JPH0642743Y2 - Eddy current type pulverizer - Google Patents
Eddy current type pulverizerInfo
- Publication number
- JPH0642743Y2 JPH0642743Y2 JP6904688U JP6904688U JPH0642743Y2 JP H0642743 Y2 JPH0642743 Y2 JP H0642743Y2 JP 6904688 U JP6904688 U JP 6904688U JP 6904688 U JP6904688 U JP 6904688U JP H0642743 Y2 JPH0642743 Y2 JP H0642743Y2
- Authority
- JP
- Japan
- Prior art keywords
- plate
- stirring plate
- base
- liner
- crushed
- 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
Links
Landscapes
- Crushing And Grinding (AREA)
Description
【考案の詳細な説明】 「産業上の利用分野」 本考案は、鉛直軸まわりに高速回転する攪拌板と、該攪
拌板の周回筒面に近接して設けられたライナーとの間に
激しい渦流を生じさせて穀類等の微粉体を得るための渦
流式微粉砕機に関する 「従来の技術」 従来の渦流式微粉砕機は、第2図に示すように、胴体1
の中心部に、多数の回転円板3を上下方向に配列した回
転軸2と、回転円板3の円先に上下方向に貫通して設け
られた複数枚の攪拌板4とを有し、該攪拌板4の周回円
筒面には内表面に鑢目などを刻設したライナー5が設け
られ、胴体1の内部上方には中心部に通気穴6が穿設さ
れた空気締まり板7が設けられ、該空気締まり板7の上
面には排気室8が設けられ、上部ファン9が配設されて
いた。DETAILED DESCRIPTION OF THE INVENTION "Industrial field of application" The present invention is directed to a strong vortex between a stirring plate that rotates at a high speed around a vertical axis and a liner that is provided close to the circumferential cylindrical surface of the stirring plate. "Prior Art" Concerning Eddy Current Type Fine Crusher for Generating Fine Particles of Cereals and the Like by Using a Conventional Vortex Flow Fine Crusher as shown in FIG.
In the central part of the, a rotary shaft 2 in which a large number of rotating discs 3 are arranged in the vertical direction, and a plurality of stirring plates 4 provided in the circular tip of the rotating disc 3 so as to penetrate in the vertical direction, A liner 5 having a groove or the like formed on the inner surface is provided on the orbiting cylindrical surface of the stirring plate 4, and an air tight plate 7 having a vent hole 6 at the center is provided above the inside of the body 1. An exhaust chamber 8 was provided on the upper surface of the air blocking plate 7, and an upper fan 9 was provided.
「考案が解決しようとする課題」 しかしながら、このような従来の渦流式微粉砕機では、
空気中の微粉が空気流の方向変換個所、例えば第2図に
おける空気締まり板7の内面aや、上部ファン9の遠心
方向に当る排気室8の立壁bなどに大量に堆積し、材料
によってはそのまま固化し、やがて剥離して微粉中に混
合したり、気流の流通を阻害して機械の能率を低下させ
るなどの問題点があった。"Problems to be solved by the invention" However, in such a conventional vortex type fine pulverizer,
A large amount of fine particles in the air are accumulated on the direction change point of the air flow, for example, on the inner surface a of the air blocking plate 7 in FIG. There are problems that it solidifies as it is, then peels off and mixes into the fine powder, and that the flow of the air flow is obstructed to reduce the efficiency of the machine.
本考案は、このような従来の技術における問題点に着目
してなされたもので、胴体内部において微粉体の堆積す
る個所がなく、固化粉体が微粉体中に混合して排出され
たり、空気流を阻んで能率を低下させることのないよう
な渦流式微粉砕機を提供することを目的としている。The present invention has been made by paying attention to such problems in the conventional technology.There is no place where fine powder is deposited inside the body, and solidified powder is mixed with the fine powder and discharged, or It is an object of the present invention to provide a vortex type fine pulverizer which does not impede the flow and reduce the efficiency.
