JPH11179222A - Pulverizer - Google Patents

Pulverizer

Info

Publication number
JPH11179222A
JPH11179222A JP36447997A JP36447997A JPH11179222A JP H11179222 A JPH11179222 A JP H11179222A JP 36447997 A JP36447997 A JP 36447997A JP 36447997 A JP36447997 A JP 36447997A JP H11179222 A JPH11179222 A JP H11179222A
Authority
JP
Japan
Prior art keywords
grindstone
casing
pulverized
rotating
fine powder
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.)
Pending
Application number
JP36447997A
Other languages
Japanese (ja)
Inventor
Yukiya Masuda
幸也 増田
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.)
Masuko Sangyo Co Ltd
Original Assignee
Masuko Sangyo Co Ltd
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 Masuko Sangyo Co Ltd filed Critical Masuko Sangyo Co Ltd
Priority to JP36447997A priority Critical patent/JPH11179222A/en
Publication of JPH11179222A publication Critical patent/JPH11179222A/en
Pending legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a pulverizer in which hardly pulverizable material can be subjected to pulverization at an ordinary temperature to effectively obtain uniform powder of superfine particles and there is no possibility of coarse particles being mixed in the product. SOLUTION: A pulverizer 1 has a fixed grindstone 2 and a rotary grindstone 3 installed in a casing 4 and a rotating blade 8 arranged on the back surface of a rotating disc 6. Fresh air sucked in from a hopper 10 is sent to between both the grindstones and is turned into a spin type rotating high speed air current A, which flows to be outward uniformly dispersed, and the air current that has gone to the outside is turned into a turning current while it is hit against the inner peripheral surface of a pulverizing chamber 4b. On the inner peripheral surface of the pulverizing chamber 4b, a corrugated lining plate 12 is attachably and detachably fitted so that material to be pulverized carried on the turning current and hit against it is pulverized. A collecting annular body 4d for distributing in layers the pulverized material according to the particle diameter is provided for the casing 4, to the upper end and the back surface of the annular body 4d, a secondary fine powder recovery tubular body 13 and a coarse particle reflux tubular body 14 communicating with a feeding pipe 9 are connected respectively.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、被粉砕物を砥石
間で摩砕すると共に、排出気流で旋回させながら粉砕す
る粉砕装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pulverizing apparatus for pulverizing an object to be pulverized between whetstones and pulverizing the object while rotating it by an exhaust airflow.

【0002】[0002]

【従来の技術】挽臼原理を採用する粉砕機は、相互の間
隔が調整できる上下2枚の砥石を有し、固定する上部砥
石と高速で回転する下部砥石との間に強力な遠心力、衝
撃摩砕力、せん断力を生じさせ、それらの総合作用によ
って被粉砕物の微粉砕化を行っている。
2. Description of the Related Art A pulverizer adopting the milling principle has two upper and lower whetstones whose distance can be adjusted. A strong centrifugal force is applied between an upper whetstone to be fixed and a lower whetstone rotating at high speed. An impact grinding force and a shear force are generated, and the object to be ground is finely pulverized by their combined action.

【0003】このような粉砕機の中で高脂質、高水分、
高蛋白質、糖質や特殊酵素を多量に含有する難粉砕性物
質にあっても適用可能な粉砕機としては、例えば特開平
7−185372号公報に記載される粉砕装置がある。
この装置は、回転砥石に付設する回転翼の作用により両
砥石面間に強力な減圧ジェット気流を生起せしめ、難粉
砕性物質の粉砕工程で発生する発熱、脂質の滲み出しに
よるべたつき、水分による粘り付き、酸化変質等による
焦げ付き、フィルム化等を抑制しながら供給される被粉
砕原料を温度上昇なしに常温微粉砕するものであった。
In such a crusher, high fat, high moisture,
A pulverizer that can be applied to hard-to-pulverize substances containing a large amount of high proteins, carbohydrates and special enzymes is, for example, a pulverizer described in JP-A-7-185372.
This device generates a strong depressurized jet stream between the surfaces of the grinding wheels due to the action of the rotating blades attached to the rotating wheel, generating heat in the grinding process of difficult-to-grind materials, stickiness due to oozing of lipids, stickiness due to moisture. The raw material to be supplied is finely pulverized at room temperature without increasing the temperature while suppressing sticking, burning due to oxidative deterioration and the like, film formation and the like.

