JPS6155427B2 - - Google Patents
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- Publication number
- JPS6155427B2 JPS6155427B2 JP55071213A JP7121380A JPS6155427B2 JP S6155427 B2 JPS6155427 B2 JP S6155427B2 JP 55071213 A JP55071213 A JP 55071213A JP 7121380 A JP7121380 A JP 7121380A JP S6155427 B2 JPS6155427 B2 JP S6155427B2
- Authority
- JP
- Japan
- Prior art keywords
- sorting
- channel
- electrode
- trough
- 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.)
- Expired
Links
Landscapes
- Electrostatic Separation (AREA)
Description
【発明の詳細な説明】
この発明は被選別物質の電気的性質の差および
静電的なクーロン力を利用して被選別物質を選別
精製する静電選別装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electrostatic separation device that uses differences in electrical properties of substances to be sorted and electrostatic Coulomb force to select and refine substances to be sorted.
最近になり都市ごみの中の厨芥成分をコンポス
トとして再利用することが実用化され始めてい
る。このための方法としては、先ず廃棄物処理プ
ラントに搬入されて来た都市ごみのうち、金属
類、ガラス、瓦礫、土砂、プラスチツク類を分類
選別して取除いた残りの生ごみを細かく粉砕して
コンポスト化装置へ送り込んでコンポスト化させ
る。またかかるコンポスト化装置では、予備発
酵,後熟発酵の工程を経て生ごみを完熟したコン
ポストに変え、更に振動篩などによる精製工程を
経てコンポスト製品を得る。しかして後熟工程を
終つて出て来るコンポストは、原料の有機物が十
分に腐敗分解して土塊状にかたまつた細かい粒状
の純粋コンポストと、腐敗分解が十分に進んでな
い成分と、その他原料に混入して来たガラス、プ
ラスチツク、瓦礫などの夾雑物との混合物であ
る。このうち腐敗分解が十分に進まなかつた大き
な塊成分、ないしは寸法の大きな夾雑物は振動篩
で分級選別できるが、純粋なコンポストと同様に
数ミリ程度に細かく粉砕された夾雑物はそのまま
篩の目を通り抜けてコンポストに混在することに
なる。このように分級選別工程を経たコンポスト
に混在する夾雑物は通常僅かに数%程度である
が、それでも農地には好ましくなく、できる限り
取除いて精製する必要があるが、篩などによる機
械的な分別選別方法では、更に細かい夾雑物だけ
を取除いてコンポストをこれ以上精製することは
極めて困難である。 Recently, the reuse of kitchen waste in municipal waste as compost has begun to be put to practical use. The method for this purpose is to first sort and separate metals, glass, rubble, sand, and plastics from the municipal waste brought into the waste treatment plant, and then finely crush the remaining garbage. The waste is then sent to a composting device and composted. In addition, in such a composting apparatus, food waste is converted into fully ripened compost through the processes of preliminary fermentation and post-fermentation, and then a compost product is obtained through a purification process using a vibrating sieve or the like. However, the compost that comes out after completing the post-ripening process is fine granular pure compost in which the raw organic matter has sufficiently decayed and decomposed and hardened into lumps of soil, components that have not sufficiently decayed and decomposed, and other raw materials. This is a mixture of foreign substances such as glass, plastic, and debris that have come into the environment. Of these, large lump components that have not fully decomposed or large-sized impurities can be classified and sorted using a vibrating sieve, but as with pure compost, impurities that have been finely ground to a few millimeters are passed through the sieve as is. It will pass through and be mixed into the compost. Although the amount of impurities mixed in the compost that has gone through the classification and sorting process is usually only a few percent, it is still undesirable for farmland and needs to be removed and purified as much as possible. Using the separate sorting method, it is extremely difficult to further refine the compost by removing only the finer impurities.
この発明は上述のように分級精製工程を経た後
のコンポストから更に細かな夾雑物を取除いてコ
ンポストの品質を高めることを主眼とする静電選
別装置に関するものである。 The present invention relates to an electrostatic sorting device whose main purpose is to improve the quality of compost by removing finer impurities from the compost after the classification and purification process as described above.
