JPS6268536A - Method and apparatus for treating particulate material - Google Patents

Method and apparatus for treating particulate material

Info

Publication number
JPS6268536A
JPS6268536A JP20827385A JP20827385A JPS6268536A JP S6268536 A JPS6268536 A JP S6268536A JP 20827385 A JP20827385 A JP 20827385A JP 20827385 A JP20827385 A JP 20827385A JP S6268536 A JPS6268536 A JP S6268536A
Authority
JP
Japan
Prior art keywords
rotary
powder
rotary plate
venting
rotary plates
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP20827385A
Other languages
Japanese (ja)
Other versions
JPH0616827B2 (en
Inventor
Shimesu Motoyama
本山 示
Setsu Sakashita
坂下 攝
No Kubota
久保田 濃
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.)
Okawara Mfg Co Ltd
Freund Corp
Original Assignee
Okawara Mfg Co Ltd
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 Okawara Mfg Co Ltd, Freund Corp filed Critical Okawara Mfg Co Ltd
Priority to JP60208273A priority Critical patent/JPH0616827B2/en
Publication of JPS6268536A publication Critical patent/JPS6268536A/en
Publication of JPH0616827B2 publication Critical patent/JPH0616827B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Glanulating (AREA)

Abstract

PURPOSE:To obtain a uniform granulated product, by a method wherein rotary plates are arranged in a treatment chamber at definite intervals in a multistage fashion through ring shaped venting members and the gas is further injected in the treatment chamber while being introduced from the inside of each ring shaped venting member to treat a particulate material by the rotation of the rotary plates and the action of a gas stream. CONSTITUTION:A rotary shaft 5 is provided to the bottom part of a treatment chamber and rotary plates 8 are arranged to the upper part of said rotary shaft 5 in a multistage structure so as to be spaced apart by the height of each venting ring 10 and to successively reduce the diameters of each rotary plates to the upward direction. The rotary plates 8 are provided with venting openings 12 inside the venting rings in the radius direction except the uppermost one and an annular space 16 is formed between the lowermost rotary plate 18 and a container 1. When a particulate stock material is changed in the treatment chamber, the stock material is fluidized from the gas stream from the annular space 16 and tumbled while receiving centrifugal tumbling action by the rotation of the rotary plates 8. Further, said stock material receives the force to the outside in the radius direction from the venting rings 10 and is pressed to the inner wall surface of the treatment container 1 to be formed into a heavy particulate material having a uniform particle size.

Description

【発明の詳細な説明】 〔技術分野〕 本発明は粉粒体処理方法および装置、特に、流動層型の
処理室内で粉粒体の造粒、コーチング、乾燥、混合など
の処理を行う粉粒体処理方法および装置に関する。
[Detailed Description of the Invention] [Technical Field] The present invention relates to a method and apparatus for processing powder and granules, and in particular, a method and apparatus for processing powder and granules that perform processes such as granulation, coating, drying, and mixing of powder and granules in a fluidized bed type processing chamber. The present invention relates to a body treatment method and device.

〔背景技術〕[Background technology]

一般に、流動層型の粉粒体処理技術としては、固定式の
孔あき板よりなる流動床の下方からガス流を噴出させて
処理室内の粉粒体を流動させ、結合材溶液により粉粒体
を凝集させるものが提案されている。
In general, fluidized bed powder processing technology involves ejecting a gas flow from below the fluidized bed made of a fixed perforated plate to fluidize the powder in the processing chamber, and using a binder solution to form the powder. A method has been proposed that aggregates the .

ところが、この従来技術では、粉粒体は専ら噴出ガス流
の作用のみで流動状態とされることにより造粒されるの
で、造粒製品は軽質で、不定形となり、粒度分布も広範
囲にばらつくなどの問題がある。
However, in this conventional technology, the powder and granules are granulated by being brought into a fluid state solely by the action of the ejected gas flow, so the granulated products are light and have an irregular shape, and the particle size distribution varies over a wide range. There is a problem.

そこで、処理室内の流動床を回転板とし、この回転板の
回転と下方からのガス流とにより粉粒体に遠心転動およ
び旋回作用を与えて均一な造粒製品を製造することが提
案されている(たとえば、特開昭59−55337号公
報参照)。
Therefore, it has been proposed to use a rotating plate as the fluidized bed in the processing chamber, and produce a uniform granulated product by applying centrifugal rolling and swirling effects to the powder and granules through the rotation of the rotating plate and the gas flow from below. (For example, see Japanese Patent Laid-Open No. 59-55337).

