JPH0642744Y2 - Eddy current type pulverizer - Google Patents

Eddy current type pulverizer

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Publication number
JPH0642744Y2
JPH0642744Y2 JP6904788U JP6904788U JPH0642744Y2 JP H0642744 Y2 JPH0642744 Y2 JP H0642744Y2 JP 6904788 U JP6904788 U JP 6904788U JP 6904788 U JP6904788 U JP 6904788U JP H0642744 Y2 JPH0642744 Y2 JP H0642744Y2
Authority
JP
Japan
Prior art keywords
fine powder
rotating
crushed
cylindrical portion
discs
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
Application number
JP6904788U
Other languages
Japanese (ja)
Other versions
JPH01174046U (en
Inventor
忠彰 川合
Original Assignee
株式会社躍進機械製作所
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 株式会社躍進機械製作所 filed Critical 株式会社躍進機械製作所
Priority to JP6904788U priority Critical patent/JPH0642744Y2/en
Publication of JPH01174046U publication Critical patent/JPH01174046U/ja
Application granted granted Critical
Publication of JPH0642744Y2 publication Critical patent/JPH0642744Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
拌板の周回円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。
DETAILED DESCRIPTION OF THE INVENTION “Industrial field of application” The present invention is directed to a violent vortex between a stirring plate that rotates at high speed around a vertical axis and a liner that is provided close to the orbiting cylindrical surface of the stirring plate. The present invention relates to a vortex type fine pulverizer for producing fine powder such as cereals.

「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とが設
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。
“Prior Art” A conventional vortex type fine pulverizer has a body 1 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 vertically penetrate The orbiting cylindrical surface of the stirring plate 4 is provided with a liner 5 in which inner surfaces are provided with holes or the like, and an air tight plate 7 having a vent hole 6 in the center is provided above the inside of the body 1. The exhaust chamber 8 is provided on the upper surface of the air blocking plate 7, and the upper fan 9 is 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、
空気中の微粉体が空気流の方向を変換して壁面に激しく
衝突する個所、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などに短時間に大量に堆積し、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 place where the fine powder in the air changes the direction of the air flow and collides violently with the wall surface, for example, the inner surface a of the air closing plate 7 in FIG. 2 or the standing wall b of the exhaust chamber 8 that hits the upper fan 9 in the centrifugal direction. However, there are problems that a large amount is deposited in a short period of time, and depending on the material, it solidifies as it is, and then peels off and mixes into the fine powder, or it obstructs the flow of air flow 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、 内部に被破砕物を導入する導入空腔を備えた基台上に、
少なくとも下部に円筒部を有する胴体を立設し、該胴体
の中心部を貫通して回転自在に軸支される回転軸と、該
回転軸に上下方向に配列して固設された複数枚の回転円
板と、各回転円板の円先を貫通して上下に結合し、半径
方向に向って取付けられた複数枚の攪拌板と、これら攪
拌板の周回円筒面に近接して前記胴体の円筒部の内周
に、表面に破砕のめたの鑢目等が施されて成るライナー
とを設け、上下に配列して設けられた前記回転円板のう
ちの最下部に配設された回転円板の下面に、被粉砕物を
吸引する吸引ファンを設け、最上部に設けられた回転円
板の上方に、生成された微粉体が吹き上がって浮遊する
上部空腔部を設けるとともに、該上部空腔部から微粉体
を導く排出ダクトと、該排出ダクトに微粉体を排出する
排出ファンと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 base having an introduction cavity for introducing a crushed material inside,
A body having at least a cylindrical portion is erected at a lower portion, a rotating shaft rotatably supported by penetrating the center of the body, and a plurality of fixed members arranged vertically on the rotating shaft. Rotating discs, a plurality of stirring plates that are vertically connected to each other by penetrating through the circular tips of the rotating discs, and are attached in a radial direction. The inner circumference of the cylindrical portion is provided with a liner whose surface is crushed, and the like, and a rotary circle arranged at the bottom of the rotary discs arranged vertically. A suction fan for sucking the object to be crushed is provided on the lower surface of the plate, and an upper cavity portion in which the generated fine powder is blown up and floated is provided above the rotating disk provided at the uppermost portion, and the upper part is provided. An exhaust duct for guiding the fine powder from the cavity and an exhaust fan for discharging the fine powder are provided in the exhaust duct. It consists in vortex Shikibi pulverizer made.

「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、擦過作
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 the surface of which is provided with holes or the like, 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吸
引ファンや、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する。胴体の円筒部から吹き上
った微粉体を含む気流は一旦上部空腔部において流速が
小さくなった後、外部に設けられた排出ファンの吸引力
によって排出される。
Inside the body, an upward airflow is generated by the suction 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 rides on this upward airflow. To rise. The air flow containing the fine powder blown up from the cylindrical portion of the body is once discharged in the upper cavity portion and then discharged by the suction force of the discharge fan provided outside.

