JPH0975851A - Method and apparatus for pneumatic sorting of solid - Google Patents

Method and apparatus for pneumatic sorting of solid

Info

Publication number
JPH0975851A
JPH0975851A JP24137195A JP24137195A JPH0975851A JP H0975851 A JPH0975851 A JP H0975851A JP 24137195 A JP24137195 A JP 24137195A JP 24137195 A JP24137195 A JP 24137195A JP H0975851 A JPH0975851 A JP H0975851A
Authority
JP
Japan
Prior art keywords
airflow
crushed mixture
tower
mesh plate
flow
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
Application number
JP24137195A
Other languages
Japanese (ja)
Other versions
JP2757333B2 (en
Inventor
Satoshi Arai
怜 荒井
Shinichi Ito
信一 伊藤
Hiroshi Sakamoto
宏 坂本
Hidefushi Ooi
英節 大井
Koki Yotsumoto
弘毅 四元
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP24137195A priority Critical patent/JP2757333B2/en
Publication of JPH0975851A publication Critical patent/JPH0975851A/en
Application granted granted Critical
Publication of JP2757333B2 publication Critical patent/JP2757333B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Combined Means For Separation Of Solids (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for pneumatic sorting of solid which can sort needle-shaped materials and non-needle-shaped materials in a crushed mixture efficiently and precisely, and an apparatus for the method. SOLUTION: An air current which ascends in a pneumatic sorting column 1 is supplied from the air current supply port 30 of the column 1, a crushed mixture of needle-shaped materials and non-needle-shaped materials is supplied from a supply port 22, and the mixture is fluidized in a fluidizing region 27 between an upper part narrow cylinder 21 and a mesh plate 25. In this region 27, the needle-shaped materials tend to be decelerated to fall with the longitudinal direction directed to the gravity direction so that they pass through the mesh plate 25 to be recovered below the column 1. The crushed mixture which repeats floating and dropping in the fluidizing region 27 is discharged through the discharge opening in the sidewall of the column 1. The lightweight materials in the crushed mixture are floated to the upper part of the column 1 to be discharged.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、廃家電製品や廃自
動車などの粗大廃棄物の破砕混合物中に混在していると
ころの、電磁石用コイルや被覆電線の切断物である銅等
の金属製針状物を、リサイクルのためにそれ以外の非針
状物から分別する方法及び装置に関するものであり、特
に、それらの形状の差異を利用して乾式により効率よく
分別する固形物の気流選別方法及び装置に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a metal such as copper, which is a cut product of a coil for an electromagnet or a covered electric wire, which is mixed in a crushed mixture of coarse waste such as waste home electric appliances and waste automobiles. The present invention relates to a method and an apparatus for separating needle-shaped materials from other non-needle-shaped materials for recycling, and in particular, a method for air-flow sorting of solids that efficiently separates them by a dry method by utilizing differences in their shapes. And the device.

【0002】[0002]

【従来の技術】種々の被覆電線やモータなどを破砕・切
断処理して得られるところの銅線等のの金属製針状物
を、ポリ塩化ビニール等の電線被覆材の切断物や、モー
タの固定枠、保護カバー、回転子鉄心などの他の非針状
物の破砕混合物から効率よく、高精度に分別すること
は、従来の風力、ジグ、テーブル、流動層、サイクロン
選別技術では困難である。そのため、本発明者らは、気
流を利用して乾式により分別する技術の開発を行い、先
に、特願平6−74300号等として提案しているが、
より一層簡便で精度の良い分別を行う技術の開発が望ま
れている。
2. Description of the Related Art Metal needles such as copper wires obtained by crushing and cutting various coated electric wires and motors are used for cutting electric wire covering materials such as polyvinyl chloride and motors. Efficient and highly accurate separation from crushed mixture of other non-needle-like materials such as fixed frame, protective cover, rotor core is difficult with conventional wind power, jig, table, fluidized bed, cyclone sorting technology. . Therefore, the present inventors have developed a technique for separating by dry method using an air flow, and have previously proposed it as Japanese Patent Application No. 6-74300.
There is a demand for the development of a technique for more simple and accurate separation.

【0003】[0003]

【発明が解決しようとする課題】本発明の技術的課題
は、破砕混合物中の針状物と非針状物とを、乾式により
効率よく分別することができる固形物の気流選別方法及
びその装置を提供することにある。また、本発明の技術
的課題は、破砕混合物中の針状物と非針状物とを、気流
中における針状物の挙動を利用して簡便に高精度で分別
することができる固形物の気流選別方法及びその装置を
提供することにある。
DISCLOSURE OF THE INVENTION The technical problem of the present invention is to provide a method and an apparatus for air separation of solid matter, which can efficiently separate needle-like substances and non-needle-like substances in a crushed mixture by a dry method. To provide. Further, the technical problem of the present invention is to separate a needle-like material and a non-needle-like material in a crushed mixture from a solid material that can be easily and highly accurately separated by utilizing the behavior of the needle-like material in an air stream. An object of the present invention is to provide an airflow selection method and an apparatus therefor.

