JPS58214355A - Electromagnetic type crushing processing device - Google Patents

Electromagnetic type crushing processing device

Info

Publication number
JPS58214355A
JPS58214355A JP9556082A JP9556082A JPS58214355A JP S58214355 A JPS58214355 A JP S58214355A JP 9556082 A JP9556082 A JP 9556082A JP 9556082 A JP9556082 A JP 9556082A JP S58214355 A JPS58214355 A JP S58214355A
Authority
JP
Japan
Prior art keywords
chamber
crushing
pulverization
electromagnetic
stage
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
JP9556082A
Other languages
Japanese (ja)
Inventor
鶴田 和博
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
Fuji Electric Corporate Research and Development Ltd
Fuji Electric Manufacturing 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 Fuji Electric Co Ltd, Fuji Electric Corporate Research and Development Ltd, Fuji Electric Manufacturing Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP9556082A priority Critical patent/JPS58214355A/en
Publication of JPS58214355A publication Critical patent/JPS58214355A/en
Pending legal-status Critical Current

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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】 この発明は例えばもみがら等のかさ密度の小さな砕料を
微粉砕するのに好適な電磁式粉砕処理装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electromagnetic pulverization apparatus suitable for pulverizing grains having a small bulk density, such as rice husks.

ライスセンタ等で発生する多量のもみがらは。Large amounts of rice husks are generated at rice centers, etc.

近年になりその活用法として、74μm程度にまで微粉
砕処理した上で樹脂系素材のフィラーに使用する、ある
いはコンポストの湿度調整材料としての活用法が注目さ
れつつあり、一部にはその専用機も実用化されている。
In recent years, attention has been focused on ways to utilize it, such as pulverizing it to about 74 μm and using it as a filler for resin materials, or as a humidity control material for compost, and some have specialized machines for this purpose. has also been put into practical use.

かかるもみがら粉砕処理に使用されている従来機は、第
1図に示すごとき機械式の衝撃粉砕機であって、ケーシ
ング1の内部には回転駆動される粉砕刃伺きのランナ2
を備えており、砕料入口3か−ら送り込凍れたもみがら
がケーソング内でランナ2により細かく粉砕され、出口
4を通じて砕料として取り出濱れる。しかして、もみが
らは殻の表面が硬く、かつ全体としては繊維組成である
ために柔軟性にも富んでいて粉砕処理が仲々困難であり
、第1図の粉砕機では粉砕刃の摩耗が早く進み、長期に
わたり安定よく微細粒度の砕製物を得ることができない
難点がある。このために膨軟化処理と称して、前段処理
でもみがらに水分を加え。
The conventional machine used for this rice husk crushing process is a mechanical impact crusher as shown in FIG.
Frozen rice husks are sent in from a pulverizing material inlet 3 and are finely pulverized by a runner 2 in the case song, and taken out as pulverized material through an outlet 4 and collected. However, rice husks have a hard surface and are made of fibers, making them very flexible and difficult to crush.In the crusher shown in Figure 1, the crushing blades wear out quickly. The problem is that it is not possible to stably obtain a crushed product with a fine particle size over a long period of time. For this purpose, moisture is added to the rice hulls in the first stage of processing, which is called swelling and softening processing.

加熱、圧縮した状態で粉砕機へ送り込む方法も実施され
ているが、この方法では粉砕性能は高くなるが粉砕後に
改めて水分を除くための乾燥操作が必要になる等、工程
が複雑となる。このために先に述べた機械式粉砕機に代
る粉砕性能、効率の良いもみがら粉砕機の出現が望まれ
ている。
Another method is to feed the powder into a pulverizer in a heated and compressed state, but although this method improves pulverization performance, it requires a drying operation to remove moisture after pulverization, making the process complicated. For this reason, there is a desire for a rice husk crusher with good crushing performance and efficiency to replace the mechanical crusher mentioned above.

