JPH01164456A - Sorting of several kinds of crushed products - Google Patents
Sorting of several kinds of crushed productsInfo
- Publication number
- JPH01164456A JPH01164456A JP32364487A JP32364487A JPH01164456A JP H01164456 A JPH01164456 A JP H01164456A JP 32364487 A JP32364487 A JP 32364487A JP 32364487 A JP32364487 A JP 32364487A JP H01164456 A JPH01164456 A JP H01164456A
- Authority
- JP
- Japan
- Prior art keywords
- crushed materials
- specific gravity
- sorting
- separated
- net
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 52
- 230000005484 gravity Effects 0.000 claims abstract description 45
- 239000000463 material Substances 0.000 claims description 78
- 238000000034 method Methods 0.000 claims description 27
- 239000002245 particle Substances 0.000 claims description 18
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 8
- 239000011707 mineral Substances 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 4
- 238000013517 stratification Methods 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 abstract description 10
- 239000002184 metal Substances 0.000 abstract description 10
- 230000010349 pulsation Effects 0.000 abstract description 9
- 150000002739 metals Chemical class 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 239000000203 mixture Substances 0.000 description 11
- 239000010419 fine particle Substances 0.000 description 8
- 229910052782 aluminium Inorganic materials 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 6
- 239000003245 coal Substances 0.000 description 5
- 239000011521 glass Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000002699 waste material Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000005060 rubber Substances 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- -1 automobiles Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、家紅用品あるいは自動車等の使用済廃棄物の
シュレッダ−破砕物等の各種破砕物を選別する方法およ
びそのための装置に関し、特にこれらの各種破砕物を水
のF下方向の脈動により比重別に成層分離して、上層の
軽比重物から順次選別分離するようにした各種破砕物の
選別方法および′!!A置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method and apparatus for sorting various shredded materials such as shredder-crushed materials from household appliances or used waste such as automobiles, and in particular to an apparatus for the same. A method for sorting various crushed materials, in which various crushed materials are stratified and separated according to specific gravity by downward pulsation of water F, and materials with lighter specific gravity in the upper layer are sequentially separated, and '! ! This is related to the A position.
従来の技術
一般に、使用済廃東物はシュレッダ−によって破砕され
、その中に含まれる鉄分は、磁性分離法によって回収さ
れ、鉄のスクラップとして製鉄用に還元されている。こ
のようなシュレッダ−破砕物における鉄以外のものは、
主としてゴム、プラスチック、ガラス、アルミ、亜鉛、
鉛、銅合金、ステンレス等の混合物であるが、この混合
物からのメタルの回収は、主に人による選別(「手選」
と称している。)にたよっている。ざらに細粒の混合物
に対しては、現在、空気と高比重物の媒体粒子とによっ
て流動層を形成し、この中に混合物を入れて軽比重物を
空気と共に取り出すことによる選別方法、あるいは混合
物中の各成分のもつ導電率の差を利用して選別する方法
であるリニアモータ法などがある。BACKGROUND OF THE INVENTION In general, used waste materials are shredded by a shredder, and the iron contained therein is recovered by a magnetic separation method and reduced as iron scrap for use in iron manufacturing. Items other than iron in such shredder-crushed materials are:
Mainly rubber, plastic, glass, aluminum, zinc,
It is a mixture of lead, copper alloy, stainless steel, etc., but the recovery of metals from this mixture is mainly through manual sorting ("hand selection").
It is called. ). Currently, for mixtures of coarse to fine particles, there is a sorting method in which a fluidized bed is formed with air and media particles with high specific gravity, the mixture is placed in this fluidized bed, and the light specific gravity particles are taken out together with the air, or the mixture is separated. There is a linear motor method, which is a method of sorting using the difference in conductivity of each component.