【0004】このように減圧ジェット気流を生起せしめ
ながら被粉砕物を砥石間で摩砕する従来の粉砕装置は、
図3に示すように上下一対の固定砥石102及び回転砥
石103、回転砥石103を装着する回転盤106に付
設して両砥石の対向面間に砥石外方へ向う排出気流を生
じさせる回転翼108、両砥石を内設するケーシング1
04、このケーシング104に連通して粉砕物を送り出
す回収管体111とを備えていた。
[0004] A conventional pulverizing apparatus for grinding an object to be pulverized between whetstones while generating a depressurized jet stream as described above,
As shown in FIG. 3, a pair of upper and lower fixed grindstones 102, a rotating grindstone 103, and a rotating blade 108 attached to a rotating disk 106 on which the rotating grindstone 103 is mounted to generate a discharge airflow toward the outside of the grindstone between opposing surfaces of the two grindstones. , Casing 1 with both whetstones inside
04, and a recovery pipe 111 that communicates with the casing 104 and sends out the pulverized material.

【0005】投入管109を介して固定砥石102の開
口部102aより投入される被粉砕原料115は、対向
する両砥石の外周部平坦摩砕面102b,103b間で
摩砕されるが、両砥石間にジェット気流を生起させて固
定砥石102の開口部102aより外気を吸引し、砥石
面間でモータ回転方向にスピン状の回転高速気流を発生
させ、供給される被粉砕原料115を巻き込みながら平
坦摩砕面間を強制的に高速通過せしめ、この気流を利用
して微粒パウダー116をケーシング104から回収管
体111に送り出していた。
[0005] The raw material 115 to be pulverized introduced from the opening 102a of the fixed grindstone 102 through the charging pipe 109 is ground between the opposed flat grinding surfaces 102b and 103b of the two grindstones. A jet airflow is generated in between, and the outside air is sucked from the opening 102a of the fixed whetstone 102, and a spin-shaped high-speed airflow is generated between the whetstone surfaces in the direction of motor rotation, and flat while entraining the supplied raw material 115 to be ground. The fine powder 116 was forcibly passed between the grinding surfaces at a high speed, and the fine powder 116 was sent from the casing 104 to the collection pipe 111 by using the airflow.

【0006】[0006]

【発明が解決しようとする課題】しかし従来の粉砕装置
101は、砥石外部に排出された粉砕物を全て回収管体
111に搬出する構成であったため、製品中に十分に微
粉化されていない粗粒子が混入する恐れもあった。又、
粉砕作用は砥石外周部の平坦摩砕面間における摩砕作用
がほとんどであったため、超微粒のパウダーを効率的に
得ることが難しく、又均一の粒径を得ることも難しかっ
た。
However, the conventional pulverizing apparatus 101 has a configuration in which all the pulverized material discharged to the outside of the grindstone is carried out to the collection pipe 111, so that the coarse pulverized product is not sufficiently pulverized in the product. There was also a risk of particles being mixed. or,
Since the crushing action was almost the crushing action between the flat crushing surfaces on the outer periphery of the grindstone, it was difficult to efficiently obtain ultrafine powder, and it was also difficult to obtain a uniform particle size.

【0007】この発明は上記課題を解決し、難粉砕性物
質であっても、常温微粉砕が可能で、超微粒で均一の粒
径を有するパウダーを効率的に得ることができ、製品中
に粗粒子が混入する恐れのない粉砕装置を提供すること
を目的としている。
[0007] The present invention solves the above-mentioned problems, and it is possible to pulverize at room temperature even with difficult-to-pulverize substances, to efficiently obtain ultrafine powder having a uniform particle size, and to obtain a powder in a product. It is an object of the present invention to provide a pulverizer that does not have a possibility of mixing coarse particles.