この従来技術によれば、所望の粒径を持つ均一な造粒製
品を製造できるなどの優れた作用効果が得られるもので
あるが、回転板が1枚のみであり、また回転板上で粉粒
体を放射方向に運動させる力は回転板の回転で与えられ
る。そのため、回転板上における粉粒体の遠心転動およ
び処理室の内壁に対する粉粒体の押圧力が不十分である
場合には所望の重質の造粒製品を得ることができなくな
る場合が起こり得る。
According to this conventional technology, excellent effects such as being able to produce a uniform granulated product with a desired particle size can be obtained, but there is only one rotating plate, and the powder is not processed on the rotating plate. The force that moves the particles in the radial direction is provided by the rotation of the rotating plate. Therefore, if the centrifugal rolling of the powder on the rotating plate and the pressing force of the powder against the inner wall of the processing chamber are insufficient, it may become impossible to obtain the desired heavy granulated product. obtain.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、重質で、均一な製品を得ることのでき
る粉粒体処理方法および装置を提供することにある。
An object of the present invention is to provide a method and apparatus for processing powder and granular material that can produce a heavy and uniform product.

本発明の他の目的は、造粒、コーチング、乾燥などの処
理効率を向上させることのできる粉粒体処理方法および
装置を提要することにある。
Another object of the present invention is to provide a powder and granule processing method and apparatus that can improve the processing efficiency of granulation, coating, drying, etc.

本発明のさらに他の目的は、処理室内の洗浄が容易で、
クロスコンタミネーションなどのない、7N浄な製品を
得ることのできる粉粒体処理方法および装置を提供する
ことにある。
Still another object of the present invention is that the inside of the processing chamber can be easily cleaned;
It is an object of the present invention to provide a method and apparatus for processing powder and granular material that can obtain a 7N clean product without cross-contamination.

本発明のさらに他の目的は、粉粒体原料の漏れのない粉
粒体処理方法および装置を提供することにある。
Still another object of the present invention is to provide a powder processing method and apparatus that prevent leakage of powder raw materials.

〔発明の概要〕[Summary of the invention]

本発明は、複数枚の回転板を環状通気部材で互いに離間
させ、この環状通気部材よりも半径方向内側における前
記回転板の通気開口から導入したガスを、前記環状通気
部材を通して半径方向外側に噴出し、かつ前記回転板を
回転させることにより、前記回転板の回転と前記環状通
気部材を通して噴出される半径方向外側へのガス流との
作用によって粉粒体上で転動させながら処理するもので
ある。
In the present invention, a plurality of rotary plates are separated from each other by an annular ventilation member, and gas introduced from a ventilation opening of the rotary plate radially inside the annular ventilation member is jetted radially outward through the annular ventilation member. and by rotating the rotary plate, the powder and granules are treated while being rolled on the powder and granular material by the action of the rotation of the rotary plate and the gas flow radially outwardly ejected through the annular ventilation member. be.

それにより、粉粒体は回転板上で遠心転動作用と半径方
向外側へのガス流による押圧作用を受け、処理室の内壁
方向への押圧力を受けながら処理されるので、重質の製
品を効率良く生産することができ、また粉漏れの防止、
洗浄性の向上を図ることができるものである。
As a result, the powder and granules are processed while being subjected to centrifugal rotation on the rotary plate and the pressing action of the gas flow radially outward, and the pressing force toward the inner wall of the processing chamber. can be produced efficiently, and can also prevent powder leakage.
This makes it possible to improve cleaning performance.

〔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
全体的略断面図、第2図はその要部の拡大部分断面図で
ある。
[Embodiment 1] FIG. 1 is an overall schematic sectional view of a powder or granular material processing apparatus according to an embodiment of the present invention, and FIG. 2 is an enlarged partial sectional view of the main parts thereof.

本実施例1において、粉粒体処理装置は粉粒体の造粒、
コーチング、混合、乾燥などの処理を行う直立筒状の処
理容器lを基台2上に立設した構造よりなる。処理容器
1内には後述の如く流動室を形成する処理室3が設けら
れる。処理室3の側面部には、粉粒体原料を供給する原
料投入口4が(1設されている。
In this Example 1, the powder/granular material processing apparatus granulates the powder/granular material,
It has a structure in which an upright cylindrical processing container 1 for performing processing such as coating, mixing, and drying is erected on a base 2. Inside the processing container 1, a processing chamber 3 forming a flow chamber is provided as will be described later. A raw material input port 4 for supplying powdered raw material is provided on the side surface of the processing chamber 3.