「課題を解決するための手段」 かかる目的を達成するための本考案の要旨とするところ
は、 上部を扁平な天井板にて覆われた円筒形の胴体と、該胴
体を基部において支持し、内部に被粉砕物を導入して前
記胴体内部に送る導入空腔を有する基台部を備え、前記
胴体の中心部を貫通して回転自在に軸支された回転軸
と、該回転軸上に上下胴体内部の前記天井板の下面近く
から、前記基台部の直上に至るまで、複数枚の回転板を
上下に並べて配列し、各回転円板の円先を貫通して半径
方向に向けて攪拌板を取付け、該攪拌板の渦流作用によ
って放射される被粉砕物を微粉化する鑢目等を刻設した
ライナーを、前記胴体内周の前記攪拌板に対応する上下
方向一杯に周設するとともに、胴体上部に、生成した微
粉体を排出する排出口を設けて成る渦流式微粉砕機に存
する。"Means for Solving the Problem" The gist of the present invention for achieving such an object is to provide a cylindrical body having an upper portion covered with a flat ceiling plate, and supporting the body at a base, A rotating shaft rotatably rotatably pierced through the center of the body, the base having an introduction cavity for introducing the object to be crushed into the body and feeding the crushed body to the inside of the body; From the lower surface of the ceiling plate inside the upper and lower bodies to right above the base part, a plurality of rotating plates are arranged side by side vertically, passing through the tip of each rotating disk in the radial direction. A stirrer plate is attached, and a liner engraved with dies or the like for finely pulverizing the material to be radiated by the swirling action of the stirrer plate is provided around the body in the vertical direction so as to correspond to the stirrer plate. , A vortex consisting of a discharge port on the upper part of the body for discharging the generated fine powder Resides in Shikibi grinder.
「作用」 基台部から胴体内部に送り込まれた被粉砕物は、高速に
回転する攪拌板によって外方に強烈に弾き出される。そ
して攪拌板の周回円筒面に構成され、面上に鑢目などが
刻設されたライナーの内面に強く打ち付けられ、摺擦作
用を繰り返しながら微粉化していく。"Action" The object to be crushed sent from the base to the inside of the body is strongly ejected outward by the stirring plate rotating at high speed. Then, it is strongly struck against the inner surface of the liner having a circular cylindrical surface of the stirring plate and having a groove or the like formed on the surface, and is pulverized while repeating the rubbing action.
胴体内部には、最下部の回転円板の下面に設けられたフ
ァンや、攪拌板の高速回転によって生じるファン作用に
よって上昇気流が発生しており、生成した粉体はこの上
昇気流に乗って上昇し、上部の排出口から外部に放出さ
れる。Inside the body, an upward air flow is generated by the fan provided on the lower surface of the lowermost rotating disk and the fan action generated by the high speed rotation of the stirring plate, and the generated powder rises on this upward air flow. Then, it is discharged to the outside through the discharge port at the top.
胴体内部には気流の淀む部分がなく、円筒形のライナー
は胴体の上方一杯に延設されており、ライナー内周面に
近接して高速周回する攪拌板も天井板に近接して設けら
れているから、粉体が堆積する個所がなく、したがって
固化した粉体が剥離脱落することもなく、また気流を阻
害して機械の処理能力を低下させることもない。There is no air flow stagnant inside the body, the cylindrical liner extends all the way up the body, and a stirring plate that rotates at high speed close to the inner surface of the liner is also provided close to the ceiling plate. Therefore, there is no place where the powder is deposited, and therefore the solidified powder is not peeled off, and the air flow is not obstructed to reduce the processing capacity of the machine.
「実施例」 以下、図面に基づき本考案の一実施例を説明する。[Embodiment] An embodiment of the present invention will be described below with reference to the drawings.
第1図は本考案の一実施例を示している。FIG. 1 shows an embodiment of the present invention.