【0008】[0008]

【課題を解決するための手段】上記課題を解決するた
め、この発明の粉砕装置のケーシングは、排出気流に乗
って旋回する粉砕物が衝突する面に脱着可能に取り付け
る波形状ライニングプレートと、粉砕物を粒径に応じて
層状分布させる補集用環状体を備え、回収管体として、
この補集用環状体の上端に連通する微粉回収管体と、補
集用環状体の下端に連通して投入管につながる粗粒子還
流管体と、これら微粉回収管体及び粗粒子還流管体の流
量調整機構を備えることを特徴としている。
In order to solve the above-mentioned problems, a casing of a pulverizing apparatus according to the present invention comprises a corrugated lining plate detachably mounted on a surface on which a pulverized material swirling in an exhaust air flow collides, A collection annular body that distributes the material layered according to the particle size, and as a collection tube,
A fine powder collection tube communicating with the upper end of the collection ring, a coarse particle reflux tube communicating with the lower end of the collection ring and connected to the charging tube, and a fine particle collection tube and a coarse particle reflux tube Characterized in that the flow rate adjusting mechanism is provided.

【0009】回転砥石を装着する回転盤には円周方向に
等間隔で複数個回転翼を付設して固定砥石の開口部より
外気を吸引し両砥石の対向面間に砥石外方へ向う排出気
流を生じさせる。投入管より投入される被粉砕原料は、
固定砥石中央に設ける開口部より両砥石間に送られ、モ
ータ回転方向のスピン状回転高速気流に巻き込まれなが
ら対向する両砥石の外周部平坦摩砕面間を強制的に高速
通過し摩砕される。
A plurality of rotating blades are provided at equal intervals in a circumferential direction on a rotating disk on which a rotating grindstone is mounted so that outside air is sucked from an opening of a fixed grindstone and discharged between the opposed surfaces of the two grindstones toward the outside of the grindstone. Create an airflow. The raw material to be pulverized from the charging pipe is
It is sent between the two grinding wheels from the opening provided in the center of the fixed grinding wheel, and while being entrained in the spinning high-speed airflow in the motor rotation direction, it is forcibly high-speed passed between the opposing outer grinding surfaces of the two grinding wheels and ground. You.

【0010】砥石外部に送り出された粉砕物は、ケーシ
ング内に生ずる旋回気流に乗って波形状ライニングプレ
ートに衝突し更に細かく粉砕される。この波形状ライニ
ングプレートは脱着可能な構成のため原料に最適な凹凸
形状、材質のものが選択可能である。
The pulverized material sent out of the grindstone collides with the corrugated lining plate on the swirling airflow generated in the casing and is further finely pulverized. Since the corrugated lining plate has a detachable structure, it is possible to select a corrugated lining plate having a concave-convex shape and material that is optimal for the raw material.

【0011】波形状ライニングプレートに連続的に衝突
しながら旋回する粉砕物は、微粉砕されると同時に補集
用環状体内で粒径に応じた層状分布となる。すなわち微
粉は上層に、粗粒子は下層にと分級され、それぞれ微粉
回収管体及び粗粒子還流管体に選別搬送される。各管体
には弁体による流量調整機構を設け、各管体に流れ込む
粉砕物の量を適正に管理することで的確な層状分布を実
現する。
The pulverized material turning while continuously colliding with the corrugated lining plate is finely pulverized and, at the same time, has a layered distribution according to the particle size in the collecting annular body. That is, the fine powder is classified into an upper layer, and the coarse particles are classified into a lower layer, and are separately conveyed to a fine powder recovery pipe and a coarse particle reflux pipe. Each pipe body is provided with a flow rate adjusting mechanism by a valve body, and an appropriate layered distribution is realized by appropriately managing the amount of pulverized material flowing into each pipe body.

【0012】粗粒子還流管体は、未だ十分に微粉化され
ていない粉砕物を投入管から両砥石間に送り込み、再度
摩砕、衝突粉砕を行う。これにより所望の粒度まで微粉
化された粉砕物が補集用環状体より微粉回収管体に送ら
れる。
In the coarse particle reflux tube, a pulverized material that has not been sufficiently pulverized is sent from the charging tube to between the two grindstones, and is subjected to grinding and collision grinding again. Thereby, the pulverized material pulverized to a desired particle size is sent from the collection ring to the fine powder collection tube.

