JPS61230730A - Apparatus for treating particulate material - Google Patents

Apparatus for treating particulate material

Info

Publication number
JPS61230730A
JPS61230730A JP7232485A JP7232485A JPS61230730A JP S61230730 A JPS61230730 A JP S61230730A JP 7232485 A JP7232485 A JP 7232485A JP 7232485 A JP7232485 A JP 7232485A JP S61230730 A JPS61230730 A JP S61230730A
Authority
JP
Japan
Prior art keywords
rotary plate
powder
granular material
rotary
processing apparatus
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.)
Pending
Application number
JP7232485A
Other languages
Japanese (ja)
Inventor
Yoshiro Funakoshi
舩越 嘉郎
Shimesu Motoyama
本山 示
Taketsune Momiyama
籾山 武經
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.)
FUROINTO SANGYO KK
Freund Corp
Original Assignee
FUROINTO SANGYO KK
Freund 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 FUROINTO SANGYO KK, Freund Corp filed Critical FUROINTO SANGYO KK
Priority to JP7232485A priority Critical patent/JPS61230730A/en
Publication of JPS61230730A publication Critical patent/JPS61230730A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To enable the accurate mass treatment of a particulate material, by providing a first rotary plate while providing a second rotary plate having a particulate rising opening formed thereto at a position above said first rotary plate and spaced apart therefrom by a predetermined interval in a rotatable manner within a container so as to arrange both rotary plates in a plurality of stages. CONSTITUTION:The particulate material on two stages of rotary plates 2, 10 is treated in the order of centrifugal tumbling fluidization, rising, centrifugal tumbling fluidization and falling between both rotary plates 2, 10 while centrifugally tumbled and fluidized on rotary surfaces having an area about two times the rotary surface of a single rotary plate structure. During this time period, desired treatments such as granulation, coating, mixing, drying, etc., can be sequentially applied with good efficiency. For example, when a liquid is supplied to the particulate material of the upper stage particulate bed 14 from a nozzle 17, fine particles are selectively coated with said liquid and the particle size of the upper stage particulate bed 14 and that of the lower stage particulate bed 13 are uniformized to enable granulation and coating showing sharp particle size distribution.

Description

【発明の詳細な説明】 〔技術分野〕 本発明は粉粒体の混合、造粒、コーチング、乾燥等に用
いて効果のある粉粒体処理装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a powder processing apparatus which is effective for mixing, granulating, coating, drying, etc. of powder and granules.

〔背景技術〕[Background technology]

一般に、たとえば医薬、食品、化成品等の各種分野にお
ける粉粒体の処理において、良質の製品を得るためには
、個々の粉粒体粒子について如何に均質な処理が万遍な
(、しかも確実に行われることが重要である。そのため
には、処理される粒子に働く力がどの部分に対してもで
きるだけ均一で、しかも粒子の働きが循環流をなすこと
が望ましい。
In general, in the processing of powder and granular materials in various fields such as pharmaceuticals, foods, and chemical products, in order to obtain high-quality products, it is important to thoroughly (and reliably) process each powder or granule. To this end, it is desirable that the force acting on the particles being treated be as uniform as possible over all parts, and that the particles work in a circular flow.

そこで、本発明者らが鋭意研究したところ、回転板によ
り粉粒体粒子に遠心流動作用を与える遠心流動型粉粒体
処理装置が粉粒体の精密な加工処理に適していることが
判明したものであり、この粉粒体処理装置は球形顆粒の
造粒、コーチング等に有効で、優れた作用効果を奏する
ものである(特開昭58−202029号公報参照)。
Therefore, the inventors of the present invention conducted extensive research and found that a centrifugal flow type powder processing device that uses a rotating plate to apply a centrifugal flow effect to powder particles is suitable for precise processing of powder particles. This powder processing device is effective for granulation, coating, etc. of spherical granules, and has excellent effects (see Japanese Patent Laid-Open No. 58-202029).

ところで、回転板を用いて遠心流動作用を与える場合、
粉粒体に加わる力は回転面による作用で伝達される関係
上、処理される粉粒体の量は回転面の面積にほぼ比例す
る。
By the way, when applying a centrifugal flow effect using a rotating plate,
Since the force applied to the powder is transmitted by the action of the rotating surface, the amount of powder to be processed is approximately proportional to the area of the rotating surface.

