JP2518800B2 - Pretreatment method for heavy liquid sorting - Google Patents
Pretreatment method for heavy liquid sortingInfo
- Publication number
- JP2518800B2 JP2518800B2 JP5305797A JP30579793A JP2518800B2 JP 2518800 B2 JP2518800 B2 JP 2518800B2 JP 5305797 A JP5305797 A JP 5305797A JP 30579793 A JP30579793 A JP 30579793A JP 2518800 B2 JP2518800 B2 JP 2518800B2
- Authority
- JP
- Japan
- Prior art keywords
- heavy liquid
- water
- sorting
- raw material
- heavy
- 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 - Fee Related
Links
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、重液選別前処理方法に
係り、更に詳しくは、例えば自動車等を破砕したダスト
から有価金属を回収する場合に使用できる重液選別の前
処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pretreatment method for heavy liquid sorting, and more particularly to a pretreatment method for heavy liquid sorting which can be used when recovering valuable metals from dust from crushed automobiles and the like.
【0002】[0002]
【従来の技術】廃車された自動車などは、プレシュレッ
ダーおよびシュレッダーにより50〜60mmの小片に
破砕された後、風力選別機により軽いダストと重いダス
トとに分離され、前記重いダストは磁力選別機により屑
鉄が除去され、屑鉄は資源として回収される。そして、
屑鉄が除去された残りの重いダスト中には、銅、アルミ
ニウム、亜鉛、ステンレスなどの非鉄金属と、ガラス、
ゴムなどが混在しているので、非鉄金属と、ゴム、ガラ
スとは風力選別またはその電気的性質を利用して分離さ
れて、さらに分離された非鉄金属内の銅、アルミニウ
ム、亜鉛、ステンレス、その他のダストなどは手選によ
り分離されていた。2. Description of the Related Art A scrapped automobile or the like is crushed into small pieces of 50 to 60 mm by a preshredder and a shredder, and then separated into light dust and heavy dust by a wind separator, and the heavy dust is separated by a magnetic separator. The scrap iron is removed and the scrap iron is recovered as a resource. And
In the remaining heavy dust from which scrap iron has been removed, non-ferrous metals such as copper, aluminum, zinc, and stainless steel, and glass,
Since non-ferrous metals are mixed with rubber and glass, they are separated by wind separation or their electrical properties, and copper, aluminum, zinc, stainless steel, etc. in the non-ferrous metals are further separated. The dust, etc. were separated by hand.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、従来の
選別方法では、このように銅、アルミニウム、亜鉛、ス
テンレス等の非鉄金属を手選により分離していたので、
作業が面倒で作業効率が極めて悪かった。そこで、本発
明者は特開平6−142546号公報に示すように、こ
れを解消するために、処理原料をマグネタイト等の磁性
粉体が混入された重液が貯液された選別容器内に投入し
て、比重差によりアルミニウムなどの浮上する軽量物と
他の沈降する重量物とに選別する軽重混合物の選別方法
を提案した。しかしながら、前記重液選別方法では処理
原料中に、塵、油分などの不純物がある場合に重液中に
塵や油分が混入しその結果重液の粘性が上がったり、更
に処理原料や塵に付着した空気が重液に混入して泡が発
生するなどの現象が発生し、処理原料を軽量物と重量物
とに分離し難くなるという問題点があった。そこで、本
願発明者は、この対策として処理原料の上から水を吹き
付けるシャワー洗浄を試験的に行ってみたが、洗浄水が
処理原料の表面全体に吹き付けられるわけではないの
で、十分な綿塵や油分の除去は困難であった。本発明は
このような事情に鑑みてなされたもので、処理原料を効
率良く重液選別できる重液選別前処理方法を提供するこ
とを目的とする。However, in the conventional sorting method, nonferrous metals such as copper, aluminum, zinc, and stainless steel are separated by hand in this way,
The work was troublesome and the work efficiency was extremely poor. Therefore, the present inventor, as disclosed in JP-A-6-142546, puts a processing raw material into a sorting container in which a heavy liquid mixed with magnetic powder such as magnetite is stored in order to solve this problem. Then, we proposed a method for sorting light and heavy mixtures that sorts out floating lightweight materials such as aluminum and other sedimenting heavy materials due to the difference in specific gravity. However, in the heavy liquid sorting method, when impurities such as dust and oil are present in the raw material for processing, dust and oil are mixed in the heavy liquid, and as a result, the viscosity of the heavy liquid is increased and further adhered to the processing raw material and dust. There is a problem that air is mixed with the heavy liquid to generate bubbles, which makes it difficult to separate the processing raw material into a lightweight material and a heavy material. Then, the inventor of the present application tried a shower cleaning in which water is sprayed from above the processing raw material as a countermeasure, but since the cleaning water is not sprayed onto the entire surface of the processing raw material, sufficient cotton dust and Removal of oil was difficult. The present invention has been made in view of such circumstances, and an object of the present invention is to provide a heavy liquid sorting pretreatment method capable of efficiently performing heavy liquid sorting of a processing raw material.