【0004】[0004]

【課題を解決するための手段】上記課題を解決するため
の本発明の固形物の気流選別方法は、針状物分別用メッ
シュ板の上方に破砕混合物の流動域を介して流路断面積
を狭窄する気流速度調節用上部狭窄筒を、上記メッシュ
板の直下に流路断面積を狭窄する気流速度調節用下部狭
窄筒を設けた気流選別塔において、上記メッシュ板上の
流動域に針状物及び非針状物の破砕混合物を供給すると
共に、下部狭窄筒の下方の気流選別塔側壁から気流選別
塔を上昇する気流を供給することにより、上記流動域に
おいて破砕混合物を流動させ、上記流動の間に、長手方
向を重力方向に向けて失速落下する針状物をメッシュ板
を通してその下方に落下させ、それを気流選別塔の下部
で回収し、破砕混合物中の軽量物を気流選別塔の上部に
浮揚させて排出すると共に、上記メッシュ板上の流動域
で流動を繰り返す破砕混合物を、気流選別塔側壁に設け
た上記流動域を臨む排出口を通して逐次排出させるるこ
とを特徴とするものである。
In order to solve the above-mentioned problems, an air flow sorting method of a solid matter of the present invention provides a flow path cross-sectional area above a needle-like object sorting mesh plate through a flow region of a crushed mixture. In an airflow selection tower in which an upper airflow speed adjusting narrowing cylinder for narrowing is provided, and an airflow speed adjusting lower narrowing cylinder for narrowing the flow passage cross-sectional area is provided immediately below the mesh plate, a needle-like object in the flow region on the mesh plate. And supplying a crushed mixture of non-needle-like substances and supplying an air stream rising up the air stream selection tower from the side wall of the air stream selection tower below the lower constriction cylinder, thereby causing the crushed mixture to flow in the above-mentioned flow region, In the meantime, needle-like objects that stall and fall with the longitudinal direction oriented in the direction of gravity are dropped through the mesh plate below and collected in the lower part of the airflow selection tower, and the light weight substances in the crushed mixture are collected in the upper part of the airflow selection tower. Levitate and discharge Together, is characterized in that the crushed mixture repeatedly flow in flow area on the mesh plates, Ruru successively drained through the discharge port facing the flow field formed in the air flow sorting column side wall.

【0005】上記気流選別方法においては、気流選別塔
側壁に設けた排出口を通して排出される破砕混合物を、
次段の気流選別塔におけるメッシュ板上に供給し、同一
の方法により再度針状物をメッシュ板の下方に落下させ
て、気流選別塔の下部で回収すると共に、軽量物を気流
選別塔の上部に浮揚させて排出し、メッシュ板上の流動
域で流動を繰り返す破砕混合物を気流選別塔側壁の排出
口を通して逐次排出させることができる。
In the above-described airflow sorting method, the crushed mixture discharged through the outlet provided on the side wall of the airflow sorting tower is
Supply it onto the mesh plate in the next airflow selection tower, drop needles below the mesh plate again by the same method, and collect it in the lower part of the airflow selection tower, and at the same time, light weight the upper part of the airflow selection tower. The crushed mixture, which is floated and discharged to the above, and which repeats the flow in the flow region on the mesh plate, can be sequentially discharged through the discharge port on the side wall of the air flow sorting column.

【0006】また、上記課題を解決するための本発明の
気流選別装置は、筒状をなす気流選別塔内に、破砕混合
物中の針状物がその長手方向を重力方向に向けた場合に
通る針状物分別用メッシュ板を配設すると共に、そのメ
ッシュ板の上方に破砕混合物の流動域を介して流路断面
積を狭窄する気流速度調節用上部狭窄筒を、上記メッシ
ュ板の直下に流路断面積を狭窄する気流速度調節用下部
狭窄筒を設け、上記気流選別塔側壁の上部狭窄筒より上
方に破砕混合物を供給する供給口を開口させると共に、
上記気流選別塔側壁の下部狭窄筒の下方に、気流選別塔
を上昇する気流を供給するための気流供給口を開口さ
せ、気流選別塔の下部に、上記メッシュ板を通過して下
方に落下した針状物を回収する回収部を設け、気流選別
塔の上部に破砕混合物中の軽量物を分離排出する分離部
を設けると共に、気流選別塔側壁に上記流動域に臨む破
砕混合物の排出口を設けたことを特徴とするものであ
る。
Further, the airflow sorting apparatus of the present invention for solving the above-mentioned problems passes through a tubular airflow sorting tower when the needle-like material in the crushed mixture has its longitudinal direction oriented in the direction of gravity. A mesh plate for separating needles is arranged, and an upper constriction tube for air flow velocity control that narrows the cross-sectional area of the flow path is flowed above the mesh plate just below the mesh plate. A lower constriction tube for air flow velocity control for constricting the road cross-sectional area is provided, and a supply port for supplying the crushed mixture is opened above the upper confinement tube on the side wall of the air flow selection tower,
Below the lower constriction cylinder of the side wall of the airflow selection tower, an airflow supply port for supplying an airflow rising in the airflow selection tower was opened, and at the bottom of the airflow selection tower, passed through the mesh plate and dropped downward. A collection unit for collecting needle-like substances is provided, a separation unit for separating and discharging the lightweight substances in the crushed mixture is provided at the upper part of the airflow selection tower, and an outlet for the crushed mixture that faces the above-mentioned flow region is provided on the side wall of the airflow selection tower. It is characterized by that.

【0007】上記気流選別装置においては、気流選別塔
の側壁に設けた破砕混合物の排出口を、同じ構成の次段
の気流選別塔におけるメッシュ板上の破砕混合物の供給
口に開口させ、複数段の気流選別塔の下部の回収部にお
いて針状物を回収することができる。
In the above-described airflow sorting apparatus, the discharge port for the crushed mixture provided on the side wall of the airflow sorting tower is opened to the supply port for the crushed mixture on the mesh plate in the next-stage airflow sorting tower having the same structure, and a plurality of stages are provided. The needle-shaped material can be collected in the collecting section below the airflow sorting tower.