しかしながら、通常の粉粒体処理装置は回転面が一つし
かないので、この構造で大きな回転面面積を得るために
は装置の径を大きくする必要がある。その結果、設置ス
ペースが大となり、加工のコストや手間も多くなる等の
問題があり、大量処理には不向きである。
However, since a typical powder processing device has only one rotating surface, it is necessary to increase the diameter of the device in order to obtain a large rotating surface area with this structure. As a result, there are problems such as an increase in installation space, increased processing costs and labor, and the method is unsuitable for mass processing.

また、精密な粉粒体処理を行うためには、造粒、コーチ
ング、混合、乾燥等の必要な詩作用を単一の処理装置で
シーケンシャルに行うことが望ましい。
In addition, in order to perform precise powder and granule processing, it is desirable to sequentially perform necessary functions such as granulation, coating, mixing, and drying using a single processing device.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、小さい設置スペースのコンパクトな構
造で大きな回転面面積を得ることができ、粉粒体の大量
処理を精密に行うことのできる粉粒体処理技術を提供す
ることにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a powder processing technology that can obtain a large rotating surface area with a compact structure requiring a small installation space, and that can accurately process a large amount of powder or granular material.

本発明の他の目的は、全体的にシーケンシャルな粉粒体
の処理を行うことのでき、る技術を提供することにある
Another object of the present invention is to provide a technique that enables sequential processing of powder and granular materials as a whole.

C発明の概要〕 本発明は、水平断面が実質的に円形状をなす容器内で回
転する第1の回転板と、この回転板から上方に所定間隔
だけ離隔した位置において前記容器内で回転可能に設け
られかつ少なくとも1個所に粉粒体上昇用開口を形成し
た第2の回転板とを多段に配設することにより、回転面
の面積を増大させ、かつ各回転面において順次所望の処
理を行わしめ、大きな回転面面積で大量の粉粒体を精密
に処理することができる。さらに、最下段の回転面から
順次処理されながら最上段の回転面に移動し、最上段の
回転面からオーバーフローさせて最下段の回転面に落下
させ、さらに最下段から最上段へと循環流を形成しなが
ら循環処理し、必要に応じてその循環流の所望の部位で
湿潤、粉末散布、転勤、あるいは混合、乾燥等の諸処理
を行い、全体としてシーケンシャルな粉粒体処理を行う
ことができるものである。
C. Summary of the Invention The present invention includes a first rotary plate that rotates within a container having a substantially circular horizontal cross section, and a first rotary plate that is rotatable within the container at a position spaced upwardly from the rotary plate by a predetermined distance. By arranging the second rotating plate in multiple stages, which is provided in The large rotating surface area allows for precise processing of large quantities of powder and granular materials. Furthermore, the flow is sequentially processed from the bottom rotating surface and moves to the top rotating surface, overflows from the top rotating surface and falls onto the bottom rotating surface, and then circulates from the bottom to the top. Circulating treatment is performed while forming, and various treatments such as wetting, powder dispersion, transfer, mixing, drying, etc. are performed at desired parts of the circulating flow as necessary, making it possible to perform sequential powder and granule treatment as a whole. It is something.

〔実施例1〕 第1図は本発明による一実施例である粉粒体処理装置の
断面図、第2図(a)と山)はそれぞれ回転板の平面図
と同図(a)のJIB−IIB線断面図、第3図は回転
板の他の実施例の平面図である。
[Example 1] Fig. 1 is a cross-sectional view of a powder/granular material processing apparatus that is an embodiment of the present invention, and Fig. 2 (a) and ridges) are a plan view of a rotary plate and a JIB in Fig. 2 (a), respectively. -IIB line sectional view, and FIG. 3 is a plan view of another embodiment of the rotating plate.