また、処理室3の底部における中心部には回転軸5が垂
直力向に設けられ、この回転軸5はモータ日により回転
される。回転軸5の上部には、複数枚の円板状の回転板
8が互いに垂直方向に所定間隙を隔てて多層状に配置さ
れている。すなわち、最下部の回転板8は回転軸5に止
め輸9で保持され、その次に上側に位置する回転板9は
スペーサおよび扮漏れ防止手段として機能する通気リン
グ10の高さ分だけ最下部の回転板8から離間されてい
る。本実施例の回転板8は5枚であり、下から3枚目よ
り上側の回転板8も前記と同様に相互間に通気リング1
0を介して多層構造に配置されている。前記回転板8は
その上面の上で粉粒体を遠心作用などで転動させるもの
であり、最下部から最上部にかけて直径が順次小さくな
るよう構成されている。最上部の回転板8はキャップ1
1を回転軸5に螺合することにより固定されるよう構成
されている。
Further, a rotating shaft 5 is provided at the center of the bottom of the processing chamber 3 in the vertical force direction, and this rotating shaft 5 is rotated by a motor. Above the rotating shaft 5, a plurality of disc-shaped rotating plates 8 are arranged in a multilayered manner with predetermined gaps in between in the vertical direction. That is, the rotary plate 8 at the bottom is held by the rotary shaft 5 with a support 9, and the rotary plate 9 located next above is held at the bottom by the height of the ventilation ring 10 which functions as a spacer and leakage prevention means. It is spaced apart from the rotary plate 8. There are five rotary plates 8 in this embodiment, and the third rotary plate 8 from the bottom and the upper rotary plates 8 also have ventilation rings between them as described above.
0 in a multilayer structure. The rotary plate 8 is used to roll powder and granules on its upper surface by centrifugal action, and is configured such that its diameter gradually decreases from the bottom to the top. The top rotating plate 8 is the cap 1
1 is screwed onto the rotating shaft 5 to be fixed.

通気リング10は回転板8の回転により軸心がずれるこ
とのないように、その上端を各回転板8の裏面の環状溝
8aに嵌め込むことによって位置決めされるようになっ
ている。
The ventilation ring 10 is positioned by fitting its upper end into an annular groove 8a on the back surface of each rotary plate 8 so that its axis does not shift due to rotation of the rotary plate 8.

前記回転板8および通気リング10はキャップ11を取
り外した状態で回転軸5に順次交互に嵌装することによ
り容易に着脱自在に組み立てることができる。したがっ
て、回転板8および通気リング10は洗浄時にはキャッ
プ11を取り外した後に順次回転軸5から抜き出せば容
易に取り外して個々に洗浄できる。このように、着脱自
在な構造であることにより、本実施例の回転板8および
通気リング1oは高い清浄度を維持でき、処理室3内を
/U浄に保つことが可能となる。
The rotating plate 8 and the ventilation ring 10 can be easily detachably assembled by sequentially and alternately fitting them onto the rotating shaft 5 with the cap 11 removed. Therefore, during cleaning, the rotating plate 8 and the ventilation ring 10 can be easily removed and washed individually by removing the cap 11 and then pulling them out from the rotating shaft 5 one after another. As described above, due to the detachable structure, the rotary plate 8 and the ventilation ring 1o of this embodiment can maintain a high level of cleanliness, and the inside of the processing chamber 3 can be kept /U clean.

通気リング10はたとえば多孔性材料やメッシ二など、
通気性を有し、かつ粉粒体の漏れ止めの役割を果たし得
る材料で作られている。
The ventilation ring 10 is made of, for example, a porous material or a mesh material.
It is made of a material that is breathable and can act as a leak-tight material.