【0004】[0004]
【課題を解決するための手段】前記目的に沿う請求項1
記載の重液選別前処理方法は、重液が貯液された選別容
器内に処理原料を投入して、該処理原料を比重差により
浮上する軽量物と沈降する重量物とに選別する重液選別
を行うにあたって、予め、前記選別容器に投入される処
理原料を、中間部に水吹き出し部を備え該水吹き出し部
から上部は上昇水流となっている水洗容器内に投入し、
前記上昇水流により、投入した前記処理原料に付着して
いた塵及び油分を洗浄すると共に、積極的に該塵及び油
分を浮上させて除去している。また、請求項2記載の重
液選別前処理方法は、請求項1記載の方法において、前
記水洗容器内の水量が、前記処理原料の重量の20倍以
上となっている。A method according to the above-mentioned object.
The heavy liquid sorting pretreatment method described is a heavy liquid that puts a processing raw material into a sorting container in which the heavy liquid is stored, and sorts the processing raw material into a lightweight material that floats due to a difference in specific gravity and a heavy material that sediments. In performing the sorting, in advance, the treatment raw material to be put into the sorting container is put into a washing container in which a water blowing portion is provided in an intermediate portion and an upper part has a rising water flow from the water blowing portion,
The rising water flow cleans the dust and oil content adhering to the input processing raw material and positively floats and removes the dust and oil content. Further, in the heavy liquid sorting pretreatment method according to claim 2, in the method according to claim 1, the amount of water in the water washing container is 20 times or more the weight of the treatment raw material.
【0005】[0005]
【作用】請求項1、2記載の重液選別前処理方法に使用
する水洗容器は、その中間部に水吹き出し部を備え、該
水吹き出し部から上部は上昇水流となっているので、上
部から投入された物は、比重が1より小さい物は当然と
して、比重が1又は1より少し大きい物であっても、上
昇水流に流されて浮上する。従って、前記水洗容器に処
理原料を投入すると、上昇水流によって洗われて下降途
中で分離した塵、油分等は上昇水流によって積極的に上
方に流されて除去される。従って、前記水洗容器から下
部に沈降した処理原料にはほとんど塵や油分が付着して
おらず、このため水洗容器から取り出された処理原料を
選別容器に投入して選別する際に、重液の粘性が上った
り、あるいは重液の実際的比重が小さくなることがない
ので、効率良く軽量物と重量物とに重液選別できる。特
に、請求項2記載の重液選別前処理方法においては、水
洗容器内の水量が、前記処理原料の重量の20倍以上な
ので、十分な水洗効果が得られる。The washing container used in the pretreatment method for heavy liquid sorting according to claims 1 and 2 is provided with a water blowing portion in the middle portion thereof, and since the upper portion from the water blowing portion has a rising water flow, As for the thrown in thing, even if the specific gravity is 1 or a little larger than 1, naturally, the thing with specific gravity smaller than 1 is flown by the rising water flow and floats. Therefore, when the treatment raw material is put into the water washing container, dust, oil and the like which are washed by the rising water flow and separated during the descending flow are positively flowed upward by the rising water flow to be removed. Therefore, almost no dust or oil is attached to the treated raw material settled to the lower portion from the water washing container. Therefore, when the treated raw material taken out of the water washed container is put into the sorting container and sorted, the heavy liquid Since the viscosity does not increase or the actual specific gravity of the heavy liquid does not decrease, it is possible to efficiently separate the heavy liquid into the light one and the heavy one. Particularly, in the heavy liquid sorting pretreatment method according to the second aspect, since the amount of water in the washing container is 20 times or more the weight of the treatment raw material, a sufficient washing effect can be obtained.
【0006】[0006]
【実施例】続いて、添付した図面を参照しつつ、本発明
を具体化した実施例につき説明し、本発明の理解に供す
る。ここに、図1は本発明の一実施例に係る重液選別前
処理方法が適用された重液選別設備の要部概略図、図2
は前記重液選別処理方法が適用された重液選別設備の全
体概略図を示している。Embodiments of the present invention will now be described with reference to the accompanying drawings to provide an understanding of the present invention. Here, FIG. 1 is a schematic view of a main part of a heavy liquid sorting facility to which a heavy liquid sorting pretreatment method according to an embodiment of the present invention is applied, and FIG.
Shows an overall schematic view of a heavy liquid sorting facility to which the heavy liquid sorting method is applied.