第1図において、水平断面が略円筒形の処理容器1の底
部には、略皿状の下部回転板2(第1の回転板)が該処
理容器1の軸心に位置した回転軸3の上部に円錐台形部
材4および取付ボルト5で取り付けられ、該回転板2は
処理容器1の底面を形成している。下部回転板2の皿状
弯曲面は処理容器1の底部周囲の弯曲面と円滑に適合し
、環状のスリット6を介して滑らかな弯曲連続面を形成
している0回転軸3の回転はモータ7により行われ、該
回転軸3の回転と共に下部回転板2も一緒に回転される
In FIG. 1, at the bottom of a processing container 1 having a substantially cylindrical horizontal cross section, a substantially dish-shaped lower rotating plate 2 (first rotating plate) is attached to a rotating shaft 3 located at the axis of the processing container 1. It is attached to the upper part with a frustoconical member 4 and mounting bolts 5, and the rotating plate 2 forms the bottom surface of the processing container 1. The dish-shaped curved surface of the lower rotary plate 2 fits smoothly with the curved surface around the bottom of the processing container 1, and the rotation of the zero-rotation shaft 3, which forms a smooth continuous curved surface through the annular slit 6, is controlled by the motor. 7, and as the rotating shaft 3 rotates, the lower rotating plate 2 is also rotated together.

前記処理容器lの下方には給気部8が取り付けられ、給
気源(図示せず)から供給される加熱空気等が該給気部
8を経て前記スリントロから処理容器l内に送り込まれ
るよう構成されている。
An air supply part 8 is attached below the processing container l, so that heated air etc. supplied from an air supply source (not shown) is sent into the processing container l from the slintro through the air supply part 8. It is configured.

また、処理容器l内の略中間部には、第2図ta+に示
すように、前記回転板2上に設けた支柱9で支持された
ドーナツ状の上部回転板10(第2の回転板)が設けら
れている。この上部回転板10は前記下部回転板2と多
段回転面を形成するもので、両回転板2と10は一緒に
回転する。
In addition, approximately in the middle of the processing container l, as shown in FIG. is provided. The upper rotating plate 10 forms a multi-stage rotating surface with the lower rotating plate 2, and both rotating plates 2 and 10 rotate together.

本実施例の上部回転板10は下部回転板2とほぼ同じ弯
曲面形状を有している。上部回転板10の中心部には粉
粒体落下用開口11が形成され、またその1個所には粉
粒体上昇用開口12(切欠き)が半径方向に切欠き形成
されている。粉粒体上昇用開口12は下部回転板2上で
遠心転勤流動される下部粉粒体層13の粉粒体を第2開
山)に破線矢印で示す如く上部回転板lO上に上昇させ
て該上部回転板10上で遠心転勤流動する上部粉粒体層
14を形成するためのものである。この上部粉粒体層1
4からオーバーフローした粉粒体は粉粒体落下用開口1
2から下部回転板2上に落下し、再び循環的に遠心転勤
流動された後、粉粒体上昇用開口12から上部回転板1
0上に上昇されて遠心転勤流動される。
The upper rotary plate 10 of this embodiment has substantially the same curved surface shape as the lower rotary plate 2. An opening 11 for falling powder and granular material is formed in the center of the upper rotary plate 10, and an opening 12 (notch) for lifting powder and granular material is cut out in the radial direction at one location. The opening 12 for raising the powder and granules allows the powder and granules in the lower powder and granule layer 13 centrifugally transferred and flowed on the lower rotary plate 2 to rise above the upper rotary plate 1O as shown by the broken line arrow in the second opening). This is for forming an upper powder layer 14 which is centrifugally transferred and fluidized on the upper rotary plate 10. This upper powder layer 1
The powder and granules that overflow from 4 are transferred to opening 1 for powder and granules to fall.
2 onto the lower rotary plate 2, and after being cyclically centrifuged and fluidized again, it is dropped from the opening 12 for raising the powder and granules onto the upper rotary plate 1.
It is raised above 0 and centrifugally transferred.

すなわち、本実施例では、処理容器l内の粉粒体は下部
回転板2と上部回転板10とよりなる2段の回転面すな
わち単一回転板構造に比して約2倍近い面積の回転面上
でそれぞれ循環的にシーケンシャルな遠心転勤流動作用
を受けながら効率良く処理される。
That is, in this embodiment, the powder and granular material in the processing container l has a two-stage rotating surface consisting of the lower rotating plate 2 and the upper rotating plate 10, that is, the area of rotation is approximately twice that of a single rotating plate structure. Each surface is efficiently processed while being subjected to sequential centrifugal transfer flow action in a cyclical manner.

