JPH0338903B2 - - Google Patents

Info

Publication number
JPH0338903B2
JPH0338903B2 JP21974785A JP21974785A JPH0338903B2 JP H0338903 B2 JPH0338903 B2 JP H0338903B2 JP 21974785 A JP21974785 A JP 21974785A JP 21974785 A JP21974785 A JP 21974785A JP H0338903 B2 JPH0338903 B2 JP H0338903B2
Authority
JP
Japan
Prior art keywords
grinding
screw shaft
processing cylinder
particles
processing
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
Application number
JP21974785A
Other languages
Japanese (ja)
Other versions
JPS6279855A (en
Inventor
Iwao Ikebuchi
Kazuo Fuse
Akira Karise
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP21974785A priority Critical patent/JPS6279855A/en
Publication of JPS6279855A publication Critical patent/JPS6279855A/en
Publication of JPH0338903B2 publication Critical patent/JPH0338903B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は摩砕粉砕装置に関する。[Detailed description of the invention] [Industrial application field] This invention relates to a grinding device.

〔従来の技術〕[Conventional technology]

この種の摩砕粉砕装置は、特公昭39−5584号公
報に記載され、第4図、第5図に示すように、竪
型処理筒1内に、上下方向のスクリユー軸2を設
けるとともに鋼球等の粉砕媒体bを充填し、スク
リユー軸2を回した状態で処理筒1内に被処理物
aを投入し、この被処理物aを、その相互間及び
前記粉砕媒体bとの摩砕により微細な生産粒子c
とし、処理筒1内を通過する空気又は水等の流体
にその生産粒子cをのせて処理筒1外に導出する
ものである。
This type of grinding and grinding device is described in Japanese Patent Publication No. 39-5584, and as shown in FIGS. 4 and 5, a vertical screw shaft 2 is provided in a vertical processing tube 1, and a steel Filled with a grinding medium b such as a ball, the workpiece a is put into the processing cylinder 1 with the screw shaft 2 turned, and the workpiece a is ground between each other and with the grinding medium b. finer production particles c
The produced particles c are placed on a fluid such as air or water passing through the processing cylinder 1 and led out of the processing cylinder 1.

ところで、従来の摩砕粉砕装置においては、前
記流体を処理筒1の底部側壁から導入し、流れに
のつて上昇する生産粒子cを筒頂付近から排出さ
せている。このように、圧送流体が側壁から導入
されると、生産粒子cの分布が処理筒1の中心か
ら一側に片寄つて蓄積されるため、速やかに導出
されず、生産能率が比較的低く、機体の大きさの
割に生産能力が小さい欠点がある。
By the way, in the conventional grinding and pulverizing apparatus, the fluid is introduced from the bottom side wall of the processing cylinder 1, and the product particles c rising with the flow are discharged from the vicinity of the top of the cylinder. In this way, when the pumped fluid is introduced from the side wall, the distribution of production particles c is biased toward one side from the center of the processing tube 1 and accumulated, so they are not drawn out quickly, resulting in relatively low production efficiency and The disadvantage is that the production capacity is small compared to its size.

そこで、第4図のごとく、スクリユー軸2を中
空軸としてその上端から流体を圧送して処理筒1
内下部中央から放射状向きに流れを生じさせ、処
理筒1上部から生産粒子cを導出したり、第5図
のごとく、中空のスクリユー軸2の上端から吸引
して処理筒1に下部中央に向かう流れを生じさ
せ、その流体とともに生産粒子cを導出して、生
産粒子cの片寄りをなくした考案がなされてい
る。
Therefore, as shown in FIG.
A flow is generated in a radial direction from the center of the inner lower part, and the produced particles c are drawn out from the upper part of the processing cylinder 1, or as shown in Fig. 5, they are sucked from the upper end of the hollow screw shaft 2 and directed toward the lower center of the processing cylinder 1 A device has been devised in which a flow is generated and the produced particles c are drawn out together with the fluid, thereby eliminating the deviation of the produced particles c.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、第4図のものは、処理筒1が外
気に対し正圧となるため、被処理物a及び生産粒
子cが筒外に漏れ易く、シール性を高めないと作
業環境が悪くなる問題がある。
However, in the case of the one shown in Fig. 4, since the processing cylinder 1 is under positive pressure with respect to the outside air, the processed material a and the produced particles c tend to leak out of the cylinder, and there is a problem that the working environment will deteriorate unless the sealing performance is improved. be.