さらに、前記回転板8には、最上部の回転板8を除いて
、前記通気リング10よりも半径方向内側において通気
間ロエ2が設けられている。通気開口12はたとえば第
5図に示すように、複数個を円周方向に互いに間隔をあ
けて配置してもよく、あるいは他の形の開口もしくはド
ーナツ状の構造のものを用いることも可能である。なお
、第5図において、回転板8の中心の孔13は回転軸5
を挿通ずる孔である。
Furthermore, the rotary plates 8 are provided with a ventilation loop 2 on the inner side of the ventilation ring 10 in the radial direction, except for the uppermost rotary plate 8. A plurality of ventilation openings 12 may be arranged circumferentially at intervals as shown in FIG. 5, or other shapes of openings or doughnut-shaped structures may be used. be. In addition, in FIG. 5, the hole 13 at the center of the rotating plate 8 is connected to the rotating shaft 5.
It is a hole through which the

一方、処理質3内の底部における回転板8の下方には、
送風機14からバルブ15を経てガスを供給するように
なっている。このガスは、回転板8の前記通気開口12
を経てjj1気リング10から半径方向外側に噴出され
る他、回転板8の周囲と処理容器1の内壁との間に形成
された環状空間16を通って処理室3内に供給され、粉
粒体原料を流動化させるガスとしての機能を果たす。
On the other hand, below the rotating plate 8 at the bottom of the treatment material 3,
Gas is supplied from a blower 14 through a valve 15. This gas flows through the ventilation openings 12 of the rotating plate 8.
In addition to being ejected radially outward from the jj1 air ring 10 through the It functions as a gas that fluidizes body materials.

最下部の回転板8とほぼ同じ高さにおける処理容器1の
側面には、製品取り出し用の排出機t* 17が設けら
れている。
A discharger t* 17 for taking out the product is provided on the side surface of the processing container 1 at approximately the same height as the lowermost rotary plate 8.

また、回転板8の側方における処理室3内には、処理中
の粉粒体の解砕を行って、かさ密度の大きい球形の製品
を得るための解砕機構18と、コーチンダ液またはバイ
ンダー液などの噴霧のための二流体式スプレーガン構造
などのスプレー装置19が設けられている。回転板8の
上方に二流体式スプレーガン構造などのスプレー装置2
0を設けることもできる。
Further, in the processing chamber 3 on the side of the rotary plate 8, there is a crushing mechanism 18 for crushing the powder and granules being processed to obtain a spherical product with a large bulk density, and a crushing mechanism 18 for crushing the powder and granules being processed to obtain a spherical product with a large bulk density, and a cochindar liquid or a binder. A spray device 19, such as a two-fluid spray gun structure, is provided for spraying liquid or the like. A spray device 2 such as a two-fluid spray gun structure is installed above the rotating plate 8.
0 can also be provided.

さらに、処理容器lの上部には、ガス流に同伴される微
粉を捕集するバグフィルタ21,4発放散用のM22、
および排気を系外に排出する排気ダクト23が設けられ
ている。
Further, in the upper part of the processing container l, there is a bag filter 21 for collecting fine powder entrained in the gas flow, an M22 for dispersing 4,
Also provided is an exhaust duct 23 for discharging exhaust gas to the outside of the system.

以下、本実施例の作用について説明する。The operation of this embodiment will be explained below.

まず、原料投入口4から処理室3内に粉粒体原料を投入
するにあたって、必要に応じてたとえば粉粒体原料が環
状空間16から漏れ落ちない程度に送風機14からのガ
スをバルブ15を経て回転板日の下方に供給しながら、
粉粒体原料の投入を行う。
First, when introducing the granular raw material into the processing chamber 3 from the raw material input port 4, if necessary, for example, gas from the blower 14 is passed through the valve 15 to an extent that the granular raw material does not leak from the annular space 16. While feeding downwards on the rotary plate,
Powder raw materials are introduced.

次に、回転軸5および回転板8を回転させ、またバルブ
15をさらに開いて環状空間19から流動化用のガスを
処理室3内に供給する。さらに、スプレーが19および
20の一方または両方から処理室3内にコーチンダ液も
しくはバインダー液を供給し、さらに必要に応して解砕
機構18を作動させる。
Next, the rotating shaft 5 and the rotating plate 8 are rotated, and the valve 15 is further opened to supply fluidizing gas from the annular space 19 into the processing chamber 3 . Furthermore, the spray supplies Cochindar liquid or binder liquid into the processing chamber 3 from one or both of 19 and 20, and further operates the crushing mechanism 18 as required.