【0013】ここで固定砥石及び回転砥石は、平坦摩砕
面を除く面に被粉砕原料を送り出す放射状深型送り溝を
設けることが望ましい。これは送り出し作用を極めて大
きくするもので、送り溝の深さや配列等については平坦
摩砕面の砥石粒度によって適宜調整する。
Here, it is desirable that the fixed grindstone and the rotary grindstone have a radial deep feed groove for feeding the raw material to be crushed on a surface other than the flat grinding surface. This is to make the feeding action extremely large, and the depth and arrangement of the feed grooves are appropriately adjusted depending on the grain size of the grinding wheel on the flat grinding surface.

【0014】又、回転砥石には、回転軸に止着する粗砕
切断カッタを設けると共にケーシングには、この粗砕切
断カッタで発生する微粉を補集するための筒体を開口部
に立設することが望ましい。粗砕切断カッタは被粉砕原
料を適正サイズに切断して両砥石間に送るものである
が、被粉砕物によっては切断と同時に微粉を生ずる場合
がある。又被粉砕物が粒子あるいは比重の軽い物質の場
合には投入と同時に微粉が舞い上がる場合がある。これ
ら開口部より立ち上がる微粉は投入管の周囲に設ける筒
体により回収する。
Further, the rotary grindstone is provided with a coarse cutting cutter fixed to the rotary shaft, and a casing is provided at the opening in the casing for collecting fine powder generated by the coarse cutting cutter. It is desirable to do. The crushing and cutting cutter cuts the raw material to be crushed into an appropriate size and sends it between the two whetstones. However, depending on the crushed material, fine powder may be generated simultaneously with the cutting. If the material to be ground is a particle or a substance having a low specific gravity, the fine powder may soar at the same time as the powder is charged. Fine powder rising from these openings is collected by a cylinder provided around the charging pipe.

【0015】[0015]

【発明の実施の形態】次にこの発明の実施形態を添付図
面に基づき詳細に説明する。図1は粉砕装置の縦断面
図、図2は図1のII−II断面を示す断面図である。粉砕
装置1は、上下一対の固定砥石2と回転砥石3をケーシ
ング4に内設する。回転砥石3は図示しない電動モータ
より延伸するシャフト5に回転盤6を介して着脱可能に
装着され、その中心部3aより突設するシャフト5先端
には粗砕切断カッタ7を設ける。又回転盤6の下面には
回転翼8を周方向に所定間隔で配設する。
Embodiments of the present invention will be described in detail with reference to the accompanying drawings. FIG. 1 is a longitudinal sectional view of the crusher, and FIG. 2 is a sectional view showing a II-II section of FIG. The crushing device 1 includes a pair of upper and lower fixed whetstones 2 and a rotary whetstone 3 provided inside a casing 4. The rotary grindstone 3 is detachably mounted on a shaft 5 extending from an electric motor (not shown) via a rotary disk 6, and a coarse crushing cutter 7 is provided at a tip of the shaft 5 protruding from a center portion 3 a thereof. On the lower surface of the rotating disk 6, the rotating blades 8 are arranged at predetermined intervals in the circumferential direction.

【0016】固定砥石2は中央に開口部2aを開設し、
同様に開口を設けるケーシング蓋部4aに着脱可能に取
り付けられる。この開口上方には被粉砕原料を供給する
投入管9が配設され、その上端にはホッパー10が取り
付けられる。又投入管9の外周には一次微粉補集筒11
を立設する。
The fixed whetstone 2 has an opening 2a in the center,
Similarly, it is detachably attached to the casing lid 4a having an opening. A charging pipe 9 for supplying a raw material to be pulverized is provided above the opening, and a hopper 10 is attached to an upper end thereof. A primary fine powder collection cylinder 11 is provided on the outer periphery of the charging pipe 9.
Is established.