【0008】上記方法及び装置による破砕混合物の気流
選別に際し、気流供給口から所要流量の気流を供給する
と、メッシュ板の直下の下部狭窄筒及びメッシュ板の上
方の上部狭窄筒において、流路の狭窄により気流の速度
が大きくなる。そのため、破砕混合物の供給口から針状
物及び非針状物の破砕混合物を供給すると、その破砕混
合物のうちの軽量物は上部狭窄筒の部分から下方に落下
することなく、気流選別塔の上方に浮揚し、気流選別塔
の上端の分離部において分離排出され、その他の針状物
及び非針状物はメッシュ板上の流動域において下方から
上昇する気流により流動せしめられ、浮揚、失速落下を
繰り返すが、その間にも軽量物は上部狭窄筒の高流速部
分を経て気流選別塔の上方に浮揚し、分離される。
When airflow of the crushed mixture is selected by the above-mentioned method and apparatus, if a required flow rate of airflow is supplied from the airflow supply port, the flow path is narrowed in the lower constriction cylinder immediately below the mesh plate and the upper constriction cylinder above the mesh plate. This increases the velocity of the air flow. Therefore, when a crushed mixture of needle-shaped materials and non-needle-shaped materials is supplied from the crushed-mixture supply port, the light weight of the crushed mixture does not fall downward from the upper constriction tube portion, and Floated, and separated and discharged at the separation part at the upper end of the airflow selection tower, and other needle-shaped and non-needle-shaped materials are made to flow by the airflow rising from below in the flow area on the mesh plate, causing levitation and stall fall. Again, during that time, the lightweight material is floated above the airflow selection tower through the high flow velocity portion of the upper constriction tube and separated.

【0009】メッシュ板上の気流中で流動する破砕混合
物は、それらが気流中で失速落下するときに、特にその
破砕混合物中の針状物が長手方向を重力方向に向けるよ
うに傾く傾向があり、このように長手方向を重力方向に
向けた針状物は気流中における浮揚力が著しく低下し、
そのため失速落下してメッシュ板を通過し、気流選別塔
の下部の回収部において回収される。一方、上記流動域
で浮揚及び落下を繰り返す破砕混合物は、それが気流選
別塔側壁の破砕混合物の排出口付近に達したときに、そ
の排出口から逐次排出される。そのため、破砕混合物
を、メッシュ板を通過する針状物と、結果的に排出口か
ら排出されるメッシュ板上の残留物と、気流選別塔の上
方に浮揚する軽量物とに容易に効率よく分別することが
できる。
The crushed mixture flowing in the airflow on the mesh plate tends to tilt when the stalls of the crushed mixture flow in the airflow, especially when the needles in the crushed mixture are oriented so that the longitudinal direction is oriented in the direction of gravity. , In this way, the levitation force in the airflow of the needle-shaped object whose longitudinal direction is oriented in the direction of gravity is significantly reduced,
Therefore, it stall-falls, passes through the mesh plate, and is collected in the collecting section below the airflow selection tower. On the other hand, the crushed mixture which is repeatedly floated and dropped in the above-mentioned fluidized region is sequentially discharged from the discharge port of the crushed mixture when it reaches the vicinity of the discharge port of the crushed mixture on the side wall of the air stream selection tower. Therefore, the crushed mixture can be easily and efficiently separated into needle-like substances that pass through the mesh plate, residues on the mesh plate that are eventually discharged from the discharge port, and lightweight substances that float above the airflow selection tower. can do.

【0010】気流選別塔を複数段に設けた場合には、第
1段の気流選別塔におけるメッシュ板上に残留して排出
口から排出された破砕混合物が、次段の気流選別塔にお
ける破砕混合物の供給口から同気流選別塔に供給され、
第1段の気流選別塔の場合と同様にして、その破砕混合
物中における針状物がメッシュ板を通して気流選別塔の
下部の回収部において回収される。このようにして、複
数段の気流選別塔において針状物を回収すると、破砕混
合物中における針状物と非針状物とを高精度に分別する
ことが可能になる。
When a plurality of airflow selection towers are provided, the crushed mixture remaining on the mesh plate in the first airflow selection tower and discharged from the outlet is the crushed mixture in the next airflow selection tower. Is supplied to the same airflow selection tower from the supply port of
Similar to the case of the first-stage airflow selection tower, the needle-like material in the crushed mixture is recovered through the mesh plate in the recovery section below the airflow selection tower. In this way, when the needle-shaped material is collected in the plurality of stages of the air flow sorting tower, it becomes possible to accurately separate the needle-shaped material and the non-needle-shaped material in the crushed mixture.

【0011】[0011]

【発明の実施の形態】以下に、図1〜図3に示す気流選
別装置の実施例を参照して本発明の実施の形態について
説明する。図1に示す気流選別装置は、廃家電製品、廃
自動車などの廃棄物のリサイクルをはかるために、それ
らを解体、破砕、選別の工程を経て各素材毎に分別する
場合に、モーターをはじめ各種のコイルや電線等の破砕
によって生じる銅線の切断物等の針状物と、それ以外の
非針状物とを、選別分離するために用いるものであり、
ここでは、互いに並列に設置された複数段の気流選別
塔、即ち、第1段の気流選別塔1と第2段の気流選別塔
2とを備えた場合を示しているが、更に多段に連設する
ことができる。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the examples of the air flow sorting apparatus shown in FIGS. The airflow sorter shown in Fig. 1 uses various types of motors, such as motors, when waste materials such as waste home electric appliances and automobiles are recycled through the steps of disassembling, crushing, and sorting in order to recycle them. Is used to separate and separate needle-like objects such as cut pieces of copper wire caused by crushing of coils and electric wires, and other non-needle-like objects,
Here, a case is shown in which a plurality of stages of airflow sorting towers, that is, a first stage airflow sorting tower 1 and a second stage airflow sorting tower 2 are provided in parallel with each other, but a further multistage cascade is provided. Can be installed.