静電選別の原理は周知であり、今迄にも各種方
式の静電選別装置が提案され、また各産業分野で
実用化されている。このうち鉱石,食品粉体の精
製に使用されている代表的な静電選別装置の原理
図を第1図に示す。該装置は回転ドラム1を一方
の接地電極としてこの側方に高電圧を印加するコ
ロナ放電電極2が対向配置され、更にドラム1の
上方には被選別混合物Mをドラム1へ供給するた
めの供給ホツパ付きフイーダ3が、ドラム1の下
方には捕集ホツパ4,5がそれぞれ配置されてい
る。なお6はドラム1の周面を摺動するブラシの
ごときスクレーパである。かかる装置の動作原理
は良く知られているところであり、ここでは動作
を簡単に述べる。先ず被選別混合物が先述したコ
ンポストである場合を例にして述べるに、被選別
混合物Mはガラス,プラスチツク類の白丸で示す
絶縁性粒子Nと、比較的高い含水率を有するため
に導電性をもつコンポストの黒丸で示す導電性粒
子Oとの混合物である。一方、コロナ放電電極2
とドラム1との間の空間には強い電界がかかつて
おり、ドラム1へ向けてコロナ電流が流れてい
る。従つてフイーダ3よりドラム1の上へ供給さ
れた夾雑物を含むコンポストが強電界域へ到達す
ると、イオンシヤワーを浴びる。この過程で導電
性粒子Oである純粋コンポストはドラム1との接
触によつてイオンの電荷を放電し、逆に静電誘導
作用によりドラム電極と同極性に帯電し、円筒ド
ラム1との間で作用するクーロン力により反発し
て矢印Aのようにコンポスト回収用ホツパ5へ向
けて前方へ落下する。一方、絶縁性粒子Nである
ガラス、プラスチツク類の夾雑物はコロナ放電電
極2と同極性の電荷を受けて帯電し、ドラム1の
表面へ吸着されたままドラム1の回転とともに移
動し、やがて最下位近傍に達して自重により夾雑
物回収用ホツパ4へ矢印Bのように落下する。な
お自重が軽く吸着されたままのものはスクレーパ
6によつて強制的にかき落される。 The principle of electrostatic separation is well known, and various types of electrostatic separation devices have been proposed and put into practical use in various industrial fields. Figure 1 shows the principle of a typical electrostatic separation device used for refining ores and food powders. In this device, a rotating drum 1 is used as one ground electrode, and a corona discharge electrode 2 for applying a high voltage is placed on the side of the rotating drum 1, and a supply is provided above the drum 1 for supplying the mixture M to be sorted to the drum 1. A feeder 3 with a hopper is disposed below the drum 1, and collection hoppers 4 and 5 are disposed, respectively. Note that 6 is a scraper like a brush that slides on the circumferential surface of the drum 1. The principle of operation of such a device is well known, and its operation will be briefly described here. First, let us take as an example the case where the mixture to be sorted is the above-mentioned compost.The mixture to be sorted M has electrical conductivity because it has insulating particles N of glass and plastics shown by white circles and a relatively high water content. It is a mixture with conductive particles O shown in black circles of compost. On the other hand, corona discharge electrode 2
A strong electric field exists in the space between the drum 1 and the drum 1, and a corona current flows toward the drum 1. Therefore, when the compost containing impurities supplied from the feeder 3 onto the drum 1 reaches the strong electric field area, it is exposed to an ion shower. In this process, the pure compost, which is conductive particles O, discharges its ionic charge by contact with the drum 1, and conversely becomes charged to the same polarity as the drum electrode due to electrostatic induction, and is transferred between the cylindrical drum 1 and the conductive particles O. It is repulsed by the applied Coulomb force and falls forward toward the compost collection hopper 5 as shown by arrow A. On the other hand, contaminants such as glass and plastic, which are insulating particles N, receive charges of the same polarity as the corona discharge electrode 2 and are charged, and move with the rotation of the drum 1 while being adsorbed to the surface of the drum 1, and eventually reach the final stage. When it reaches the vicinity of the lower level, it falls into the foreign matter recovery hopper 4 as shown by arrow B due to its own weight. Incidentally, objects whose own weight is light and remain adsorbed are forcibly scraped off by the scraper 6.