【0017】回転翼8を駆動するとホッパー10より吸
引される外気は両砥石間に送られ、モータ回転方向のス
ピン状回転高速気流Aとなり、外方向に均等に分散して
流れる。砥石外部に出た気流は、ケーシング4の内周面
に衝突しながら旋回気流Bとなる。このケーシング4は
耐減圧機能を備え、両砥石外方の粉砕室4bの内周面に
は波形状ライニングプレート12を脱着可能に取り付け
る。波形状ライニングプレート12は旋回気流Bに乗っ
て衝突する被粉砕原料が微粉化されるよう原料に最適な
凹凸形状、材質のものを選択する。
When the rotary wings 8 are driven, the outside air sucked from the hopper 10 is sent between the two grindstones and becomes a spinning high-speed airflow A in the motor rotation direction, which is uniformly dispersed in the outside direction. The airflow that has flowed out of the grindstone becomes a swirling airflow B while colliding with the inner peripheral surface of the casing 4. The casing 4 has an anti-decompression function, and a wave-shaped lining plate 12 is detachably attached to the inner peripheral surface of the pulverizing chamber 4b on the outer side of both whetstones. As the corrugated lining plate 12, a material having the optimum uneven shape and material is selected so that the material to be pulverized colliding with the swirling airflow B is pulverized.

【0018】粉砕室4bの上方にはドーナツ状の筒体4
cを立設し、粉砕室4bと併せて粉砕物を粒径に応じて
層状分布させる補集用環状体4dを構成する。この補集
用環状体4dの上端には二次微粉回収管体13を連通
し、下面には粗粒子還流管体14を接続する。粗粒子還
流管体14は投入管9に連通している。
Above the grinding chamber 4b, a donut-shaped cylindrical body 4 is provided.
The collection circular body 4d is set up and the collection chamber 4b is arranged together with the pulverizing chamber 4b to distribute the pulverized material in layers according to the particle size. A secondary fine powder recovery pipe 13 is connected to the upper end of the collection ring 4d, and a coarse particle reflux pipe 14 is connected to the lower face. The coarse particle reflux pipe 14 communicates with the charging pipe 9.

【0019】投入管9を介して固定砥石2の開口部2a
より投入される被粉砕原料15は、粗砕切断カッタ7に
より適正サイズに切断される。この切断と同時に立ち上
がる一次微粉16は一次微粉補集筒11より図示しない
回収ケースに送られる。それ以外の被粉砕原料15は両
砥石間に送られ、スピン状回転高速気流Aに巻き込まれ
ながら対向する両砥石の外周部に設ける平坦摩砕面2
b,3b間を強制的に高速通過し摩砕される。
The opening 2a of the fixed grindstone 2 through the input pipe 9
The raw material 15 to be pulverized is cut into an appropriate size by the coarse cutting cutter 7. The primary fine powder 16 rising simultaneously with the cutting is sent from the primary fine powder collection cylinder 11 to a collection case (not shown). The other raw material 15 to be crushed is sent between the two grindstones, and is entangled in the spinning high-speed air flow A while being provided on the outer peripheral portions of the opposed grindstones 2.
b and 3b are forcibly passed at a high speed and ground.

【0020】これら両砥石には平坦摩砕面2b,3bを
除く面に被粉砕原料を送り出す放射状深型送り溝2c,
3cを設ける。これは送り出し作用を極めて大きくする
もので、送り溝の深さや配列等については平坦摩砕面2
b,3bの砥石粒度によって適宜調整する。平坦摩砕面
2b,3bの幅は25mm以下が望ましく、平坦摩砕面
間の相互間隔は100μ〜3,000μ程度に調整する。なお、
砥石は原料に適した材質のものを選択する。
These two grindstones have a radial deep feed groove 2c, which feeds the raw material to be ground to the surfaces other than the flat grinding surfaces 2b, 3b.
3c is provided. This greatly enhances the feeding action, and the depth and arrangement of the feed grooves are determined by the flat grinding surface 2.
Adjust appropriately according to the grain size of b and 3b. The width of the flat grinding surfaces 2b and 3b is desirably 25 mm or less, and the mutual interval between the flat grinding surfaces is adjusted to about 100 μ to 3,000 μ. In addition,
The whetstone should be of a material suitable for the raw material.