なお、粉粒体上昇用開口12は第3図の如く3個所に設
けること等も可能であり、また図示しないが、円形また
は四角形の如き開口として部分的に形成してもよい、さ
らに、第2開山)に二点鎖線で示す如く、開口12の回
転板回転方向前縁部10aが回転方向後側に向けて下方
に傾斜していてもよく、この場合には、開口12による
粉粒体すくい上げ効果をより良好にすることができる。
Incidentally, the openings 12 for raising the powder or granular material can be provided at three locations as shown in FIG. 2), the front edge 10a of the opening 12 in the rotating direction of the rotating plate may be inclined downward toward the rear side in the rotating direction. It is possible to improve the scooping effect.

処理容器lの底部側面には、処理済みの粉粒体を排出す
るための排出機構15が設けられている。
A discharge mechanism 15 for discharging the processed powder is provided on the bottom side of the processing container l.

一方、処理容器1の上部には、粉粒体原料を供給するた
めのホッパ16、およびバインダ液等の供給用のスプレ
ーノズル17が設けられている。
On the other hand, a hopper 16 for supplying powder raw material and a spray nozzle 17 for supplying binder liquid and the like are provided at the upper part of the processing container 1.

以下、本実施例1の作用について説明する。Hereinafter, the operation of the first embodiment will be explained.

まず、給気源(図示せず)から給気部8および環状のス
リット6を経て処理容器1内に加熱または冷却空気の如
き気体を吹き込みながら、ホッパ16から処理容器1内
に粉粒体原料を供給すると共に、モータ7で回転軸3を
回転させて下部回転板2と上部回転板lOをたとえば時
計方向に回転させる。
First, while blowing gas such as heated or cooled air into the processing container 1 from an air supply source (not shown) through the air supply section 8 and the annular slit 6, the granular material is introduced into the processing container 1 from the hopper 16. At the same time, the motor 7 rotates the rotary shaft 3 to rotate the lower rotary plate 2 and the upper rotary plate lO, for example, in a clockwise direction.

それにより、両回転板2と10の上には、両回転板の回
転による遠心力と回転力で両回転板上を外周方向すなわ
ち容器内壁方向に遠心転勤流動し、かつ上部から容器中
心方向に降下するフローパターンで第1図の破線矢印の
如くそれぞれ遠心転勤流動される粉粒体層13と14が
形成される。しかも、その場合、処理容器1内に少なく
とも両回転板2と10との間の距離以上の深さまでの量
の粉粒体を供給することにより、第1図に示す如(、下
部回転板2上の粉粒体層13は上部回転板10の下面に
接触する。それによって、粉粒体層13の上部に遠心転
勤流動して来た粉粒体は、上部の回転板10の粉粒体上
昇用間口12を通って該上部回転板lOの上にすくい上
げられ、該上部回転板10上で遠心転勤流動する粉粒体
層14を形成する。
As a result, a centrifugal flow is generated on both rotary plates 2 and 10 due to the centrifugal force and rotational force caused by the rotation of both rotary plates, and a centrifugal flow is generated on both rotary plates toward the outer circumference, that is, toward the inner wall of the container, and from the top toward the center of the container. With the descending flow pattern, powder layers 13 and 14 are formed which are centrifugally transferred as indicated by the broken line arrows in FIG. 1, respectively. Moreover, in that case, by supplying the powder and granular material to a depth at least equal to the distance between both rotary plates 2 and 10 into the processing container 1, as shown in FIG. The upper powder layer 13 comes into contact with the lower surface of the upper rotating plate 10.Thereby, the powder that has centrifugally transferred to the upper part of the powder layer 13 is transferred to the upper rotating plate 10. It is scooped up onto the upper rotary plate 10 through the lifting opening 12, and forms a powder layer 14 which is centrifugally transferred and flows on the upper rotary plate 10.