渦流式微粉砕機10は、円筒形の胴体11内に、回転軸12と
ともに高速に回転する攪拌板13と、この攪拌板13の周回
円筒面に設けられ、被粉砕物が摺擦して微粉化するライ
ナー14とが備えられている。The vortex type fine pulverizer 10 is provided in a cylindrical body 11 with a stirring plate 13 that rotates at a high speed together with a rotating shaft 12 and an orbiting cylindrical surface of the stirring plate 13. And a liner 14 that
胴体11の底部は底板15となっており、中心部には被粉砕
物を受け入れる中心孔16が開口している。The bottom of the body 11 is a bottom plate 15, and a center hole 16 for receiving the object to be crushed is opened in the center.
胴体11の基部は基台部17に接続されており、基台部17
は、脇方向に延びて、該部に被粉砕物を投入するホッパ
18と、エアフィルタ19を備えた空気取り入れ口20が設け
られている。そしてこの空気取り入れ口20に続いては空
気とともに被粉砕物を導く導通路21が設けられており、
導通路21の途中には取り入れ空気量を調節するダンパ22
が設けられている。さらに基台部17の内部には、前記導
通路21に連通して被粉砕物を受け、胴体11の前記中心孔
16から胴体内部に送入する導入空腔23が構成されてい
る。The base of the body 11 is connected to the base 17 and the base 17
Is a hopper that extends to the side and puts the material to be crushed into the part.
An air intake 20 provided with 18 and an air filter 19 is provided. Then, following this air intake port 20, a conduction path 21 for guiding the object to be ground together with air is provided,
A damper 22 for adjusting the intake air amount is provided in the middle of the conduction path 21.
Is provided. Further, inside the base portion 17, the central hole of the body 11 is communicated with the conduction path 21 to receive the object to be crushed.
An introduction cavity 23 that is fed from 16 into the body is formed.
回転軸12は、前記導入空腔23の仕切板24を貫通し、上方
は胴体11の扁平な天井板25を貫通して軸受26および27に
枢支されている。そして一端は駆動モータ28に結合され
ている。The rotary shaft 12 penetrates a partition plate 24 of the introduction cavity 23, and penetrates a flat ceiling plate 25 of the body 11 at the upper side, and is pivotally supported by bearings 26 and 27. One end is connected to the drive motor 28.
回転軸12には一定間隔をおいて多数枚の回転円板29が固
設されており、前記攪拌板13はこれら回転円板29の円先
を貫通して鉛直に複数枚嵌めこまれており、板の方向は
回転円板29の半径方向を向いている。A large number of rotating discs 29 are fixedly installed on the rotating shaft 12 at regular intervals, and the stirring plate 13 is vertically inserted into the rotating discs 29 by penetrating the circular tips of the rotating discs 29. The direction of the plate is the radial direction of the rotating disc 29.
回転円板29の最下部の円板29aの下面には基台部17の前
記導入空腔23内から被粉砕物を吸い上げるためのファン
30が設けられている。A fan for sucking up the object to be crushed from the inside of the introduction cavity 23 of the base 17 on the lower surface of the lowermost disk 29a of the rotating disk 29.
30 are provided.
一方、回転円板29のうちの最上部に位置する回転円板29
bは、図示のように扁平に成された天井板25の下面に近
接して設けられており、攪拌板13の上端部も天井板25の
下面を掃くように胴体11の長さ一杯に延びて設けられて
おり、対するライナー14も胴体11の天井板25の下面に密
接する位置まで一杯に設けられている。そして胴体11の
側壁最上部には粉体を外部に排出する排出口31が設けら
れている。On the other hand, the rotating disc 29 located at the top of the rotating discs 29
b is provided close to the lower surface of the flat ceiling plate 25 as shown in the drawing, and the upper end portion of the stirring plate 13 also extends the full length of the body 11 so as to sweep the lower surface of the ceiling plate 25. The corresponding liner 14 is also provided up to a position in close contact with the lower surface of the ceiling plate 25 of the body 11. A discharge port 31 for discharging the powder to the outside is provided at the uppermost portion of the side wall of the body 11.
次に作用を説明する。Next, the operation will be described.
