JP3206884B2 - Glass particle sorting and collecting system and method for collecting the same - Google Patents

Glass particle sorting and collecting system and method for collecting the same

Info

Publication number
JP3206884B2
JP3206884B2 JP24185196A JP24185196A JP3206884B2 JP 3206884 B2 JP3206884 B2 JP 3206884B2 JP 24185196 A JP24185196 A JP 24185196A JP 24185196 A JP24185196 A JP 24185196A JP 3206884 B2 JP3206884 B2 JP 3206884B2
Authority
JP
Japan
Prior art keywords
crushed
crushed material
particle size
glass
collecting
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 - Lifetime
Application number
JP24185196A
Other languages
Japanese (ja)
Other versions
JPH1085670A (en
Inventor
哲哉 工藤
安正 出井
均 今田
Original Assignee
富士車輌株式会社
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Filing date
Publication date
Application filed by 富士車輌株式会社 filed Critical 富士車輌株式会社
Priority to JP24185196A priority Critical patent/JP3206884B2/en
Publication of JPH1085670A publication Critical patent/JPH1085670A/en
Application granted granted Critical
Publication of JP3206884B2 publication Critical patent/JP3206884B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/60Glass recycling

Landscapes

  • Refuse Collection And Transfer (AREA)
  • Processing Of Solid Wastes (AREA)
  • Combined Means For Separation Of Solids (AREA)

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】本願発明は、ガラス粒分別収
集システム及びその収集方法、更に詳しくはガラス瓶等
の破砕物を破砕することでガラス粒として、該ガラス粒
を粒径に応じて分別して収集するためのガラス粒分別収
集システム及び方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a system for separating and collecting glass particles and a method for collecting the same. More specifically, the present invention relates to a method for crushing a crushed product such as a glass bottle to obtain glass particles. And a method and apparatus for sorting and collecting glass particles.

【0002】[0002]

【従来の技術】従来、ガラス瓶等のガラスは、そのまま
廃棄される他、リサイクルつまり家庭等で使用したガラ
スを回収して再度ガラスの原料等として繰り返し利用さ
れる場合がある。特に、昨今に於いてはガラスを丸みを
もった(角のない)ガラス粒に破砕する破砕機が開発さ
れ、これによりガラス瓶等のガラスは人工砂、舗装用骨
材等に幅広くリサイクルされることが提案されている。
2. Description of the Related Art Conventionally, glass such as glass bottles is sometimes discarded as it is, or recycled, that is, glass used at home or the like is collected and reused again as a raw material for glass. In particular, in recent years, a crusher has been developed to crush glass into rounded (no-angle) glass particles, which allows glass such as glass bottles to be widely recycled into artificial sand and pavement aggregates. Has been proposed.

【0003】そして、このようにガラス瓶等を人工砂、
舗装用骨材等として再利用する為のガラス粒分別収集シ
ステムとしては、回収したガラスを一次破砕機によって
粗破砕し、該粗破砕された破砕物を一次振動ふるい機に
よって分別して所定粒径以上のものを一次破砕機に返送
し、所定粒径以下のものを二次破砕機によって丸みをも
ったガラス粒に破砕して、このガラス粒を二次振動ふる
い機によって所望の粒径のガラス粒に分別して夫々収集
するシステムも考えられる。
[0003] Then, a glass bottle or the like is made of artificial sand,
As a glass particle sorting and collecting system for reuse as pavement aggregate, etc., the recovered glass is roughly crushed by a primary crusher, and the coarsely crushed material is separated by a primary vibrating sieve to have a predetermined particle size or more. Is returned to the primary crusher, those having a predetermined particle size or less are crushed into rounded glass particles by a secondary crusher, and the glass particles having a desired particle size are crushed by a secondary vibrating sieve. It is also conceivable that the system collects the information separately.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、かかる
ガラス粒分別収集システムにあっては、ガラス粒の収集
に際して、回収したガラス瓶に付着しているラベル或い
はガラス瓶の首部に残存する王冠等に基づいて、収集し
たガラス粒内に紙、鉄、アルミ等の不純物が混在すると
いう問題を有する。
However, in such a system for collecting and separating glass particles, the glass particles are collected based on a label attached to the collected glass bottle or a crown remaining on the neck of the glass bottle. There is a problem that impurities such as paper, iron, and aluminum are mixed in the collected glass particles.

【0005】そこで、本願発明はこのような問題を解決
すべくなされたものであり、不純物の混在を減少でき、
ガラス粒を粒径に応じて分別して収集できるガラス粒分
別収集システムを提供することにある。
Accordingly, the present invention has been made to solve such a problem, and can reduce the mixture of impurities.
An object of the present invention is to provide a glass particle sorting and collecting system capable of sorting and collecting glass particles according to their particle diameters.

【0006】[0006]

【課題を解決するための手段】本願発明に係るガラス粒
分別収集システムは、上記の課題を解決すべく、ラベル
の付着したガラス瓶等の被破砕物を破砕する破砕装置A
と、該破砕装置Aにより破砕された破砕物を粒径に応じ
て分別すると共に、分別された所定粒径以下の破砕物を
さらに粒径に応じて二種以上に分別する分別手段Bと、
二種以上に分別された破砕物のそれぞれに応じて設け
られた搬出路60を介してこれらを夫々収集する収集手段
Cとを有してなり、しかも、前記収集手段Cは、少なく
とも二つの搬出路60に、紙等の不純物を除去すべく送風
可能な風力選別手段67を夫々設けた構成からなる。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, a glass particle sorting and collecting system according to the present invention has a crushing device A for crushing a crushed object such as a glass bottle having a label attached thereto.
And the crushed material crushed by the crushing device A is separated according to the particle size, and the crushed material having a predetermined particle size or less is separated.
Further, a separation means B for separating into two or more kinds according to the particle size ,
Provided in accordance with each of the two or more types of crushed material
Was through the discharge passage 60 becomes a collection means C for these respective collection, moreover, the collector means C is the least <br/> two-out path 60, removing impurities such as paper It has a configuration in which wind power selecting means 67 capable of blowing air is provided .