【0012】上記第1段の気流選別塔1は、実質的に筒
状をなすもので、複数の円筒11〜15をコラム状に連
設することにより構成し、これらの各円筒は、それぞれ
の端部のフランジにおいて図示しないボルトにより連結
している。気流選別塔1の一部を構成する最上位の円筒
11は、その上部に破砕混合物中の軽量物の分離部を形
成する浮揚物回収筒18を連設している。この浮揚物回
収筒18は、円筒11よりも十分に大径のもので、その
上面に浮揚物飛散防止用メッシュ板19が張設され、そ
の下部周囲に回収した浮揚物を排出する排出筒20が連
結されている。
The first-stage airflow selection tower 1 has a substantially cylindrical shape, and is constituted by connecting a plurality of cylinders 11 to 15 in a column shape, and each of these cylinders has its own shape. The flanges at the ends are connected by bolts (not shown). The uppermost cylinder 11 that constitutes a part of the airflow sorting tower 1 is provided with a float collection cylinder 18 that is connected to the upper part of the cylinder 11 to form a separation portion of the lightweight material in the crushed mixture. The floating material collecting cylinder 18 has a diameter sufficiently larger than that of the cylinder 11. A floating material scattering prevention mesh plate 19 is stretched on the upper surface of the floating material collecting cylinder 18, and a discharge cylinder 20 for discharging the collected floating material around the lower part thereof. Are connected.

【0013】この円筒11にフランジを介して接続され
た円筒12は、下端内壁に流路断面積を狭窄する気流速
度調節用の上部狭窄筒21を着脱可能に取り付け、その
上部狭窄筒21より上方における円筒12の側壁に、上
記針状物とそれ以外の非針状物からなる破砕混合物を選
別分離のために供給する破砕混合物供給口22を開口さ
せ、この供給口22にホッパー23を連設している。上
記ホッパー23は、スライド式ダンパ24a,24b及
び傾斜板24cが取り付けられ、ダンパ24aを開いて
破砕混合物を供給した後、そのダンパ24aを閉じてダ
ンパ24bを破砕混合物が徐々に落下する程度に開き、
破砕混合物が傾斜板24c及びホッパー23の底面を滑
って円筒12内に供給されるものである。なお、ホッパ
ー23に適当なバイブレーターを装着すると、破砕混合
物を定量的に供給することができる。
A cylinder 12 connected to the cylinder 11 via a flange is detachably attached to an upper narrowing cylinder 21 for adjusting an air velocity for narrowing a flow passage cross sectional area on an inner wall of a lower end thereof, and is arranged above the upper narrowing cylinder 21. In the side wall of the cylinder 12 in, the crushed mixture supply port 22 for supplying the crushed mixture consisting of the above needle-shaped material and the other non-needle-shaped material for sorting and separation is opened, and the hopper 23 is connected to this supply port 22. are doing. The hopper 23 is provided with slide type dampers 24a and 24b and an inclined plate 24c. After the damper 24a is opened to supply the crushed mixture, the damper 24a is closed and the damper 24b is opened to such an extent that the crushed mixture gradually falls. ,
The crushed mixture is supplied into the cylinder 12 by sliding on the bottom surfaces of the inclined plate 24c and the hopper 23. If the hopper 23 is equipped with an appropriate vibrator, the crushed mixture can be quantitatively supplied.

【0014】上記円筒12の下端にフランジにより接続
された円筒13は、上記円筒12に取付けた上部狭窄筒
21と共に流動選別のための主要部として機能するもの
で、その円筒13の内部に針状物分別用メッシュ板25
を架設すると共に、そのメッシュ板25の直下に流路断
面積を狭窄する気流速度調節用下部狭窄筒26を着脱自
在に取付け、メッシュ板25上で前記上部狭窄筒21と
の間に破砕混合物の流動域27を形成し、気流選別塔の
側壁には、その流動域27に臨む破砕混合物の排出口2
8を設けている。上記メッシュ板25は、多孔板により
構成し、あるいは、金網等からなるメッシュを直接円筒
13内に架設し、またはそれを保持枠に組み込んだ上で
円筒13内に架設するようにしたもので、破砕混合物中
の針状物がその長手方向を重力方向に向けた場合には通
るが、それよりも大きいものは通過させない網目を有す
るものである。
The cylinder 13, which is connected to the lower end of the cylinder 12 by a flange, functions as a main part for flow selection together with the upper constriction cylinder 21 attached to the cylinder 12, and has a needle-like shape inside the cylinder 13. Mesh plate for sorting 25
And a lower constriction tube 26 for air flow velocity control for constricting the cross-sectional area of the flow path is detachably attached directly below the mesh plate 25, and the crushed mixture is mixed on the mesh plate 25 with the upper constriction tube 21. A fluidized zone 27 is formed, and a discharge port 2 for the crushed mixture facing the fluidized zone 27 is formed on the side wall of the airflow selection tower.
8 are provided. The mesh plate 25 is constituted by a perforated plate, or a mesh made of wire mesh or the like is directly installed in the cylinder 13, or is installed in a holding frame and then installed in the cylinder 13. The needle-like material in the crushed mixture has a mesh that passes when its longitudinal direction is oriented in the direction of gravity, but larger ones do not pass.

【0015】上記円筒13にフランジ16を介して接続
した送風筒として機能する円筒14は、その側壁に下部
狭窄筒26の下方から気流選別塔を上昇する気流を供給
するための気流供給口30を開口させ、この気流供給口
30には、図示しない供給源からの気流の供給量を調節
するダンパ32を設けた気流供給筒31を接続してい
る。このダンパ32は、気流の流量を調整し、あるいは
気流の流量を間欠的に変動させることができるものであ
る。
The cylinder 14, which is connected to the cylinder 13 via the flange 16 and functions as a blower tube, has an air flow supply port 30 on its side wall for supplying an air flow rising from the lower constriction tube 26 to the air flow selection tower. An airflow supply cylinder 31 provided with a damper 32 for opening and opening a supply amount of an airflow from a supply source (not shown) is connected to the airflow supply port 30. The damper 32 is capable of adjusting the flow rate of the air flow or changing the flow rate of the air flow intermittently.