その結果、送風機14からのガスは回転板8の通気開口
12から通気リングIOを経て各回転板8間で半径方向
外側に噴出され、かつ環状空間16を遣って処理室3内
に供給される。
As a result, the gas from the blower 14 is ejected radially outwardly between each rotating plate 8 through the ventilation opening 12 of the rotary plate 8 through the ventilation ring IO, and is supplied into the processing chamber 3 using the annular space 16. .

したがって、粉粒体原料は環状空間16からのガス流で
流動化され、また前記回転板8の回転により、各回転板
8上の粉粒体原料は遠心転動作用を受けて転動を行うの
に加えて、通気リング1゜から半径方向外側に噴出され
るガス流により粉粒体原料は半径方向外側への力を受け
、処理容器Iの内壁面に押圧されるので、前記遠心力と
この半径方向外側への力により重質の製品を得ることが
できる。
Therefore, the granular raw material is fluidized by the gas flow from the annular space 16, and due to the rotation of the rotary plate 8, the granular raw material on each rotary plate 8 undergoes centrifugal rolling action and rolls. In addition to this, the granular raw material receives a radially outward force due to the gas flow ejected radially outward from the ventilation ring 1°, and is pressed against the inner wall surface of the processing container I, so that the centrifugal force and This radially outward force allows a heavy product to be obtained.

また、粉粒体は回転板8の回転による遠心転動作用に加
えて半径方向外側へのガス流の作用を受けることにより
、その転動や分散などの作用が促進されるので、均一な
粒度の球形製品を得ることができる他、たとえばコーチ
ンダ液の膜の延伸速度の向上や乾燥速度の向上などによ
って、処理効率を向上させることができる。
Furthermore, in addition to the centrifugal rolling action caused by the rotation of the rotary plate 8, the powder and granular material is subjected to the action of the gas flow outward in the radial direction, which promotes its rolling and dispersion, so that uniform particle size can be achieved. In addition to being able to obtain spherical products, processing efficiency can be improved, for example, by increasing the stretching speed and drying speed of the Cochindia liquid film.

このようにして製造された製品は排出機構17を開ける
ことにより外部に取り出して回収される。
The product thus manufactured is taken out and collected by opening the discharge mechanism 17.

〔実施例2〕 第3図は本発明の他の実施例の要部を示す拡大部分断面
図である。
[Embodiment 2] FIG. 3 is an enlarged partial sectional view showing a main part of another embodiment of the present invention.

この実施例2では、回転軸5が上方から下方に延ヒ・下
端にナンド24を螺合することにより複数枚の回転板8
および通気リング1oを多層状に着脱自在に組み立てた
構造よりなる。
In this second embodiment, the rotary shaft 5 extends from the top to the bottom, and the Nand 24 is screwed to the lower end, so that a plurality of rotary plates 8
It consists of a structure in which a ventilation ring 1o is detachably assembled in a multi-layered manner.

本実施例2の場合にも、回転板8の回転により遠心力と
、通気リング1oがら噴出される半径方向外側へのガス
流の力とにより、重質の製品を効率良く製造できるもの
である。
In the case of the second embodiment as well, heavy products can be manufactured efficiently by the centrifugal force generated by the rotation of the rotary plate 8 and the force of the gas flow radially outwardly ejected from the ventilation ring 1o. .

〔実施例3〕 第4図は本発明のさらに他の実施例を示す拡大部分断面
図である。
[Embodiment 3] FIG. 4 is an enlarged partial sectional view showing still another embodiment of the present invention.

本実施例3においては、前記実施例1における通気性物
質よりなる通気リング1oの代わりに、粉粒体の漏れを
防止できる大きさのガス噴出孔10bを設けた通気リン
グ10aが用いられている。
In Example 3, instead of the ventilation ring 1o made of a breathable material in Example 1, a ventilation ring 10a provided with gas ejection holes 10b large enough to prevent leakage of powder and granules is used. .

この通気リング10aは前記通気リングIQよりも直径
が小さく、各通気リングIOaで離間される回転板8の
直径よりもかなり小さい寸法の直径を有している。
This ventilation ring 10a has a smaller diameter than the ventilation ring IQ, and has a diameter considerably smaller than the diameter of the rotary plate 8 separated by each ventilation ring IOa.