また、使用済を葉物ではないが、石炭の選別分離方法と
して、破砕された石炭を水槽内に入れて、水槽内の水に
脈動を与えて細粒の大きさに応じて成層分離し、下層の
比重の大きい部分から取り出して選別することが行われ
ている。In addition, as a method for sorting and separating used coal, although it is not a leaf, the crushed coal is placed in a water tank and the water in the tank is pulsated to perform stratified separation according to the size of the fine particles. Sorting is done by extracting and sorting from the lower layer with higher specific gravity.
発明が解決しようとづる問題点 このような方法においては、次のような問題点がある。The problem that the invention seeks to solve This method has the following problems.
即ち、手選による場合、選別可能な細粒の混合物の粒度
はせいぜい50M以ヒであり、それ以下の粒度の混合物
に対しては、上記のような乾式流動法あるいはりニアモ
ータ法などが用いられているが、いずれも15m以下の
細粒の部分については満足すべき選別精度が得られてい
ない。That is, in the case of manual selection, the particle size of a mixture of fine particles that can be sorted is at most 50 M or more, and for mixtures with a particle size smaller than that, the dry flow method or linear motor method as described above is used. However, none of these methods has achieved satisfactory sorting accuracy for fine grains of 15 m or less.
このように、使用淡廃棄物の細粒に対しては有効適切な
選別方法が開発されていない。As described above, no effective and appropriate sorting method has been developed for fine particles of used waste.
また、上記のような石炭の選別方法を用いた場合には、
各層部分を取り出す上で複雑な装置構造が必要であり、
また下から取り出すために各層部分が上層の小量あるい
は混合に伴う問題を生じ、各層を選別精度を上げて取り
出すには不適当であった。In addition, when using the coal sorting method described above,
A complex device structure is required to extract each layer,
In addition, since each layer is taken out from the bottom, problems occur due to the small amount or mixing of the upper layer, making it unsuitable for picking out each layer with increased sorting accuracy.
本発明は、各秤破砕物の細粒混合物からメタル分を高い
選別効率で選別し、15m以下1#程度までの細粒に対
しても正確な分離を行うようにした各種破砕物の選別方
法を提供することを目的とするものである。The present invention is a method for sorting various types of crushed materials, in which the metal content is sorted out with high sorting efficiency from the fine particle mixture of each scale-crushed material, and accurate separation is performed even for fine particles with a size of 1# or less than 15 m. The purpose is to provide the following.
問題点を解決するための手段
上記目的を達成するために、各種破砕物の選別方法は、
水槽内に浸された網体上に、鉱物、家庭用品あるいは自
動車等の各種破砕物を連続的に載置し、この載置された
破砕物に水の上下方向の脈動を与えて、各粒子のもつ比
重に従い複数の層に成層分離せしめ、この成層分離され
た上層の軽比重物から下層の重比重物へと、順次各比重
物ごとに前記水槽に供給される水の水平水流によって前
記破砕物の進行方向に対して直角方向に溢流せしめ、前
記破砕物を比重別に選別分離することを特徴とする。Means for solving the problem In order to achieve the above purpose, the method of sorting various crushed materials is as follows:
Various crushed objects such as minerals, household goods, and automobiles are continuously placed on a mesh body immersed in a water tank, and the placed crushed objects are subjected to vertical pulsations of water, so that each particle The material is stratified into a plurality of layers according to its specific gravity, and the stratified materials are separated into layers, from the light specific gravity material in the upper layer to the heavy specific gravity material in the lower layer. The method is characterized in that the crushed materials are overflowed in a direction perpendicular to the direction in which the materials travel, and the crushed materials are sorted and separated according to their specific gravity.
作用
本発明の上記方法によって、ゴム、木片、プラスチック
、ガラスおよび各種金属を含む家庭用品、自動車あるい
は鉱物等の各種破砕物が次のように選別分離される。Function: According to the above method of the present invention, various crushed materials such as rubber, wood chips, plastics, glass, household goods containing various metals, automobiles, minerals, etc. are sorted and separated as follows.
