JPS6279855A - Grinding and crushing apparatus - Google Patents
Grinding and crushing apparatusInfo
- Publication number
- JPS6279855A JPS6279855A JP21974785A JP21974785A JPS6279855A JP S6279855 A JPS6279855 A JP S6279855A JP 21974785 A JP21974785 A JP 21974785A JP 21974785 A JP21974785 A JP 21974785A JP S6279855 A JPS6279855 A JP S6279855A
- Authority
- JP
- Japan
- Prior art keywords
- processing cylinder
- grinding
- screw shaft
- particles
- air
- 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
Links
Landscapes
- Crushing And Grinding (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
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.
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、上下方向のスクリュー軸2を設けるとともに鋼
球等の粉砕媒体すを充填し、スクリュー軸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す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 cylinder 1, and Filled with grinding media such as balls, the workpiece a is put into the processing cylinder 1 with the screw shaft 2 turned, and the workpiece a is
are ground into fine product particles C by grinding between them and with the grinding medium, and the product particles C are placed on a fluid such as air or water passing through the processing cylinder 1 and guided out of the processing cylinder 1. It is something.
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、流れにのって上昇する
生産粒子Cを両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って蓄積されるため、
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 both tops. In this way, when the pumped fluid is introduced from the side wall, the distribution of the produced particles C is biased toward one side from the center of the processing cylinder 1 and accumulated.
The drawback is that it cannot be derived quickly, the production efficiency is relatively low, and the production capacity is small compared to the size of the aircraft.
そこで、第4図のごとく、スクリュー軸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
放射状上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、中空のスクリュ
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. 4, the screw shaft 2 is used as a hollow shaft and the fluid is pumped from its upper end to generate a flow radially upward from the center of the lower part of the processing cylinder 1, and the produced particles C are drawn out from the upper part of the processing cylinder 1. As shown in Fig. 5, suction is applied from the upper end of the hollow screw shaft 2 to create a flow toward the center of the lower part of the processing cylinder 1, and the produced particles C are drawn out together with the fluid, thereby eliminating the deviation of the produced particles C. A new idea has been devised.
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が湾外に漏
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 shown in Fig. 4, since the processing cylinder 1 is under positive pressure with respect to the outside air, the object to be processed and the produced particles C tend to leak out of the bay, 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、スクリュー軸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 the one shown in Fig. 5, unpulverized heavy particles settle at the bottom of the processing tube 1, so there is a risk of inhaling them, and there are many problems with the particle size of the produced product particles C, which are large. If the particles cannot be sucked in, they will remain and the lower end suction portion of the screw shaft 2 will be blocked, causing a problem in that the produced particles C cannot be drawn out smoothly.
〔発明の目的〕
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。[Object of the Invention] The object of the present invention is to solve the problems of the grinding and crushing apparatus shown in FIGS. 4 and 5 above.
〔目的2)達成するための手段〕
上記目的を達成するため、この発明にあうでは、スクリ
ュー軸を中空とした摩砕粉砕装置において、スクリュー
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ァン又は吸引ポンプなど
の吸込機を接続したのである。[Objective 2) Means for Achieving] In order to achieve the above object, the present invention provides a grinding and pulverizing device in which the screw shaft is hollow, with the upper end of the screw shaft serving as a fluid suction port, and the lower end serving as a processing cylinder. It was opened at the bottom, and a suction device such as an intake fan or a suction pump was connected to the top of the processing cylinder.
この様に構成される装置は、スクリュー軸を回した状態
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、スクリュー軸を
通って処理筒内に流体が流入し、スクリュー軸下部から
放射状上向きの流れが生じ、この流れにのって前記生産
粒子が上昇して湾外に導出される。The device configured in this manner charges the material to be processed into the processing cylinder while rotating the screw shaft, grinds the material between themselves and with a grinding medium, and grinds the material into fine production particles. By suctioning from the upper part of the processing cylinder, fluid flows into the processing cylinder through the screw shaft, and a radial upward flow is generated from the lower part of the screw shaft, and the produced particles rise along with this flow and flow out of the bay. derived.