【0007】図2に示すように、本発明の一実施例を適
用する重液選別設備10は、廃車をプレシュレッダーお
よびシュレッダーにより50〜60mm以下に破砕し、
周知の風力選別機により軽いダストが除去され、磁力選
別機により鉄などの磁性物が除去された処理原料中か
ら、小物、大物、電線やワイヤなどの長尺物を選別する
長尺選別機11と、選別された所定サイズの処理原料に
付着した塵や油分を水洗いする水洗機12と、水洗い後
の処理原料を重液13により軽量物14と重量物15と
に分離する重液選別機16と、選別された軽量物14お
よび重量物15に付着した重液13を洗い落とす一対の
水切り篩17、18と、それぞれの水切り篩17、18
から排出された重液13中の磁性粉体を吸着分離する磁
選機19と、磁選機19の排水が貯液されて、底部に沈
下した排水中の不純物を搬出する排出コンベア20を有
する水タンク21と、磁選機19により吸着された磁性
粉体の脱磁機22と、脱磁機22により脱磁された重液
13を重液選別機16に供給する重液タンク24とを備
えている。As shown in FIG. 2, in the heavy liquid sorting equipment 10 to which an embodiment of the present invention is applied, a scrap car is crushed into 50 to 60 mm or less by a pre-shredder and a shredder,
A long sorter 11 that sorts small items, large items, long items such as electric wires and wires from the processing raw materials from which light dust has been removed by a well-known wind force sorter and magnetic substances such as iron have been removed by a magnetic force sorter 11. A washing machine 12 for washing dust and oil content adhering to the selected treatment material of a predetermined size with water, and a heavy liquid sorting machine 16 for separating the treated material after washing with the heavy fluid 13 into a light weight article 14 and a heavy article 15. And a pair of draining sieves 17 and 18 for washing off the heavy liquid 13 adhering to the selected lightweight articles 14 and heavy articles 15 and the respective draining sieves 17 and 18
Water tank having a magnetic separator 19 for adsorbing and separating the magnetic powder in the heavy liquid 13 discharged from the separator, and a discharge conveyor 20 for discharging the impurities in the waste water stored in the bottom of the magnetic separator 19 and sinking to the bottom. 21, a demagnetizer 22 for the magnetic powder adsorbed by the magnetic separator 19, and a heavy liquid tank 24 for supplying the heavy liquid 13 demagnetized by the demagnetizer 22 to the heavy liquid sorter 16. .
【0008】筒篩形の回転体である長尺選別機11より
上流には、複数個のコンベアからなる搬入装置25が配
置されており、この長尺選別機11の下方には、小物、
大物や長物の分別装置26が配置されており、それぞれ
分別されたものが小物回収箱27、大物回収箱28、長
物回収箱29に収納されるようになっている。A carry-in device 25 composed of a plurality of conveyors is arranged upstream of the long-sized sorter 11 which is a cylindrical sieve-shaped rotating body. Below the long-sized sorter 11, small articles,
A large-sized or long-sized sorting device 26 is arranged, and the sorted products are stored in a small-sized collection box 27, a large-sized collection box 28, and a long-sized collection box 29, respectively.
【0009】図1に示すように、水洗機12は、大型で
ほぼ角筒形の水洗容器30を有しており、水洗容器30
の原料投入部30aに、水洗により浮き上がった塵や油
分などの不要物Dを受け取る樋状のダスト類排出部30
cが設けられている。また、水洗容器30内の下部から
原料排出部30b上にかけて、駆動される対となるチェ
ーン間に一定間隔毎に多数枚の掻き上げ板が設けられた
排出コンベア31が傾斜配置されている。また、水洗容
器30の投入側の上下部周側面には、循環水槽30A
(図2参照)からポンプ30Bにより圧送された水の水
吹き出し部32が上下一対設けられている。なお、水洗
容器30内の水量は、十分な水洗効果が得られるように
処理原料重量のほぼ20倍であり(例えば、処理原料4
トンに対して水80m3)、また水吹き出し部32の水
吹き出し方向は斜め上方である。水洗により処理原料に
付着した塵や油分は、原料投入部30aに設けられたダ
スト類排出部30cから溢れ出てダストボックス30C
に回収される(図2参照)。As shown in FIG. 1, the washing machine 12 has a large-sized, substantially rectangular tubular washing container 30.
A trough-shaped dust discharging section 30 for receiving the unwanted matter D such as dust and oil floating up by washing with water in the raw material charging section 30a
c is provided. Further, from the lower part of the water washing container 30 to the raw material discharge part 30b, a discharge conveyor 31 provided with a large number of scraping plates at a constant interval is provided between the driven chains to be inclined. In addition, a circulating water tank 30A is provided on the upper and lower peripheral side surfaces on the charging side of the washing container 30.
A pair of upper and lower water outlets 32 of water pumped by the pump 30B (see FIG. 2) are provided. The amount of water in the washing container 30 is about 20 times the weight of the processing raw material so that a sufficient washing effect can be obtained (for example, the processing raw material 4).
80 m 3 of water with respect to ton), and the water blowing direction of the water blowing unit 32 is obliquely upward. Dust and oil attached to the treated raw material by washing with water overflow from the dust discharge section 30c provided in the raw material input section 30a and flow into the dust box 30C.