前記破砕物は、水槽に所定の深さで浸、された網体上に
順次供給され、網体上で水の上下方向の脈lI]装置に
より繰り返し脈動が与えられ、前記破砕物中の各種鉱物
の粒子の個々の真比重に応じて、上層にゴム、プラスチ
ック等の軽比重物、中層にはガラス、セラミック等の中
間比重物、そして下層にはアルミ、銅を含むステンレス
等の高比重物が成層分離される。このように分離された
粒子は、網体に沿って前記水槽に設けられた複数の溢流
堰において、前記水槽の水の水平水流を利用して各層に
対応した堰高さの異なる溢流堰から上層の軽比重物そし
て中層の中間比重物へと順次渦流によって前記破砕物の
進行方向に対して直角方向に取り出される。取り出され
た各比重物は脱水して回収される。そして、残った下層
の重比重物は網体の移動または網体の振動による移動に
より水槽から取り出され、脱水されて回収される。The crushed material is sequentially supplied onto a mesh body immersed in a water tank at a predetermined depth, and pulses are repeatedly applied to the mesh body by a device that pulses the water in the vertical direction. Depending on the true specific gravity of each mineral particle, the upper layer is made of light specific gravity materials such as rubber and plastic, the middle layer is made of intermediate specific gravity materials such as glass and ceramics, and the lower layer is made of high specific gravity materials such as stainless steel containing aluminum and copper. is stratified. The particles separated in this way are transported along the net body to a plurality of overflow weirs provided in the water tank, using the horizontal water flow of the water in the water tank to create overflow weirs with different weir heights corresponding to each layer. The crushed materials are taken out in a direction perpendicular to the direction of movement of the crushed materials by a vortex flow from the upper layer of light specific gravity materials to the middle layer of intermediate specific gravity materials. Each specific gravity substance taken out is dehydrated and recovered. Then, the remaining heavy substances in the lower layer are taken out from the water tank by movement of the net or movement by vibration of the net, and are dehydrated and recovered.
実施例
以下、図面について本発明の詳細な説明すると、1は選
別水槽であって、一つのU字管をなして形成され、2は
前記選別水槽に水を送るための給水管、3は網室、4は
溢流堰であって、ここで給水管2から供給され閘室3を
通った水が溢流される。5はU字型の選別水槽1の閘室
3とは反対側の水面部分に設けられたプランジャー、6
は前記プランジャー5に上下動を与えるためのエキセン
トリックホイールであって、回転中心の偏心距離によっ
て上下動のストロークが決定され、前記選別水槽1内の
水に前記ストロークによって上下脈動の波高さが与えら
れる。7はモータであって、その回転数の選定によって
水の上下脈動の脈動数が決められる。通常、波高さは1
2〜110m+の範囲であり、前記脈動数は50〜30
0 r、I)、Lの範囲であって、その原料のサイズお
よび比重の構成によって最適値が選定される。8は網体
をなす移動ネットコンベヤであって、前記選別水槽1の
閘室3に浸されて配置され、9は溢流樋であって、前記
選別水槽1の前記溢流11ii4の部分に、シュレッダ
−破砕物の供給方向に対して直角方向に設けられ、溢流
によって流された破砕物の粒子をスクリーン(図示せず
。)に導く。1oは前記U字型の選別水槽1の組字3側
の半分を収容して、前記移動ネットコンベヤ8の戻り部
分が浸された水槽である。11は前記移動ネットコンベ
ヤ8がエンドレスに移動するように巻き掛けられたプー
リ、12はシュレッダ−破砕物を前記選別水槽1の閘室
3に供給するためのベルトコンベヤである。EXAMPLE Hereinafter, the present invention will be described in detail with reference to the drawings. 1 is a sorting water tank, which is formed as one U-shaped pipe, 2 is a water supply pipe for sending water to the sorting water tank, and 3 is a network. Chamber 4 is an overflow weir, and water supplied from water supply pipe 2 and passed through lock chamber 3 is overflowed here. 5 is a plunger installed on the water surface of the U-shaped sorting water tank 1 on the opposite side from the lock chamber 3;
is an eccentric wheel for giving vertical movement to the plunger 5, the stroke of the vertical movement is determined by the eccentric distance of the rotation center, and the wave height of the vertical pulsation is given to the water in the sorting water tank 1 by the stroke. It will be done. 7 is a motor, and the number of pulsations of the vertical pulsation of the water is determined by selecting its rotation speed. Usually the wave height is 1