ところで、上記した従来の静電選別では、多量
の被選別物、例えばコンポストを精製処理する場
合には、実用上次に述べるような難点がある。 By the way, the above-mentioned conventional electrostatic sorting has the following practical difficulties when purifying a large amount of material to be sorted, for example, compost.
(1) 処理能力が小さいこと、
先に述べたように夾雑物をドラムに吸着させて
取除くためには、これら夾雑物にコロナ放電によ
るイオンを荷電させる必要がある。このためには
フイーダからのコンポストの供給量を制限して、
ドラム上に夾雑物が一層状をなしてコロナ放電電
極へ向けて露呈させることが必要である。しかし
て、夾雑物を露呈させてドラム上に分布させるた
めにはフイーダからの供給量を十分に制限して夾
雑物とコンポストがドラム上で重ならないように
しなければならない。この点が原因して上記従来
の装置では回転ドラムの軸方向の単位長さ当りの
処理能力が小さく、実用化する場合には装置の大
きさが非常に大形になる。(1) The processing capacity is small. As mentioned earlier, in order to remove foreign matter by adsorption to the drum, it is necessary to charge the foreign matter with ions by corona discharge. To do this, limit the amount of compost supplied from the feeder,
It is necessary for the contaminants to form a layer on the drum and be exposed towards the corona discharge electrode. Therefore, in order to expose the foreign matter and distribute it on the drum, the amount of feeder must be sufficiently restricted so that the foreign matter and the compost do not overlap on the drum. Due to this point, the conventional apparatus described above has a small processing capacity per unit length in the axial direction of the rotating drum, and when put into practical use, the size of the apparatus becomes very large.
(2) 処理できる夾雑物の寸法、形状に制限がある
こと、
第2図に示すように絶縁性の夾雑物Nはドラム
1に付着して移動するが、プラスチツクス.フイ
ルム状の薄くて軽い細片では、細片上のプラスイ
オンq+とドラム表面のマイナスイオンq-とが引
き合う時の離隔距離dが小さいのでクーロン力が
大きく作用し、ドラムの下端に来ても自重で落ち
ることはない。しかし、ガラスなどの厚肉の細片
は離隔距離dが大きいために引き合うクーロン力
が少さく、しかも自重が重いためにドラムに付着
していることができず、直ちにドラムからすべり
落ちてしまつてコンポスト側のホツパへ落下し、
再びコンポストへ混入してしまうことがある。従
来の静電選別装置に関し、さらに特公昭32―5402
号公報に開示された下記のものが知られている。
即ち、傾斜せしめた上部電極と無端帯間に高電圧
を印加し、ホツパーより供給せる混合粒子を、上
部電極と無端帯間の電界、無端帯の遡上、および
成分粒子相互の干渉によつて生ずる撹拌、抑制、
制止、飛揚および積層の諸作用を利用し、各成分
粒子に固有な電気的飛揚力の大小によつて、傾斜
の下方および上方に移動させて、夫々を捕集する
ようにした無端帯遡上式静電選鉱装置である。本
装置においては、無端帯の進行方向上下で選別対
象物を分離回収するので回収線長が短く、1基当
りの処理量の大きさを問題にされるコンポストの
ような選別対象には不向きである。さらに処理量
の増大を図るために複数基上下方向に多段にする
場合にはホツパーが高電位を有するため上下方向
の絶縁距離が過大となつて、水平方向に多段にせ
ざるを得ず、設置面積の増大を免れないという欠
点があつた。(2) There are restrictions on the size and shape of contaminants that can be treated.As shown in Figure 2, insulating contaminants N adhere to the drum 1 and move, but plastics. In a thin and light strip like a film, the separation distance d when the positive ions q + on the strip and the negative ions q - on the drum surface are attracted to each other is small, so a large Coulomb force acts, and even when they reach the bottom of the drum, It won't fall under its own weight. However, thick pieces such as glass have a large separation distance d, so the Coulomb force that attracts them is small, and their own weight is heavy, so they cannot stick to the drum and immediately slide off the drum. It falls into the hopper on the compost side,
It may end up getting mixed into the compost again. Regarding conventional electrostatic sorting equipment, furthermore,
The following is known as disclosed in the above publication.