一方最近になシ、移動磁界を使ってワーキングピースに
電磁力を働かせて砕料を処理する新しい電磁式粉砕機が
開発されている。次にこの粉砕機の構成、原理を第2図
および第3図について述べる。図において、5は被処理
物としての砕料6とともに強磁性材あるいは非磁性導電
材で作られた多数のワーキングピース7を収容した処理
容器であり、この容器5を中央に挾んでその両側にはい
わゆるリニアモータとしてよく知られた移動磁界発生装
置8と9が対向配置されており、かつその移動磁界φ8
.φ、は互に逆向きに定めである。
On the other hand, recently, a new electromagnetic crusher has been developed that uses a moving magnetic field to apply electromagnetic force to a working piece to process crushed materials. Next, the structure and principle of this crusher will be described with reference to FIGS. 2 and 3. In the figure, reference numeral 5 denotes a processing container that houses a large number of working pieces 7 made of ferromagnetic or non-magnetic conductive material along with crushed material 6 as the object to be processed. The moving magnetic field generators 8 and 9, which are well known as so-called linear motors, are arranged opposite each other, and the moving magnetic field φ8
.. φ, are defined in opposite directions.

かかる構成によυ、移動磁界φ1.φ、の作用する磁場
に置かれたワーキングピース7には磁化。
With this configuration, υ, moving magnetic field φ1. The working piece 7 placed in the magnetic field affected by φ is magnetized.

渦電流が生じ、移動磁界との相互作用に基づく電磁力が
働く。これによりワーキングピース7は移動磁界方向へ
の並進力、浮上刃、および重心のまわシに自転する磁気
トルクを受け、更にはワーキングピース同士の衝突、ワ
ーキングピースと容器壁との衝突が加わり、容器5の中
で複雑かつ激しいランダム運動を生起する。そしてこの
ランダム運動によって砕料6は衝撃粉砕、摩擦粉砕され
ることになる。
Eddy currents are generated and electromagnetic forces act due to interaction with the moving magnetic field. As a result, the working piece 7 is subjected to a translational force in the direction of the moving magnetic field, a rotating magnetic torque around the floating blade, and the center of gravity, and furthermore, collisions between the working pieces and collisions between the working pieces and the container wall are added, and the container 5, causing complex and intense random motion. This random movement causes the crushed material 6 to be crushed by impact and friction.

この電磁式粉砕機は第1図に示した在来の機械式粉砕機
と異なり、ワーキングピースのランダム運動で粉砕を行
うものであって、粉砕刃の摩耗等の問題がなく長期にわ
たって安定した粉砕性能が得られ、かつ粉砕処理時間も
短かくて済む。発明者の行った実験によれば、この電磁
式粉砕機を用いてもみがらを粉砕処理したところ、第1
図の粉砕機と較べてその粉砕処理時間も短かくて済み。
This electromagnetic pulverizer differs from the conventional mechanical pulverizer shown in Figure 1 in that it pulverizes by random movement of the working pieces, which eliminates problems such as wear of the pulverizing blades and provides stable pulverization over a long period of time. Performance can be obtained and the pulverization processing time can be shortened. According to experiments conducted by the inventor, when rice husks were crushed using this electromagnetic crusher, the first
Compared to the crusher shown in the figure, the crushing time is shorter.

かつ微粉砕も可能であることが確められている。It has also been confirmed that fine pulverization is also possible.

しかしながらこのように粉砕性能の良い電磁式粉砕機を
用いてもみがらを粉砕処理する場合にも砕料6を同じ室
の中で粗粉砕から微粉砕まで継続して粉砕を行うバッチ
方式では、運転効率およびその他の面でのS点がある。
However, even when pulverizing rice hulls using an electromagnetic pulverizer with good pulverizing performance, the batch method in which the pulverized material 6 is continuously pulverized from coarse to fine pulverization in the same chamber is not suitable for operation. There is an S point in terms of efficiency and other aspects.