The range is from 2 to 110 m+, and the pulsation number is from 50 to 30
0 r, I), L, and the optimum value is selected depending on the size and specific gravity of the raw material. 8 is a moving net conveyor in the form of a net, which is disposed so as to be immersed in the lock chamber 3 of the sorting water tank 1; 9 is an overflow gutter; Shredder - installed perpendicular to the direction of supply of shredded material and directs shredded material particles washed away by overflow to a screen (not shown). 1o is a water tank that accommodates the half of the U-shaped sorting water tank 1 on the side of the font 3, and in which the return portion of the mobile net conveyor 8 is immersed. 11 is a pulley around which the mobile net conveyor 8 is wound endlessly, and 12 is a belt conveyor for supplying the shredded material to the lock chamber 3 of the sorting water tank 1.
前記閘室3は、第2図および第3図に示すように、前記
移動ネットコンベヤ8が所定の深さに設置されて、その
上でシュレッダ−破砕物の成層分離を行う第−区、軽比
重物を溢流させる第二区、ぞして中間比重物を溢流させ
る第三区からなる。As shown in FIGS. 2 and 3, the lock chamber 3 has the movable net conveyor 8 installed at a predetermined depth, and is used for the shredder and the light storage section where the shredded material is stratified and separated. It consists of a second section where specific gravity substances overflow, and a third section where intermediate specific gravity substances overflow.
これらの第二区および第三区には、前記選別水槽1にお
ける前記破砕物の供給方向の部分に各比重物の層高さに
応じて溢流堰4が水の水平水流によって溢流されるよう
に設けられ、溢流樋9と共に取り出し装置をなす。In these second and third sections, overflow weirs 4 are installed in the part of the sorting water tank 1 in the direction in which the crushed material is supplied, so that the horizontal flow of water overflows according to the layer height of each specific gravity material. It forms a take-out device together with the overflow gutter 9.
選別されるシュレッダ−破砕物の一例として、自動車破
砕物組成が第4図に示されている。これは、鉄成分を除
いた後の15m以下の粒度のものがアルミを含むメタル
を約50%含み、それ以外の異物であるガラス塩Fの軽
比重物を約50%占めている混合破砕物であることを示
している。As an example of the shredder-shredded material to be sorted, the composition of automobile shredded material is shown in FIG. This is a mixed crushed material in which particles with a particle size of 15 m or less after iron components are removed contain about 50% of metals including aluminum, and about 50% of the light specific gravity of glass salt F, which is the other foreign material. It shows that.
このようなシュレッダ−破砕物を選別分離するには、こ
のシュレッダ−破砕物がベルトコンベヤ12により選別
水槽1に送られ、網体である移動ネットコンベヤ8が浸
された閘室3に供給される。In order to sort and separate such shredder-crushed materials, the shredder-crushed materials are sent to a sorting water tank 1 by a belt conveyor 12, and then supplied to a lock chamber 3 in which a moving net conveyor 8 is immersed. .
この閘室3の第−区において、シュレッダ−破砕物は、
モータ7により回転されたエキセントリックホイール6
によりプランジャー5が上下動され、選別水槽1中の水
に上下方向の脈動が与えられる。In the ward of this lock room 3, the shredder crushed material is
Eccentric wheel 6 rotated by motor 7
The plunger 5 is moved up and down, and the water in the sorting water tank 1 is given vertical pulsation.