【0016】また、上記円筒14にフランジを介して接
続されて、気流選別塔1の下端に位置する円筒15は、
上記メッシュ板25を通過して下方に落下した針状物を
回収する回収部を構成するもので、その下部に十字バル
ブ33を設けている。この十字バルブ33の開閉によ
り、上記メッシュ板25を通過した針状物を円筒15の
下端から回収することができる。
Further, the cylinder 15 which is connected to the cylinder 14 through a flange and is located at the lower end of the air flow sorting tower 1 is
It constitutes a recovery unit for recovering the needle-shaped objects that have passed through the mesh plate 25 and dropped downward, and a cross valve 33 is provided below the recovery unit. By opening and closing the cross valve 33, the needle-shaped material that has passed through the mesh plate 25 can be collected from the lower end of the cylinder 15.

【0017】第2段の気流選別塔2は、上述の第1段の
気流選別塔1と実質的に同じ構成を有するものである
が、その第1段の気流選別塔1のように供給口22にホ
ッパー23を設けることなく、破砕混合物の供給口に第
1段の気流選別塔1における破砕混合物の排出口28に
接続した連結筒34を開口させている。なお、上述した
ように、第2段の気流選別塔2は、前記第1段の気流選
別塔1と実質的に同じ構成を有しているため、第1段の
気流選別塔と同一の部分に同一の符号を付してその構成
についての説明を省略する。
The second-stage airflow selection tower 2 has substantially the same structure as the above-described first-stage airflow selection tower 1, but like the first-stage airflow selection tower 1, it has a supply port. A hopper 23 is not provided on the connecting member 22, and a connecting cylinder 34 connected to the discharge port 28 for the crushed mixture in the first-stage airflow sorting tower 1 is opened at the crushed mixture supply port. As described above, since the second-stage airflow sorting tower 2 has substantially the same configuration as the first-stage airflow sorting tower 1, the same portion as the first-stage airflow sorting tower is used. Are denoted by the same reference numerals, and the description of the configuration will be omitted.

【0018】また、この第2段の気流選別塔2における
破砕混合物の排出口28に接続した連結筒34は、第1
段及び第2段と同じ構成を有する第3段の気流選別塔に
おける破砕混合物の供給口に開口させることもできる
が、図示した非針状物の排出筒35に連結することもで
きる。このようにして複数段の気流選別塔を連設するこ
とにより、その下部の回収部において針状物を効率よく
回収することが可能になる。
Further, the connecting cylinder 34 connected to the discharge port 28 for the crushed mixture in the second-stage airflow selection tower 2 is the first
Although it can be opened to the supply port for the crushed mixture in the third-stage airflow sorting column having the same configuration as the first and second stages, it can also be connected to the illustrated non-needle-like discharge pipe 35. By thus connecting a plurality of stages of airflow selection towers in series, it is possible to efficiently collect the needle-shaped material in the recovery section below the tower.

【0019】次に、上記気流選別装置による分別動作に
ついて説明する。ダンパ32等によって適宜な供給量に
調節された気流を、気流供給筒31から気流供給口30
を通して第1気流選別塔1及び第2気流選別塔2内を上
方に向けて供給し、針状物や非針状物の破砕混合物をホ
ッパー23から第1気流選別塔1内に供給すると、破砕
混合物のうちの軽量物は上部狭窄筒21の部分から下方
に落下することなく、上記気流により第1気流選別塔1
内を上昇して浮揚物回収筒18に達し、この浮揚物回収
筒18内で失速して、排出筒20より分離排出される。
但し、非常に細い銅線(例えば、0.1mm程度以下)
の切断物は、気流が速度を増す上部狭窄筒21の部分を
下方に落下することなく上方に移送され、浮揚物回収筒
18に達して排出筒20に排出されることがある。
Next, the sorting operation by the air flow sorting device will be described. The airflow adjusted to an appropriate amount by the damper 32 or the like is supplied from the airflow supply cylinder 31 to the airflow supply port 30.
The first airflow sorting tower 1 and the second airflow sorting tower 2 are supplied upward, and the crushed mixture of the crushed needles and non-needles is fed from the hopper 23 into the first airflow sorted tower 1 and crushed. The light weight of the mixture does not fall downward from the portion of the upper constriction cylinder 21, and the first airflow selection tower 1 is provided by the airflow.
It rises inside and reaches the floating material collecting cylinder 18, stalls in the floating material collecting cylinder 18, and is separated and discharged from the discharge cylinder 20.
However, very thin copper wire (for example, about 0.1 mm or less)
The cut object may be transferred upward without falling downward in the portion of the upper constriction cylinder 21 where the airflow increases in speed, reach the floating material recovery cylinder 18, and may be discharged to the discharge cylinder 20.

