation mixing action of the powder and granules 10 is promoted.
したがつて、本実施例によれば、造粒、コーチ
ングされる粉粒体は均一な流動混合作用に加え
て、適度の転動作用、さらには渦巻状の循環混合
作用を受けながら造粒、コーチングされるので、
均一な粒度を持つ粉粒体を得ることができ、また
団粒のない、重質の粒子を作ることができ、従来
の撹拌造粒機における局所的な過大剪断力による
粉破壊を防止し、また粉粒体の滞溜も防止でき
る。 Therefore, according to this example, the powder to be granulated and coated is subjected to not only a uniform fluid mixing action but also a moderate rolling action and further a spiral circulation mixing action. Because you will be coached,
It is possible to obtain powder with uniform particle size, and it is possible to make heavy particles without agglomerates, and it prevents powder destruction due to local excessive shearing force in conventional stirring granulators. It is also possible to prevent particles from accumulating.
さらに、本実施例の造粒ならびにコーチング装
置は空気分散板がないので、粉粒体10は完全に
容器1内に保持され、粉粒体10を容器1から排
出した後に容器の洗浄を行なう場合、回転板8を
回転軸7から少し持ち上げるだけで完全な洗浄を
行なうことができ、GMP上の見地からも非常に
優れたものである。 Furthermore, since the granulation and coating apparatus of this embodiment does not have an air dispersion plate, the powder 10 is completely retained in the container 1, and when the container is cleaned after the powder 10 is discharged from the container 1. , complete cleaning can be carried out by simply lifting the rotary plate 8 slightly from the rotary shaft 7, which is extremely excellent from a GMP standpoint.
第4図は本発明における回転板の切欠部の他の
実施例を示す部分断面図である。この実施例で
は、回転板8の平板部8bの切欠部11は回転板
8の回転方向前縁部11bが容器1の底壁方向す
なわち下方向に曲げられ、その先端部は容器底面
と極めて接近している。したがつて、この場合に
は、容器底面上の粉粒体は回転板8の回転につれ
てこの彎曲した回転方向前縁部11bでより容易
かつ確実にすくい上げられ、回転板8の平板部8
bの上に戻される。 FIG. 4 is a partial sectional view showing another embodiment of the cutout portion of the rotating plate according to the present invention. In this embodiment, the notch 11 of the flat plate part 8b of the rotary plate 8 is such that the front edge 11b in the rotation direction of the rotary plate 8 is bent toward the bottom wall of the container 1, that is, downward, and its tip is very close to the bottom of the container. are doing. Therefore, in this case, as the rotating plate 8 rotates, the powder and granules on the bottom of the container are more easily and reliably scooped up by the curved front edge 11b in the rotational direction, and the powder and granules on the bottom surface of the container are scooped up more easily and reliably by the curved front edge 11b in the rotational direction,
It is returned to the top of b.
第5図および第6図は本発明における回転板の
他の実施例を示す平面図である。すなわち、第5
図の実施例では、回転板8の平板部8bの切欠部
11が直径方向の2個所に180度離れて形成され
ている。また、第6図の実施例では、切欠部11
は互いに120度の位置に合計3個形成されている。
なお、切欠部11はこれに限定されることなく、
たとえば4個以上形成することもでき、複数個の
切欠部11を形成した場合には、1個だけのもの
より粉粒体のすくい上げ効果は大きくなる。 FIGS. 5 and 6 are plan views showing other embodiments of the rotating plate according to the present invention. That is, the fifth
In the illustrated embodiment, the notches 11 of the flat plate portion 8b of the rotating plate 8 are formed at two locations 180 degrees apart in the diametrical direction. In addition, in the embodiment shown in FIG.
A total of three are formed at 120 degrees from each other.
Note that the notch 11 is not limited to this,
For example, four or more cutouts 11 can be formed, and when a plurality of cutouts 11 are formed, the effect of scooping up the powder or granular material becomes greater than when only one cutout section 11 is formed.
第7図は本発明による造粒ならびにコーチング
装置の他の実施例を示す断面図である。この実施
例では、容器1aの側壁部が彎曲形状に形成さ
れ、上端に行くにつれて直径が小さくなつてい
る。このような容器1aの場合、容器内の粉粒体
の循環混合作用がより良好になるという利点があ
る。また、本実施例では、容器側壁の内側に設け
ることのできるバツフル板は省略されているが、
バツフル板を設けてもよい。 FIG. 7 is a sectional view showing another embodiment of the granulation and coating apparatus according to the present invention. In this embodiment, the side wall portion of the container 1a is formed into a curved shape, and the diameter becomes smaller toward the upper end. In the case of such a container 1a, there is an advantage that the circulation mixing effect of the powder and granular material in the container becomes better. Furthermore, in this embodiment, the buttful plate that can be provided inside the side wall of the container is omitted;
A full board may also be provided.
第8図は本発明のさらに他の実施例を示す断面
図である。この実施例では、容器1aの側壁部の
他に底壁部も彎曲形状とされ、回転板8の平板部
もこの彎曲した底壁部に沿つて彎曲する皿状の彎
曲板部8cとして形成されている。この実施例で
も、良好な転動作用および循環混合作用を得るこ
とができる。 FIG. 8 is a sectional view showing still another embodiment of the present invention. In this embodiment, in addition to the side wall portion of the container 1a, the bottom wall portion is also curved, and the flat plate portion of the rotary plate 8 is also formed as a dish-shaped curved plate portion 8c that curves along the curved bottom wall portion. ing. In this embodiment as well, good rolling action and circulation mixing action can be obtained.
なお、本発明は前記実施例に限定されるもので
はなく、他の様々な変形が可能である。 Note that the present invention is not limited to the above embodiments, and various other modifications are possible.