この脈動の繰り返しにより、移動ネットコンベヤ8上の
破砕物はその中に含まれる各種鉱物の粒子が個々の真比
重に応じて、上層に軽比重物であるゴム、プラスチック
等を、中層に中間比重物であるガラス、セラミック等を
、そして下層には重比重物であるアルミ、銅を含むステ
ンレス等を整然とした層に形成させる。By repeating this pulsation, the crushed material on the moving net conveyor 8 is divided into particles of various minerals contained therein, depending on their individual true specific gravity. Materials such as glass and ceramics are formed in an orderly layer, and the lower layer is heavy materials such as aluminum and stainless steel containing copper.
前記取り出し装置においては、前記閘室3の第−区で成
層分離された各種破砕物は、移動ネットコンベヤ8の移
動により閘室3の第二区に移動され、該第二区において
は軽比重物が、選別水槽1への給水管2からの給水によ
る水平水流でもって生じる成層の上層に対応した高さの
溢流堰4を越える溢流によって前記破砕物の進行方向に
対し直角方向に溢流樋9へ取り出される。そして、第三
区においては中間比重物がその層高さに応じて各溢流[
4を越えて取り出される。このようにして各比重物は、
溢流樋9を通ってスクリーンに送られ、脱水された後回
収される。最後に移動ネットコンペ178に残留したメ
タル等の重比重物は、第3図に承すようにある一定の距
離を水中から上げられて脱水され、最高の位謂にあるプ
ーリ11において機外に排出される。In the take-out device, the various crushed materials stratified and separated in the first section of the lock chamber 3 are moved to the second section of the lock chamber 3 by the movement of the moving net conveyor 8, and in the second section, the crushed materials are The crushed materials overflow in a direction perpendicular to the direction of movement of the crushed materials due to overflow over the overflow weir 4 whose height corresponds to the upper layer of stratification caused by horizontal water flow from the water supply pipe 2 to the sorting water tank 1. It is taken out to the gutter 9. Then, in the third section, intermediate specific gravity materials flow into each overflow [
More than 4 are taken out. In this way, each specific gravity is
It is sent to a screen through an overflow gutter 9, and is recovered after being dehydrated. Finally, heavy materials such as metals remaining in the moving net competition 178 are lifted out of the water a certain distance and dehydrated, as shown in Figure 3, and removed from the machine at the highest pulley 11. It is discharged.
このようにして、家庭用品あるいは自動車等のシュレッ
ダ−破砕物等に含まれる各秤鉱物(よ、15#Im以下
の粒度のものを成層分離により分離さVることができ、
成層分離された粒子を上層から各層ごとに選別するので
、第4図に示すような自動車破砕物に含まれるような鉄
成分を取り除いた15m以下の粒度のものの場合、アル
ミニウムを含むメタル類を95%以上の回収率で回収し
、他の異物を除去することができる。In this way, various scale minerals (those with a particle size of 15 #Im or less) contained in shredder-crushed materials such as household goods or automobiles can be separated by stratified separation.
Since the stratified particles are sorted in each layer starting from the upper layer, in the case of particles with a particle size of 15 m or less from which iron components have been removed, such as those contained in shredded automobiles, as shown in Figure 4, metals including aluminum are separated by 95%. % or more, and other foreign substances can be removed.
なお、前記取り出し装置に関しては、軽比重物と中間の
比重物だけについて説明したが、さらに複数の層に分離
するものであれば、この成層数に応じた高さの溢流堰を
複数設けてもよいことは勿論である。Regarding the above-mentioned extraction device, only light specific gravity materials and intermediate specific gravity materials have been explained, but if the material is to be further separated into multiple layers, multiple overflow weirs with heights corresponding to the number of layers may be provided. Of course, this is a good thing.