【0020】上記軽量物以外の針状物及び非針状物から
なる破砕混合物は、上部狭窄筒21を通過してメッシュ
板25上に達し、メッシュ板25上の流動域27におい
て下方から上昇する気流により浮揚力を受けながら流動
せしめられ、浮揚、転動、失速落下等を繰り返すが、そ
の間にも軽量物は上部狭窄筒21の高流速部分を経て気
流選別塔1の上方に浮揚し、分離される。メッシュ板2
5上の気流中で流動する破砕混合物は、それらが気流中
で失速落下するときに、特に、その破砕混合物中の針状
物が長手方向を重力方向に向けるように傾く傾向があ
り、このように長手方向を重力方向に向けた針状物は気
流中における浮揚力が著しく低下し、そのため失速落下
してメッシュ板25の網目を通過し、気流選別塔1の下
部の回収部において十字バルブ33上に集積される。従
って、該バルブ33を開閉操作することにより、排出コ
ンベア上やフィーダー上に取り出すことができる。
The crushed mixture consisting of needle-shaped materials and non-needle-shaped materials other than the above lightweight materials passes through the upper constriction tube 21 and reaches the mesh plate 25, and rises from below in the flow region 27 on the mesh plate 25. It is made to flow while receiving a levitation force by the air flow, and is repeatedly floated, tumbled, stalled, and the like, but during that time, the lightweight object floats above the air flow selection tower 1 through the high flow velocity portion of the upper constriction cylinder 21 and separated. To be done. Mesh plate 2
The crushed mixture flowing in the air stream above 5 tends to tilt, especially when the stalls fall in the air stream, with the needles in the crushed mixture tilting so that the longitudinal direction is in the direction of gravity. In the needle-shaped material whose longitudinal direction is oriented in the direction of gravity, the levitation force in the air flow is significantly reduced, so that it stalls and falls through the mesh of the mesh plate 25, and the cross valve 33 in the recovery section at the bottom of the air flow selection tower 1 Accumulated on top. Therefore, by opening and closing the valve 33, it can be taken out on the discharge conveyor or the feeder.

【0021】一方、上記流動域27における円筒内壁面
付近では、メッシュ板25の下方から上昇する気流の流
速が、内壁面との摩擦抵抗によって筒中央部のそれより
遅くなる。そのため、円筒内壁面付近では、破砕混合
物、即ち非針状物やメッシュ板25を通過することでき
なかった銅線の切断物等に対する浮揚力が小さくなり、
それらが円筒内壁面に沿って落下するが、流動域27の
中央部の流速の大きい気流により再び浮揚する。そし
て、このように浮揚及び落下を繰り返す破砕混合物は、
円筒内周壁に沿って旋回移動する傾向があり、それらが
気流選別塔1の側壁の破砕混合物の排出口28付近に達
したときに、その排出口28から逐次排出される。その
ため、破砕混合物を、メッシュ板25を通過する針状物
と、メッシュ板上から排出口28に排出される非針状物
(分別されなかった針状物を含む。)と、気流選別塔の
上方に浮揚する軽量物とに容易に効率よく分別すること
ができる。
On the other hand, in the vicinity of the inner wall surface of the cylinder in the flow region 27, the flow velocity of the air flow rising from below the mesh plate 25 becomes slower than that in the central portion of the cylinder due to the frictional resistance with the inner wall surface. Therefore, in the vicinity of the inner wall surface of the cylinder, the levitation force against the crushed mixture, that is, the non-needle-shaped object or the cut object of the copper wire that cannot pass through the mesh plate 25 becomes small,
Although they fall along the inner wall surface of the cylinder, they are levitated again by the air flow having a high flow velocity in the central portion of the flow region 27. Then, the crushed mixture which repeats the levitating and falling like this,
There is a tendency to swivel along the inner peripheral wall of the cylinder, and when they reach the vicinity of the outlet 28 of the crushed mixture on the side wall of the airflow sorting tower 1, they are sequentially discharged from the outlet 28. Therefore, the crushed mixture is passed through the mesh plate 25, the needle-like substances discharged from the mesh plate to the discharge port 28 (including the needle-like substances that have not been separated), and the airflow selection tower. It can be easily and efficiently separated into a lightweight material that floats upward.

【0022】気流選別塔1,2等を複数段に設けた場合
には、第1段の気流選別塔1におけるメッシュ板25上
に残留して排出口28から排出された破砕混合物が、連
結筒34を通して次段の気流選別塔2における破砕混合
物の供給口22に供給され、第1段の気流選別塔1の場
合と同様にして、その破砕混合物中における針状物がメ
ッシュ板25を通して気流選別塔2の下部の回収部にお
いて回収される。このようにして、複数段の気流選別塔
において針状物を回収すると、破砕混合物中における針
状物と非針状物とを高精度に分別することが可能にな
る。
When the airflow selection towers 1, 2, etc. are provided in a plurality of stages, the crushed mixture remaining on the mesh plate 25 in the first-stage airflow selection tower 1 and discharged from the discharge port 28 is a connecting cylinder. Is supplied to the crushed mixture supply port 22 in the next-stage airflow selection tower 2 through 34, and the needle-like material in the crushed mixture is airflow-selected through the mesh plate 25 in the same manner as in the first-stage airflow selection tower 1. It is recovered in the recovery section at the bottom of the tower 2. In this way, when the needle-shaped material is collected in the plurality of stages of the air flow sorting tower, it becomes possible to accurately separate the needle-shaped material and the non-needle-shaped material in the crushed mixture.

【0023】なお、図2に示すような、気流速度調節用
の切頭円錐状内面を有する円筒41や、図3に示すよう
な気流速度調節用狭窄筒43が組み込まれた円筒42、
あるいは上記狭窄筒43を組み込んでいない単なる円筒
を、それらに設けたフランジにより円筒12と円筒13
との間に組み込み、針状物や非針状物の破砕混合物が浮
揚と落下を繰り返すスパンを長くすれば、これら混合物
の浮揚と落下の繰り返し、即ち、対流が促進されるの
で、軽量物を一層効果的に分別することが可能になる。
A cylinder 41 having a frustoconical inner surface for adjusting the air flow rate as shown in FIG. 2 and a cylinder 42 in which a constriction tube 43 for adjusting the air flow rate as shown in FIG. 3 is incorporated,
Alternatively, a simple cylinder not incorporating the constriction cylinder 43 is replaced by a flange provided on the cylinder 12 and the cylinder 13.
If the crushed mixture of needles and non-needles is floated and dropped repeatedly by increasing the span of the mixture, the levitation and fall of these mixtures, that is, convection, is promoted. It becomes possible to sort more effectively.