また、第5図のものにおいては、粉砕されてい
ない重い粒子が処理筒1の下部に沈降するため、
それを吸い込む危惧があり、導出される生産粒子
cの粒度に問題が多いうえに、大きな粒子を吸い
込めない場合にはそれらが滞留することとなり、
スクリユー軸2の下端吸引部分が閉塞されて生産
粒子cの導出が円滑になされない問題がある。
In addition, in the case of FIG. 5, unpulverized heavy particles settle at the bottom of the processing tube 1, so
There is a risk of inhaling it, and there are many problems with the particle size of the produced particles c that are extracted, and if large particles cannot be inhaled, they will remain.
There is a problem in that the lower end suction portion of the screw shaft 2 is blocked and the produced particles c cannot be drawn out smoothly.

〔発明の目的〕[Purpose of the invention]

この発明は上記第4図、第5図の摩砕粉砕装置
の問題点を解決することを目的とする。
The object of the present invention is to solve the problems of the grinding apparatus shown in FIGS. 4 and 5.

〔目的を達成するための手段〕[Means to achieve the purpose]

上記目的を達成するため、この発明にあつて
は、スクリユー軸を中空とした摩砕粉砕装置にお
いて、スクリユー軸の上端を流体吸込口とすると
ともに下端を処理筒下部に開口し、処理筒上部に
吸気フアン又は吸引ポンプなどの吸込機を接続し
たのである。
In order to achieve the above object, in the present invention, in a grinding and pulverizing apparatus having a hollow screw shaft, the upper end of the screw shaft is used as a fluid suction port, the lower end is opened at the lower part of the processing cylinder, and the upper end of the screw shaft is opened at the lower part of the processing cylinder. A suction device such as an intake fan or a suction pump was connected.

〔作用〕[Effect]

この様に構成される装置は、スクリユー軸を回
した状態で処理筒内に被処理物を投入し、この被
処理物を、その相互間及び粉砕媒体との摩砕によ
り微細な生産粒子とし、処理筒上部から吸引する
ことにより、スクリユー軸を通つて処理筒内に流
体が流入し、スクリユー軸下部から放射状上向き
の流れが生じ、この流れにのつて前記生産粒子が
上昇して筒外に導出される。
The apparatus configured in this manner charges the material to be processed into the processing cylinder while rotating the screw shaft, and grinds the material between each other and with a grinding medium to form fine production particles. By suctioning from the top of the processing cylinder, fluid flows into the processing cylinder through the screw shaft, and a radial upward flow is generated from the bottom of the screw shaft, and the produced particles rise along with this flow and are led out of the cylinder. be done.

〔実施例〕〔Example〕

以下、この発明の実施例を添付図面に基づいて
説明する。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

第1図に示すように、上下面を閉塞した竪型の
円筒状処理筒10の中心軸上にスクリユー軸11
が設けられ、この軸11は、処理筒10上面を貫
通してスラスト軸受等の支持手段により懸垂支持
されており、図示しないモータにより回転する。
スクリユー軸11は、中空軸となつてその上端が
機外に連通されているとともに下端が処理筒10
の下部に開口し、処理筒10内が負圧となること
により、この軸11を通して処理筒10下部に空
気が流入する。
As shown in FIG.
The shaft 11 passes through the upper surface of the processing cylinder 10 and is suspended and supported by support means such as a thrust bearing, and is rotated by a motor (not shown).
The screw shaft 11 is a hollow shaft whose upper end is communicated with the outside of the machine, and whose lower end is connected to the processing cylinder 11.
is opened at the lower part of the processing cylinder 10, and by creating a negative pressure inside the processing cylinder 10, air flows into the lower part of the processing cylinder 10 through this shaft 11.