【0021】粉砕室4bに送り出された粉砕物は、旋回
気流Bに乗って波形状ライニングプレート12の溝部に
衝突し更に細かく粉砕される。このように波形状ライニ
ングプレート12に連続的に衝突しながら旋回する粉砕
物は、微粉砕されると同時に補集用環状体4d内で粒径
に応じた層状分布となる。すなわち二次微粉17は上層
に、粗粒子18は下層にと分級され、それぞれ二次微粉
回収管体13及び粗粒子還流管体14に選別搬送され
る。
The pulverized product sent to the pulverizing chamber 4b rides on the swirling airflow B and collides with the groove of the corrugated lining plate 12 to be further pulverized. The pulverized material that turns while continuously colliding with the corrugated lining plate 12 is finely pulverized and has a layered distribution according to the particle size in the collection annular body 4d. That is, the secondary fine powder 17 is classified into an upper layer, and the coarse particles 18 are classified into a lower layer, and are separately conveyed to a secondary fine powder recovery pipe 13 and a coarse particle reflux pipe 14, respectively.

【0022】なお各管体に流れ込む粉砕物の量は、二次
微粉回収管体13及び粗粒子還流管体14に夫々設ける
弁体19,20によって調整される。これら弁体19,
20の開度を適正に管理することで的確な層状分布が実
現できる。又ケーシング4の外部には冷却室21を設け
粉砕物の温度上昇を防止する。
The amount of the pulverized material flowing into each tube is adjusted by valves 19 and 20 provided in the secondary fine powder recovery tube 13 and the coarse particle reflux tube 14, respectively. These valve elements 19,
By appropriately managing the opening degree of the 20, an accurate layered distribution can be realized. A cooling chamber 21 is provided outside the casing 4 to prevent the temperature of the crushed material from rising.

【0023】粗粒子還流管体14は、未だ十分に微粉化
されていない粗粒子18を投入管9から両砥石間に送り
込み、再度摩砕、衝突粉砕を行う。これにより所望の粒
度まで微粉化された二次微粉17が補集用環状体4dよ
り二次微粉回収管体13に送られる。
The coarse particle reflux pipe 14 feeds the coarse particles 18 that have not yet been sufficiently pulverized from the charging pipe 9 between the two grindstones, and performs grinding and collision grinding again. As a result, the secondary fine powder 17 pulverized to a desired particle size is sent to the secondary fine powder recovery tube 13 from the collection ring 4d.

【0024】[0024]

【発明の効果】以上説明したように、この発明の粉砕装
置は、被粉砕原料を砥石で摩砕すると同時に回転翼の作
用で排出気流に乗って砥石外部に排出し、旋回する粉砕
物が衝突する面に脱着可能に波形状ライニングプレート
を取り付けるので難粉砕性物質であっても、常温微粉砕
が可能であり、しかも摩砕後に衝突粉砕を行うのでより
粒度の細かい超微粒を得ることができる。波形状ライニ
ングプレートは脱着可能なパーツであるため簡単に交換
でき原料に合ったものが選択できる。
As described above, the pulverizing apparatus of the present invention grinds the raw material to be pulverized with the grindstone, and at the same time, discharges it to the outside of the grindstone by the action of the rotating blades on the discharge airflow. Since the corrugated lining plate is detachably attached to the surface to be ground, it is possible to finely pulverize at room temperature even if the material is difficult to grind, and it is possible to obtain ultra-fine particles with a finer particle size because collision grinding is performed after grinding. . Since the corrugated lining plate is a detachable part, it can be easily replaced and the one that matches the raw material can be selected.

【0025】更に、ケーシングには補集用環状体を備え
るので粉砕物を粒径に応じて層状分布させることがで
き、これを微粉回収管体と粗粒子還流管体とに分別搬送
するので均一の粒径を有するパウダーを効率的に得るこ
とができ、製品中に粗粒子が混入する恐れがなくなり、
安定した粉砕が可能となる。
Furthermore, since the casing is provided with a collecting annular body, the pulverized material can be distributed in layers according to the particle size. Powder can be efficiently obtained, and there is no danger of coarse particles being mixed into the product,
Stable pulverization becomes possible.