【0024】[0024]

【発明の効果】以上に詳述した本発明の気流選別方法及
び装置によれば、破砕混合物中の針状物と非針状物と
を、乾式により効率よく分別することができ、しかも、
破砕混合物中の針状物と非針状物とを、気流中における
針状物の挙動を利用して簡便に高精度で分別することが
できる。
According to the airflow sorting method and apparatus of the present invention described in detail above, the needle-like material and the non-needle-like material in the crushed mixture can be efficiently separated by the dry method, and further,
The needle-like material and the non-needle-like material in the crushed mixture can be easily and accurately separated by utilizing the behavior of the needle-like material in the air flow.

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

【図1】本発明の気流選別装置の実施例を示す断面図で
ある。
FIG. 1 is a cross-sectional view showing an embodiment of an airflow selection device of the present invention.

【図2】上記気流選別装置において付加的に使用できる
円筒の一例の断面図である。
FIG. 2 is a cross-sectional view of an example of a cylinder that can be additionally used in the airflow sorting device.

【図3】上記気流選別装置において付加的に使用できる
円筒の多例の断面図である。
FIG. 3 is a cross-sectional view of multiple examples of a cylinder that can be additionally used in the airflow sorting device.

【符号の説明】[Explanation of symbols]

1 第1段の気流選別塔 2 第2段の気流選別塔 18 浮揚物回収筒 21 上部狭窄筒 22 供給口 25 メッシュ板 26 下部狭窄筒 27 流動域 28 排出口 30 気流供給口 1 First-stage airflow selection tower 2 Second-stage airflow selection tower 18 Float recovery cylinder 21 Upper constriction cylinder 22 Supply port 25 Mesh plate 26 Lower constriction cylinder 27 Flow zone 28 Discharge port 30 Airflow supply port

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大井 英節 茨城県つくば市小野川16番3 工業技術院 資源環境技術総合研究所内 (72)発明者 四元 弘毅 茨城県つくば市小野川16番3 工業技術院 資源環境技術総合研究所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Eiji Oi 16-3 Onogawa, Tsukuba-shi, Ibaraki Institute of Industrial Science and Technology, National Institute of Resources and Environmental Technology (72) Inventor Hiroki Shigen 16-3 Onogawa, Tsukuba-shi, Ibaraki Industrial technology Institute for Natural Resources and Environment Technology

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】針状物分別用メッシュ板の上方に破砕混合
物の流動域を介して流路断面積を狭窄する気流速度調節
用上部狭窄筒を、上記メッシュ板の直下に流路断面積を
狭窄する気流速度調節用下部狭窄筒を設けた気流選別塔
において、 上記メッシュ板上の流動域に針状物及び非針状物の破砕
混合物を供給すると共に、下部狭窄筒の下方の気流選別
塔側壁から気流選別塔を上昇する気流を供給することに
より、上記流動域において破砕混合物を流動させ、 上記流動の間に、長手方向を重力方向に向けて失速落下
する針状物をメッシュ板を通してその下方に落下させ、
それを気流選別塔の下部で回収し、 破砕混合物中の軽量物を気流選別塔の上部に浮揚させて
排出すると共に、上記メッシュ板上の流動域で流動を繰
り返す破砕混合物を、気流選別塔側壁に設けた上記流動
域を臨む排出口を通して逐次排出させる、ことを特徴と
する固形物の気流選別方法。
1. An upper constriction tube for adjusting an air velocity, which narrows a flow passage cross-sectional area through a flow region of a crushed mixture above a needle-like material sorting mesh plate, and a flow passage cross-sectional area immediately below the mesh plate. An airflow selection tower provided with a lower constriction cylinder for controlling the airflow speed that constricts, in addition to supplying a crushed mixture of needles and non-needles to the flow region on the mesh plate, and an airflow selection tower below the lower constriction cylinder. The crushed mixture is made to flow in the above-mentioned flow region by supplying an airflow rising from the side wall to the airflow selection tower, and during the above-mentioned flow, needle-like objects that stall and fall in the longitudinal direction toward the direction of gravity are passed through the mesh plate. Drop it down,
It is collected in the lower part of the airflow selection tower, the lightweight material in the crushed mixture is floated above the airflow selection tower and discharged, and the crushed mixture that repeats the flow in the fluidized area on the mesh plate is removed from the side wall of the airflow selection tower. A method for air flow sorting of solids, characterized in that the solid matter is sequentially discharged through a discharge port facing the above-mentioned flow region.
【請求項2】気流選別塔側壁に設けた排出口を通して排
出される破砕混合物を、次段の気流選別塔におけるメッ
シュ板上に供給し、同一の方法により再度針状物をメッ
シュ板の下方に落下させて、気流選別塔の下部で回収す
ると共に、軽量物を気流選別塔の上部に浮揚させて排出
し、メッシュ板上の流動域で流動を繰り返す破砕混合物
を気流選別塔側壁の排出口を通して逐次排出させる、こ
とを特徴とする請求項1に記載の固形物の気流選別方
法。
2. The crushed mixture discharged through a discharge port provided on the side wall of the airflow selection tower is supplied onto the mesh plate in the next-stage airflow selection tower, and the needle-shaped material is again placed below the mesh plate by the same method. It is dropped and collected at the bottom of the airflow selection tower, and the lightweight material is floated at the top of the airflow selection tower and discharged, and the crushed mixture that repeats flow in the flow area on the mesh plate is passed through the outlet on the side wall of the airflow selection tower. The solid matter airflow sorting method according to claim 1, wherein the solid matter is sequentially discharged.
【請求項3】筒状をなす気流選別塔内に、破砕混合物中
の針状物がその長手方向を重力方向に向けた場合に通る
針状物分別用メッシュ板を配設すると共に、そのメッシ
ュ板の上方に破砕混合物の流動域を介して流路断面積を
狭窄する気流速度調節用上部狭窄筒を、上記メッシュ板
の直下に流路断面積を狭窄する気流速度調節用下部狭窄
筒を設け、 上記気流選別塔側壁の上部狭窄筒より上方に破砕混合物
を供給する供給口を開口させると共に、上記気流選別塔
側壁の下部狭窄筒の下方に、気流選別塔を上昇する気流
を供給するための気流供給口を開口させ、 気流選別塔の下部に、上記メッシュ板を通過して下方に
落下した針状物を回収する回収部を設け、気流選別塔の
上部に破砕混合物中の軽量物を分離排出する分離部を設
けると共に、気流選別塔側壁に上記流動域に臨む破砕混
合物の排出口を設けた、ことを特徴とする固形物の気流
選別装置。
3. A mesh plate for sorting needles through which the needles in the crushed mixture pass when the longitudinal direction of the crushed mixture is oriented in the direction of gravity is provided in a tubular airflow selection tower, and the mesh thereof is provided. An upper airflow velocity adjusting narrowing tube for narrowing the flow passage cross-sectional area is provided above the plate and a lower airflow velocity adjusting narrowing pipe for narrowing the flow passage cross-sectional area is provided immediately below the mesh plate. A supply port for supplying the crushed mixture is opened above the upper constriction cylinder on the side wall of the airflow selection tower, and below the lower constriction cylinder on the side wall of the airflow selection tower, for supplying an airflow rising in the airflow selection tower. An air flow supply port is opened, and at the bottom of the air flow selection tower, a collection unit is provided to collect needles that have passed through the mesh plate and dropped downward, and at the top of the air flow selection tower, the lightweight materials in the crushed mixture are separated. A separate part to discharge is provided and the airflow Provided an outlet crushed mixture facing the flow field in a different column side wall, the airflow sorting apparatus of solids, characterized in that.
【請求項4】請求項3に記載の気流選別塔側壁に設けた
破砕混合物の排出口を、同じ構成の次段の気流選別塔に
おけるメッシュ板上の破砕混合物の供給口に開口させ、 複数段の気流選別塔の下部の回収部において針状物を回
収する、ことを特徴とする固形物の気流選別方法。
4. The outlet for the crushed mixture provided on the side wall of the airflow selection tower according to claim 3 is opened to the supply port for the crushed mixture on the mesh plate in the next-stage airflow selection tower having the same structure, and a plurality of stages are provided. A method for air flow sorting of solids, comprising collecting needles in a lower part of the air flow sorting tower.
JP24137195A 1995-09-20 1995-09-20 Method and apparatus for airflow separation of solid matter Expired - Lifetime JP2757333B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24137195A JP2757333B2 (en) 1995-09-20 1995-09-20 Method and apparatus for airflow separation of solid matter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24137195A JP2757333B2 (en) 1995-09-20 1995-09-20 Method and apparatus for airflow separation of solid matter