胴体内部には、微粉体が強く衝突して堆積する個所がな
く、短時間に大量の粉体堆積を生じることがない。ま
た、粉体を外部に取り出すための排出ファンを重厚な胴
体の外部に設けたから、排出ファンや排出ダクトを開放
することは容易であり、ダクト内などに多少堆積しても
容易に取り除くことが可能である。
Since there is no place where the fine powder collides strongly and is deposited inside the body, a large amount of powder deposition does not occur in a short time. Also, since the exhaust fan for taking out the powder to the outside is provided outside the heavy body, it is easy to open the exhaust fan and the exhaust duct, and even if a little accumulated in the duct, it can be easily removed. It is possible.

「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、銅長の円筒部11aを有し、上部に
は前記円筒部11aよりも大径で大きな内容積を有する上
部空腔部11bから成る胴体11の内部に、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
面に近接して設けられ、被粉砕物が擦過して微粉化する
ライナー14とが備えられている。
The vortex type fine pulverizer 10 has a copper-shaped cylindrical portion 11a, and an upper hollow portion 11b having a larger inner diameter and a larger internal volume than the cylindrical portion 11a at the upper portion thereof, and a rotating shaft 12 inside the body 11. Further, a stirring plate 13 that rotates at a high speed and a liner 14 that is provided in the vicinity of the orbiting cylindrical surface of the stirring plate 13 and that crushes the object to be crushed into fine powder are provided.

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 the partition plate 24 of the introduction cavity 23, and the upper part thereof penetrates the ceiling plate 25 of the body 11 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吸引フ
ァン30が設けられている。
On the lower surface of the lowermost disk 29a of the rotary disk 29, a suction fan 30 for sucking up the material to be crushed from the introduction cavity 23 of the base 17 is 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、図示のように胴体11の円筒部11aの上端部相当位置
に設けられており、対するライナー14も円筒部11aの内
周面に沿って設けられている。
On the other hand, the rotating disc 29 located at the top of the rotating discs 29
As shown in the figure, b is provided at a position corresponding to the upper end of the cylindrical portion 11a of the body 11, and the corresponding liner 14 is also provided along the inner peripheral surface of the cylindrical portion 11a.

前記最上部の回転円板29bの上方は大きな内容積を有す
る上部空腔部11bと成っており、該部には粉体を外部に
排出する排出ダクト31と排出ファン32が設けられてい
る。
Above the uppermost rotary disc 29b is an upper cavity 11b having a large internal volume, and an exhaust duct 31 and an exhaust fan 32 for exhausting the powder to the outside are provided in the upper cavity 11b.

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、吸引ファン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る。
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 inside the body 11 is strongly directed outward, and the suction fan 30 is installed in the center hole 16 of the bottom plate 15.
Since air is sucked from the air, it merges with these air to generate a violent updraft.

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、吸引ファン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
全な微粉体となる。
The object to be crushed that has entered the body 11 is repelled by the suction fan 30 and collides with the liner 14, is repelled by the stirring plate 13 and is hit back to the liner 14 again, and is lifted and rotated in the circumferential direction and centrifugally. While repeating complex and intense exercises such as centripetal, the surface of the liner 14 is rubbed. Since the surface of the liner 14 is engraved with dies or the like, it is crushed into pieces during repeated vigorous rubbing and striking motions, and finally becomes a fine powder.

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の円筒部11a内において生成された微粉体は、円
筒部11aをはなれたところで大きな内容積を有する上部
空腔部11b内に導入され、ここで流速は急に遅くなって
相対的にゆっくりと排出ダクト31に導かれていく。この
ため微粉体は側壁などに強く衝突することがなく、短時
間に大量の堆積をみるようなことがない。
The fine powder generated in the cylindrical portion 11a of the body 11 is introduced into the upper cavity portion 11b having a large internal volume at a position apart from the cylindrical portion 11a, where the flow velocity suddenly slows and becomes relatively slow. And it is led to the discharge duct 31. Therefore, the fine powder does not collide strongly with the side wall and the like, and a large amount of deposition is not observed in a short time.

また、このような渦流式微粉砕機10は、極めて激しい粉
砕加工作用を行なわせるために、胴体11などは相当に重
厚に構成されているので、内部の開放は容易ではない
が、排出ファン32は胴体11外に設けられているから、開
放は容易であり、内部に多少の微粉体の堆積があったと
しても頻繁に開放して堆積物を取り除くことは極めて容
易である。
Further, in such a vortex type fine pulverizer 10, since the body 11 and the like are configured to be considerably heavy in order to perform an extremely vigorous pulverization processing action, it is not easy to open the inside, but the discharge fan 32 is Since it is provided outside the body 11, it can be opened easily, and even if some fine powder is deposited inside, it is very easy to open it frequently and remove the deposit.