処理筒10の上部には、粉砕媒体bの投入口1
2及び被処理物投入口13が形成され、前者の投
入口12からセラミツク、石、鋼球等の粉砕媒体
bが図示Lレベルまで充填され、後者の投入口1
3からスクリユーコンベア等により気密を保つて
被処理物aが送り込まれ、前記スクリユー軸11
の回転により、粉砕媒体b及び被処理物aが図示
矢印のごとく移動撹拌されて、被処理物aがその
相互間及び粉砕媒体bとの摩砕により微細な生産
粒子cに粉砕される。
At the top of the processing cylinder 10, there is an input port 1 for the grinding medium b.
2 and a material input port 13 are formed, and the former input port 12 is filled with grinding media b such as ceramics, stones, steel balls, etc. up to the L level shown in the figure, and the latter input port 1 is filled with grinding media b such as ceramics, stones, steel balls, etc.
3, the workpiece a is sent in an airtight manner by a screw conveyor or the like, and the workpiece a is sent to the screw shaft 11
As a result of the rotation, the grinding medium b and the workpiece a are moved and stirred as shown by the arrows in the figure, and the workpiece a is ground into fine product particles c by grinding between them and with the grinding medium b.

スクリユー軸11の処理筒10内上部には、逆
円錐状の分級部材14が設けられ、第2図に示す
ように、この部材14の外面に対向する処理筒1
0内面に羽根15がスクリユー軸11の回転方向
にわん曲して等間隔に設けられており、部材14
と羽根15の間を気流が通過する際、羽根15に
より旋回流となつて分級が行なわれる。分級部材
14の上側処理筒10上面には、吸気口16が形
成され、この吸気口16に、バツクフイルター、
サイクロン等の製品捕集装置17を介して吸気フ
アン18が接続され、このフアン18の吸気によ
り処理筒10内が負圧となり、スクリユー軸11
の上端から空気が流入する。
An inverted conical classifying member 14 is provided at the upper part of the screw shaft 11 inside the processing cylinder 10, and as shown in FIG.
0 inner surface, blades 15 are curved in the direction of rotation of the screw shaft 11 and are provided at equal intervals.
When the airflow passes between the blades 15 and the blades 15, the blades 15 create a swirling flow and classification is performed. An intake port 16 is formed on the upper surface of the upper processing cylinder 10 of the classification member 14, and a back filter,
An intake fan 18 is connected via a product collection device 17 such as a cyclone, and the intake air of this fan 18 creates a negative pressure inside the processing cylinder 10, which causes the screw shaft 11
Air flows in from the top of the

なお、所望の粒度の生産粒子cを得たり、円滑
な操業を行なうためには、各種のパラメータを抽
出してそれらに基づいて行なえばよく、例えば、
処理筒10内の原料レベル、処理筒10内の気流
速さ(風量)、製品粒度等を検出する。原料レベ
ルはレベル計で直接に検出してもよいが、処理筒
10の気流出入口(吸気口16とスクリユー軸1
1の上端)の差圧で算出してもよい。また、気流
速さは吸入部分(スクリユー軸11の上端)でオ
リフイス、ベンチユーリー管などで検出する。原
料レベルに対しては原料投入量の調整で、気流速
さに対してはフアン回転数の調整でそれぞれ制御
する。
In addition, in order to obtain the production particles c of the desired particle size and to perform smooth operation, it is sufficient to extract various parameters and perform the process based on them. For example,
The raw material level in the processing cylinder 10, the air flow velocity (air volume) in the processing cylinder 10, the product particle size, etc. are detected. The raw material level may be detected directly with a level meter, but the
It may also be calculated using the differential pressure at the upper end of 1). Further, the air flow velocity is detected at the suction portion (the upper end of the screw shaft 11) using an orifice, a vent Urie tube, or the like. The raw material level is controlled by adjusting the raw material input amount, and the air flow rate is controlled by adjusting the fan rotation speed.

図中、19は粉砕媒体の取出し口である。 In the figure, reference numeral 19 is a port for taking out the grinding media.

実施例は以上のように構成されており、つぎに
その作用について説明する。
The embodiment is configured as described above, and its operation will be explained next.