それはもみがらのかさ密度が0.12t/−と極めて小
さく、運転開始当初に適正な充填率でもみがらをワーキ
ングピース7と一諸に処理容器5へ収容して運転を開始
すると、僅かな時間で粗粉砕されたもみがらのかさは頭
初の充填量の1/2ないし1/4に減じるため、その後
の微粉砕までの運転は処理容器5の容積に比して砕料6
が少ない低充填率のままでの運転が強いられることにな
る。しかもこの期間中もワーキングピースの駆動を行う
ために電磁式粉砕機に給電を行う必要があし、このため
に粉砕機の処理容量から見た利用効率および、消電電力
量に対する運転効率を低める結果となる。また砕料を同
じ室内で所望の微細粒径になるまで継続的に粉砕動作を
行うと、砕料の一部は過粉砕され、これによって生じた
超微粉が粉砕の継続の障害物として働き、その後の粉砕
効率を急激に低下させて粉砕エネルギーの損失増加を招
く。
The bulk density of the rice husks is extremely small at 0.12 t/-, and if the rice husks are stored together with the working piece 7 in the processing container 5 at an appropriate filling rate at the beginning of the operation, it will take only a short time. Since the bulk of the coarsely crushed rice husks is reduced to 1/2 to 1/4 of the initial filling amount, the subsequent operation up to fine pulverization requires only 6 crushed grains compared to the volume of the processing container 5.
This means that they will be forced to operate at a low filling rate. Moreover, during this period, it is necessary to supply power to the electromagnetic crusher in order to drive the working pieces, which results in lower utilization efficiency in terms of the crusher's processing capacity and operating efficiency in terms of power consumption. Become. Furthermore, if the crushed material is continuously crushed in the same room until it reaches the desired fine particle size, a portion of the crushed material will be over-pulverized, and the resulting ultra-fine powder will act as an obstacle to the continuation of the crushing. The subsequent grinding efficiency is rapidly reduced, leading to increased loss of grinding energy.

この発明は上記の点にかんがみなされたものであり、そ
の目的は前記の電磁式粉砕機による粉砕処理時の問題点
を解決し、運転効率、粉砕効率の向上を図った電磁式粉
砕処理装置を提供することにある。
This invention has been made in consideration of the above points, and its purpose is to solve the problems encountered during the pulverization process using the electromagnetic pulverizer, and to provide an electromagnetic pulverization device that improves operating efficiency and pulverization efficiency. It is about providing.

かかる目的はこの発明により、互に移動磁界方向を互向
きに定めて対向配置された一対の移動磁界発生装置の間
の磁場に置かれた処理容器にそれぞれ入口、出口を有す
る複数段の粗粉砕用および微粉砕用の粉砕室を仕切り、
かつ各段の粉砕室の相互間を粗粉砕室から微粉砕室の順
に連ねて気流搬送式の砕料搬送ダクトを接続するとと4
に、各段の粉砕室ごとにその入口側には各室内に収容さ
れたワーキングピースの飛び出しを防ぐスクリーンを、
出口側にはその粉砕室に対応した分級ふるいを装備し、
前記搬送ダクトを通じて搬送気流により砕料を連続的に
送り込み、粗粉砕および微粉砕工程を経て砕製物を得る
ように構成したことにより達成される。
This purpose is achieved by the present invention, which provides a multi-stage coarse pulverizer having an inlet and an outlet, respectively, in a processing container placed in a magnetic field between a pair of moving magnetic field generators arranged oppositely with the directions of the moving magnetic fields set to be mutually directed. Separate the grinding chamber for grinding and fine grinding.
And if the grinding chambers of each stage are connected in the order from the coarse grinding chamber to the fine grinding chamber and connected with an air flow conveying type powder conveying duct, the result is 4.
In addition, a screen is installed on the entrance side of each stage of the grinding chamber to prevent the working pieces stored in each chamber from flying out.
The exit side is equipped with a classification sieve that corresponds to the crushing chamber.
This is achieved by constructing a structure in which the crushed material is continuously fed through the conveying duct by means of a conveying air stream, and a crushed product is obtained through coarse crushing and fine crushing steps.

以下この発明を図示実施例に基づいて説明する。The present invention will be explained below based on illustrated embodiments.