That is, a high voltage is applied between the inclined upper electrode and the endless belt, and the mixed particles supplied from the hopper are controlled by the electric field between the upper electrode and the endless belt, the running up of the endless belt, and the mutual interference of the component particles. resulting agitation, suppression,
An endless strip run-up system that utilizes the effects of restraint, flight, and stacking to move each component particle down and up the slope and collect it, depending on the magnitude of the electric flying force specific to each component particle. This is an electrostatic ore beneficiation device. Since this device separates and collects the objects to be sorted at the top and bottom of the endless belt in the direction of movement, the collection line length is short, making it unsuitable for sorting objects such as compost, where the amount of processing per unit is an issue. be. Furthermore, when multiple hoppers are stacked vertically in order to increase throughput, the insulation distance in the vertical direction becomes excessive because the hopper has a high potential. The disadvantage was that it was inevitable that there would be an increase in
本発明は上記の点にかんがみさされたものであ
り、上記従来の静電選別装置の難点を除去して、
処理能力が大きく、かつ選別できる夾雑物の形状
寸法の範囲が広い静電選別装置を提供することを
目的とする。 The present invention has been made in consideration of the above points, and eliminates the drawbacks of the conventional electrostatic sorting device described above.
It is an object of the present invention to provide an electrostatic sorting device that has a large processing capacity and a wide range of shapes and dimensions of contaminants that can be sorted.
次に第3図、第4図については本発明実施例の
構造並びに動作原理を述べる。各図において、1
0は第1図における回転ドラム1に相当する選別
ステージであり、該選別ステージ10はリング状
円板である選別板11の上面中央部に周方向に沿
つて内外周に2条の仕切フエンス12を設け、該
仕切フエンス間に樋状チヤンネル13を区画形成
したものとして成り、かつたて軸の回転軸14へ
上下複数段に並べて支承されている。上下各段の
選別ステージ10は回転軸14とともに駆動モー
タ15により減速機構を介して緩い速さで矢印C
方向に回転操作される。更に前記選別ステージ1
0に対し選別板11の周上に被選別混合物の供給
位置および選別回収位置を定め、この両位置間の
周方向領域には選別ステージ10を接地電極とし
て選別板の上方に直流高圧電極20が対向配置さ
れている。この高圧電極20は第5図に明示され
ているように同極性に充電される針状ないし細線
状のコロナ放電電極21と平板状電極22とを対
として1組と成し、かつ選別ステージ10の回転
方向Cに沿つて円状にコロナ放電電極21、平板
状電極22の順に配列するよう一組ないし複数組
が設置されている。一方前記した混合物供給位置
には被選別混合物Mを供給するフイーダ30の供
給口31が上方よりチヤンネル13に臨んで開口
している。また選別回収位置には絶縁性粒子Nの
回収用ホツパ40に連なる吸込管41を上方より
チヤンネル13に向けて開口配置するとともに、
選別板11の内外周の側方には導電性粒子Oの回
収用ホツパ50に連なる導管51が下方より開口
配置されている。また60は選別板11の内周お
よび外周域に片寄りして移送されて来た導電性粒
子Oを前記ホツパ50へ向けて掻き落すためのス
クレーパである。なお高圧電極20などの各部品
は上下各段の選別ステージごとにそれぞれ対向し
て設置されている。上記の多段式選別ステージの
組立体はカバーケース70の中に収容されてお
り、カバーケース70に取付けたブツシング71
を介して高圧電極20に高圧直流電源80が接続
されている。 Next, referring to FIGS. 3 and 4, the structure and operating principle of the embodiment of the present invention will be described. In each figure, 1
0 is a sorting stage corresponding to the rotating drum 1 in FIG. 1, and the sorting stage 10 has two partition fences 12 on the inner and outer peripheries along the circumferential direction at the center of the upper surface of the sorting plate 11, which is a ring-shaped disc. A trough-like channel 13 is formed between the partition fences, and is supported on a rotating shaft 14, which is a vertical shaft, in a plurality of vertical stages. The upper and lower sorting stages 10 are moved at a slow speed by an arrow C by a rotating shaft 14 and a drive motor 15 via a deceleration mechanism.