また、本実施例3では、最上部と最下部のものを除いた
回転板8がドーナツ状の構造を存し、さらに最上部の回
転板8にもその下側の通気リング10aよりも半径方向
内側の部位において上下方向への通気孔25が設けられ
ている。
In addition, in the third embodiment, the rotary plates 8 excluding the top and bottom ones have a donut-shaped structure, and the top rotary plate 8 also has a radial direction more than the ventilation ring 10a below. A ventilation hole 25 extending in the vertical direction is provided in the inner part.

本実施例3の場合にも、回転板8の回転とガス噴出孔1
0bから半径方向外側に噴出されるガス流により重質の
製品を効率的に得ることができ、また複数の回転板8と
通気リング10aとはキャンプ11を取り外すだけで容
易に着脱自在に組立および分解でき、洗浄性が良好であ
るので、その清浄度を保ち、衛生的な処理を長期的に行
うことができる。
Also in the case of the third embodiment, the rotation of the rotary plate 8 and the gas nozzle 1
Heavy products can be efficiently obtained by the gas flow ejected outward in the radial direction from 0b, and the plurality of rotary plates 8 and the ventilation ring 10a can be assembled and detached easily by simply removing the camp 11. Since it can be disassembled and has good cleaning properties, its cleanliness can be maintained and sanitary processing can be performed for a long period of time.

なお、本実施例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 this embodiment is not limited to the above embodiment, and various other modifications are possible.

たとえば、処理容器の形状を第5図に1aで示す如く略
球形にすることができる。
For example, the shape of the processing container can be made approximately spherical as shown by 1a in FIG.

また、通気リングや回転板の直径や回転板の枚数なども
適宜選ぶことができる。
Further, the diameter of the ventilation ring and rotating plates, the number of rotating plates, etc. can be selected as appropriate.

さらに、回転板を所定間隔で回転軸に固定することもで
きる。
Furthermore, the rotating plates can also be fixed to the rotating shaft at predetermined intervals.

また、ガス噴出孔を通気リングの接線方向に形成しても
よい。
Further, the gas ejection holes may be formed in the tangential direction of the ventilation ring.

〔効果〕〔effect〕

(1)、複数の回転板の回転による遠心転動作用と、該
回転板相互の間の間隙を形成する環状通気部材から半径
方向外側に噴出されるガス流の作用とにより、粉粒体は
処理室の内壁方向に押圧されるので、重質の製品を得る
ことができる。
(1) Due to the centrifugal rotation caused by the rotation of a plurality of rotary plates and the action of the gas flow jetted radially outward from the annular ventilation member that forms the gap between the rotary plates, the powder and granules are Since it is pressed toward the inner wall of the processing chamber, a heavy product can be obtained.

(2)、半径方向外側へのガス流の作用により粉粒体の
造粒、コーチング、混合、あるいは乾燥などの処理効率
を向上させることができる。
(2) The efficiency of processing such as granulation, coating, mixing, or drying of powder particles can be improved by the action of the gas flow outward in the radial direction.

(3)、環状通気部材により回転板の通気開口への粉粒
体の漏れを防止でき、材料の無駄をなくし、かつ衛生的
な粉粒体処理が可能となる。
(3) The annular ventilation member can prevent powder from leaking into the ventilation openings of the rotary plate, eliminating waste of materials and making it possible to process powder and granules in a sanitary manner.

(4)8回転板および該回転板どうしを離間させる通気
性の環状部材が相互に着脱自在となるよう交互に配置さ
れていることにより、容易に分解して洗浄でき、高い清
浄度を維持できるので、クロスコンタミネーションなど
を起こすことなく、極めて衛生的な処理を行うことが可
能となり、いわゆるGM P (Good Manuf
acturing Practice )上非常に有利
であり、医薬品、食品などの処理にも有益である。
(4) The 8 rotating plates and the air permeable annular members that separate the rotating plates are alternately arranged so that they can be attached to and removed from each other, making it easy to disassemble and clean and maintain a high level of cleanliness. Therefore, it is possible to perform extremely hygienic processing without causing cross-contamination, etc.
It is very advantageous in terms of acturing practice, and is also useful in processing pharmaceuticals, foods, etc.