【0007】該構成からなる本願発明に係るガラス粒分
別収集システムは、ガラス瓶等の破砕物を破砕装置Aに
よって破砕し、その破砕物を分別手段Bによって粒径に
応じて分別して、この分別された破砕物を搬出路60を介
して収集手段Cに収集されることとなる。そして、分別
手段Bで分別された少なくとも一種の破砕物の搬出路60
に風力選別手段67を設けてなるので、該風力選別手段67
によって破砕物内の不純物を搬出路60で除去しつつ収集
することが可能である。特に、搬出路60に於ける破砕物
は既に分別手段Bで粒径に応じて分別されたものである
ので、その粒径のガラス粒を除去しない程度に風力選別
手段の風力を設定することができ、これにより所望の風
力で紙等の不純物を除去することが可能である。
In the system for separating and collecting glass particles according to the present invention having the above-mentioned structure, a crushed material such as a glass bottle is crushed by a crushing device A, and the crushed material is separated by a separation means B according to the particle size, and the crushed material is separated. The crushed material is collected by the collecting means C via the carry-out path 60. Then, the carry-out path 60 of at least one kind of the crushed material separated by the separation means B
Is provided with a wind power sorting means 67,
Accordingly, it is possible to collect while removing impurities in the crushed material in the carry-out path 60. In particular, since the crushed material in the carry-out path 60 has already been separated according to the particle size by the separation device B, it is necessary to set the wind force of the wind separation device to such an extent that the glass particles of the particle size are not removed. This makes it possible to remove impurities such as paper with a desired wind force.

【0008】ここで、本願発明において風力選別手段67
とは、搬出路60で搬送される破砕物の不純物を除去でき
るように風を送ることのできる全ての手段を意味し、例
えば破砕物の搬出方向に対して垂直方向の風を送り紙等
の不純物を除去する装置を採用することも可能である
が、請求項2記載の如く搬出路60を破砕物が自重により
落下する自重落下部65b を設け、該自重落下部65b を落
下する破砕物の落下方向と対向する対向風を送風可能に
設けることが好ましい。
[0008] Here, in the present invention, the wind separation means 67
The term means all means capable of blowing air so that impurities in the crushed material conveyed in the carry-out path 60 can be removed. It is also possible to employ an apparatus for removing impurities, however, it is also possible to provide a self-weight dropping portion 65b in which the crushed material falls by its own weight in the carry-out path 60 as described in claim 2, and a crushed material falling down the self-weighted falling portion 65b. It is preferable to provide an opposing wind that opposes the falling direction so that it can be blown.

【0009】該構成からなる請求項2記載のガラス粒分
別収集システムにあっては、分別手段Bにより分別され
て搬出路60の自重落下部65b を落下する破砕物が、その
落下の際に風力選別手段67の対向風によって不純物が除
去されることとなる。そして、自重落下部65b の破砕物
の落下の際に、破砕物内の不純物とガラス粒とが互いに
離間しやすく、より確実に対向風によって不純物を除去
することができる。
In the glass particle sorting and collecting system according to the second aspect of the present invention, the crushed material which is separated by the separating means B and falls down the weight dropping portion 65b of the carry-out path 60 is subjected to wind force at the time of the fall. The impurities are removed by the counter wind of the sorting means 67. Then, when the crushed material falls at the dead weight falling portion 65b, the impurities in the crushed material and the glass particles are easily separated from each other, and the impurities can be more reliably removed by the opposed wind.

【0010】[0010]

【0011】[0011]

【0012】また、本願発明に係るガラス粒分別収集シ
ステムは、請求項3記載の如く、風力選別手段67がガラ
ス粒の粒径に応じて風力を調整可能に設けられた構成を
採用することもできる。
[0012] In the glass particle sorting and collecting system according to the present invention, the wind sorting means 67 may include a glass sorting device.
It is also possible to adopt a configuration in which the wind force can be adjusted according to the particle size of the grains .

【0013】該構成からなる請求項3記載のガラス粒分
別収集システムにあっては、収集後のガラス粒の利用目
的に応じて、その都度風力選別手段67の風力を調整する
ことができ、例えばガラス粒の収集後の利用目的によっ
て不純物を確実に除去する必要がある場合にあっては風
力を強くし、一方不純物がある程度含有されても良い場
合には風力を弱く設定することが可能である。
In the glass particle sorting and collecting system according to the third aspect of the present invention, the wind force of the wind force sorting means 67 can be adjusted each time according to the purpose of use of the collected glass particles. When it is necessary to reliably remove impurities depending on the purpose of use after collection of glass particles, it is possible to increase the wind power, while it is possible to set the wind power weaker if impurities can be contained to some extent .

【0014】さらに、本願発明に係るガラス粒分別収集
システムにおいて、分別手段Bが請求項4記載の如く、
前記破砕装置Aにより破砕された破砕物を所定粒径以下
と所定粒径以上の二種に分別可能な返送用分別機25と、
該返送用分別機25で分別された所定粒径以下の破砕物を
受取る搬送路50と、前記返送用分別機25で分別された所
定粒径以上の破砕物を破砕装置Aに返送可能な返送路29
と、前記搬送路50により搬送される所定粒径以下の破砕
物を夫々粒径に応じて前記各搬出路60に搬出すべく少な
くとも二種以上に分別可能な収集用分別機52とを具備す
る構成を採用することもできる。
Further, in the glass particle sorting and collecting system according to the present invention, the sorting means B is as described in claim 4 .
The crushed material crushed by the crushing device A is a predetermined particle size or less.
And a return sorting machine 25 capable of separating into two types having a predetermined particle size or more,
The crushed material having a particle size equal to or less than a predetermined particle size separated by the
The receiving path 50 and the place separated by the return sorter 25
Return path 29 capable of returning crushed material having a particle size or more to crushing device A
And crushing of a predetermined particle size or less which is conveyed by the conveying path 50
It is necessary to take a small amount of
It is also possible to adopt a configuration including at least two types of collection sorters 52 capable of sorting .

【0015】該構成からなる請求項4記載のガラス粒分
別収集システムにあっては、破砕装置Aによって破砕さ
れた破砕物のうち所定粒径以上の破砕物は返送用分別機
25、返送路29を介して再度破砕装置Aによって破砕さ
れ、また所定粒径以下の破砕物は搬送路50を介して収集
用分別機52に搬送されることとなる。このように、所定
粒径以上の破砕物を破砕装置Aに返送する返送路29が設
けられてなるので、所定粒径以上の破砕物を捨てること
なくガラス瓶等の被破砕物を有効に利用することができ
る。特に、破砕装置Aにより破砕された破砕物を収集用
分別機Cに搬送する搬送路50が設けられてなるので、破
砕装置Aと収集用分別機Cとを所望の場所に設置するこ
とが可能であり、さらに返送用分別機Bの設置場所を返
送路29に合わせて設定することで所望距離の返送路29を
設けることが可能である。具体的には、例えば返送用分
別機25を破砕装置Aの直下に設けることで返送路29を短
く設計することが可能であり、一方返送路29に非鉄金属
除去装置等を介在させる場合にあっては搬送路50途中に
返送用分別機25を設けて返送路29を所望距離設けること
も可能である。
[0015] In the glass particle sorting and collecting system according to claim 4, the crushed material having a predetermined particle size or more among the crushed materials crushed by the crushing device A is a return sorting machine.
25, crushed again by the crushing device A via the return path 29, and the crushed material having a predetermined particle size or less is conveyed to the collection sorter 52 via the conveyance path 50. As described above, since the return path 29 for returning the crushed material having the predetermined particle size or more to the crushing apparatus A is provided, the crushed material such as a glass bottle is effectively used without discarding the crushed material having the predetermined particle size or more. be able to. In particular, since the transport path 50 for transporting the crushed material crushed by the crushing device A to the sorting device C for collection is provided, the crushing device A and the sorting device C for collection can be installed at desired locations. The return path 29 having a desired distance can be provided by setting the installation location of the return sorting machine B in accordance with the return path 29. Specifically, for example, it is possible to design the return path 29 short by providing the return sorter 25 immediately below the crushing apparatus A. On the other hand, when the return path 29 is provided with a non-ferrous metal removing device or the like. In addition, it is possible to provide the return sorting device 25 in the middle of the transport path 50 and provide the return path 29 with a desired distance.