「考案の効果」 本考案に係る渦流式微粉砕機によれば、円筒部と該円筒
部の上部に容積の大きな上部空腔部とを有する胴体を設
け、前記円筒部の内周に擦過・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を設けて成っ
ているから、円筒部の領域で微粉化された粉体は前記上
部空腔部で流速が小さくなり、激しく壁面に衝突するこ
とがなく、胴体外に設けられた排出ファンによって緩や
かに排出されていき、胴体内には生成した微粉体が堆積
しない。
[Advantage of Invention] According to the vortex type fine pulverizer according to the present invention, a body having a cylindrical portion and an upper cavity portion having a large volume is provided on the upper portion of the cylindrical portion, and the inner periphery of the cylindrical portion is rubbed and crushed. Since the liner for use is made to pass through and a stirring plate that circulates in close proximity to the liner is provided, the powder finely divided in the region of the cylindrical portion has a low flow velocity in the upper cavity portion, and becomes violent. It does not collide with the wall surface and is gently discharged by the discharge fan provided outside the body, and the fine powder generated does not accumulate in the body.

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

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 11a…円筒部、11b…上部空腔部 12…回転軸、13…攪拌板 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…吸引ファン、31…排出ダクト 32…排出ファン
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 11a ... Cylindrical part, 11b ... Upper cavity part 12 ... Rotating shaft, 13 ... Stirring plate 14 ... Liner, 17 ... Base part 18 ... Hopper, 20 ... Air intake 21 ... Conduction path, 22 ... Damper 23 ... Introductory cavity, 25 ... Ceiling plate 26, 27 ... Bearing, 29 ... Rotating disc 29b ... Top rotating disc 30 ... Suction fan, 31 ... Exhaust duct 32 ... Exhaust fan

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】内部に被破砕物を導入する導入空腔を備え
た基台上に、少なくとも下部に円筒部を有する胴体を立
設し、該胴体の中心部を貫通して回転自在に軸支される
回転軸と、該回転軸に上下方向に配列して固設された複
数枚の回転円板と、各回転円板の円先を貫通して上下に
結合し、半径方向に向って取付けられた複数枚の攪拌板
と、これら攪拌板の周回円筒面に近接して前記胴体の円
筒部の内周に、表面に破砕のための鑢目等が施されて成
るライナーとを設け、上下に配列して設けられた前記回
転円板のうちの最下部に配設された回転円板の下面に、
被粉砕物を吸引する吸引ファンを設け、最上部に設けら
れた回転円板の上方に、生成された微粉体が吹き上がっ
て浮遊する上部空腔部を設けるとともに、該上部空腔部
から微粉体を導く排出ダクトと、該排出ダクトに微粉体
を排出する排出ファンとを設けて成る渦流式微粉砕機。
1. A body having at least a lower portion having a cylindrical portion is erected on a base having an introduction cavity for introducing a material to be crushed therein, and a shaft is rotatably passed through a central portion of the body. The rotating shaft to be supported, a plurality of rotating discs fixedly arranged in the vertical direction on the rotating shaft, and fixed to the rotating disc by penetrating through the circular tips of the rotating discs and connecting in the vertical direction. Providing a plurality of attached stirring plates and a liner formed on the inner circumference of the cylindrical portion of the body close to the orbiting cylindrical surfaces of these stirring plates, the surface of which is provided with dies for crushing, etc. On the lower surface of the rotary disc disposed at the bottom of the rotary discs arranged in an array,
A suction fan for sucking the object to be crushed is provided, and an upper cavity portion in which the generated fine powder is blown up and floats is provided above the rotating disc provided at the uppermost portion, and the fine powder from the upper cavity portion is provided. An eddy current type fine pulverizer comprising an exhaust duct for guiding a body and an exhaust fan for exhausting fine powder to the exhaust duct.
JP6904788U 1988-05-25 1988-05-25 Eddy current type pulverizer Expired - Lifetime JPH0642744Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6904788U JPH0642744Y2 (en) 1988-05-25 1988-05-25 Eddy current type pulverizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6904788U JPH0642744Y2 (en) 1988-05-25 1988-05-25 Eddy current type pulverizer

Publications (2)

Publication Number Publication Date
JPH01174046U JPH01174046U (en) 1989-12-11
JPH0642744Y2 true JPH0642744Y2 (en) 1994-11-09

Family

ID=31294340

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6904788U Expired - Lifetime JPH0642744Y2 (en) 1988-05-25 1988-05-25 Eddy current type pulverizer

Country Status (1)

Country Link
JP (1) JPH0642744Y2 (en)

Also Published As

Publication number Publication date
JPH01174046U (en) 1989-12-11

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