Are collected (see FIG. 2).
【0010】同じく図1に示すように、重液選別機16
は水洗機12とほぼ同一形状の装置であり、本体となる
選別容器33、選別容器33の投入側の周側面に形成さ
れた重液13の上下一対の吹き出し部34、選別容器3
3の下部内に沈下したダスト(ガラスなど)、銅、亜
鉛、ステンレス、鉄などの重量物15を排出するチェー
ンコンベアからなる排出コンベア35とを有し、上方に
流れを与えて重液13(γ=2.5)の見かけ上の比重
を大きくし(γ=2.7)、混入したアルミニウムの選
別を行っている。アルミニウムなどの軽量物14は選別
容器33の原料投入部33aに設けられた桶状の軽量物
排出部33cから流出し、重量物15は排出コンベア3
5により選別容器33の重量物排出部33bから排出さ
れる。図2に示すように、軽量物14は重液選別機16
から重液13と共に排出され、前記水切り篩17に送ら
れる前に重液分離篩36により篩い取られる。なお、重
液分離篩36から排出された排水は、タンク36aによ
り一旦貯液されて重液13と不純物を含む水に分離さ
れ、そのうちの重液13は重液タンク24に戻される一
方、水は水切り篩17、18より排出された不純物を含
む排水と共に前記磁選機19に送られる。Similarly, as shown in FIG. 1, a heavy liquid sorter 16
Is a device having substantially the same shape as the water washing machine 12, and is a sorting container 33 as a main body, a pair of upper and lower blowing portions 34 for the heavy liquid 13 formed on the peripheral side surface of the sorting container 33 on the input side, and the sorting container 3
3 has a discharge conveyor 35 composed of a chain conveyor that discharges dust (glass or the like) that has settled in, a heavy material 15 such as copper, zinc, stainless steel, iron, etc. The apparent specific gravity of γ = 2.5) is increased (γ = 2.7), and the mixed aluminum is selected. The lightweight material 14 such as aluminum flows out from the trough-shaped lightweight material discharging portion 33c provided in the raw material charging portion 33a of the sorting container 33, and the heavy material 15 is discharged from the discharging conveyor 3
5 is discharged from the heavy-weight discharge part 33b of the sorting container 33. As shown in FIG. 2, the lightweight object 14 is a heavy liquid sorter 16
Is discharged together with the heavy liquid 13 and is sifted by the heavy liquid separating screen 36 before being sent to the draining screen 17. The wastewater discharged from the heavy liquid separation sieve 36 is temporarily stored in the tank 36a and separated into the heavy liquid 13 and water containing impurities, and the heavy liquid 13 is returned to the heavy liquid tank 24 while Is sent to the magnetic separator 19 together with the drainage containing impurities discharged from the draining screens 17, 18.
【0011】水切り篩17、18の下方には、軽量物ホ
ッパ37と重量物ホッパ38がそれぞれ配置されてお
り、両ホッパ37、38の排出部の下方に一対のフィー
ダ39が設けられている。フィーダ39の下方には、下
流の上方に磁選機40が吊下された選別コンベア41が
配置されており、磁選機40により軽量物14および重
量物15中の鉄が吸着除去されて鉄回収ボックス42内
に投下される。選別コンベア41の下流側の下方にはフ
ィーダ43が配置されており、フィーダ43の下方にリ
ニアモータの原理を応用した非鉄選別機44が配置され
ている。非鉄選別機44の下方には複数個のコンベアか
らなる分別装置45が配置されており、前記軽量物14
および重量物15をそれぞれ別々に投入することによ
り、分別されたアルミニウム、ダスト、銅、亜鉛、ステ
ンレスが、アルミニウム回収ボックス46、ダスト回収
ボックス47、銅亜鉛回収ボックス48およびステンレ
ス回収ボックス49に回収される。Below the draining screens 17 and 18, a lightweight hopper 37 and a heavy hopper 38 are disposed, respectively, and a pair of feeders 39 are provided below the discharge parts of both hoppers 37 and 38. Below the feeder 39, a sorting conveyer 41, in which a magnetic separator 40 is suspended above the downstream, is arranged. The magnetic separator 40 adsorbs and removes iron in the lightweight objects 14 and the heavy objects 15 to remove the iron. Dropped into 42. A feeder 43 is arranged below the sorting conveyor 41 on the downstream side, and a non-ferrous sorting machine 44 applying the principle of a linear motor is arranged below the feeder 43. Below the non-ferrous sorter 44, a sorting device 45 composed of a plurality of conveyors is arranged.