【0016】また、本願発明に係るガラス粒分別収集方
法は、請求項5記載の如く、ラベルの付着したガラス瓶
等の被破砕物を破砕する破砕工程と、該破砕工程で破砕
された破砕物を粒径に応じて二種の破砕物に分別して、
所定粒径以上の破砕物を前記破砕工程に返送する返送用
分別工程と、該返送用分別工程で分別された所定粒径以
下の破砕物を粒径に応じて二種以上に分別する収集用分
別工程と、該収集用分別工程によって分別された破砕物
のそれぞれに応じて設けられた搬出路60を介してこれら
夫々収集する収集工程とからなり、且つ、前記収集工
程において少なくとも二種の破砕物の搬出路60で風力選
別手段67によって紙等の不純物を除去することを特徴と
する。
In the method for separating and collecting glass particles according to the present invention, a crushing step of crushing a crushed object such as a glass bottle having a label attached thereto, and a crushed material crushed in the crushing step may be performed. Separate into two types of crushed materials according to the particle size,
A return separation step of returning a crushed material having a predetermined particle size or more to the crushing step, and a collection step of separating the crushed material having a predetermined particle size or less separated in the return separation step into two or more types according to the particle size. Crushed material separated by the separation step and the collection separation step
These through the discharge passage 60 provided in accordance with each
And collecting the impurities such as paper in the collecting step by the wind separation means 67 in the discharge path 60 of the at least two kinds of crushed materials.

【0017】該構成からなる本願請求項5記載のガラス
粒分別収集方法は、返送用分別工程で破砕物のうち所定
粒径以上の破砕物を返送することで所定粒径以上の破砕
物を捨てることなくガラス瓶等の被破砕物を有効に利用
することができ、また収集用分別工程後に風力選別手段
67によって破砕物内の不純物を搬出路60で除去すること
により、破砕物の粒径に応じてガラス粒を除去しない程
度に風力選別手段67の風力を設定することができ、これ
により紙等の不純物を的確に除去することが可能であ
る。
In the method for separating and collecting glass particles according to the fifth aspect of the present invention, the crushed material having a predetermined particle size or more is returned from the crushed material in the separating step for returning, so that the crushed material having a predetermined particle size or more is discarded. The material to be crushed, such as a glass bottle, can be used effectively without any
By removing impurities in the crushed material by the carry-out path 60 by the 67, it is possible to set the wind force of the wind force sorting means 67 to such an extent that the glass particles are not removed according to the particle size of the crushed material, thereby making it possible to remove paper and the like. Impurities can be accurately removed.

【0018】[0018]

【発明の実施の形態】以下、図1乃至図3に参酌しつ
つ、本願発明に係るガラス粒分別収集システムの実施形
態について説明する。本実施形態のガラス粒分別収集シ
ステムは、王冠、ラベル等の付着したガラス瓶(被破砕
物)を破砕する破砕装置Aと、該破砕装置Aにより破砕
された破砕物を粒径に応じて分別可能な分別手段Bと、
該分別手段Bによって分別されたガラス粒を夫々収集可
能な収集手段Cとからなる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a glass particle sorting and collecting system according to the present invention will be described below with reference to FIGS. The glass particle sorting and collecting system according to the present embodiment is capable of separating a crushing device A for crushing a glass bottle (a material to be crushed) to which a crown, a label, etc. are attached, and a crushed material crushed by the crushing device A according to a particle size. Separation means B,
A collection unit C capable of collecting the glass particles separated by the separation unit B;

【0019】前記破砕装置Aは、ガラス瓶を粗破砕する
一次破砕部10と、該粗破砕された破砕物を丸みをもった
ガラス粒に破砕する二次破砕部16と、該二次破砕部16に
より破砕された破砕物から埃等を除去する為のサイクロ
ン22とからなる。
The crushing apparatus A includes a primary crushing section 10 for coarsely crushing a glass bottle, a secondary crushing section 16 for crushing the coarsely crushed material into rounded glass particles, and a secondary crushing section 16. And a cyclone 22 for removing dust and the like from the crushed material.

【0020】該一次破砕部10には、ガラス瓶が投入され
るホッパー12及び該ホッパー12に投入された被破砕物を
所定量ずつ破砕機13に供給する為のスクリューフィーダ
ー14が設けられている。これにより、ショベル等により
ホッパー12に大量のガラス瓶を投入することができ、し
かも投入された大量のガラス瓶はスクリューフィーダー
14によって一定量ずつ破砕機13に送られ、粗破砕作業が
確実に行われる。
The primary crushing unit 10 is provided with a hopper 12 into which a glass bottle is to be charged and a screw feeder 14 for supplying a predetermined amount of the material to be crushed into the hopper 12 to a crusher 13. As a result, a large amount of glass bottles can be put into the hopper 12 by a shovel or the like, and the large amount of glass bottles put into the hopper 12 can be supplied by a screw feeder.
The fixed amount is sent to the crusher 13 by the constant amount by the 14 and the coarse crushing operation is reliably performed.

【0021】また、二次破砕部16には、前記一次破砕部
10によって破砕された破砕物を受け入れるホッパー18及
び該ホッパー18に投入された破砕物を所定量ずつ破砕機
19に供給する為の振動フィーダー20が設けられている。
The secondary crushing section 16 includes the primary crushing section.
A hopper 18 for receiving the crushed material crushed by 10 and a crusher
A vibration feeder 20 for supplying to 19 is provided.