そして、各種破砕物の成層分離された破砕物は、網体に
より移動させているが、網体を固定式にしてそれ自体に
振動を与えることにより重比重物を移動させるようにし
てもよいことは勿論である。Furthermore, the stratified and separated crushed materials of various types of crushed materials are moved by the net, but the net may be fixed and vibrate itself to move the heavy specific gravity materials. Of course.
また、以上においては、シュレッダ−破砕物について説
明したが、破砕物であれば、脈石と金属鉱石の混合破砕
物の場合にも、比重の比較的軽い脈石(比重2.7)と
比重の重い金属鉱石(比重 −3,5以上の銅、鉛、亜
鉛等)とを選別するため 4゜に適用することができる
。これは石炭と岩石の混合物から石炭と岩石とを選別す
る場合にも同様に適用することができる。In addition, although the above description deals with shredder-crushed materials, in the case of mixed crushed materials of gangue and metal ore, gangue with a relatively light specific gravity (specific gravity 2.7) and It can be applied at 4° to separate heavy metal ores (copper, lead, zinc, etc. with a specific gravity of -3.5 or more). This can be similarly applied to the case of separating coal and rock from a mixture of coal and rock.
発明の詳細
な説明したように、本発明の各種破砕物の選別方法にに
れば、鉱物、家庭用品あるいは自動車等の各種破砕物の
15馴以下の細粒が、選別水槽に浸されて設けられた網
体に載置され【、選別水槽の水に上下方向の脈動が繰り
返し与えられ、前記細粒の各粒子を比重別に成層分離せ
しめ、層高さに対応した高さの異なる溢流堰において、
上層の軽比重物から順次重比重物へと選別し分離された
破砕物を、その進行方向に対して直角方向に前記水槽の
溢流により取り出すことができるので、アルミニウムを
含むメタル類を各種破砕物からその中に含まれる全量の
95%以上を回収することができ、鉱物、家庭用品ある
いは自動車等の各種破砕物である廃棄物中から有用金属
を効率よく回収することができるという優れた効果があ
る。As described in detail of the invention, according to the method for sorting various crushed materials of the present invention, fine particles of 15 mm or less of various crushed materials such as minerals, household goods, automobiles, etc. are immersed in a sorting water tank. The water in the sorting tank is repeatedly pulsated in the vertical direction, and the fine particles are stratified and separated according to their specific gravity. In,
The crushed materials that have been sorted and separated from the upper layer of light specific gravity materials to heavy specific gravity materials can be taken out by the overflow of the water tank in a direction perpendicular to the direction of movement of the crushed materials, so it is possible to crush various metals including aluminum. It has the excellent effect of being able to recover more than 95% of the total amount contained in objects, and enabling efficient recovery of useful metals from various types of waste, such as minerals, household goods, and crushed automobiles. There is.
第1図は本発明に係る各種破砕物の選別方法がなされる
装置の一実施例の断面図、第2図は第1図に示す装置の
平面図、第3図は同じ装置の第2図における矢印■−■
方向にみた側面図、および第4図は15m+以下の粒度
の自動車破砕物組成を示すグラフである。
1・・・選別水槽、3・・・閘室、4・・・溢流堰、5
・・・プランジャー、8・・・移動ネットコンベヤ。FIG. 1 is a sectional view of an embodiment of the apparatus for carrying out the method for sorting various crushed materials according to the present invention, FIG. 2 is a plan view of the apparatus shown in FIG. 1, and FIG. 3 is a second view of the same apparatus. Arrow ■−■
The side view and FIG. 4 are graphs showing the composition of automobile debris with a particle size of 15 m+ or less. 1... Sorting water tank, 3... Lock room, 4... Overflow weir, 5
...Plunger, 8...Moving net conveyor.