Rotation operation is performed in the direction. Furthermore, the sorting stage 1
0, a supply position and a sorting collection position of the mixture to be sorted are set on the circumference of the sorting plate 11, and a DC high voltage electrode 20 is installed above the sorting plate in the circumferential area between these two positions with the sorting stage 10 as a ground electrode. They are placed opposite each other. As clearly shown in FIG. 5, this high voltage electrode 20 is made up of a pair of a needle-like or thin wire-like corona discharge electrode 21 and a flat electrode 22, which are charged with the same polarity, and the sorting stage 10 One set or a plurality of sets of corona discharge electrodes 21 and flat plate electrodes 22 are arranged in a circular shape along the rotation direction C of the electrode. On the other hand, at the above-mentioned mixture supply position, the supply port 31 of the feeder 30 for supplying the mixture M to be sorted is opened facing the channel 13 from above. In addition, at the sorting and collection position, a suction pipe 41 connected to a hopper 40 for collection of insulating particles N is arranged with an opening toward the channel 13 from above,
On the sides of the inner and outer peripheries of the sorting plate 11, a conduit 51 connected to a hopper 50 for collecting conductive particles O is opened from below. Further, 60 is a scraper for scraping off the conductive particles O that have been transferred to the inner and outer peripheries of the sorting plate 11 toward the hopper 50 . Note that each component such as the high-voltage electrode 20 is installed facing each other in each of the upper and lower sorting stages. The assembly of the multistage sorting stage described above is housed in a cover case 70, and a bushing 71 attached to the cover case 70
A high voltage DC power supply 80 is connected to the high voltage electrode 20 via.
上記構成の一段を取出して円周方向に沿つて展
開した構成配置は第5図のごとく表わされ、更に
第5図の図中に記したないしの各部断面を示
すと第6図のようになる。 The arrangement of one stage of the above structure taken out and developed along the circumferential direction is shown in FIG. 5, and furthermore, when the cross sections of the parts indicated in FIG. Become.
次に第5図および第6図に照して本発明実施例
の選別動作について述べる。まず高圧直流電源8
0より高圧電極20へ電圧を印加すると、接地側
の選別ステージ10との間でコロナ放電電極21
の直下にはコロナ放電電界域が、また平板状電極
22の直下には強電界域がそれぞれ形成される。
この状態で選別ステージ10を矢印C方向に回転
操作し、かつ供給端において供給フイーダ30
よりチヤンネル13内へ頭述した純粋コンポスト
である導電性粒子Oと、夾雑物である絶縁性粒子
Nとが混合した被選別混合物Mを供給すれば、選
別ステージ10の回転移動に伴つてまず混合物M
がコロナ放電電界域に入ると、混合物Mはコロ
ナ放電電極21より多量のプラスイオンシヤワー
を浴びてプラス電荷q+を得る。この場合に絶縁
性粒子N(白丸で示す)はプラス電荷を長時間保
持するのでマイナス極性の選別ステージ10へ吸
着し、チヤンネル13内に閉じ込められたまま移
送される。これに対し導電性粒子O(黒丸で示
す)はイオンシヤワーを浴びて獲得したプラス電
荷を選別ステージ10へ放電し、逆に静電誘導に
よつてマイナス極性に帯電される。次いで回転が
進んで強電界域に入ると、絶縁性粒子Nはチヤ
ンネル内に吸着されたままであるのに対し、導電
性粒子Oは電界に沿つて作用するクーロン力によ
り選別ステージより反発して飛び上り、プラス極
性の平板状電極22へ向けて吸引衝突し、更に電
極22との接触により放電して電荷を失うと下方
へ落下して再び静電誘導作用によつてマイナス極
性に帯電するごとく、マイナス極性の帯電→平板
状電極への吸引→放電→落下のサイクルを繰返え
し、第6図のに明示されているように選別ステ
ージ10と平板状電極2との間で激しく上下往復
運動を繰返えし、遂には仕切フエンス12を乗り
越えてチヤンネル13より左右両側へ飛び出して
選別板11の内周側と外周側へ片寄りするように
集まつていく。また同時に前記粒子の上下運動に
より、チヤンネル13内に層をなして供給された
混合物Mは撹拌作用を受ける。したがつていまま
で層下に埋もれていた粒子も表面に露呈して次の
コロナ放電電界域および強電界域で電界に直
接さらされるようになり、全体が万遍なく静電選
別作用を受けるようになる。かくして選別ステー
ジ10の回転が進んで選別回収位置に至れば、絶
縁粒子Nがチヤンネル13内に止どまつているの
に対し、導電性粒子Oはチヤンネル外の内外周域
に振り分けられた分布状態となる。したがつて導
電性粒子Oは回収位置でスクレーパ60により
掻き落されて回収ホツパ50へ回収され、一方絶
縁性粒子Nは回収位置で例えばパグフイルタを
用いた回収ホツパ40へ吸引回収されることにな
る。上記の選別動作は上下各段の選別ステージご
とに平行して行われる。 Next, the sorting operation of the embodiment of the present invention will be described with reference to FIGS. 5 and 6. First, high voltage DC power supply 8
When a voltage is applied to the high voltage electrode 20 from 0, the corona discharge electrode 21
A corona discharge electric field region is formed directly below the plate electrode 22, and a strong electric field region is formed directly below the flat electrode 22.