【0026】又請求項2記載の粉砕装置は、平坦摩砕面
を除く面に被粉砕原料を送り出す放射状深型送り溝を設
ける固定砥石及び回転砥石を使用するので送り出し作用
を極めて大きくすることができる。請求項3記載の粉砕
装置は、粗砕切断カッタを設けると共に粗砕切断カッタ
で発生する微粉を補集するための筒体を開口部に立設す
るので微粉を効率的に回収することができる。
Further, the grinding device according to the second aspect uses a fixed grindstone and a rotary grindstone provided with a radial deep feed groove for feeding the raw material to be ground on the surface other than the flat grinding surface, so that the feeding action can be extremely increased. it can. In the crushing device according to the third aspect, since the crushing and cutting cutter is provided and the cylindrical body for collecting the fine powder generated by the crushing and cutting cutter is erected at the opening, the fine powder can be efficiently collected. .

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

【図1】粉砕装置の縦断面図である。FIG. 1 is a longitudinal sectional view of a crusher.

【図2】図1のII−II断面を示す断面図である。FIG. 2 is a sectional view showing a II-II section in FIG. 1;

【図3】従来の粉砕装置の縦断面図である。FIG. 3 is a longitudinal sectional view of a conventional pulverizing device.

【符号の説明】[Explanation of symbols]

1 粉砕装置 2 固定砥石 2a 開口部 2b 平坦摩砕面 3 回転砥石 3b 平坦摩砕面 4 ケーシング 4d 補集用環状体 6 回転盤 8 回転翼 12 波形状ライニングプレート 13 二次微粉回収管体 14 粗粒子還流管体 15 被粉砕原料 17 二次微粉 18 粗粒子 DESCRIPTION OF SYMBOLS 1 Crusher 2 Fixed grindstone 2a Opening 2b Flat grind surface 3 Rotating grindstone 3b Flat grind surface 4 Casing 4d Collection circular body 6 Turntable 8 Rotor blade 12 Wavy lining plate 13 Secondary fine powder collection pipe 14 Coarse Particle reflux tube 15 Raw material to be crushed 17 Secondary fine powder 18 Coarse particles

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 投入管を介して被粉砕原料を投入する開
口部を中央に設け外周部に平坦摩砕面を有する固定砥石
と、固定砥石の下方に対向して配設され外周部に平坦摩
砕面を有する回転砥石と、この回転砥石を装着する回転
盤に付設して両砥石の対向面間に砥石外方へ向う排出気
流を生じさせる回転翼と、両砥石を内設すると共に平坦
摩砕面間で摩砕され排出気流により砥石外部に排出され
た粉砕物を旋回させながら収容するケーシングと、この
ケーシングに連通して旋回する粉砕物を排出気流で送り
出す回収管体とを備える粉砕装置において、前記ケーシ
ングは、旋回する粉砕物が衝突する面に脱着可能に取り
付ける波形状ライニングプレートと、前記粉砕物を粒径
に応じて層状分布させる補集用環状体を備え、前記回収
管体は、この補集用環状体の上端に連通する微粉回収管
体と、補集用環状体の下端に連通して前記投入管につな
がる粗粒子還流管体と、これら微粉回収管体及び粗粒子
還流管体の流量調整機構を備えることを特徴とする粉砕
装置。
1. A fixed whetstone having an opening for charging raw material to be ground via a charging pipe at the center and having a flat grinding surface on an outer peripheral portion, and a flat grinding wheel disposed below and opposed to the fixed whetstone. A rotating grindstone having a grinding surface, a rotating blade attached to a rotating disk to which the rotating grindstone is attached, and generating a discharge airflow toward the outside of the grindstone between the opposing surfaces of the two grindstones, and both grindstones provided inside and flat A crusher comprising a casing for accommodating the crushed material that has been crushed between the crushing surfaces and discharged to the outside of the grindstone by the discharge airflow while rotating the crushed material, and a recovery pipe body that communicates the crushed material that is circulated to the casing and sends out the crushed material by the discharge airflow. In the apparatus, the casing includes a corrugated lining plate detachably attached to a surface on which the revolving crushed material collides, and a collecting annular body for distributing the crushed material in a layered manner in accordance with a particle diameter. For this collection A fine powder collection pipe communicating with the upper end of the annular body, a coarse particle reflux pipe communicating with the lower end of the collection annular body and connected to the charging pipe, and flow rate adjustment of the fine powder recovery pipe and the coarse particle reflux pipe A crushing device comprising a mechanism.
【請求項2】 前記固定砥石及び回転砥石は、平坦摩砕
面を除く面に被粉砕原料を送り出す放射状深型送り溝を
設けることを特徴とする請求項1記載の粉砕装置。
2. The crusher according to claim 1, wherein the fixed grindstone and the rotary grindstone are provided with a radial deep feed groove for feeding the raw material to be crushed on a surface other than a flat grinding surface.
【請求項3】 前記回転砥石は、回転軸に止着する粗砕
切断カッタを設け、前記ケーシングは、この粗砕切断カ
ッタで発生する微粉を補集するための筒体を前記開口部
に立設することを特徴とする請求項1又は請求項2記載
の粉砕装置。
3. A rotary grinding stone is provided with a coarse cutting cutter fixed to a rotating shaft, and the casing is provided with a cylindrical body for collecting fine powder generated by the coarse cutting cutter at the opening. The crushing device according to claim 1, wherein the crushing device is provided.
JP36447997A 1997-12-18 1997-12-18 Pulverizer Pending JPH11179222A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP36447997A JPH11179222A (en) 1997-12-18 1997-12-18 Pulverizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP36447997A JPH11179222A (en) 1997-12-18 1997-12-18 Pulverizer