一方、上部回転板10上の粉粒体層14からオーバーフ
ローした粉粒体は、粉粒体落下用開口11を通って下部
回転板2の上に落下し、再び該下部回転板2の回転によ
る遠心力と回転力で粉粒体層13の中に遠心転勤流動し
た後、粉粒体上昇用開口12を通って上部回転板10上
に上昇して遠心転勤流動する粉粒体層14を形成しなが
ら処理され、さらにオーバーフローして粉粒体落下用開
口11から下部回転板2上に落下する。
On the other hand, the powder overflowing from the powder layer 14 on the upper rotating plate 10 falls onto the lower rotating plate 2 through the powder falling opening 11, and is again caused by the rotation of the lower rotating plate 2. After being centrifugally transferred into the powder layer 13 by centrifugal force and rotational force, it rises through the powder lifting opening 12 onto the upper rotary plate 10 to form a centrifugally transferred powder layer 14. The particles are processed while being processed, and further overflow and fall onto the lower rotary plate 2 from the powder drop opening 11.

したがって、本実施例では、2段の回転板2゜10上に
おける粉粒体は、単一回転板構造に比して約2倍近い面
積の回転面上で遠心転勤流動されながら、両回転板間で
遠心転勤流動、上昇、遠心転勤流動、落下の順序で処理
され、その間に造粒。
Therefore, in this example, the powder and granules on the two rotary plates 2°10 are centrifugally transferred and flowed on a rotating surface with an area approximately twice as large as that of a single rotary plate structure. Processed in the order of centrifugal transfer flow, rising, centrifugal transfer flow, fall, and granulation during.

コーチング、混合、乾燥等の所望の処理をシーケンシャ
ルに効率良く施すことができる。たとえば、上段の粉粒
体層14の粉粒体にノズル17から液を供給し湿潤させ
かつホッパ16から粉粒体原料を供給すると、その粉粒
体は下部回転板2上の粉粒体層13の粉粒体よりも細か
い粒径のものが多くなる傾向にあるが、その細粒に選択
的にコーチングされることになるので、上段の粉粒体層
14の粒径と下段の粉粒体層13の粒径が均一化され、
粒度分布のシャープな造粒、コーチングが可能となる。
Desired treatments such as coating, mixing, and drying can be performed sequentially and efficiently. For example, when liquid is supplied from the nozzle 17 to the powder in the upper powder layer 14 to moisten it, and a powder raw material is supplied from the hopper 16, the powder is transferred to the powder layer on the lower rotary plate 2. There is a tendency for the particles to be finer than those in the powder layer 13, but since the fine particles are selectively coated, the particle size in the upper powder layer 14 and the powder in the lower layer tend to be smaller. The particle size of the body layer 13 is made uniform,
Enables granulation and coating with sharp particle size distribution.

〔実施例2〕 第4図は本発明による粉粒体処理装置の他の実施例を示
す断面図である。
[Embodiment 2] FIG. 4 is a sectional view showing another embodiment of the powder processing apparatus according to the present invention.

本実施例2では、前記実施例1における上部回転板10
に相当する回転板が103と10bで示す如く2段に設
けられ、それぞれ支柱9a、9bで支持され、それぞれ
の上に粉粒体層14a、14bを独立に形成する。した
がって、下部回転板2と合わせて3段の回転面により単
一回転板構造に比して約3倍近い面積の回転面でさらに
効率的な粉粒体処理が可能となる。
In the second embodiment, the upper rotary plate 10 in the first embodiment is
Rotary plates corresponding to the above are provided in two stages as shown by 103 and 10b, supported by support columns 9a and 9b, respectively, and powder layers 14a and 14b are independently formed on each. Therefore, with the three stages of rotating surfaces including the lower rotating plate 2, more efficient powder and granular material processing is possible with the rotating surface having an area approximately three times larger than that of a single rotating plate structure.

なお、本実施例2においては、平板状の下部回転板2の
下方には処理容器1自体の底面が別途形成され、この底
面と下部回転板2との間には回転軸3に形成した給気路
18を経てパージ等のための気体が噴出され、かつ処理
容器1の下部回転板2よりもやや上方の位置には給気管
19が接続され、図示しない給気源から粉粒体層13の
中に空気等の気体を供給するよう構成されている。また
、最下段の粉粒体層13の湿度を自動的に感知するため
の湿度センサ20が設けられているが、中段および最上
段の粉粒体層14a、14bにも湿度センサ20を設け
てもよい。
In the second embodiment, the bottom surface of the processing container 1 itself is separately formed below the flat plate-shaped lower rotary plate 2, and between this bottom surface and the lower rotary plate 2 there is a feeder formed on the rotary shaft 3. Gas for purging, etc. is ejected through the air passage 18, and an air supply pipe 19 is connected to a position slightly above the lower rotary plate 2 of the processing container 1, and supplies the powder layer 13 from an air supply source (not shown). The device is configured to supply gas such as air into the device. Further, although a humidity sensor 20 is provided to automatically sense the humidity of the powder layer 13 at the bottom stage, humidity sensors 20 are also provided at the middle and top powder layers 14a and 14b. Good too.