【0022】さらに、前記サイクロン22は前記二次破砕
部16に直結されており、サイクロン22はバグフィルター
23を介して吸引器に接続されている。これにより二次破
砕部16で破砕された破砕物から吸引除去した埃等はバグ
フィルター23によって除去される。
Further, the cyclone 22 is directly connected to the secondary crushing section 16, and the cyclone 22 is a bag filter.
Connected to the aspirator via 23. As a result, dust and the like sucked and removed from the crushed material crushed in the secondary crushing unit 16 are removed by the bag filter 23.

【0023】前記分別手段Bは、収集手段Cの搬出路60
に夫々搬出すべく粒径に応じて三種の破砕物に分別可能
な収集用分別機52と、該収集用分別機52に破砕物を搬送
する搬送路50と、破砕装置Aのサイクロン22の排出部に
直結され破砕物を粒径に応じて二種の破砕物に分別可能
な返送用分別機25と、該返送用分別機25によって分別さ
れた所定粒径以上の破砕物を二次破砕部16のホッパー18
に返送する返送路29とからなる。
The sorting means B is provided at the carry-out path 60 of the collecting means C.
A sorter for collection 52 capable of sorting into three types of crushed materials according to the particle size to be carried out, a conveying path 50 for conveying the crushed materials to the sorter for collection 52, and discharge of the cyclone 22 of the crushing device A. A return sorting machine 25 which is directly connected to the section and can separate the crushed material into two types of crushed material according to the particle size, and a crushed material having a predetermined particle size or more separated by the return sorting device 25 and a secondary crushing unit. 16 hoppers 18
And a return path 29 for returning to the vehicle.

【0024】前記返送用分別機25は、サイクロン22の排
出部より排出された破砕物を粒径5.0mm 以上のものと5.
0mm 以下のものとに分別すべく、孔径5.0mm の孔が網目
状に設けられた粗分別板27を有し、該粗分別板27により
破砕物が粒径に応じて分別されるよう該粗分別板27は振
動可能に設けられている。
The return sorting machine 25 determines whether the crushed material discharged from the discharge part of the cyclone 22 has a particle diameter of 5.0 mm or more.
In order to separate the crushed material into particles having a diameter of 5.0 mm or less in a mesh shape, the coarse separation plate 27 separates the crushed material according to the particle size. The separation plate 27 is provided so as to be able to vibrate.

【0025】前記返送路29は、返送用分別機25によって
分別された粒径5.0mm 以上の破砕物が投入される返送ホ
ッパー31を有し終端に向けて上方に傾斜した第一返送コ
ンベア32と、非鉄金属除去装置39及び返送用風力選別装
置42を介して第一返送コンベア32から破砕物を受け取り
二次破砕部16に返送する第二返送コンベア35とからな
る。
The return path 29 has a return hopper 31 into which crushed material having a particle size of 5.0 mm or more separated by the return separator 25 is charged, and has a first return conveyor 32 inclined upward toward the end. And a second return conveyor 35 that receives the crushed material from the first return conveyor 32 via the non-ferrous metal removing device 39 and the return wind separation device 42 and returns the crushed material to the secondary crushing unit 16.

【0026】前記非鉄金属除去装置39は、第一返送コン
ベア32の終端から落下する破砕物を受け取る振動フィー
ダー39a と、該振動フィーダー39a から一定量ずつ破砕
物が供給され終端で非鉄金属、鉄類金属、非金属との三
種に分けることができる非鉄除去用コンベア39b と、該
非鉄除去用コンベア39b によって分けられた破砕物を夫
々排出可能な排出口39c,…とからなる。
The non-ferrous metal removing device 39 includes a vibrating feeder 39a for receiving the crushed material falling from the end of the first return conveyor 32, a crushed material supplied from the vibrating feeder 39a by a predetermined amount, and a non-ferrous metal and irons at the end. It comprises a non-ferrous removal conveyor 39b which can be divided into three types, metal and non-metal, and discharge ports 39c, which can respectively discharge the crushed materials separated by the non-ferrous removal conveyor 39b.

【0027】ここで、非鉄除去用コンベア39b の終端の
内部には強い磁性を帯びた複数の磁石がNS交互に配置
されたローターが高速回転しており、これにより破砕物
が非鉄金属、鉄類金属、非金属との三種に分けられる。
つまり、アルミ等の磁性を帯びない非鉄金属は、ロータ
ーの高速回転による磁界の変化により内部に渦電流を生
じ、この渦電流により生ずる磁界とローター内の磁石の
磁界とが反発して、コンベア39b の終端から搬送方向に
飛び出し、コンベア39b の搬出側(図1において右側)
に設けられた非鉄排出口39c より排出される。また、鉄
等の磁性を帯びる鉄類金属は、磁石の磁界に対応した磁
力を帯びて、この磁力によりコンベア39b 側に引きつけ
られ、コンベア39b の下側まで搬送され、磁石による磁
界が弱まった位置で落下して、コンベア39b の搬出反対
側(図1において左側)に設けられた鉄類排出口39e よ
り排出される。一方、ガラス等の磁性を帯びず且つ通電
性を有さない物質は、コンベア39b の終端より垂直方向
に落下して、コンベア39bの終端下方に設けられたガラ
ス排出口39d より排出される。
Here, a rotor in which a plurality of magnets having strong magnetism are alternately arranged NS is rotated at a high speed inside the end of the non-ferrous material removing conveyor 39b. It is divided into three types: metal and non-metal.
In other words, non-ferrous metals that do not have magnetism, such as aluminum, generate an eddy current inside due to a change in the magnetic field due to the high-speed rotation of the rotor, and the magnetic field generated by the eddy current and the magnetic field of the magnet in the rotor are repelled, and the conveyor 39b Jumps out from the end of the conveyor 39b in the transport direction and unloads the conveyor 39b (right side in FIG. 1).
It is discharged from the non-ferrous discharge port 39c provided in Also, the ferrous metal having magnetism, such as iron, has a magnetic force corresponding to the magnetic field of the magnet, is attracted to the conveyor 39b side by this magnetic force, is conveyed to the lower side of the conveyor 39b, and is weakened by the magnet. , And is discharged from the iron outlet 39e provided on the opposite side (left side in FIG. 1) of the conveyor 39b. On the other hand, non-magnetic and non-conductive substances such as glass fall vertically from the end of the conveyor 39b and are discharged from a glass outlet 39d provided below the end of the conveyor 39b.