第4図および第5図において、左右に対向位置する一対
の移動磁界発生装置8と9の間に挾まれてその磁場内に
置れた処理容器5には、その内部に中仕切板を設けて上
段よシ粗粉砕室51.中粉砕室5■、微分砕室5III
の順に複数段の粉砕室が仕切られている。また各段の粉
砕室51〜5nIはその前後面を開口して砕料入口、出
口となすとともに、これ等各室の相互間を1段目の粗粉
砕室5■から中、微粉砕室5n、5111の順に連ねて
、砕料投入ホッパト0から砕製物回収容器11に到る間
に気流搬送式の砕料搬送ダクト12が配管されている。
In FIGS. 4 and 5, a processing container 5 placed between a pair of moving magnetic field generators 8 and 9 facing each other on the left and right and placed in the magnetic field is provided with an internal partition plate. Move to the upper stage and move to the coarse grinding chamber 51. Medium crushing chamber 5■, differential crushing chamber 5III
A plurality of stages of crushing chambers are partitioned in this order. In addition, the grinding chambers 51 to 5nI of each stage have their front and back surfaces opened to form the inlet and outlet of the crushed material, and the spaces between these chambers are connected from the coarse grinding chamber 5 of the first stage to the medium and fine grinding chambers 5n. , 5111, an airflow conveying type crushed material conveying duct 12 is piped between the crushed material input hopper 0 and the crushed material recovery container 11.

この搬送ダクト12は図示のように入口ダクト12人、
出口ダクト12B、および中継ダクト12C,12D 
 とで構成されている。この場合に粉砕室51〜5■の
入口、出口の向きは1段目の室5■から交互に逆向きに
定めてあり、互に隣り合う粉砕室の相互間では前段室の
出口と後段室の入口との間がU字形の中継ダク)12C
,12D を介して接続されている。また処理容器5に
戻り、各段の粉砕室51,511,5I[1の入口には
各室内に収容されているワーキングピース71,7TJ
As shown in the figure, this conveyance duct 12 has an entrance duct for 12 people,
Outlet duct 12B, and relay ducts 12C, 12D
It is made up of. In this case, the directions of the inlets and outlets of the crushing chambers 51 to 5■ are alternately set in opposite directions from the first stage chamber 5■, and between the adjacent crushing chambers, the outlet of the front stage chamber and the outlet of the rear stage chamber are set in opposite directions. (U-shaped relay duct between the entrance and the entrance) 12C
, 12D. Returning to the processing container 5, the working pieces 71, 7TJ accommodated in each chamber are placed at the entrance of each stage of the crushing chambers 51, 511, 5I [1].
.

7mの飛び出しを防ぐスクリーン13が、−刃出口には
粗、中、微粉砕用の各室51,5■、5111ごとにそ
れぞれ異なるメツシュ目に定めた分級ふるい141.1
411.14m がそれぞれ装備されている。このふる
いは1段目のふるい141  のメツシュ目が最も粗で
あり、141.14111 の順に目が細かくなってい
る。更に各段の粉砕室51.5m。
There is a screen 13 that prevents 7m from flying out, and a classification sieve 141.1 with a different mesh size for each chamber 51, 5, 5111 for coarse, medium, and fine pulverization at the blade outlet.
411.14m each. This sieve has the coarsest mesh of the first sieve 141, and the mesh becomes finer in the order of 141.14111. Furthermore, each stage of grinding chamber is 51.5m long.

5川の室内空間の容積も1段目を基準に2段目。The volume of the interior space of the 5 rivers is also based on the 2nd tier, based on the 1st tier.

3段目の順に小さくなるようにその断面積を順次狭めで
ある。更に加えて前記の中継ダクト12C112Dには
、その端面に中間砕製物取出用の開閉扉151.15■
 が設けである。なお16はホッパ10と並べてダク)
12Aの入口側、および各中継ダク)12C,12D 
の中にそれぞれ配置された送風ファンであり、これ等送
風ファンを運転することにより1点線矢印のように各段
の粉砕室5■〜5川の中を通って搬送ダクト12に流れ
る砕料搬送気流が生じる。
The cross-sectional area is gradually narrowed so that it becomes smaller in the order of the third stage. In addition, the relay duct 12C112D has an opening/closing door 151.15 on its end surface for taking out intermediate crushed products.
is the provision. Note that 16 is placed side by side with hopper 10)
12A entrance side and each relay duct) 12C, 12D
By operating these fans, the crushed material is transported through the crushing chambers 5 to 5 of each stage to the transport duct 12 as indicated by the dotted line arrows. An air current is generated.