【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
全体的略断面図、第2図はその要部の拡大部分断面図、
第3図は本発明の他の実施例の要部を示す拡大部分断面
図、第4図は本発明のさらに他の実施例を示す拡大部分
断面図、第5図は回転板の一例を示す平面図である。 1、la・・・処理容器、 2・・・・基台、 3・・・・処理室、 4・・・・原料投入口、 5・・・・回転軸、 6・・・・モータ、 8・・・・回転板、 8a・・・環状溝、 9・・・・止め輪、 10.103・・・・通気リング、 10b・・・ガス噴出孔、 11・・・・キャンプ、 12・・・・通気開口、 13・・・・孔、 14・・・・送風機、 15・・・・バルブ、 16・・・・環状空間、 17・・・・搬出機構、 18・・・・解砕機構、 19.20・・・スプレー装置、 21・・・・バグフィルタ、 22・・・・爆発放散用の蓋、 23・・・・排気ダクト、 24・・・・ナツト、 25・・・・通気孔。 第2図 第3図 図面の浄書(内容に変更ない 第1図 第4図 第5図 手続主甫正書(自発) 昭和60年10月28日 特許庁長官  宇 賀 遵 部 殿 2、発明の名称 粉粒体処理方法および装置 3、補正をする者 事件との関係  特許出願人 住 所  東京都新宿区高田馬場2丁目14番2号名 
称  フロイント産業株式会社 代表者  伏 島 端 豊
FIG. 1 is an overall schematic sectional view of a powder/granular material processing apparatus that is an embodiment of the present invention, and FIG. 2 is an enlarged partial sectional view of the main parts thereof.
FIG. 3 is an enlarged partial sectional view showing a main part of another embodiment of the present invention, FIG. 4 is an enlarged partial sectional view showing still another embodiment of the invention, and FIG. 5 shows an example of a rotary plate. FIG. 1, la...processing container, 2...base, 3...processing chamber, 4...raw material inlet, 5...rotating shaft, 6...motor, 8 ... Rotating plate, 8a ... Annular groove, 9 ... Retaining ring, 10.103 ... Ventilation ring, 10b ... Gas outlet, 11 ... Camp, 12 ... ... Ventilation opening, 13 ... Hole, 14 ... Blower, 15 ... Valve, 16 ... Annular space, 17 ... Carrying out mechanism, 18 ... Crushing mechanism , 19.20... Spray device, 21... Bag filter, 22... Lid for explosion dissipation, 23... Exhaust duct, 24... Nut, 25... Conduit. stomata. Fig. 2 Fig. 3 Engraving of the drawings (no changes in content Fig. 1 Fig. 4 Fig. 5 Procedural principal authorship (spontaneous) October 28, 1985 Commissioner of the Patent Office Mr. Junbu Uga 2, Invention Name Powder processing method and device 3, relationship with the case of the person making the amendment Patent applicant address 2-14-2 Takadanobaba, Shinjuku-ku, Tokyo
Name: Freund Sangyo Co., Ltd. Representative: Yutaka Fushishima Hata

Claims (3)

【特許請求の範囲】[Claims] (1)、処理室内において環状通気部材を介して相互に
所定間隔で多層に配置された回転板の前記環状通気部材
よりも半径方向内側の通気開口から導入したガスを、前
記環状通気部材を通して半径方向外側に噴出し、前記回
転板の回転と、前記環状通気部材を通して噴出される半
径方向外側へのガス流との作用により粉粒体を前記回転
板上で転動させながら処理することを特徴とする粉粒体
処理方法。
(1) Gas is introduced into the processing chamber through the annular ventilation member from a ventilation opening radially inner than the annular ventilation member of a rotary plate arranged in multiple layers at predetermined intervals. The powder and granular material is treated while rolling on the rotary plate due to the action of the rotation of the rotary plate and the gas flow jetted outward in the radial direction through the annular ventilation member. A method for processing powder and granular materials.
(2)、流動層型の粉粒体の処理室と、この処理室内の
中央部に立設された回転軸と、この回転軸に相互に所定
の間隙を隔てて多層状に支持される複数枚の回転板と、
前記回転板を相互に垂直方向に離間させる環状通気部材
と、この環状通気部材よりも半径方向内側の部位におい
て前記回転板に形成された通気開口と、前記回転軸を回
転駆動する手段と、前記回転板の下方からガス流を供給
する手段とからなることを特徴とする粉粒体処理装置。
(2) A fluidized bed type processing chamber for powder and granular materials, a rotating shaft installed in the center of the processing chamber, and a plurality of layers supported by the rotating shaft in a multilayered manner with a predetermined gap between each other. a rotating plate,
an annular ventilation member for vertically separating the rotary plates from each other; a ventilation opening formed in the rotary plate at a portion radially inner than the annular ventilation member; and means for rotationally driving the rotary shaft; A powder and granular material processing apparatus comprising means for supplying a gas flow from below a rotary plate.
(3)、前記回転板および前記環状通気部材が相互に着
脱自在となるよう交互に配置されていることを特徴とす
る特許請求の範囲第2項記載の粉粒体処理装置。
(3) The granular material processing apparatus according to claim 2, wherein the rotary plate and the annular ventilation member are alternately arranged so that they can be attached to and detached from each other.
JP60208273A 1985-09-20 1985-09-20 Granule processing method and device Expired - Lifetime JPH0616827B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60208273A JPH0616827B2 (en) 1985-09-20 1985-09-20 Granule processing method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60208273A JPH0616827B2 (en) 1985-09-20 1985-09-20 Granule processing method and device