【0028】さらに、前記返送用風力選別装置42は、前
記ガラス排出口39d に直下して受入口42a が設けられて
おり、該受入口42a より二箇所の折曲部を有する落下部
42bが設けられている。該落下部42b の下方側には風力
調整弁44を介して送風機45に連結された送風路42c が接
続され、また落下部42b の上方の折曲部より直線上に排
風路42d が接続されている。これにより、送風機45の風
力が風力調整弁44により調整され、この調整された風が
送風路42c を介して落下部42b を破砕物の落下方向と対
向して通過して、排風路42d に至ることとなる。尚、前
記排風路42d に至った風は、サイクロン46で不純物が取
り除かれ、その後バグフィルター47を介して大気に放出
される。
Further, the return wind sorter 42 is provided with a receiving port 42a directly below the glass discharge port 39d, and a drop section having two bent portions from the receiving port 42a.
42b is provided. An air passage 42c connected to a blower 45 via a wind control valve 44 is connected to a lower side of the falling portion 42b, and an exhaust passage 42d is connected linearly from a bent portion above the falling portion 42b. ing. Thereby, the wind force of the blower 45 is adjusted by the wind force adjusting valve 44, and the adjusted wind passes through the falling part 42b through the air passage 42c in a direction opposite to the falling direction of the crushed material, and enters the exhaust air passage 42d. Will lead to. Incidentally, the wind reaching the exhaust air passage 42d has its impurities removed by a cyclone 46, and then is discharged to the atmosphere via a bag filter 47.

【0029】尚、非鉄排出口39c 及び鉄類排出口39e よ
り排出された破砕物は夫々ショベルカー等により収集さ
れて、夫々リサイクルに供される。
The crushed materials discharged from the non-ferrous outlet 39c and the ferrous outlet 39e are collected by a shovel or the like, respectively, and provided for recycling.

【0030】また、前記第二返送コンベア35は、前記返
送用風力選別装置42の落下部42b より落下した破砕物を
受取り、前記二次破砕部16のホッパー18に投入可能に設
けられてなる(図1に示すI参照)。
The second return conveyor 35 is provided so as to receive the crushed material dropped from the dropping portion 42b of the return air separation device 42 and to put it into the hopper 18 of the secondary crushing portion 16 ( 1 shown in FIG. 1).

【0031】前記搬送路50は、破砕装置Aにより破砕さ
れ返送用分別機25で分別された粒径5.0mm 以下の破砕物
を受取り、前記収集用分別機52に搬送可能に設けられて
なる。
The transfer path 50 is provided so as to receive the crushed material having a particle size of 5.0 mm or less crushed by the crushing device A and separated by the return separation device 25, and to be conveyed to the collection separation device 52.

【0032】そして、該収集用分別機52は、破砕物を粒
径0.6 mm以下、0.6mm 乃至2.0mm 、2.0mm 以上の三種に
分別すべく、孔径2.0mm の孔が網目状に設けられた第一
分別板55及び孔径0.6mm の孔が網目状に設けられた第二
分別板56を有し、該分別板55,56 により破砕物が粒径に
応じて分別されるようこの分別板55,56 は振動可能に設
けられている。
The collecting sorter 52 is provided with a mesh-like hole having a pore diameter of 2.0 mm in order to separate the crushed material into three types having a particle size of 0.6 mm or less, 0.6 mm to 2.0 mm, and 2.0 mm or more. It has a first sorting plate 55 and a second sorting plate 56 in which holes having a hole diameter of 0.6 mm are provided in a mesh shape. The sorting plates 55 and 56 are used to separate crushed materials according to the particle size. , 56 are provided so as to be able to vibrate.

【0033】前記収集手段Cには、該収集用分別機52に
より分別された破砕物を夫々粒径に応じて収集すべく各
搬出路60, …を有しており、該搬出路60を介して収容容
器61内部に各ガラス粒が収容されることとなる。
The collecting means C has discharge paths 60,... For collecting the crushed materials separated by the collecting sorter 52 in accordance with the respective particle diameters. As a result, each glass particle is stored in the storage container 61.

【0034】ここで、三つの搬出路60, …のうち粒径0.
6mm 乃至2.0mm の破砕物に対応する搬出路60及び粒径2.
0mm 以上の破砕物に対応する搬出路60には自重落下部65
b を有する風力選別装置65が設けられている。該自重落
下部65b には落下する破砕物の落下方向と対向する対向
風を送風可能な風力選別手段67が設けられている。
Here, among the three discharge paths 60,...
Unloading path 60 for crushed material of 6 mm to 2.0 mm and particle size 2.
The unloading path 60 corresponding to the crushed material of
b is provided. The self-weight dropping portion 65b is provided with a wind force selection means 67 capable of blowing an opposing wind facing the falling direction of the falling crushed material.

【0035】該自重落下部65b は、ガラス粒受入口65a
より二箇所の折曲部を有してなり、該自重落下部65b の
下方側は各風力調整弁69を介して同一の送風機45に連結
された送風路65c が接続されている。
The dead weight drop portion 65b is provided with a glass grain receiving port 65a.
It has two bent portions, and the lower side of the dead-weight drop portion 65b is connected to an air passage 65c connected to the same blower 45 via each wind control valve 69.

【0036】該風力調整弁69は所望の風力で自重落下部
65b に送風可能に風力を調整可能に形成されており、ま
た該風力調整弁69と送風機45とが前記風力選別手段67に
相当する。尚、該送風機45は前記返送用風力選別装置42
用の送風機45と同一の送風機を使用している。また、該
自重落下部65b の上方側には、上方の折曲部より直線上
に排風路65dが接続されており、該排風路65d は前記返
送用風力選別装置42と連結されるバグフィルター47に連
結されている(図1に示すII参照)。これにより、送風
機45の風力を風力調整弁69によりガラス粒の粒径及びガ
ラス粒の利用目的に応じた所望の風力に設定して、この
調整された風が送風路65c を介して自重落下部65b を破
砕物の落下方向と対向して通過して、排風路65d に至
り、その後バグフィルター47を介して大気に放出される
こととなる。
The wind control valve 69 is operated by a desired wind force to drop its own weight.
The wind force adjustment valve 69 and the blower 45 correspond to the wind force selection means 67. Note that the blower 45 is provided with the return wind separation device 42.
The same blower as the blower 45 is used. An exhaust path 65d is connected to the upper side of the dead weight dropping section 65b in a straight line from the upper bent section, and the exhaust path 65d is connected to the return wind separation device 42. It is connected to a filter 47 (see II shown in FIG. 1). Thus, the wind force of the blower 45 is set to a desired wind force according to the particle size of the glass particles and the purpose of use of the glass particles by the wind force adjusting valve 69, and the adjusted wind is passed through the air passage 65c to drop its own weight. The crushed material passes through 65b in a direction opposite to the falling direction of the crushed material, reaches the exhaust air passage 65d, and is then discharged to the atmosphere via the bag filter 47.