In this state, the sorting stage 10 is rotated in the direction of arrow C, and the supply feeder 30 is
If the mixture M to be sorted, which is a mixture of the conductive particles O, which is pure compost, and the insulating particles N, which are impurities, is fed into the channel 13, as the sorting stage 10 rotates, the mixture will first be separated. M
When M enters the corona discharge electric field region, the mixture M is showered with a large amount of positive ions from the corona discharge electrode 21 and gains a positive charge q + . In this case, the insulating particles N (indicated by white circles) retain a positive charge for a long time, so they are attracted to the negative polarity sorting stage 10 and transported while being confined within the channel 13. On the other hand, the conductive particles O (indicated by black circles) discharge the positive charges acquired by being exposed to the ion shower to the sorting stage 10, and conversely are charged to negative polarity by electrostatic induction. Then, as the rotation progresses and enters the strong electric field region, the insulating particles N remain adsorbed within the channel, while the conductive particles O are repelled from the sorting stage by the Coulomb force acting along the electric field and fly away. It rises, attracts and collides with the flat electrode 22 of positive polarity, and further discharges due to contact with the electrode 22 and loses its charge, then falls downward and is charged to negative polarity again by electrostatic induction. The cycle of negative polarity charging → attraction to the flat electrode → discharge → falling is repeated, and as shown in FIG. This process is repeated, and the particles eventually climb over the partition fence 12 and jump out from the channel 13 to both the left and right sides, and gather toward the inner and outer peripheries of the sorting plate 11. At the same time, due to the vertical movement of the particles, the mixture M supplied in layers into the channel 13 is subjected to a stirring action. Therefore, the particles that were previously buried under the layer are exposed to the surface and are directly exposed to the electric field in the next corona discharge electric field area and strong electric field area, so that the entire particle is evenly subjected to the electrostatic sorting effect. become. In this way, when the rotation of the sorting stage 10 progresses and reaches the sorting and collection position, the insulating particles N remain in the channel 13, while the conductive particles O are distributed in the inner and outer circumferential regions outside the channel. becomes. Therefore, the conductive particles O are scraped off by the scraper 60 at the collection position and collected into the collection hopper 50, while the insulating particles N are sucked and collected at the collection position into the collection hopper 40 using, for example, a pug filter. . The above sorting operation is performed in parallel for each of the upper and lower sorting stages.
なお特殊なケースとして混合物Mに混入してい
る絶縁性粒子Nが導電性粒子Oに比較して比重の
大なる物質のみである場合には、コロナ放電電極
21を省略し平板状電極22のみで高圧電極20
を構成しても、比重の大きな粒子Nはクーロン力
にさからつてチヤンネル外へ飛び出ることがない
ので、先記実施例と同様な振り分け選別が可能で
ある。 As a special case, if the insulating particles N mixed in the mixture M are only substances with a higher specific gravity than the conductive particles O, the corona discharge electrode 21 may be omitted and only the flat electrode 22 may be used. High voltage electrode 20
Even with this structure, the particles N having a large specific gravity do not escape from the channel due to the Coulomb force, so that sorting can be performed in the same way as in the previous embodiment.