Publications (1)

Publication Number Publication Date
JPH11179222A true JPH11179222A (en) 1999-07-06

Family

ID=18481914

Family Applications (1)

Application Number Title Priority Date Filing Date
JP36447997A Pending JPH11179222A (en) 1997-12-18 1997-12-18 Pulverizer

Country Status (1)

Country Link
JP (1) JPH11179222A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007105559A (en) * 2005-10-11 2007-04-26 Sanyo Electric Co Ltd Mill
CN102380454A (en) * 2011-09-22 2012-03-21 栾清杨 Winnowing device of solid wastes
CN104689877A (en) * 2014-08-10 2015-06-10 安徽工程大学 Feeding device for grinding miller
CN104998732A (en) * 2015-08-14 2015-10-28 无锡乐华自动化科技有限公司 Chinese herbal medicine pulverizer
CN111530554A (en) * 2020-05-13 2020-08-14 王永安 Color paste grinding and processing device
JP2020142159A (en) * 2019-03-04 2020-09-10 増幸産業株式会社 Mill with circulation path
CN114798079A (en) * 2022-04-21 2022-07-29 攀枝花瑞峰水泥有限公司 Combined grinding system with strong adaptability and transformation method thereof

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007105559A (en) * 2005-10-11 2007-04-26 Sanyo Electric Co Ltd Mill
CN102380454A (en) * 2011-09-22 2012-03-21 栾清杨 Winnowing device of solid wastes
CN104689877A (en) * 2014-08-10 2015-06-10 安徽工程大学 Feeding device for grinding miller
CN104998732A (en) * 2015-08-14 2015-10-28 无锡乐华自动化科技有限公司 Chinese herbal medicine pulverizer
JP2020142159A (en) * 2019-03-04 2020-09-10 増幸産業株式会社 Mill with circulation path
CN111530554A (en) * 2020-05-13 2020-08-14 王永安 Color paste grinding and processing device
CN111530554B (en) * 2020-05-13 2022-01-14 王永安 Color paste grinding and processing device
CN114798079A (en) * 2022-04-21 2022-07-29 攀枝花瑞峰水泥有限公司 Combined grinding system with strong adaptability and transformation method thereof
CN114798079B (en) * 2022-04-21 2024-03-19 攀枝花瑞峰水泥有限公司 Combined grinding system with high adaptability and transformation method thereof

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