【0037】さらに、本実施形態においては、該ガラス
粒が収容された収容容器61を次の袋詰装置71に搬送する
為のホイスト70が上方より吊り下げられてなる。
Further, in the present embodiment, a hoist 70 for transporting the container 61 containing the glass particles to the next bagging device 71 is suspended from above.

【0038】前記袋詰装置71は、収容容器61内のガラス
粒を受入可能なホッパー72と、該ホッパー72内のガラス
粒を一定量ずつ搬送可能な振動フィーダー73と、該振動
フィーダー73より搬送されたガラス粒を袋に詰めつつ計
量可能な計量器74と、該計量器74によって計量され所定
量のガラス粒が詰められた袋をシールするシール機75と
からなる。
The bag filling device 71 includes a hopper 72 capable of receiving the glass particles in the storage container 61, a vibrating feeder 73 capable of conveying the glass particles in the hopper 72 by a fixed amount, and a vibrating feeder 73. It comprises a weighing device 74 capable of weighing the measured glass particles in a bag, and a sealing machine 75 which seals the bag weighed by the weighing device 74 and filled with a predetermined amount of glass particles.

【0039】本実施形態のガラス粒分別収集システムは
上記構成からなり、以下の使用方法により使用される。
The glass particle sorting and collecting system according to the present embodiment has the above-described configuration and is used in the following manner.

【0040】まず、一次破砕部10のホッパー12にガラス
瓶が投入される。尚、投入されるガラス瓶を予め手作業
によって分別して一定の色のガラス瓶のみを投入するこ
とで、最終的に収集されるガラス粒を装飾効果をもった
舗装用骨材として利用することができる。
First, a glass bottle is put into the hopper 12 of the primary crushing unit 10. In addition, the glass bottle to be thrown in is manually separated in advance, and only the glass bottle of a certain color is thrown in, so that the finally collected glass grains can be used as a pavement aggregate having a decorative effect.

【0041】そして、ホッパー12内に投入されたガラス
瓶は一次破砕部10及び二次破砕部16によってガラスが丸
みをもったガラス粒に破砕され(破砕工程)、サイクロ
ン22で埃等が取り除かれ、その後に返送用分別機25に送
り込まれる。このように、返送用分別機25に送られる前
にサイクロン22で埃等が取り除かれるので、返送用分別
機25の目詰まり等を防止することができる。
Then, the glass bottle put into the hopper 12 is crushed into round glass particles by the primary crushing unit 10 and the secondary crushing unit 16 (crushing step), dust and the like are removed by the cyclone 22, Thereafter, it is sent to the sorting machine 25 for return. As described above, since dust and the like are removed by the cyclone 22 before being sent to the return sorting machine 25, clogging of the return sorting machine 25 can be prevented.

【0042】そして、返送用分別機25では粒径5.0mm 以
上の破砕物は返送路29を介して前記二次破砕部16に返送
される(返送用分別工程)。この際、返送路29に於い
て、鉄類からなる不純物及び非鉄金属からなる不純物は
非鉄金属除去装置39によって除去され、返送用風力選別
装置42によって紙等の不純物が除去される。このよう
に、一定粒径以上の破砕物は返送路29を介して返送され
再度破砕されるのでガラス瓶全体を有効に再利用に供す
ることができる。しかも、該返送路29で返送される破砕
物は既に二次破砕されているものであるので、前記非鉄
金属除去装置39及び返送用風力選別装置42による不純物
の除去が確実に行いうる。つまり、一次破砕部による粗
破砕後に分別した一定粒径以上の破砕物内の不純物を非
磁性金属除去装置により除去することも考えられるが、
かかる箇所に返送路及び非鉄金属除去装置等を設けるな
らばガラス瓶の首部等に残存する王冠等がそのままガラ
ス瓶と一体となっていることが多く、確実に王冠等の不
純物を除去することができない。これに対して、本実施
形態の如く被破砕物をガラス粒となるよう破砕した後に
分別・返送を行い、該返送路で王冠等の不純物を除去す
ることにより、ガラス粒と分離した状態での不純物の除
去がより確実に行いうる利点を有する。
Then, the crushed material having a particle size of 5.0 mm or more is returned to the secondary crushing unit 16 through the return path 29 in the return separation device 25 (return separation step). At this time, in the return path 29, the impurities composed of irons and the impurities composed of non-ferrous metals are removed by the non-ferrous metal removal device 39, and the impurities such as paper are removed by the return wind separation device. As described above, the crushed material having a certain particle size or more is returned through the return path 29 and crushed again, so that the entire glass bottle can be effectively reused. Moreover, since the crushed material returned in the return path 29 has already been subjected to secondary crushing, impurities can be reliably removed by the non-ferrous metal removing device 39 and the return air separation device 42. In other words, it is conceivable to remove impurities in the crushed material having a certain particle size or more separated after the coarse crushing by the primary crushing unit by the non-magnetic metal removing device,
If a return path, a non-ferrous metal removing device, or the like is provided at such a location, the crown or the like remaining at the neck or the like of the glass bottle is often integrated with the glass bottle as it is, so that impurities such as the crown cannot be reliably removed. On the other hand, as described in the present embodiment, the crushed material is crushed into glass particles and then separated and returned, and impurities such as a crown are removed in the return path, whereby the glass particles are separated from the glass particles. There is an advantage that the removal of impurities can be performed more reliably.

【0043】また、返送用分別機25で分別された粒径5.
0mm 以下の破砕物は搬送路50を介して収集用分別機52に
よって三種の粒径の破砕物に分別され(収集用分別工
程)、各搬出路60を介して各収容容器61に収容されるこ
ととなる(収集工程)。該収集工程において、粒径0.6m
m 乃至2.0mm の破砕物に対応する搬出路60及び粒径2.0m
m 以上の破砕物に対応する搬出路60には自重落下部65b
が形成されており、該搬出路60を破砕物が通過する際に
落下方向と対向する風によって、紙などの不純物が除去
されることとなる。特に、搬出路60に於ける破砕物は既
に分別手段Bで粒径に応じて分別されたものであるの
で、その粒径のガラス粒に応じて各風力調整弁69で風力
を設定することにより、不純物を高い精度でもって除去
することが可能である。また、自重落下部65b の破砕物
の落下の際に破砕物内の不純物とガラス粒とは互いに離
間しやすいので、より確実に対向風によって不純物を除
去することができる。
The particle size of the particles separated by the return separator 25 is 5.
The crushed material having a size of 0 mm or less is separated into three types of crushed material by the collection separator 52 via the transfer path 50 (collection separation step), and stored in each storage container 61 through each discharge path 60. (Collection process). In the collecting step, the particle size is 0.6 m
Unloading route 60 for crushed materials of m to 2.0 mm and particle size 2.0 m
The self-weight drop section 65b
Is formed, and impurities such as paper are removed by the wind facing the falling direction when the crushed material passes through the carry-out path 60. In particular, since the crushed material in the carry-out path 60 has already been separated according to the particle size by the separation means B, the wind force is set by each wind control valve 69 according to the glass particle having the particle size. It is possible to remove impurities with high accuracy. Further, when the crushed material falls at the dead weight dropping portion 65b, the impurities in the crushed material and the glass particles are easily separated from each other, so that the impurities can be more reliably removed by the facing wind.