以上述べたように本発明は、たて軸のまわりに
回転操作される樋状チヤンネル付きの選別ステー
ジの上方に、選別ステージを相手方の電極として
高圧電極を対向配置し、かつ供給位置より樋状チ
ヤンネル内に被選別混合物を供給するとともに、
選別回収位置に粒子別の回収ホツパをそれぞれ樋
状チヤンネルの内、外に臨ませて配置構成し、被
選別混合物のうち絶縁性粒子を樋状チヤンネル内
に閉じ込めたまま、導電性粒子のみをクーロン力
に基づく選別ステージと高圧電極間での往復運動
によつて樋状チヤンネル外へ取り出して振り分け
選別するようにしたものである。したがつて導電
性粒子の運動に伴う混合物の撹拌効果により、層
をなして供給された被選別混合物の全体に万遍な
く静電選別が作用するので処理能力、選別効率の
向上化が図れるし、更に混合物のうち導電性粒子
のみをクーロン力によりはね飛ばしてチヤンネル
の外方へ取り出して選別するようにしたので、頭
記したコンポストの精製処理に用いる場合には絶
縁性夾雑物が混入することのない純粋コンポスト
のみを選別して精製できるなどの優れた効果が得
られる。加えて本発明においては、図示実施例の
ように選別ステージを上下多段式に構成すること
により、狭い空間を有効に活用して処理能力の大
きな装置をコンパクト化できる利点が得られる。 As described above, the present invention has a method in which a high-voltage electrode is disposed facing above a sorting stage with a trough-like channel that is rotatably operated around a vertical axis, with the sorting stage as the other electrode, and In addition to supplying the mixture to be sorted into the channel,
At the sorting and collection position, collection hoppers for each particle are arranged so as to face the inside and outside of the trough-like channel, and only the conductive particles are collected by coulombization while the insulating particles of the mixture to be sorted are confined within the trough-like channel. By reciprocating motion between a force-based sorting stage and a high-voltage electrode, the particles are taken out of the trough-like channel and sorted. Therefore, due to the stirring effect of the mixture caused by the movement of the conductive particles, electrostatic separation acts evenly on the entire mixture to be sorted, which is supplied in layers, thereby improving processing capacity and sorting efficiency. In addition, since only the conductive particles in the mixture are repelled by Coulomb force and taken out to the outside of the channel for sorting, insulating impurities are not mixed in when used for the compost purification process mentioned above. Excellent effects such as being able to select and refine only pure compost can be obtained. In addition, in the present invention, by configuring the sorting stage in an upper and lower multistage manner as in the illustrated embodiment, there is an advantage that a narrow space can be effectively utilized and an apparatus with a large processing capacity can be made compact.
なお本発明はいままで説明したコンポスト精製
分野以外の鉱物、食品、薬品などの粒状物を扱う
各種分野にも適用できることはもちろんである。 It goes without saying that the present invention can also be applied to various fields that handle granular materials such as minerals, foods, and medicines other than the field of compost refining described above.
第1図は従来における代表的な静電選別装置の
原理図、第2図は第1図における絶縁性粒子の吸
着作用の説明図、第3図および第4図は本発明実
施例の全体の構成配置を示す側面図および平面
図、第5図および第6図は本発明実施例の選別動
作の説明図であり、第5図は選別ステージの周方
向展開図、第6図は第5図に記した符号〜の
各部における選別動作を順序に従つて周方向と直
角の方向から見て表わした断面図である。
10……選別ステージ、11……選別板、12
……仕切フエンス、13……樋状チヤンネル、1
4……たて軸の回転軸、20……直流高圧電極、
21……コロナ放電電極、22……平板状電極、
30……被選別混合物供給フイーダ、40……絶
縁性粒子回収用ホツパ、50……導電性粒子回収
用ホツパ、60……スクレーパ、80……高圧直
流電源、C……選別ステージの回転方向、M……
被選別混合物、N……絶縁性粒子、O……導電性
粒子。
Fig. 1 is a principle diagram of a typical conventional electrostatic separation device, Fig. 2 is an explanatory diagram of the adsorption effect of insulating particles in Fig. 1, and Figs. A side view and a plan view showing the configuration arrangement, and FIGS. 5 and 6 are explanatory diagrams of the sorting operation of the embodiment of the present invention, FIG. 5 is a developed view in the circumferential direction of the sorting stage, and FIG. FIG. 3 is a cross-sectional view showing the sorting operations in the respective parts indicated by the symbols . 10... Sorting stage, 11... Sorting board, 12
...Partition fence, 13...Gutter channel, 1
4... Vertical rotation axis, 20... DC high voltage electrode,
21... Corona discharge electrode, 22... Flat electrode,
30... Mixture supply feeder to be sorted, 40... Hopper for collecting insulating particles, 50... Hopper for collecting conductive particles, 60... Scraper, 80... High voltage DC power supply, C... Rotation direction of sorting stage, M...