駆動モータ28を始動して回転軸12を駆動する。本実施例
では約5000RPMの回転数で駆動すると、攪拌板13の外縁
周速は約120メートル毎秒にも達する高速となる。攪拌
板13は円周方向に向けられているから胴体11内の空気は
強く外方に向けられ、ファン30は底板15の中心孔16から
空気を吸入するから、これらの空気と合流して激しい上
昇気流を発生させ、排出口31から吹き出す。The drive motor 28 is started to drive the rotary shaft 12. In this embodiment, when driven at a rotation speed of about 5000 RPM, the outer peripheral speed of the stirring plate 13 becomes a high speed of about 120 meters per second. Since the stirring plate 13 is oriented in the circumferential direction, the air in the body 11 is strongly oriented outward, and the fan 30 sucks air from the center hole 16 of the bottom plate 15, so that it merges with these air and is violent. An updraft is generated and blown out from the outlet 31.
上記上昇気流は空気取り入れ口20から大量の空気を取り
入れ、基台部17の導通路21を高速気流となって導入空腔
23内に進入する。そこでホッパ18から大豆などの被粉砕
物を投入すると、これら被粉砕物は前記気流とともに導
入空腔23内に導入され、中心孔16を通って胴体11内に進
入する。The ascending airflow takes in a large amount of air from the air intake port 20, and the conduction path 21 of the base 17 becomes a high-speed airflow and is an introduction cavity.
Enter within 23. Then, when crushed substances such as soybeans are fed from the hopper 18, these crushed substances are introduced into the introduction cavity 23 together with the airflow, and enter the body 11 through the center hole 16.
胴体11内に入った被粉砕物は、ファン30に弾かれてライ
ナー14に衝突し、攪拌板13の方に弾きかえされ、再びラ
イナー14に打ち返され、上昇と円周方向や、遠心と求心
などの複雑でしかも激しい運動を繰り返しながらライナ
ー14面上を擦過していく。ライナー14の表面には鑢目な
どが刻設されているから、このような激しい擦過と打撃
運動を繰り返すうちに粉々に粉砕されてついには完全な
微粉体となり、排出口31から図示省略した捕集部に送出
される。The object to be crushed that has entered the body 11 is repelled by the fan 30 and collides with the liner 14, is repelled by the stirring plate 13 and is hit back by the liner 14 again, rising and in the circumferential direction, centrifuging and centripetal. Rubbing on the surface of the liner 14 while repeating complicated and intense exercises such as. Since the surface of the liner 14 is engraved on the surface of the liner, it is crushed into fine particles during repeated vigorous rubbing and striking motions, and finally becomes a fine powder. Sent to the department.
上記の作用中に吸入空気量が多すぎて生成粉体が粗くな
ったような場合には、導通路21に設けられたダンパ22を
加減して気流をやわらげる。When the amount of intake air is too large and the generated powder becomes coarse during the above operation, the damper 22 provided in the conduction path 21 is adjusted to soften the air flow.
胴体11の内部には、ライナー14が天井板25に密接するま
で一杯に施されており、攪拌板13も天井板25に極く近接
していっぱいに設けられているから、粉体が堆積する個
所がなく、したがって粉体が固化することもなく、固化
した粉体が微分体に混入して排出することもない。Inside the body 11, the liner 14 is fully filled until it comes into close contact with the ceiling plate 25, and the stirring plate 13 is also provided in close proximity to the ceiling plate 25 so that the powder is deposited. There are no points, therefore, the powder does not solidify, and the solidified powder is not mixed with the differential body and discharged.
「考案の効果」 本考案に係る渦流式微粉砕機によれば、円筒状になされ
た胴体内に、扁平な天井板に密接するまで擦過・粉砕用
のライナーを繞らせ、該ライナーに近接して周回する攪
拌板も上端部を前記天井板に近接して設けたから、胴体
内には生成した微粉体が堆積する所がなく、したがって
粉体が固化したり、剥落した固化粉体が微粉体に混入し
て排出されることもなく、気流を妨げて加工能率を低下
させることもない。[Advantage of device] According to the vortex type fine crusher according to the present invention, a liner for rubbing and crushing is put in a cylindrical body until it comes into close contact with a flat ceiling plate, and the liner is placed close to the liner. Since the stirring plate that revolves around is also provided with the upper end portion close to the ceiling plate, there is no place for the generated fine powder in the body, and therefore the powder solidifies or the solidified powder that has fallen off is a fine powder. It is not mixed with and discharged to the air and does not interfere with the air flow to reduce the processing efficiency.