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ュー軸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。As shown in FIG. 1, a screw shaft 11 is provided on the central axis of a vertical cylindrical processing tube 10 whose upper and lower surfaces are closed. It is suspended and supported by support means and rotated by a motor (not shown).
スクリュー軸11は、中空軸となっ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。The screw shaft 11 is a hollow shaft whose upper end communicates with the outside of the machine and whose lower end opens at the lower part of the processing cylinder 10. By creating a negative pressure inside the processing cylinder 10, this shaft 11
Air flows into the lower part of the processing cylinder 10 through.
処理筒10の上部には、粉砕媒体すの投入口12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
ラミック、石、鋼球等の粉砕媒体すが図示Lレベルまで
充填され、後者の投入口13からスクリューコンベア等
により気密を保って被処理物aが送り込まれ、前記スク
リュー軸11の回転により、粉砕媒体す及び被処理物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す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, an input port 12 for a crushing medium and a material input port 13 are formed, and the crushing medium such as ceramics, stones, steel balls, etc. is filled from the former input port 12 to the L level shown in the figure. , the material to be processed a is fed from the latter input port 13 by a screw conveyor or the like in an airtight manner, and by the rotation of the screw shaft 11, the grinding media and the material to be processed are fed.
are moved and stirred as shown by the arrows in the figure, and the material to be processed A is ground between them and with the grinding medium, resulting in fine product particles C.
crushed into
スクリュー軸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10内面に羽根15がス
クリュー軸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により旋回流となっ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、バックフィルター、サイク
ロン等の製品捕集装置17を介して吸気ファン18が接
続され、このファン18の吸気により処理筒10内が負
圧となり、スクリュー軸11の上端から空気が流入する
。An inverted cone-shaped classification member 14 is provided at the upper part of the screw shaft 11 inside the processing cylinder 10, and as shown in FIG. The airflow is curved in the direction of rotation of the member 14 and arranged at equal intervals, and when the airflow passes between the member 14 and the blades 15, the blades 15 create a swirling flow for classification. An intake port 16 is formed on the upper surface of the upper processing cylinder 10 of the classification member 14, and an intake fan 18 is connected to this intake port 16 via a product collection device 17 such as a back filter or cyclone. The intake air creates a negative pressure inside the processing cylinder 10, and air flows in from the upper end of the screw shaft 11.
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内の気流速さく風量)、製品粒度等を
検出する。原料レベルはレベル針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とスクリュ
ー軸11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(スクリュー軸11の上端)でオリフィ
ス、ベンチュ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ァン
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 with the desired particle size and to perform smooth operation, it is sufficient to extract various parameters and perform the operation based on them. For example, the raw material level in the processing cylinder 10, Detects the airflow speed (airflow rate), product particle size, etc. The raw material level may be detected directly with a level needle, but may also be calculated based on the differential pressure between the air inlet and outlet of the processing cylinder 10 (intake port 16 and the upper end of the screw shaft 11). Further, the air flow velocity is detected at the suction portion (the upper end of the screw shaft 11) using an orifice, a Venturi tube, or the like. The raw material level is controlled by adjusting the raw material input amount, and the air flow speed is controlled by adjusting the fan rotation speed.
M中、19は粉砕媒体の取出し口である。In M, 19 is an outlet for 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、スクリュー軸11を回転し、被処理物aを適宜に
投入すると、スクリュー軸11の撹拌作用により、被処
理物aは、その相互間及び粉砕媒体すとの摩砕により微
細な生産粒子Cに粉砕されて軽くなる。Now, when the screw shaft 11 is rotated and the material to be processed a is thrown in as appropriate, the material to be processed a is ground into fine production particles C by the stirring action of the screw shaft 11 and by grinding between them and the grinding medium. It is crushed and becomes lighter.
一方、吸気ファン18により吸気されると、スクリュー
軸11をとおって空気が処理筒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。この気流にのって前記の
軽くなった生産粒子Cが上昇し、分級部材14と羽根1
5とにより粗いものは分離されて吸気口16から捕集袋
W17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 into the lower part of the processing cylinder 10 through the screw shaft 11, 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 are transferred to the classification member 14 and the blade 1.