Mixture to be sorted, N: insulating particles, O: conductive particles.
Claims (1)
軸上に上下複数段設けられた選別板の上面中央部
に周方向に沿つた樋状チヤンネルを形成して成る
複数段の選別ステージと、各選別板の周上に定め
た被選別混合物の供給位置と選別回収位置との間
の周方向領域で選別ステージを相手方の電極とし
て各選別板の上方に対向配置したコロナ放電電極
およびコロナ放電電極に続く平板状電極とを組合
わせた複数段の直流高圧電極と、前記供給位置で
樋状チヤンネル内へ向けて開口した被選別混合物
の供給フイーダと、前記選別回収位置で樋状チヤ
ンネルに向けて開口した絶縁性粒子回収用ホツ
パ、および樋状チヤンネル外の円板側方に開口し
た導電性粒子回収用ホツパとを備えたことを特徴
とする静電選別装置。 2 特許請求の範囲第1項に記載の静電選別装置
において、選別ステージがリング状円板としての
選別板の上面中央部に周方向に沿つて2条の仕切
フエンスを突設し、該仕切フエンス間に樋状チヤ
ンネルを区画形成したものとして成ることを特徴
とする静電選別装置。[Scope of Claims] 1. A plurality of stages formed by forming a gutter-like channel along the circumferential direction at the center of the upper surface of a sorting plate that is rotated in a predetermined direction around a vertical axis and provided on the same axis in a plurality of upper and lower stages. The corona discharge is arranged oppositely above each sorting plate with the sorting stage as the other electrode in the circumferential region between the sorting stage and the supply position and sorting collection position of the mixture to be sorted, which are set on the circumference of each sorting plate. A multi-stage DC high-voltage electrode that combines electrodes and a flat plate electrode following a corona discharge electrode, a supply feeder for the mixture to be sorted that opens into the trough-like channel at the supply position, and a trough at the sorting and collection position. 1. An electrostatic sorting device comprising: a hopper for collecting insulating particles that is open toward a trough-like channel; and a hopper for collecting conductive particles that is open to the side of a disc outside the trough-like channel. 2. In the electrostatic sorting device according to claim 1, the sorting stage has two partition fences protruding along the circumferential direction from the center of the upper surface of the sorting plate as a ring-shaped disk, and the partition 1. An electrostatic sorting device characterized by forming a trough-like channel between fences.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7121380A JPS56166954A (en) | 1980-05-28 | 1980-05-28 | Electrostatic sorting apparatus |
| DE3120945A DE3120945A1 (en) | 1980-05-28 | 1981-05-26 | ELECTROSTATIC SORTING DEVICE |
| US06/267,510 US4374727A (en) | 1980-05-28 | 1981-05-27 | Electrostatic sorting apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7121380A JPS56166954A (en) | 1980-05-28 | 1980-05-28 | Electrostatic sorting apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56166954A JPS56166954A (en) | 1981-12-22 |
| JPS6155427B2 true JPS6155427B2 (en) | 1986-11-27 |
Family
ID=13454170
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7121380A Granted JPS56166954A (en) | 1980-05-28 | 1980-05-28 | Electrostatic sorting apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56166954A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111036409B (en) * | 2020-02-09 | 2021-09-28 | 羽源洋(宁波)科技有限公司 | Garbage separating device capable of realizing density sorting treatment of plastic garbage |
-
1980
- 1980-05-28 JP JP7121380A patent/JPS56166954A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56166954A (en) | 1981-12-22 |
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