次に上記構成の粉砕処理装置における砕料、粉砕動作に
ついて述べる。まず予じめ各段の粉砕室51.511.
5111にはそれぞれ粗粉砕、中粉砕。
Next, the crushed material and the crushing operation in the crushing apparatus having the above configuration will be described. First, each stage of crushing chamber 51.511.
5111 has coarse grinding and medium grinding, respectively.

微粉砕に適した寸法、形状のワーキングピース71.7
11,7111が収容されている。次に移動磁界発生装
置8.9および各ファン】6を運転した状態で、ホッパ
10へもみがら等の砕料6を投入すれば、搬送気流に乗
ってまず未粉砕の砕料6が1段目の粗粉砕室5Iへ送シ
込まれ、ここでワーキングピース7Iのランダム運動に
よって粗粉砕される。室5Iで所定の粒径まで粗粉砕さ
れた粗粉は、搬送気流によって分級ふるい14Iを透過
し、次いで中継ダク)12Cを経由して2段目の中粉砕
室5■に送り込まれ、ここで更に細かく粉砕される。次
に分級ふるい1411を透過した砕料は終段の微粉砕室
5■へ導入され、ここで微粉砕される。最後に最も細か
いメツシュ目の分級ふるい1411を通過し得た微粉が
砕製物17として回収容器11に排出される。なお上記
の粉砕動作は運転中に連続して行われる。また必要によ
り、運転の途中で開閉J%151あるいは1511を開
放すると、この扉開口部を通じて粗粉砕段階あるいは中
粉砕段階まで粉砕が進んだ粒径以下の砕製物を抽出する
ことが可能である。なお図示例は処理容器5を3股の室
に区分した例を示したが、2段あるいは4段以上に分け
て実施することもできる。
Working piece 71.7 with dimensions and shape suitable for fine grinding
11,7111 are accommodated. Next, when the moving magnetic field generator 8.9 and each fan 6 are in operation, if crushed material 6 such as rice husks is put into the hopper 10, the unpulverized crushed material 6 will be transported to the first stage by the conveying airflow. It is fed into the coarse grinding chamber 5I, where it is coarsely ground by random movement of the working piece 7I. The coarse powder coarsely ground to a predetermined particle size in the chamber 5I is passed through the classification sieve 14I by the conveying air current, and then sent to the second stage medium grinding chamber 5■ via the relay duct) 12C, where it is It is further finely ground. Next, the crushed material that has passed through the classification sieve 1411 is introduced into the final stage pulverization chamber 5■, where it is pulverized. Finally, the fine powder that has passed through the finest mesh classification sieve 1411 is discharged into the recovery container 11 as a crushed product 17. Note that the above-mentioned crushing operation is performed continuously during operation. Furthermore, if necessary, by opening the opening/closing J% 151 or 1511 during operation, it is possible to extract crushed products with a particle size smaller than the particle size that has been pulverized to the coarse or medium pulverization stage through this door opening. . Although the illustrated example shows an example in which the processing container 5 is divided into three chambers, it can also be divided into two or four or more stages.