〔実施例3〕 第5図は本発明のさらに他の実施例を示す断面図である
[Embodiment 3] FIG. 5 is a sectional view showing still another embodiment of the present invention.

本実施例3では、処理容器1の底面と下部回転板2との
間において撹拌部材21が回転軸3に取り付けられてい
る。
In the third embodiment, a stirring member 21 is attached to the rotating shaft 3 between the bottom surface of the processing container 1 and the lower rotating plate 2.

したがって、この攪拌部材21により粉粒体の攪拌を行
い、混合効果をさらに高めることができる。
Therefore, the stirring member 21 can stir the granular material to further enhance the mixing effect.

〔実施例4〕 第6図は本発明のさらに他の実施例を示す断面図である
[Embodiment 4] FIG. 6 is a sectional view showing still another embodiment of the present invention.

この実施例4においては、回転軸3は処理容器1の上方
から軸心に垂下され、その下端に下部回転板2が取り付
けられている。
In this embodiment 4, the rotating shaft 3 is suspended from above the processing container 1 toward the axis, and the lower rotating plate 2 is attached to the lower end thereof.

また、下部回転板2および処理容器lの底面には、それ
ぞれ通気孔22.23が形成され、周期部8からの気体
がこれらの通気孔23.22および環状のスリット6を
経て処理容器1内の処理室に送り込まれ、乾燥効果およ
び流動効果をさらに高めることができる。
Further, ventilation holes 22.23 are formed in the bottom of the lower rotating plate 2 and the processing container l, respectively, and gas from the periodic part 8 passes through these ventilation holes 23.22 and the annular slit 6 into the processing container 1. The drying effect and fluidization effect can be further enhanced.

なお、本発明は前記実施例に限定されるものではな(、
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 (
Various other variations are possible.

たとえば、処理容器を円錐状、または逆円錐状のものと
したり、回転板を4段以上の多段にしたりすることもで
きる。
For example, the processing container may have a conical shape or an inverted conical shape, and the rotating plate may have four or more stages.

また、本発明は、たとえば錠剤、細粒剤、顆粒剤、カプ
セル剤等の医薬、チョコレート等の食品、粉末冶金触媒
、フェライト、セラミックス、洗剤、化粧品、染料、顔
料等に用いられる粉粒体の造粒、コーチング、乾燥、混
合等に広く適用できる。
Furthermore, the present invention is applicable to powder and granular materials used in medicines such as tablets, fine granules, granules, capsules, foods such as chocolate, powder metallurgy catalysts, ferrites, ceramics, detergents, cosmetics, dyes, pigments, etc. Widely applicable to granulation, coating, drying, mixing, etc.

〔効果〕〔effect〕

(1)、水平断面が実質的に円形状をなす容器内で回転
する第1の回転板と、この回転板から上方に所定間隔だ
け離隔した位置において前記容器内で回転可能に設けら
れかつ少なくとも一個所に粉粒体°上昇用開口を形成し
た第2の回転板とを多段に配設してなることにより、回
転面の面積が増大し、大量の粉粒体を効率良く、精密に
処理することができる。
(1) a first rotating plate that rotates within a container having a substantially circular horizontal cross section; and at least By arranging a second rotary plate in multiple stages with an opening for raising the powder and granular material in one place, the area of the rotating surface increases, allowing efficient and precise processing of large amounts of powder and granular material. can do.