Claims (4)
選別する方法において、水槽内に浸された網体上に、前
記各種破砕物を連続的に載置し、この載置された破砕物
に水の上下方向の脈動を与えて、各粒子のもつ比重に従
い複数の層に成層分離せしめ、この成層分離された上層
の軽比重物から下層の重比重物へと、順次各比重物ごと
に前記水槽に供給される水の水平水流によつて前記破砕
物の進行方向に対して直角方向に溢流せしめ、前記破砕
物を比重別に選別分離することを特徴とする各種破砕物
の選別方法。(1) In a method for sorting various types of crushed materials such as minerals, household goods, or automobiles, the various types of crushed materials are continuously placed on a net immersed in a water tank, and the placed crushed materials are The water is pulsated in the vertical direction to cause the particles to be stratified and separated into multiple layers according to their specific gravity, and each particle is separated from the light specific gravity in the upper layer to the heavy specific gravity in the lower layer. A method for sorting various types of crushed materials, characterized in that a horizontal stream of water supplied to the water tank overflows in a direction perpendicular to the traveling direction of the crushed materials, and the crushed materials are sorted and separated according to their specific gravity.
、前記網体上に残留する高比重破砕物を移動せしめて外
部に取り出すために、前記網体を連続的に移動せしめて
前記破砕物を移動させることを特徴とする各種破砕物の
選別方法。(2) In the sorting method according to claim 1, in order to move the high specific gravity crushed materials remaining on the net and take them out, the net is continuously moved to crush the crushed materials. A method for sorting various types of crushed materials, which is characterized by moving the materials.
、前記網体に振動を与えることによつて前記網上の高比
重破砕物を移動させることを特徴とする各種破砕物の選
別方法。(3) A method for sorting various crushed materials according to claim 1, characterized in that high specific gravity crushed materials on the net are moved by applying vibration to the net. .
、前記各種破砕物の選別分離が、前記破砕物の進行方向
に対して平行になるよう前記水槽の側面に並置して設け
られかつ分離された成層に対応した高さを有する複数の
溢流堰においてなされることを特徴とする各種破砕物の
選別方法。(4) In the sorting method according to claim 1, the sorting and separation of the various types of crushed materials are provided in parallel to the side surface of the water tank so as to be parallel to the traveling direction of the crushed materials, and A method for sorting various types of crushed materials, characterized in that the method is carried out in a plurality of overflow weirs having heights corresponding to separated stratification.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32364487A JPH01164456A (en) | 1987-12-21 | 1987-12-21 | Sorting of several kinds of crushed products |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32364487A JPH01164456A (en) | 1987-12-21 | 1987-12-21 | Sorting of several kinds of crushed products |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01164456A true JPH01164456A (en) | 1989-06-28 |
JPH0329462B2 JPH0329462B2 (en) | 1991-04-24 |
Family
ID=18157024
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32364487A Granted JPH01164456A (en) | 1987-12-21 | 1987-12-21 | Sorting of several kinds of crushed products |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01164456A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5461465A (en) * | 1992-04-10 | 1995-10-24 | Fuji Xerox Co., Ltd. | Developing apparatus |
CN103056018A (en) * | 2012-10-19 | 2013-04-24 | 南京梅山冶金发展有限公司 | Big-skipping concentrate weir plate enabling user to easily disassemble and change |
CN105289832A (en) * | 2015-11-19 | 2016-02-03 | 李宝囯 | Piston type jigging machine without water sealing diaphragm |
-
1987
- 1987-12-21 JP JP32364487A patent/JPH01164456A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5461465A (en) * | 1992-04-10 | 1995-10-24 | Fuji Xerox Co., Ltd. | Developing apparatus |
CN103056018A (en) * | 2012-10-19 | 2013-04-24 | 南京梅山冶金发展有限公司 | Big-skipping concentrate weir plate enabling user to easily disassemble and change |
CN105289832A (en) * | 2015-11-19 | 2016-02-03 | 李宝囯 | Piston type jigging machine without water sealing diaphragm |
Also Published As
Publication number | Publication date |
---|---|
JPH0329462B2 (en) | 1991-04-24 |
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