Coarse particles are separated by the air intake port 16 and sent to the collection bag W17, where the produced particles C are collected.
この作用時、気流はスクリュー軸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を撹散するため、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、吸気ファン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, since the intake air of the intake fan 18 generates an airflow for discharging the produced particles C, the inside of the processing cylinder 10 becomes negative pressure, and there is no need for sealing performance to prevent contamination of the working environment. Operation control also becomes easier.
さらに、吸気口16における流速・流量は吸気ファン1
8によっ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, the flow velocity and flow rate at the intake port 16 are determined by the intake fan 1
8, production particles C having a uniform particle size can be obtained.
なお、第3図に示すように、分級部材14をスクリュー
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
1S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。As shown in FIG. 3, the classification member 14 is configured as an impeller 14' that is rotatable with respect to the screw shaft 11 and rotated separately by an external motor 20, and the inner surface of the processing cylinder 10 is used instead of the impeller 1S. An annular member 15' having a triangular cross section is provided around the entire circumference, and both 14' are rotated by the rotation of the impeller 14'.
, 15' may be classified by creating a swirling flow in the airflow passing between the airflow.
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。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15、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 blades 15, and the member 15' are not necessarily provided, and in that case, the material to be processed a is coarse and heavy, so it falls without being sucked into the intake 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 used, or liquids such as water may also be used.
さらに、吸引機の排気口をスクリュー軸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、スクリュー軸11へは、吸引
機の排出量の3分の2程度を供給し、スクリュー軸11
内は正圧となっても下端開口付近では零圧となって処理
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 machine is supplied to the screw shaft 11.
The suction machine is controlled so that even if the pressure inside is positive, the pressure is zero near the bottom opening, and the inside of the processing cylinder 1 is under negative pressure.
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.
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
の各側の概略図である。
1.10・・・・・・処理筒、2.11・・・・・・ス
クリュー軸、13・・・・・・被処理物投入口、16・
・・・・・吸気口、18・・・・・・吸気ファン、a・
・・・・・被処理物、b・・・・・・粉砕粒子、C・・
・・・・生産粒子。
特許出願人 久保田鉄工株式会社
同 代理人 鎌 1)文 二FIG. 1 is a cross-sectional view of an embodiment of the grinding device of the present invention;
Fig. 2 is a sectional view taken along the line X-X of Fig. 1, Fig. 3 is a sectional view of main parts of another embodiment, and Figs. 4 and 5 are schematic views of each side of a conventional grinding device. be. 1.10... Processing cylinder, 2.11... Screw shaft, 13... Processing material inlet, 16.
...Intake port, 18...Intake fan, a.
...Product to be processed, b...Crushed particles, C...
...Produced particles. Patent applicant: Kubota Iron Works Co., Ltd. Agent: Kama 1) Bun 2
Claims (1)
もに粉砕媒体を充填し、前記スクリュー軸を回した状態
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、前記スクリュー軸を、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。A vertical processing cylinder is provided with a vertical screw shaft and filled with a grinding medium, and while the screw shaft is turned, a workpiece is put into the processing cylinder, and the workpiece is separated between each other and In the grinding and grinding device that produces fine product particles by grinding with the grinding medium, the screw shaft is a hollow shaft whose upper end serves as a fluid suction port and whose lower end opens at the bottom of the processing cylinder, and the screw shaft is a hollow shaft whose upper end serves as a fluid suction port and whose lower end opens at the bottom of the processing cylinder. A grinding and grinding device characterized by a connected machine.
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 true JPS6279855A (en) | 1987-04-13 |
JPH0338903B2 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) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0422444A (en) * | 1990-05-16 | 1992-01-27 | Kubota Corp | Pulverizing and grinding apparatus |
-
1985
- 1985-10-01 JP JP21974785A patent/JPS6279855A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0422444A (en) * | 1990-05-16 | 1992-01-27 | Kubota Corp | Pulverizing and grinding apparatus |
JPH0753250B2 (en) * | 1990-05-16 | 1995-06-07 | 株式会社クボタ | Grinding equipment |
Also Published As
Publication number | Publication date |
---|---|
JPH0338903B2 (en) | 1991-06-12 |
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