By separately introducing the heavy object 15 and the heavy object 15, the separated aluminum, dust, copper, zinc, and stainless steel are recovered in the aluminum recovery box 46, the dust recovery box 47, the copper-zinc recovery box 48, and the stainless steel recovery box 49. It
【0012】図において、符号50は給水ポンプ、符号
51は銅線などの不純物のダストボックス、符号52は
重液ポンプ、符号53は使用する重液13より比重の重
い重液を貯液する重質タンク、符号54は濃度計を示し
ている。In the figure, reference numeral 50 is a water supply pump, reference numeral 51 is a dust box of impurities such as copper wire, reference numeral 52 is a heavy liquid pump, and reference numeral 53 is a heavy liquid for storing a heavy liquid having a specific gravity higher than that of the heavy liquid 13 used. The tank, reference numeral 54, represents a densitometer.
【0013】続いて、重液選別設備10の動作を説明す
る。図2に示すように、破砕され軽量ダストおよび屑鉄
が除去された処理原料は搬入装置25により長尺選別機
11内に投入されて、小物、大物や長物が除去され、除
去物は分別装置26により小物回収箱27、大物回収箱
28、長物回収箱29にそれぞれ回収される。Next, the operation of the heavy liquid sorting equipment 10 will be described. As shown in FIG. 2, the processing raw material from which the light dust and scrap iron have been crushed and removed is introduced into the long sorter 11 by the carry-in device 25 to remove small items, large items and long items, and the removed items are separated by the sorting device 26. As a result, the small item collection box 27, the large item collection box 28, and the long item collection box 29 are collected.
【0014】図1に示すように、所定寸法の処理原料だ
けが水洗機12まで搬送され、原料投入部30aより水
洗容器30内に投下されて水中を下降する。一方、水洗
容器30に形成された水吹き出し部32からは、ポンプ
30Bの圧力により斜め上方に向かって水が吹き出して
おり、これが上昇水流になって下降中の処理原料に吹き
付けられると、処理原料に含まれる油分や塵等の不要物
Dが浮き上がって水面からダスト類排出部30c内に流
れ落ち、その後、ダストボックス30cに投下されて回
収される。また、水洗容器30の底面から取り出された
排水は、循環水槽30A内に流れ落ちて、ポンプ30B
により水洗機12用の水として循環使用され、また、循
環水槽30A内に溜まった不純物は内蔵するコンベアに
よりダストボックス30Cに排出される。As shown in FIG. 1, only the treated raw material having a predetermined size is conveyed to the water washing machine 12 and is dropped into the water washing container 30 from the raw material feeding portion 30a to descend in water. On the other hand, from the water blowing portion 32 formed in the water washing container 30, water is blown obliquely upward due to the pressure of the pump 30B, and when this becomes a rising water flow and is sprayed on the processing raw material that is descending, water is fed. Undesired substances D such as oil and dust contained in the oil float up and flow down from the water surface into the dust discharge unit 30c, and then are dropped into the dust box 30c and collected. In addition, the waste water taken out from the bottom surface of the washing container 30 flows down into the circulating water tank 30A, and the pump 30B
By this, the water is circulated and used as water for the water washing machine 12, and the impurities accumulated in the circulating water tank 30A are discharged to the dust box 30C by a built-in conveyor.
【0015】不要物Dが取り除かれた処理原料は、水洗
機12の下部に配置された搬出コンベア31により原料
排出部30b上まで持ち上げられ、その後、重液選別機
16の選別容器33の原料投入部33a内に投入され
て、選別容器33内の重液13により軽量物14と重量
物15に分離される。この際、重液選別機16に投下さ
れた処理原料には、水洗機12による効果的な洗浄によ
り塵や油分といった不要物D、空気等の付着がほとんど
ないので、水洗容器30から取り出された処理原料を重
液選別機16に投入して選別する際に重液13の液面上
に泡が発生しなくなり、処理原料を効率良く軽量物14
と重量物15とに重液選別できる。The treated raw material from which the unnecessary substances D have been removed is lifted up to the raw material discharge section 30b by the carry-out conveyor 31 arranged at the lower part of the water washing machine 12, and then the raw material is put into the sorting container 33 of the heavy liquid sorting machine 16. The liquid is put into the portion 33 a and separated into the light weight 14 and the heavy weight 15 by the heavy liquid 13 in the sorting container 33. At this time, since the treatment raw material thrown into the heavy liquid sorter 16 has almost no adhering of the unnecessary substances D such as dust and oil and air due to the effective washing by the washing machine 12, it is taken out from the washing container 30. When the processing raw material is put into the heavy liquid sorting machine 16 and sorted, bubbles are not generated on the liquid surface of the heavy liquid 13, and the processing raw material is efficiently and lightly weighted.
It is possible to sort heavy liquid into the heavy load 15 and the heavy load 15.