【0044】そして、このようにガラス粒が収容された
収容容器61はホイスト70により牽引されて、次の袋詰装
置71によってガラス粒が一定量の袋詰めされる。
Then, the container 61 containing the glass particles is pulled by the hoist 70, and a predetermined amount of the glass particles is packed by the next bagging device 71.

【0045】本実施形態のガラス粒分別収集システムは
上記構成からなる上記使用方法によって使用されるの
で、粒径に応じたガラス粒を不純物の少ない状態で収集
することができる利点を有する。
Since the glass particle sorting and collecting system of this embodiment is used by the above-mentioned use method having the above-described configuration, it has an advantage that glass particles corresponding to the particle diameter can be collected in a state with few impurities.

【0046】また、各搬出路60に設けられた二つの風力
選別手段67を各風力調整弁69と一の送風機45によって構
成した為、システム自体のコストの低廉化を図ることが
でき、特に該送風機45は返送用風力選別装置42と同一の
ものが使用されるのでよりコストの低減を図ることがで
きる利点を有する。
Further, since the two wind power selecting means 67 provided in each of the carry-out paths 60 are constituted by each of the wind power regulating valves 69 and one blower 45, the cost of the system itself can be reduced, and in particular, the cost can be reduced. Since the blower 45 is the same as the return wind separation device 42, it has an advantage that the cost can be further reduced.

【0047】さらに、前記風力選別手段67の風力調整弁
69は適宜風力を調整可能であるので、収集後のガラス粒
の利用目的に応じて、その都度各搬出路60の風力の調整
を行うことで、利用目的に応じて不純物の除去の確実性
を高める或いは収集作業の効率化を図ることもできる。
Further, a wind regulating valve of the wind sorting means 67
Since 69 can adjust the wind force as appropriate, the wind force of each carry-out path 60 is adjusted each time according to the purpose of use of the glass particles after collection, so that the certainty of the removal of impurities according to the purpose of use is improved. It is also possible to improve the efficiency of collection work.

【0048】また、破砕装置Aにより破砕された破砕物
を収集用分別機52に搬送する搬送路50を有するので、破
砕装置Aと収集用分別機52とを所望の場所に設置するこ
とが可能であり、さらに返送用分別機25の設置場所を返
送路29に合わせて設定することで所望距離の返送路29を
設けることが可能である。
Also, since there is a transport path 50 for transporting the crushed material crushed by the crushing device A to the collecting separator 52, the crushing device A and the collecting separator 52 can be installed at desired locations. Further, the return path 29 having a desired distance can be provided by setting the installation location of the return separator 25 in accordance with the return path 29.

【0049】尚、本実施形態のガラス粒分別収集システ
ムは、上記構成からなり上記ガラス粒分別収集方法の如
く使用されるので上述の如き利点を有したが、本願発明
はこれに限定されるものでない。
The system for separating and collecting glass particles according to the present embodiment has the above-mentioned advantages because it has the above-mentioned configuration and is used like the method for separating and collecting glass particles, but the present invention is not limited to this. Not.

【0050】つまり、上記実施形態に於いては粗破砕を
行う一次破砕部10と細破砕を行う二次破砕部16との二つ
の破砕部から破砕装置Aを構成したが、本願発明はこれ
に限定されるものでなくガラス瓶をガラス粒に破砕可能
な装置であれば適宜設計変更可能である。
That is, in the above-described embodiment, the crushing apparatus A is composed of two crushing units, the primary crushing unit 10 for performing coarse crushing and the secondary crushing unit 16 for performing fine crushing. There is no limitation, and the design can be changed as appropriate as long as the device can crush a glass bottle into glass particles.

【0051】また、上記実施形態に於いては分別手段B
が収集用分別機52と搬送路50と分別機25と返送路29とを
具備するものについて説明したが、本願発明において破
砕装置Aにより破砕された破砕物を粒径に応じて分別す
ることができるものであれば良く、搬送路50等は必須の
要件ではない。
In the above embodiment, the separating means B
Has been described that includes the collection separator 52, the transport path 50, the separator 25, and the return path 29, but in the present invention, it is possible to separate the crushed material crushed by the crushing device A according to the particle size. The transport path 50 and the like are not indispensable requirements as long as they can be used.

【0052】さらに、返送路29を有する場合にあって
も、上記実施形態の如く、非鉄金属除去装置39及び返送
用風力選別装置42を設けるものに限定されるものでな
い。しかも、アルミ等の非鉄金属が不純物内に少ない場
合等にあっては、非鉄金属除去装置39のかわりに、例え
ば図3に示すように吊り下げマグネットの如き鉄類除去
装置37を設けることもできる。
Further, even in the case where the return path 29 is provided, the present invention is not limited to the one provided with the non-ferrous metal removal device 39 and the return wind separation device 42 as in the above embodiment. Further, in the case where the amount of non-ferrous metal such as aluminum is small in the impurities, etc., instead of the non-ferrous metal removing device 39, for example, as shown in FIG. .

【0053】また、一次破砕部10と二次破砕部16とから
破砕装置Aを構成した場合に、返送路29によって二次破
砕部16に返送する以外に、図3に示すように一次破砕部
10に返送することも可能である。
When the crushing device A is composed of the primary crushing unit 10 and the secondary crushing unit 16, the crushing unit A is returned to the secondary crushing unit 16 by the return path 29, as shown in FIG.
It is also possible to return it to 10.

【0054】さらに、本願発明に於いて収集手段Cは、
分別手段Bによって分別された破砕物を収集可能な手段
であれば適宜設計変更可能であり、上記実施形態の如く
収容容器61によりガラス粒を収容するものに限定される
ものでなく、例えば分別手段Bによって分別されたガラ
ス粒を夫々次工程に搬送するコンベア等であっても本願
発明の意図する範囲内である。
Further, in the present invention, the collecting means C comprises:
The design can be changed as appropriate as long as it is a means that can collect the crushed material separated by the separation means B, and is not limited to the one that stores the glass particles in the storage container 61 as in the above-described embodiment. Even a conveyor or the like that transports the glass particles separated by B to the next step is within the range intended by the present invention.