上記の装置によれば、まず粉砕動作過程で、粉砕の進行
につれてもみがら等のかさ密度の小さな砕料6Fi順次
そのかさ密度の増加、つまり見かけ上の体積が′減少す
るが、先述のように各段の粉砕室51,511,5]1
fの容積をこの順に小さくなるように予め定めておくこ
とにより、砕料の見かけ上の体積減少分に合わせて各段
の粉砕室は殆ど過不足なく常に適量の砕料で満たされる
。したがって処理容器5の各室内空間がすべて有効に使
われることになり、これにより運転効率の向上が図れる
。更に各段の粉砕室で所定の粒径にまで粉砕された砕料
はいつ1でも同じ室内に止まってなく、素早や〈分級ふ
るいを透過して後段の粉砕室へ向けて排出されるので、
過粉砕の生じる度合が少なくなシ、シたがって粉砕動作
の継続罠支障を与えることがなくて高い粉砕効率を維持
できるし、また過粉砕に伴う粉砕エネルギーの浪費も未
然に防止されることになる。加えて図示例のように前段
粉砕室と後段粉砕室との中間位置で砕料搬送ダクトの途
中に開閉扉15i、1511  を設けたことにより、
必要によシ各種籾径の砕製品を抽出して取シ出すことが
できる。
According to the above-mentioned apparatus, first, in the process of crushing, as the crushing progresses, the bulk density of the crushed material 6Fi, such as rice husks, with a small bulk density increases, that is, the apparent volume decreases, but as mentioned earlier, Grinding chambers 51, 511, 5]1 in each stage
By predetermining the volume of f so that it decreases in this order, the crushing chambers of each stage are always filled with an appropriate amount of crushed material, with almost no excess or deficiency, in accordance with the apparent volume reduction of the crushed material. Therefore, all the indoor spaces of the processing container 5 are effectively used, thereby improving operational efficiency. Furthermore, the crushed material crushed to a predetermined particle size in each stage of the crushing chamber does not remain in the same chamber at all times, but quickly passes through the classification sieve and is discharged to the subsequent crushing chamber.
The degree of over-grinding is small, so there is no hindrance to the continuation of the crushing operation, and high crushing efficiency can be maintained, and the wastage of crushing energy due to over-grinding is also prevented. Become. In addition, as shown in the illustrated example, by providing opening/closing doors 15i, 1511 in the middle of the crushed material conveying duct at an intermediate position between the front-stage crushing chamber and the rear-stage crushing chamber,
If necessary, crushed products of various diameters of rice can be extracted and taken out.

以上述べたようにこの発明によれば、高運転効率、高粉
砕効率を図シつつ砕料の連続粉砕処理が行え、砕料処理
能力および粉砕性能の優れた電磁式粉砕処理装置を提供
することができる。
As described above, according to the present invention, it is possible to provide an electromagnetic pulverization device that can perform continuous pulverization of granules while achieving high operating efficiency and high pulverization efficiency, and has excellent granulation processing capacity and pulverization performance. I can do it.

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

第1図は在来の機械式粉砕機の構成断面図、第2図は電
磁式粉砕機の構成原理図、第3図は第2図の矢視III
−III断面図、第4図はこの発明の実施例の略示構成
図、第5図は第4図の矢視■−■断面図である。 5・・・処理容器、51〜5■・・・粉砕室、6・・・
砕料、7.71〜’7111・・・ワーキングピース、
8.9・・・移動磁界発生装置、12・・・砕料搬送ダ
ク)、13・・・スクリーン、141〜1411I・・
・分級ふるい。 151.1511・・・開閉扉、16・・・送風ファン
、17・・・砕製物。 才1 口 才2胆       −73t8 才S口
Figure 1 is a sectional view of the configuration of a conventional mechanical crusher, Figure 2 is a diagram of the configuration principle of an electromagnetic crusher, and Figure 3 is a view taken in the direction of arrow III in Figure 2.
-III sectional view, FIG. 4 is a schematic configuration diagram of an embodiment of the present invention, and FIG. 5... Processing container, 51~5■... Grinding chamber, 6...
Grinding material, 7.71~'7111...working piece,
8.9... Moving magnetic field generator, 12... Granule transport duct), 13... Screen, 141-1411I...
・Classifying sieve. 151.1511...Opening/closing door, 16...Blower fan, 17...Crushed product. Sai 1 Mouth Sai 2 Bold -73t8 Sai S Mouth

Claims (1)