【0016】選別された軽量物14は、軽量物排出部3
3cから重液分離篩36を介して水切り篩17に送ら
れ、対する重量物15は排出コンベア35により重量物
排出部33bから水切り篩18に送られる。それぞれの
水切り篩17、18により分離された軽量物14や重量
物15は、一旦軽量物ホッパ37と重量物ホッパ38に
収納され、時間をずらして各々個別にフィーダ39によ
り選別コンベア41上に落下され、その後、フィーダ4
3を介して非鉄選別機44により各種金属に分けられ
て、それぞれの金属は分別装置45によりアルミニウム
回収ボックス46、ダスト回収ボックス47、銅亜鉛回
収ボックス48およびステンレス回収ボックス49に回
収される。なお、処理原料中に含まれる鉄は選別コンベ
ア41の下流に吊下された磁選機40により吸着されて
鉄回収ボックス42内に回収される。The selected lightweight articles 14 are transferred to the lightweight article discharge section 3
3c is sent to the draining screen 17 through the heavy liquid separating screen 36, and the heavy object 15 to the counter 3c is sent to the draining screen 18 from the heavy object discharging part 33b by the discharging conveyor 35. The lightweight objects 14 and the heavy objects 15 separated by the draining screens 17 and 18 are once stored in the lightweight object hopper 37 and the heavy object hopper 38, respectively, and after a staggered time, they individually fall onto the sorting conveyor 41 by the feeder 39. And then feeder 4
Various metals are separated by the non-ferrous sorter 44 via 3, and each metal is recovered by the sorting device 45 into the aluminum recovery box 46, the dust recovery box 47, the copper zinc recovery box 48, and the stainless recovery box 49. The iron contained in the processing raw material is adsorbed by the magnetic separator 40 suspended downstream of the selection conveyor 41 and recovered in the iron recovery box 42.
【0017】さて、水切り篩17、18から排出された
銅線などの不純物を含む排水は、重液選別機16の底面
から取り出された重液13と、重液分離篩36からタン
ク36aを介して排出された希釈側の排水と共に磁選機
19に送られる。磁選機19では排水中に含まれる磁性
粉体だけが吸着分離され、その後、磁性粉体は脱磁機2
2により脱磁されて重液タンク24内に供給される。な
お、重液タンク24には、タンク36aから排出された
重液側の排水が直接流入されている。The drainage containing impurities such as copper wires discharged from the drainage screens 17 and 18 is discharged from the bottom of the heavy liquid separator 16 and the heavy liquid 13 from the heavy liquid separation screen 36 through the tank 36a. It is sent to the magnetic separator 19 together with the discharged wastewater on the dilution side. In the magnetic separator 19, only the magnetic powder contained in the waste water is adsorbed and separated, and then the magnetic powder is removed by the demagnetizer 2.
It is demagnetized by 2 and supplied into the heavy liquid tank 24. The heavy liquid tank 24 directly receives the heavy liquid wastewater discharged from the tank 36a.
【0018】重液タンク24内の重液13は、濃度計5
4を用いて比重が2.5になるように重質タンク53か
ら高濃度の重液が供給されて比重調整され、その後、重
液ポンプ52により重液選別機16内に圧送されて循環
使用される。一方、磁性粉体が除去された磁選機19の
排水は、一旦、水タンク21に貯液される。これによ
り、銅線などの不純物が水タンク21の下部に沈下し、
沈下した不純物は排出コンベア20により掻き上げられ
て水タンク21の排出部よりダストボックス51に回収
される。そして、水タンク21の上澄み水だけが給水ポ
ンプ50により水切り篩17、18側に圧送されて循環
使用される。The heavy liquid 13 in the heavy liquid tank 24 is a concentration meter 5
4, a high-concentration heavy liquid is supplied from the heavy tank 53 so that the specific gravity becomes 2.5, the specific gravity is adjusted, and thereafter, the heavy liquid is pumped by the heavy liquid pump 52 into the heavy liquid sorter 16 for circulation use. To be done. On the other hand, the waste water of the magnetic separator 19 from which the magnetic powder has been removed is temporarily stored in the water tank 21. As a result, impurities such as copper wires sink to the bottom of the water tank 21,
The settled impurities are scraped up by the discharge conveyor 20 and collected in the dust box 51 from the discharge part of the water tank 21. Then, only the supernatant water of the water tank 21 is pumped to the draining sieves 17 and 18 side by the water supply pump 50 and is circulated and used.
【0019】以上、本発明の実施例を説明したが、本発
明はこの実施例に限定されるものではなく、要旨を逸脱
しない範囲での設計変更などがあっても本発明に含まれ
る。例えば、水洗容器から取り出した使用後の水に、湿
潤剤(例えば、日本香料株式会社製のWA−20#)を
添加し、その後、例えば沈澱や濾過などにより不純物を
取り除いて水を循環使用することもできる。さらに、実
施例では、水洗容器内の水量を、処理原料のほぼ20倍
としたが、これに限定しなくても処理原料の20倍以上
であればよい。Although the embodiment of the present invention has been described above, the present invention is not limited to this embodiment, and any modification of the design without departing from the scope of the invention is included in the present invention. For example, a wetting agent (for example, WA-20 # manufactured by Nippon Perfume Co., Ltd.) is added to the used water taken out from the water washing container, and then impurities are removed by, for example, precipitation or filtration, and the water is circulated and used. You can also Further, in the examples, the amount of water in the water washing container was set to approximately 20 times the amount of the processing raw material, but it is not limited to this and may be 20 times or more the processing raw material.