いま、スクリユー軸11を回転し、被処理物a
を適宜に投入すると、スクリユー軸11の攪拌作
用により、被処理物aは、その相互間及び粉砕媒
体bとの摩砕により微細な生産粒子cに粉砕され
て軽くなる。
Now, rotate the screw shaft 11 and remove the workpiece a.
When the material to be processed is suitably added, due to the stirring action of the screw shaft 11, the material to be processed a is ground into fine product particles c by grinding with each other and with the grinding medium b, thereby becoming lighter.

一方、吸気フアン18により吸気されると、ス
クリユー軸11をとおつて空気が処理筒10下部
に流れ込んで周囲にまんべんなく広がり、上昇し
て分級部材14と羽根15の間を通る気流が生じ
る。この気流にのつて前記の軽くなつた生産粒子
cが上昇し、分級部材14と羽根15とにより粗
いものは分離されて吸気口16から捕集装置17
に至り、ここで、生産粒子cが捕集される。
On the other hand, when air is taken in by the intake fan 18, the air flows through the screw shaft 11 into the lower part of the processing cylinder 10, spreads evenly around the periphery, rises, and generates an airflow passing between the classification member 14 and the blades 15. The lightened production particles c rise along with this airflow, and the coarse particles are separated by the classification member 14 and the blades 15, and then passed through the intake port 16 to the collection device 17.
At this point, the produced particles c are collected.

この作用時、気流はスクリユー軸11の下端か
ら周囲にまんべんなく広がり、その流れで粉砕粒
子b、被処理物aを攪散するため、それらが滞留
することがない。
During this action, the airflow spreads evenly from the lower end of the screw shaft 11 to the periphery, and the flow agitates the pulverized particles b and the object to be processed a, so that they do not stagnate.

また、吸気フアン18の吸気により生産粒子c
の排出用気流を生じさせているため、処理筒10
内は負圧となり、作業環境汚染防止のためのシー
ル性を要求されることもないうえに、操業制御も
容易となる。
In addition, the particles c produced by the intake air of the intake fan 18
Since the discharge airflow is generated, the processing cylinder 10
There is a negative pressure inside, so there is no need for sealing to prevent contamination of the working environment, and operation control becomes easier.

さらに、吸気口16における流速・流量は吸気
フアン18によつて容易に制御できるため、均一
な粒子径の生産粒子cを得ることができる。
Furthermore, since the flow rate and flow rate at the intake port 16 can be easily controlled by the intake fan 18, it is possible to obtain the produced particles c with a uniform particle size.

なお、第3図に示すように、分級部材14をス
クリユー軸11に対し回転可能な羽根車14′と
して、外部のモータ20により別途回転するよう
にするとともに、羽根15に代えて処理筒10内
面全周に断面三角状の環状部材15′を設け、羽
根車14′の回転により両者14′,15′間を通
る気流に旋回流を生じさせて分級してもよい。三
角状部材15′を設ければ、通路が狭くなり旋回
流が生じ易いが、羽根車14′だけでもよい。
As shown in FIG. 3, the classifying member 14 is configured as an impeller 14' rotatable with respect to the screw shaft 11, which is separately rotated by an external motor 20, and the inner surface of the processing cylinder 10 is used instead of the impeller 15. An annular member 15' having a triangular cross section may be provided around the entire circumference, and the rotation of the impeller 14' may generate a swirling flow in the airflow passing between the two members 14' and 15' for classification. If the triangular member 15' is provided, the passage becomes narrower and swirling flow is likely to occur, but only the impeller 14' may be used.

しかし、分級部材14、羽根車14′、羽根1
5、部材15′は必ずしも設ける必要はなく、そ
の場合、被処理物aは粒子が粗く重いため、吸気
口16に吸引されることなく落下する。
However, the classification member 14, the impeller 14', the blade 1
5. It is not always necessary to provide the member 15'; in that case, the object to be treated a is coarse and heavy, and therefore falls without being sucked into the suction port 16.

また、空気を熱風にすれば、乾燥粉砕が可能と
なり、生産粒子cの搬送流体を空気に代えて、他
の気体を採用してもよく、水等の液体を使用する
こともできる。
Further, if the air is turned into hot air, dry pulverization becomes possible, and instead of air as the carrier fluid for the production particles c, other gases may be employed, or liquids such as water may also be used.