第1図は本考案の一実施例を示す渦流式微粉砕機の縦断
面図、第2図は従来の渦流式微粉砕機の縦断面図であ
る。 10…渦流式微粉砕機 11…胴体、12…回転軸 13…攪拌板、13a…攪拌板の上端部 14…ライナー、17…基台部 18…ホッパ、20…空気取り入れ口 21…導通路、22…ダンパ 23…導入空腔、25…天井板 26,27…軸受、29…回転円板 29b…最上部の回転円板 30…ファン、31…排出口FIG. 1 is a vertical sectional view of an eddy current type fine pulverizer showing an embodiment of the present invention, and FIG. 2 is a vertical sectional view of a conventional eddy current type fine pulverizer. 10 ... Eddy current type pulverizer 11 ... Body, 12 ... Rotating shaft 13 ... Stirring plate, 13a ... Stirring plate upper end 14 ... Liner, 17 ... Base part 18 ... Hopper, 20 ... Air intake 21 ... Conducting path, 22 … Damper 23… Introductory cavity, 25… Ceiling plate 26, 27… Bearings, 29… Rotating disc 29b… Top rotating disc 30… Fan, 31… Discharge port
Claims (1)
胴体と、該胴体を基部において支持し、内部に被粉砕物
を導入して前記胴体内部に送る導入空腔を有する基台部
を備え、前記胴体の中心部を貫通して回転自在に軸支さ
れた回転軸と、該回転軸上に上記胴体内部の前記天井板
の下面近くから、前記基台部の直上に至るまで、複数枚
の回転板を上下に並べて配列し、各回転円板の円先を貫
通して半径方向に向けた攪拌板を取付け、該攪拌板の渦
流作用によって放射される被粉砕物を微粉化する鑢目等
を刻設したライナーを、前記胴体内周の前記攪拌板に対
応する上下方向一杯に周設するとともに、胴体上部に、
生成した微粉体を排出する排出口を設けて成る渦流式微
粉砕機。1. A base having a cylindrical body whose upper part is covered with a flat ceiling plate, and an introduction cavity which supports the body at a base and introduces a substance to be crushed into the interior of the body. A rotation shaft that includes a base portion and is rotatably supported by penetrating the center portion of the body, and extends from near the lower surface of the ceiling plate inside the body on the rotation shaft to directly above the base portion. Up to a plurality of rotating plates are arranged side by side up and down, and a stirring plate that passes through the circular tip of each rotating disk and is oriented in the radial direction is attached, and the crushed object radiated by the vortex action of the stirring plate is finely divided. A liner engraved with dents and the like is formed so as to fully surround in the up-down direction corresponding to the stirring plate on the inner circumference of the body, and on the upper part of the body,
A vortex type fine pulverizer provided with an outlet for discharging the generated fine powder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6904688U JPH0642743Y2 (en) | 1988-05-25 | 1988-05-25 | Eddy current type pulverizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6904688U JPH0642743Y2 (en) | 1988-05-25 | 1988-05-25 | Eddy current type pulverizer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01174045U JPH01174045U (en) | 1989-12-11 |
JPH0642743Y2 true JPH0642743Y2 (en) | 1994-11-09 |
Family
ID=31294339
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6904688U Expired - Lifetime JPH0642743Y2 (en) | 1988-05-25 | 1988-05-25 | Eddy current type pulverizer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0642743Y2 (en) |
-
1988
- 1988-05-25 JP JP6904688U patent/JPH0642743Y2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH01174045U (en) | 1989-12-11 |
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