以上説明したように、本発明によれば、局所的
に過大な剪断力で粒破壊を起こすことがなく、均
一な粒度を持つ粉粒体を造粒ならびにコーチング
でき、団粒を発生することなく、重質の粒を作る
ことができ、かつ容器底面と回転板との間への粉
粒体の滞溜を防止し、GMP的にも優れた効果を
得ることができる。特に、本発明においては、回
転板の切欠きが回転軸から外周縁まで連続的に延
び、しかもこの切欠き部の回転板の回転方向の前
縁部を容器底面に近づけるよう形成してあるの
で、回転板の下方に落下した粉粒体は、回転板と
容器底面との間に導入される空気の働きとも相ま
つて、容器底面上から回転板上に確実にすくい上
げられる。 As explained above, according to the present invention, granules with uniform particle size can be granulated and coated without causing grain breakage due to locally excessive shearing force, and without generating aggregates. It is possible to produce heavy grains, prevent granules from accumulating between the bottom of the container and the rotary plate, and achieve excellent effects in terms of GMP. In particular, in the present invention, the notch in the rotary plate extends continuously from the rotating shaft to the outer peripheral edge, and the front edge of the notch in the rotational direction of the rotary plate is formed close to the bottom surface of the container. Together with the action of air introduced between the rotary plate and the bottom of the container, the powder and granules that have fallen below the rotary plate are reliably scooped up from above the bottom of the container onto the rotary plate.
また、本発明では、回転板の面積が容器底面の
ほぼ全面を蔽うので、粉粒体は回転板上での遠心
転動流動作用により、均一で良質の造粒コーチン
グ製品を得ることができる。 Further, in the present invention, since the area of the rotating plate covers almost the entire bottom surface of the container, a uniform and high-quality granulated coating product can be obtained by the centrifugal rolling flow action of the powder particles on the rotating plate.
第1図は本発明による造粒ならびにコーチング
装置の一実施例を示す断面図、第2図は回転板の
半平面図、第3図は第2図の―線断面図、第
4図は回転板の切欠部の他の実施例を示す部分断
面図、第5図および第6図はそれぞれ回転板の他
の実施例を示す平面図、第7図は本発明の造粒な
らびにコーチング装置の他の実施例を示す断面
図、第8図は本発明の装置のさらに他の実施例を
示す断面図である。
1,1a……容器、2……カバー、3……粉末
供給管、6……スプレーノズル、7……回転軸、
8……回転板、8a……円錐台形部、8b……平
板部、8c……彎曲板部、10……粉粒体、11
……切欠部、11a,11b……回転方向前縁
部、12……空気供給路、14……空気ノズル、
16……シユート、17……バルブ。
Fig. 1 is a sectional view showing an embodiment of the granulation and coating apparatus according to the present invention, Fig. 2 is a half plan view of a rotating plate, Fig. 3 is a sectional view taken along the line - - of Fig. 2, and Fig. 4 is a rotating plate. FIGS. 5 and 6 are plan views showing other embodiments of the rotary plate, and FIG. 7 is a partial sectional view showing other embodiments of the cutout portion of the plate, and FIG. FIG. 8 is a sectional view showing still another embodiment of the apparatus of the present invention. 1, 1a... Container, 2... Cover, 3... Powder supply pipe, 6... Spray nozzle, 7... Rotating shaft,
8... Rotating plate, 8a... truncated conical part, 8b... flat plate part, 8c... curved plate part, 10... granular material, 11
...Notch portion, 11a, 11b...Rotational direction front edge portion, 12...Air supply path, 14...Air nozzle,
16...shoot, 17...valve.
Claims (1)
に設けた回転軸に、その1個所以上に、該回転軸
から外周縁まで連続的に延びるほぼ半径方向の切
欠きを有する回転板を、前記容器の底面に沿うよ
う設け、前記回転板の面積は容器底面のほぼ全面
を蔽い、前記回転板の切欠き部の回転板回転方向
の前縁部を容器底面に近づけるように形成し、さ
らに前記容器の底部領域に、該容器内の粉粒体を
流動させるための気体を該容器内に導入する気体
導入手段を設けたことを特徴とする造粒ならびに
コーチング装置。1. A rotating plate having a substantially radial notch extending continuously from the rotating shaft to the outer peripheral edge at one or more locations on the rotating shaft provided at the center of a container having a substantially circular horizontal cross section, The rotary plate is provided along the bottom surface of the container, the area of the rotary plate covers almost the entire bottom surface of the container, and the front edge of the notch of the rotary plate in the rotating direction of the rotary plate is formed close to the bottom surface of the container, The granulation and coating apparatus further comprises a gas introduction means provided in the bottom region of the container for introducing gas into the container for causing the powder and granules in the container to flow.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57085384A JPS58202029A (en) | 1982-05-20 | 1982-05-20 | Granulation and coaching equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57085384A JPS58202029A (en) | 1982-05-20 | 1982-05-20 | Granulation and coaching equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58202029A JPS58202029A (en) | 1983-11-25 |
| JPH0256935B2 true JPH0256935B2 (en) | 1990-12-03 |
Family
ID=13857238
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57085384A Granted JPS58202029A (en) | 1982-05-20 | 1982-05-20 | Granulation and coaching equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58202029A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2793652B2 (en) * | 1989-09-09 | 1998-09-03 | 鐘紡株式会社 | Powder seasoning coated food |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2551578A1 (en) * | 1975-11-17 | 1977-05-26 | Werner Glatt | Granulator with rotary stirrer and upright cylindrical vessel - through which drying air flows vertically upwards |
-
1982
- 1982-05-20 JP JP57085384A patent/JPS58202029A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58202029A (en) | 1983-11-25 |
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