Publications (2)

Publication Number Publication Date
JPH0975851A true JPH0975851A (en) 1997-03-25
JP2757333B2 JP2757333B2 (en) 1998-05-25

Family

ID=17073296

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24137195A Expired - Lifetime JP2757333B2 (en) 1995-09-20 1995-09-20 Method and apparatus for airflow separation of solid matter

Country Status (1)

Country Link
JP (1) JP2757333B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005144372A (en) * 2003-11-18 2005-06-09 Techno Polymer Co Ltd Apparatus and method for recovering solid by separating foreign matter
WO2013145871A1 (en) * 2012-03-28 2013-10-03 独立行政法人産業技術総合研究所 Particle sorting machine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005144372A (en) * 2003-11-18 2005-06-09 Techno Polymer Co Ltd Apparatus and method for recovering solid by separating foreign matter
WO2013145871A1 (en) * 2012-03-28 2013-10-03 独立行政法人産業技術総合研究所 Particle sorting machine
JPWO2013145871A1 (en) * 2012-03-28 2015-12-10 国立研究開発法人産業技術総合研究所 Particle sorter

Also Published As

Publication number Publication date
JP2757333B2 (en) 1998-05-25

Similar Documents

Publication Publication Date Title
US5116486A (en) Apparatus and method for separating recyclable waste
US7708145B2 (en) Dry separating table, a separator and equipment for the compound dry separation with this table
KR830002053B1 (en) Air elutriation device for recovering char fines in discharge waste from iron oxido reclucing kiln
US3975263A (en) Material separation apparatus and method
US4950388A (en) Separation of mixtures in a wind tunnel
JPH0975851A (en) Method and apparatus for pneumatic sorting of solid
JP2535778B2 (en) Air flow sorting method and device for solid matter
JP2001328120A (en) Device and method for treating mixed waste plastic
JP2636160B2 (en) Method and apparatus for airflow separation of solid matter
JPH0985176A (en) Sorting device
JP2803996B2 (en) Waste sorting equipment
JP3160948B2 (en) Waste separation vibrating conveyor
AU592010B2 (en) Separation of mixtures in a wind tunnel
JP3325502B2 (en) Waste sorting equipment
JP2659087B2 (en) Intermediate floating material recovery device in solid material air flow separation device
EP0065493A1 (en) Device to sort compost
JP3325503B2 (en) Waste sorting equipment
JP2003340375A (en) Waste separation apparatus
JP2742030B2 (en) Waste sorting equipment
JPH0839005A (en) Fractionating method for industrial waste and its device
JPH0985175A (en) Sorting device
SU799837A2 (en) Pneumatic classifier for separating loose materials
JPH0751627A (en) Sorting device for waste
JPH0999275A (en) Sorter for waste
JP2001239220A (en) Vibration feeder and valuable material recovering device

Legal Events

Date Code Title Description
S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

EXPY Cancellation because of completion of term