【0020】[0020]
【発明の効果】以上の説明からも明らかなように、請求
項1、2記載の重液選別前処理方法においては、予め水
洗容器による効果的な洗浄を処理原料に施しておくの
で、重液選別機に投入される処理原料には塵や油分の付
着がほとんどなく、これにより重液選別する際に重液の
液面上に泡が発生しなくなり、処理原料を効率良く軽量
物と重量物とに選別できる。そして、前記水洗容器の中
間部に水吹き出し部を備え、該水吹き出し部から上部の
水は上昇水流となっているので、処理原料の洗浄の他、
分離された油分や塵を積極的に浮上させて分離している
ので、より効率的に洗浄が可能となる。特に、請求項2
記載の重液選別前処理方法においては、水洗容器内の水
量が、処理原料の重量の20倍以上と洗浄に大量の水を
使用するので、十分な水洗効果を得ることができる。As is apparent from the above description, in the pretreatment method for heavy liquid sorting according to claims 1 and 2, the treatment liquid is preliminarily subjected to effective cleaning in a water washing container, and therefore, Almost no dust or oil adheres to the processing raw material fed into the sorter, which prevents bubbles from forming on the liquid surface of the heavy liquid during heavy liquid sorting, making the processing raw material efficient and lightweight. You can select Further, a water blowing portion is provided in an intermediate portion of the water washing container, and the water above the water blowing portion has an upward flow, so that in addition to washing the processing raw material,
Since the separated oil and dust are positively floated and separated, more efficient cleaning is possible. In particular, claim 2
In the described heavy liquid sorting pretreatment method, since the amount of water in the water washing container is 20 times or more the weight of the treatment raw material and a large amount of water is used for washing, a sufficient water washing effect can be obtained.
【図1】本発明の一実施例に係る重液選別前処理方法が
適用された重液選別設備の要部概略図である。FIG. 1 is a schematic view of a main part of a heavy liquid sorting facility to which a heavy liquid sorting pretreatment method according to an embodiment of the present invention is applied.
【図2】前記重液選別処理方法が適用された重液選別設
備の全体概略図である。FIG. 2 is an overall schematic view of a heavy liquid sorting facility to which the heavy liquid sorting method is applied.
10 重液選別設備 11 長尺選別
機 12 水洗機 13 重液 14 軽量物 15 重量物 16 重液選別機 17 水切り篩 18 水切り篩 19 磁選機 20 排出コンベア 21 水タンク 22 脱磁機 24 重液タン
ク 25 搬入装置 26 分別装置 27 小物回収箱 28 大物回収
箱 29 長物回収箱 30 水洗容器 30a 原料投入部 30b 原料排
出部 30c ダスト類排出部 30A 循環水
槽 30B ポンプ 30C ダスト
ボックス 31 排出コンベア 32 水吹き出
し部 33 選別容器 33a 原料投
入部 33b 重量物排出部 33c 軽量物
排出部 34 吹き出し部 35 排出コン
ベア 36 重液分離篩 36a タンク 37 軽量物ホッパ 38 重量物ホ
ッパ 39 フィーダ 40 磁選機 41 選別コンベア 42 鉄回収ボ
ックス 43 フィーダ 44 非鉄選別
機 45 分別装置 46 アルミニ
ウム回収ボックス 47 ダスト回収ボックス 48 銅亜鉛回
収ボックス 49 ステンレス回収ボックス 50 給水ポン
プ 51 ダストボックス 52 重液ポン
プ 53 重質タンク 54 濃度計10 Heavy Liquid Sorting Equipment 11 Long Sorting Machine 12 Water Washing Machine 13 Heavy Liquid 14 Lightweight 15 Heavy Weight 16 Heavy Liquid Sorting Machine 17 Draining Sieve 18 Draining Sieve 19 Magnetic Separator 20 Discharge Conveyor 21 Water Tank 22 Demagnetizer 24 Heavy Liquid Tank 25 Carrying-in device 26 Sorting device 27 Small-sized collection box 28 Large-sized collection box 29 Long-sized collection box 30 Rinsing container 30a Raw material input part 30b Raw material discharging part 30c Dust discharging part 30A Circulating water tank 30B Pump 30C Dust box 31 Discharging conveyor 32 Water blowing part 33 Sorting Container 33a Raw material charging part 33b Heavy material discharging part 33c Light material discharging part 34 Discharging part 35 Discharging conveyor 36 Heavy liquid separating sieve 36a Tank 37 Light material hopper 38 Heavy material hopper 39 Feeder 40 Magnetic separator 41 Sorting conveyor 42 Iron recovery box 43 Feeder 44 Non-ferrous sorting 45 fractionator 46 aluminum collection box 47 dust collecting box 48 of copper zinc recovery box 49 stainless recovery box 50 feed water pump 51 the dust box 52 duplex pump 53 Heavy tank 54 densitometer
Claims (2)
を投入して、該処理原料を比重差により浮上する軽量物
と沈降する重量物とに選別する重液選別を行うにあたっ
て、 予め、前記選別容器に投入される処理原料を、中間部に
水吹き出し部を備え該水吹き出し部から上部は上昇水流
となっている水洗容器内に投入し、 前記上昇水流により、投入した前記処理原料に付着して
いた塵及び油分を洗浄すると共に、積極的に該塵及び油
分を浮上させて除去することを特徴とする重液選別前処
理方法。1. When performing a heavy liquid sorting in which a processing raw material is put into a sorting container in which a heavy liquid is stored, and the processing raw material is sorted into a lightweight material that floats due to a difference in specific gravity and a heavy material that sediments, In advance, the processing raw material to be charged into the sorting container is charged into a washing container in which a water blowing part is provided in an intermediate part and an upper part has a rising water flow from the water blowing part, and the processing flow introduced by the rising water flow. A method for pretreatment of heavy liquid sorting, which comprises cleaning dust and oil attached to a raw material and positively floating and removing the dust and oil.