さらに、吸引機の排気口をスクリユー軸11の
上端及び捕集装置17の吸込口に接続して流体の
流れをクローズとしてもよい。この場合、スクリ
ユー軸11へは、吸引機の排出量の3分の2程度
を供給し、スクリユー軸11内は正圧となつても
下端開口付近では零圧となつて処理筒1内が負圧
となるように吸引機を制御する。
Furthermore, the flow of fluid may be closed by connecting the exhaust port of the suction device to the upper end of the screw shaft 11 and the suction port of the collection device 17. In this case, approximately two-thirds of the discharge amount of the suction device is supplied to the screw shaft 11, and even though there is positive pressure inside the screw shaft 11, there is zero pressure near the lower end opening, and the inside of the processing cylinder 1 becomes negative. Control the suction machine to achieve the desired pressure.

〔発明の効果〕〔Effect of the invention〕

この発明は、以上のように構成したので、均一
な生産粒子を円滑に得ることができるうえに、処
理筒内が負圧となるため作業環境もよいものとす
ることができ、操業も容易なものとなる。
Since this invention is configured as described above, it is possible to smoothly obtain uniform production particles, and the working environment is also good because the inside of the processing cylinder is under negative pressure, and the operation is easy. Become something.

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

第1図はこの発明の摩砕粉砕装置の一実施例の
断面図、第2図は第1図のX−X線断面図、第3
図は他の実施例の要部断面図、第4図及び第5図
は従来の摩砕粉砕装置の各例の概略図である。 1,10……処理筒、2,11……スクリユー
軸、13……被処理物投入口、16……吸気口、
18……吸気フアン、a……被処理物、b……粉
砕粒子、c……生産粒子。
FIG. 1 is a cross-sectional view of one embodiment of the grinding and crushing apparatus of the present invention, FIG. 2 is a cross-sectional view taken along the line X-X in FIG. 1, and FIG.
The figure is a sectional view of a main part of another embodiment, and FIGS. 4 and 5 are schematic views of each example of a conventional grinding and grinding apparatus. 1, 10... Processing tube, 2, 11... Screw shaft, 13... Processing material inlet, 16... Inlet port,
18... Intake fan, a... Processing object, b... Pulverized particles, c... Production particles.

Claims (1)

【特許請求の範囲】[Claims] 1 竪型処理筒内に、上下方向のスクリユー軸を
設けるとともに粉砕媒体を充填し、前記スクリユ
ー軸を回した状態で処理筒内に被処理物を投入
し、この被処理物を、その相互間及び前記粉砕媒
体との摩砕により微細な生産粒子とする摩砕粉砕
装置において、前記スクリユー軸を、上端が流体
吸込口となり下端が処理筒下部に開口した中空軸
とし、前記処理筒上部に流体吸込機を接続したこ
とを特徴とする摩砕粉砕装置。
1. A vertical screw shaft is provided in the vertical processing cylinder, and a grinding medium is filled with the processing material. The workpiece is placed in the processing cylinder with the screw shaft turned, and the workpiece is inserted between the two. and a grinding and grinding device that produces fine product particles by grinding with the grinding medium, wherein the screw shaft is a hollow shaft with an upper end serving as a fluid suction port and a lower end opening at the bottom of the processing cylinder, and a fluid A grinding and grinding device characterized by being connected to a suction machine.
JP21974785A 1985-10-01 1985-10-01 Grinding and crushing apparatus Granted JPS6279855A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21974785A JPS6279855A (en) 1985-10-01 1985-10-01 Grinding and crushing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21974785A JPS6279855A (en) 1985-10-01 1985-10-01 Grinding and crushing apparatus

Publications (2)

Publication Number Publication Date
JPS6279855A JPS6279855A (en) 1987-04-13
JPH0338903B2 true JPH0338903B2 (en) 1991-06-12

Family

ID=16740357

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21974785A Granted JPS6279855A (en) 1985-10-01 1985-10-01 Grinding and crushing apparatus

Country Status (1)

Country Link
JP (1) JPS6279855A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0753250B2 (en) * 1990-05-16 1995-06-07 株式会社クボタ Grinding equipment

Also Published As

Publication number Publication date
JPS6279855A (en) 1987-04-13

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