Publications (2)

Publication Number Publication Date
JPS6268536A true JPS6268536A (en) 1987-03-28
JPH0616827B2 JPH0616827B2 (en) 1994-03-09

Family

ID=16553506

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60208273A Expired - Lifetime JPH0616827B2 (en) 1985-09-20 1985-09-20 Granule processing method and device

Country Status (1)

Country Link
JP (1) JPH0616827B2 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5949838A (en) * 1982-09-16 1984-03-22 Fuji Paudaru Kk Method and device for granulation
JPS60183030A (en) * 1984-02-29 1985-09-18 Fuji Paudaru Kk Granulation and coating apparatus
JPS61164635A (en) * 1985-01-17 1986-07-25 Fuji Paudaru Kk Granulation and coating apparatus
JPS61213201A (en) * 1985-03-20 1986-09-22 Fuji Paudaru Kk Spherical granule of fine crystalline cellulose and production thereof
JPH06187A (en) * 1992-06-19 1994-01-11 Matsushita Electric Ind Co Ltd Ultrasonic doppler blood flow meter

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5949838A (en) * 1982-09-16 1984-03-22 Fuji Paudaru Kk Method and device for granulation
JPS60183030A (en) * 1984-02-29 1985-09-18 Fuji Paudaru Kk Granulation and coating apparatus
JPS61164635A (en) * 1985-01-17 1986-07-25 Fuji Paudaru Kk Granulation and coating apparatus
JPS61213201A (en) * 1985-03-20 1986-09-22 Fuji Paudaru Kk Spherical granule of fine crystalline cellulose and production thereof
JPH06187A (en) * 1992-06-19 1994-01-11 Matsushita Electric Ind Co Ltd Ultrasonic doppler blood flow meter

Also Published As

Publication number Publication date
JPH0616827B2 (en) 1994-03-09

Similar Documents

Publication Publication Date Title
US4532155A (en) Apparatus and process for coating, granulating and/or drying particles
JP4898002B2 (en) Apparatus for producing a pourable product and method for using this apparatus
US10132565B2 (en) Rotary dryer star and method for treating solid particles
US5718764A (en) Apparatus for coating solid particles
JP2763806B2 (en) Granulation coating method and apparatus
US6270801B1 (en) Apparatus and a method for treating particulate materials
JP2014517766A (en) Equipment for continuous processing of solids in fluidized bed equipment
JPH06500266A (en) Fluidized bed equipment for processing granular materials
RU2334180C1 (en) Vortical evaporation-drying chamber with inertial nozzle
JP2004122057A (en) Fluidized bed apparatus
JPS6268536A (en) Method and apparatus for treating particulate material
JPS63501058A (en) Equipment for treating substances in gas streams
RU2328673C1 (en) Plant for drying of solutions and suspensions in boiling layer of inertial bodies
RU2326303C1 (en) Spray dryer
JPH05245363A (en) Apparatus for allowing particle to be moved and treating the same
JPS6268535A (en) Method and apparatus for treating particulate material
JP3805453B2 (en) Powder processing apparatus and powder processing method using the same
JP3997390B2 (en) Powder processing equipment
RU2650252C1 (en) Vortex evaporation drying chamber
RU2332624C1 (en) Counter-swirl flow (csf) spray-drier with inert carrier
JP4048465B2 (en) Powder processing equipment
JPS62160137A (en) Method and apparatus for trating granular material
JPS5949838A (en) Method and device for granulation
JPS61230730A (en) Apparatus for treating particulate material
JPS63137744A (en) Continuous manufacture of granule from solid by fluidized substance bed