の重量の20倍以上である請求項1記載の重液選別前処
理方法。2. The pretreatment method for heavy liquid sorting according to claim 1, wherein the amount of water in the water washing container is 20 times or more the weight of the treatment raw material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5305797A JP2518800B2 (en) | 1993-11-10 | 1993-11-10 | Pretreatment method for heavy liquid sorting |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5305797A JP2518800B2 (en) | 1993-11-10 | 1993-11-10 | Pretreatment method for heavy liquid sorting |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07132244A JPH07132244A (en) | 1995-05-23 |
JP2518800B2 true JP2518800B2 (en) | 1996-07-31 |
Family
ID=17949477
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5305797A Expired - Fee Related JP2518800B2 (en) | 1993-11-10 | 1993-11-10 | Pretreatment method for heavy liquid sorting |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2518800B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2381483A (en) * | 2001-09-10 | 2003-05-07 | Waste Mechanics Ltd | Floatation separation with nozzles and weir |
CN100363112C (en) * | 2003-01-30 | 2008-01-23 | 谢明明 | Method and device for separate collecting weight garbage |
JP2004305957A (en) * | 2003-04-09 | 2004-11-04 | Dowa Mining Co Ltd | Method for sorting metal from combustion residue |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS48100760A (en) * | 1972-04-01 | 1973-12-19 |
-
1993
- 1993-11-10 JP JP5305797A patent/JP2518800B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH07132244A (en) | 1995-05-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP3404501B2 (en) | Method of treating waste material containing at least partially reusable components | |
US4802976A (en) | Method for recovering fine clean coal | |
JP4943309B2 (en) | Powder processing system and powder processing method | |
JP2000510397A (en) | Method and apparatus for separating and treating recoverable waste | |
JP2012115838A (en) | Wet sorting apparatus | |
US4325819A (en) | Coal washing plant | |
JP4697719B2 (en) | Method for purifying contaminated soil and separation apparatus used therefor | |
JP2518800B2 (en) | Pretreatment method for heavy liquid sorting | |
AU640905B2 (en) | Waterflow differential electrical charging process for ores | |
JP2530554B2 (en) | How to sort light and heavy mixtures | |
GB2223191A (en) | Separating coal washery residue | |
JP2819070B2 (en) | Method and apparatus for separating and recovering mixed waste | |
GB2583460A (en) | Method and modular system for washing and grading sand and aggregate | |
JPH11253833A (en) | Separation of contaminant and washing device | |
US3467594A (en) | Separating method and apparatus | |
JPH0760153A (en) | Heavy fluid sorting device | |
JP4931841B2 (en) | Wet sorting device | |
JP4376178B2 (en) | Shredder dust treatment method and equipment | |
US4191201A (en) | Apparatus for selectively reclaiming parts from film cartridges | |
US4584094A (en) | Method and apparatus for reclaiming coal | |
KR970003861B1 (en) | Method for processing particles and equipment thereof | |
WO2020186241A1 (en) | System and method for recovering metal from ash | |
KR0134162B1 (en) | Method for separating light material from heavy material in mixture and apparatus thereof | |
CA3134047A1 (en) | System and method for recovering desired materials using a ball mill or rod mill | |
US5169005A (en) | Apparatus for separating material of lighter specific gravity from material of a heavier specific gravity |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090517 Year of fee payment: 13 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100517 Year of fee payment: 14 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100517 Year of fee payment: 14 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110517 Year of fee payment: 15 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110517 Year of fee payment: 15 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120517 Year of fee payment: 16 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130517 Year of fee payment: 17 |
|
LAPS | Cancellation because of no payment of annual fees |