(2)、また、前記(11により、各回転面において順
次所望の処理を行うことができるので、最下段の回転面
から最上段の回転面に順次移動し、最上段の回転面から
オーバーフローさせて最下段の回転面に落下させ、さら
に最下段から最上段へと循環流を形成しながら循環処理
することができ、必要に応じてその循環流の所望の部位
で湿潤、粉末散布、転動、造粒、コーチング、混合、乾
燥等の諸処理を行い、全体としてシーケンシャルな粉粒
体処理を7つの処理装置で得ることができる。
(2) Also, according to (11) above, it is possible to sequentially perform the desired processing on each rotating surface, so the rotation surface is sequentially moved from the lowest rotating surface to the highest rotating surface, and the overflow from the highest rotating surface is prevented. It can be dropped onto the rotating surface of the lowest stage, and then circulated while forming a circulating flow from the lowest stage to the highest stage.Wetting, powder scattering, and rolling can be carried out at desired parts of the circulating flow as necessary. , granulation, coating, mixing, drying, etc., and overall sequential powder and granule processing can be obtained using seven processing devices.

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

第1図は本発明による一実施例である粉粒体処理装置の
断面図、第2図(alと(blはそれぞれ回転板の平面
図と同図(alのIIB−IIB線断面図、第3図は回
転板の他の実施例の平面図、第4図は本発明による粉粒
体処理装置の他の実施例を示す断面図、第5図は本発明
のさらに他の実施例を示す断面図、第6図は本発明のさ
らに他の実施例を示す断面図である。 1・・・処理容器、 2・・・下部回転板(第1の回転板)、3・・・回転軸
、   4・・・円錐台形部材、5・・・取付ボルト、
 6・・・スリット、7・・・モータ、   8・・・
給気部、9.9a、9b・・・支柱、 10・・・上部回転板(第2の回転板)、10a、10
b−−・回転板、 11・・・粉粒体落下用開口、 12・・・粉粒体上昇用開口、 13・・・下部粉粒体層、 14・・・上部粉粒体層、 14a、  14b−−・粉粒体層、 15・・・排出機構、  16・・・ホッパ、17・・
・スプレーノズル、 18・・・給気路、   19・・・給気管、20・・
・湿度センサ、 21・・・攪拌部材、 22.23・・・通気孔。
FIG. 1 is a cross-sectional view of a powder/granular material processing apparatus that is an embodiment of the present invention, and FIG. FIG. 3 is a plan view of another embodiment of the rotary plate, FIG. 4 is a sectional view showing another embodiment of the granular material processing apparatus according to the present invention, and FIG. 5 is a plan view of another embodiment of the present invention. 6 is a cross-sectional view showing still another embodiment of the present invention. 1... Processing container, 2... Lower rotating plate (first rotating plate), 3... Rotating shaft , 4... truncated conical member, 5... mounting bolt,
6...Slit, 7...Motor, 8...
Air supply part, 9.9a, 9b... Support column, 10... Upper rotating plate (second rotating plate), 10a, 10
b--Rotating plate, 11... Opening for powder/granular material falling, 12... Opening for powder/granular material rising, 13... Lower powder/granular material layer, 14... Upper powder/granular material layer, 14a , 14b--Powder layer, 15... Discharge mechanism, 16... Hopper, 17...
・Spray nozzle, 18...Air supply path, 19...Air supply pipe, 20...
- Humidity sensor, 21... Stirring member, 22.23... Ventilation hole.

Claims (10)