【特許請求の範囲】 1)磁性材あるいは非磁性導電材で作られた多数のワー
キングピースが収容された処理容器内に砕料を送シ込み
、この処理容器へ外部から移動磁界を作用させることに
より、移動磁界との相互作用に基づく電磁力でワーキン
グピースにランダム運動を生起させて砕料を粉砕処理す
る電磁式粉砕処理装置において、互に移動磁界方向を逆
向きに定めて対向配置された一対の移動磁界発生装置の
間の磁場に置かれた処理容器にそれぞれに入口、出口を
有する複数段の粗粉砕用および微粉砕用の各粉砕室を仕
切凱かっ各段の粉砕室の相互間を粗粉砕室から微粉砕室
の順に直列に連ねて気流搬送式の砕料搬送ダクトを接続
するとともに、各段の粉砕室ごとにその入口側には各室
内に収容されたワーキングピースの飛び出しを防ぐスク
リーンf:、出口側にはその粉砕室に対応した分級ふる
いを装備し、前記搬送ダクトを通じて気流搬送により砕
料を連続的に送シ込み、粗粉砕および微粉砕工程を経て
砕製物を得るようにしたことを特徴とする電磁式粉砕処
理装置。 2、特許請求の範囲第1項記載の粉砕処理装置において
、各段の粉砕室はその容積が1段目の粗粉砕室から順に
次第に小さくなるように画成されていることを特徴とす
る電磁式粉砕処理装置。 3)%許請求の範囲第1項または第2項記載の粉砕処理
装置において、処理容器に画成された各粉砕室の入口、
出口の向きを交互に逆向きに定め、かつ互に隣接し合う
前段室の出口と後段室の入口との相互間がU字形の中継
ダクトで接続されていることを特徴とする電磁式粉砕処
理装置。 4)特許請求の範囲第3項記載の粉砕処理装置において
、中継ダクトに中間砕製物取出用の開閉扉が設置されて
いることを特徴とする電磁式粉砕処理装置。
[Claims] 1) Particles are fed into a processing container containing a large number of working pieces made of magnetic or non-magnetic conductive materials, and a moving magnetic field is applied to the processing container from the outside. In an electromagnetic pulverization device that uses electromagnetic force based on the interaction with a moving magnetic field to generate random motion in a working piece to pulverize crushed materials, two pieces are placed facing each other with the directions of the moving magnetic fields set in opposite directions. A processing container placed in a magnetic field between a pair of moving magnetic field generators is partitioned into multiple stages of grinding chambers for coarse grinding and fine grinding, each having an inlet and an outlet. are connected in series from the coarse grinding chamber to the fine grinding chamber, and are connected to an air flow conveyance type powder conveying duct, and the working pieces stored in each chamber are ejected from the entrance side of each stage of the crushing chamber. Preventing screen f: The exit side is equipped with a classification sieve corresponding to the crushing chamber, and the crushed material is continuously fed through the conveying duct by air flow conveyance, and the crushed material is processed through coarse crushing and fine crushing processes. An electromagnetic crushing device characterized by: 2. The pulverization processing apparatus according to claim 1, characterized in that the pulverization chambers in each stage are defined so that their volumes gradually decrease from the coarse pulverization chamber in the first stage. Type crushing equipment. 3) In the pulverization processing apparatus according to claim 1 or 2, an inlet of each pulverization chamber defined in the processing container;
An electromagnetic crushing process characterized in that the exit directions are alternately set in opposite directions, and the exits of the front chamber and the entrance of the rear chamber which are adjacent to each other are connected to each other by a U-shaped relay duct. Device. 4) An electromagnetic crushing device according to claim 3, characterized in that the relay duct is provided with an opening/closing door for taking out intermediate crushed products.
JP9556082A 1982-06-03 1982-06-03 Electromagnetic type crushing processing device Pending JPS58214355A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9556082A JPS58214355A (en) 1982-06-03 1982-06-03 Electromagnetic type crushing processing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9556082A JPS58214355A (en) 1982-06-03 1982-06-03 Electromagnetic type crushing processing device

Publications (1)

Publication Number Publication Date
JPS58214355A true JPS58214355A (en) 1983-12-13

Family

ID=14140968

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9556082A Pending JPS58214355A (en) 1982-06-03 1982-06-03 Electromagnetic type crushing processing device

Country Status (1)

Country Link
JP (1) JPS58214355A (en)

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