【特許請求の範囲】[Claims] (1)、水平断面が実質的に円形状をなす容器内で回転
する第1の回転板と、この回転板から上方に所定間隔だ
け離隔した位置において前記容器内で回転可能に設けら
れかつ少なくとも1個所に粉粒体上昇用開口を形成した
第2の回転板とを多段に配設してなる粉粒体処理装置。
(1) a first rotating plate that rotates within a container having a substantially circular horizontal cross section; and at least A powder and granular material processing device comprising a second rotary plate having an opening for raising the powder and granular material arranged in multiple stages.
(2)、前記第2の回転板が、半径方向中心側に粉粒体
落下用開口を形成し、半径方向外周側に前記粉粒体上昇
用開口を形成した略ドーナツ状の円板であることを特徴
とする特許請求の範囲第1項記載の粉粒体処理装置。
(2) The second rotary plate is a substantially donut-shaped disc having an opening for falling powder and granular material formed on the center side in the radial direction, and an opening for raising the powder and granular material on the outer peripheral side in the radial direction. A granular material processing apparatus according to claim 1, characterized in that:
(3)、前記第2の回転板が多段に形成されていること
を特徴とする特許請求の範囲第1項記載の粉粒体処理装
置。
(3) The granular material processing apparatus according to claim 1, wherein the second rotary plate is formed in multiple stages.
(4)、前記第2の回転板が前記第1の回転板の上に支
柱で支持されていることを特徴とする特許請求の範囲第
1項記載の粉粒体処理装置。
(4) The granular material processing apparatus according to claim 1, wherein the second rotary plate is supported by a support on the first rotary plate.
(5)、前記第1の回転板と前記第2の回転板とが同一
の回転軸で回転されることを特徴とする特許請求の範囲
第1項記載の粉粒体処理装置。
(5) The granular material processing apparatus according to claim 1, wherein the first rotary plate and the second rotary plate are rotated about the same rotation axis.
(6)、前記回転軸が前記容器の上方から該容器内に延
びていることを特徴とする特許請求の範囲第5項記載の
粉粒体処理装置。
(6) The granular material processing apparatus according to claim 5, wherein the rotating shaft extends into the container from above the container.
(7)、前記回転軸に、半径方向外側に延びる攪拌羽根
が略水平方向に取り付けられていることを特徴とする特
許請求の範囲第5項記載の粉粒体処理装置。
(7) The granular material processing apparatus according to claim 5, wherein stirring blades extending radially outward are attached to the rotating shaft in a substantially horizontal direction.
(8)、前記第1の回転板が前記容器の底面を構成して
いることを特徴とする特許請求の範囲第1項記載の粉粒
体処理装置。
(8) The granular material processing apparatus according to claim 1, wherein the first rotary plate constitutes a bottom surface of the container.
(9)、前記第2の回転板の粉粒体上昇用開口が半径方
向に形成した切欠きであることを特徴とする特許請求の
範囲第1項記載の粉粒体処理装置。
(9) The granular material processing apparatus according to claim 1, wherein the opening for raising the granular material in the second rotary plate is a notch formed in the radial direction.
(10)、前記第2の回転板の前記切欠きの回転板回転
方向前縁部が回転方向後側に向けて下方に傾斜している
ことを特徴とする特許請求の範囲第9項記載の粉粒体処
理装置。
(10) The front edge of the notch of the second rotary plate in the rotary plate rotation direction is inclined downward toward the rear side in the rotation direction. Powder processing equipment.
JP7232485A 1985-04-05 1985-04-05 Apparatus for treating particulate material Pending JPS61230730A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7232485A JPS61230730A (en) 1985-04-05 1985-04-05 Apparatus for treating particulate material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7232485A JPS61230730A (en) 1985-04-05 1985-04-05 Apparatus for treating particulate material

Publications (1)

Publication Number Publication Date
JPS61230730A true JPS61230730A (en) 1986-10-15

Family

ID=13485983

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7232485A Pending JPS61230730A (en) 1985-04-05 1985-04-05 Apparatus for treating particulate material

Country Status (1)

Country Link
JP (1) JPS61230730A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5514065A (en) * 1993-03-31 1996-05-07 Hitachi Metals, Ltd. Wear- and seizing-resistant roll for hot rolling and method of making the roll
JP2002018266A (en) * 2000-05-01 2002-01-22 Freunt Ind Co Ltd Apparatus and method for fluidized bed granulating and coating
JP2007300861A (en) * 2006-05-11 2007-11-22 Pauretsuku:Kk Device and method for coating chocolate, and method for molding solid chocolate
US7908765B2 (en) * 2006-12-22 2011-03-22 Collette Nv Continuous granulating and drying apparatus

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5514065A (en) * 1993-03-31 1996-05-07 Hitachi Metals, Ltd. Wear- and seizing-resistant roll for hot rolling and method of making the roll
JP2002018266A (en) * 2000-05-01 2002-01-22 Freunt Ind Co Ltd Apparatus and method for fluidized bed granulating and coating
JP4663887B2 (en) * 2000-05-01 2011-04-06 フロイント産業株式会社 Fluidized bed granulation coating apparatus and fluidized bed granulation coating method
JP2007300861A (en) * 2006-05-11 2007-11-22 Pauretsuku:Kk Device and method for coating chocolate, and method for molding solid chocolate
US7908765B2 (en) * 2006-12-22 2011-03-22 Collette Nv Continuous granulating and drying apparatus

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