【0055】[0055]

【発明の効果】叙上の様に、本願発明に係るガラス粒分
別収集システムは、上述の如き構成からなり、ガラス瓶
等の破砕物を破砕装置によって破砕し、その破砕物を分
別手段によって粒径に応じて分別して、かかる粒径に応
じて分別された破砕物内の紙等の不純物を風力選別手段
によって除去して収集することができ、これにより収集
されたガラス粒に混在する不純物を減少させることがで
きるという効果を奏する。
As described above, the system for separating and collecting glass particles according to the present invention has the above-mentioned configuration, and crushes a crushed material such as a glass bottle with a crushing device, and separates the crushed material with a particle size by a separation means. And the impurities such as paper in the crushed material separated according to the particle size can be removed and collected by a wind separation means, thereby reducing impurities mixed in the collected glass particles. The effect that it can be made to play is produced.

【0056】また、本願請求項2記載のガラス粒分別収
集システムは、自重落下部を落下する破砕物の落下方向
と対向する対向風を送風可能に風力選別手段が設けられ
てなるので、不純物とガラス粒とが混在する破砕物を自
重落下部で互いに離間せしめて対向風によって不純物を
除去することができ、これにより不純物をより減少させ
た状態でガラス粒を収集することができるという効果を
奏する。
Further, in the glass particle sorting and collecting system according to the second aspect of the present invention, since the wind separation means is provided so as to be able to blow a counter wind facing the falling direction of the crushed material falling down the dead weight dropping portion, impurities are eliminated. The crushed material in which the glass particles are mixed is separated from each other at the dead weight drop portion, and the impurities can be removed by the counter wind, so that there is an effect that the glass particles can be collected with the impurities further reduced. .

【0057】[0057]

【0058】また、本願請求項3記載の発明に係るガラ
ス粒分別収集システムは、風力選別手段が風力を調整可
能に設けられてなるので、風力選別手段の風力を調整す
ることで収集後のガラス粒の利用目的に応じた収集作業
を行いうるという効果を奏する。
In the glass particle sorting and collecting system according to the third aspect of the present invention, since the wind force sorting means is provided so as to adjust the wind force, the glass after collection is adjusted by adjusting the wind force of the wind force sorting means. There is an effect that the collecting operation can be performed according to the purpose of using the grains.

【0059】さらに、本願請求項4記載の発明に係るガ
ラス粒分別収集システムは、所定粒径以上の破砕物を破
砕装置に返送する返送路が設けられてなるので、所定粒
径以上の破砕物を捨てることなくガラス瓶等の被破砕物
を有効に利用することができるという効果を有するとと
もに、破砕装置と収集用分別機との間に搬送路が設けら
れてなるので、破砕装置と収集用分別機とを所望の場所
に設置することが可能であり、さらに返送用分別機の設
置場所を返送路に合わせて設定することで所望距離の返
送路を設けることが可能であり、これにより該システム
を工場等に容易に設置することができるという効果を有
する。
Further, the glass particle sorting and collecting system according to the invention of claim 4 of the present application is provided with a return path for returning the crushed material having a predetermined particle size or more to the crushing apparatus. It has the effect that the crushed material such as a glass bottle can be effectively used without discarding the waste, and a transport path is provided between the crushing device and the collection separator, so that the crushing device and the collection separator are separated. Can be installed at a desired location, and a return path of a desired distance can be provided by setting the installation location of the return sorting machine in accordance with the return path. Can be easily installed in a factory or the like.

【0060】また、本願請求項5記載のガラス粒分別収
集方法は、破砕物のうち所定粒径以上の破砕物を返送す
ることで所定粒径以上の破砕物を捨てることなくガラス
瓶等の被破砕物を有効に利用することができ、しかも収
集用分別工程後に風力選別手段により不純物を除去する
ことで、粒径に応じて分別された破砕物内の紙等の不純
物を的確に除去して収集することができ、これにより収
集されたガラス粒に混在する不純物を減少させることが
できるという効果を奏する。
The method for separating and collecting glass particles according to the fifth aspect of the present invention is characterized in that, among the crushed materials, crushed materials having a predetermined particle size or more are returned so that crushed materials such as glass bottles are not discarded. The material can be used effectively, and after the separation process for collection, impurities are removed by the wind separation means, so that impurities such as paper in the crushed material separated according to the particle size can be accurately removed and collected. Accordingly, there is an effect that impurities mixed in the collected glass particles can be reduced.

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

【図1】本願発明に係るガラス粒分別収集システムの一
実施形態の概略図。
FIG. 1 is a schematic view of an embodiment of a glass particle sorting and collecting system according to the present invention.

【図2】本願発明に係るガラス粒分別収集システムの一
実施形態のフローチャート。
FIG. 2 is a flowchart of an embodiment of a glass particle sorting and collecting system according to the present invention.

【図3】本願発明に係るガラス粒分別収集システムの他
実施形態の概略図。
FIG. 3 is a schematic view of another embodiment of the glass particle sorting and collecting system according to the present invention.

【符号の説明】[Explanation of symbols]

A…破砕装置、B…分別手段、C…収集手段、10…一次
破砕部、16…二次破砕部、25…返送用分別機、29…返送
路、37…磁性体除去装置(吊下マグネット)、39…非磁
性金属除去装置、42…返送用風力選別装置、42b …落下
部、45…送風機、52…収集用分別機、60…搬出路、61…
収容容器、65…風力選別装置、65b …自重落下部、67…
風力選別手段、69…風力調整弁、71…袋詰装置
A: crushing device, B: separating means, C: collecting means, 10: primary crushing section, 16: secondary crushing section, 25: return separator, 29: return path, 37: magnetic material removing device (suspension magnet) ), 39: Non-magnetic metal removal device, 42: Wind separator for return, 42b: Falling part, 45: Blower, 52: Sorter for collection, 60: Outgoing path, 61 ...
Storage container, 65: Wind separator, 65b: Self-weight falling part, 67 ...
Wind power sorting means, 69… Wind pressure regulating valve, 71… Packing device

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭51−64666(JP,A) (58)調査した分野(Int.Cl.7,DB名) B07B 1/00 - 15/00 ────────────────────────────────────────────────── (5) References JP-A-51-64666 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B07B 1/00-15/00

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ラベルの付着したガラス瓶等の被破砕物
を破砕する破砕装置(A) と、該破砕装置(A) により破砕
された破砕物を粒径に応じて分別すると共に、分別され
た所定粒径以下の破砕物をさらに粒径に応じて二種以上
に分別する分別手段(B) と、該二種以上に分別された破
砕物のそれぞれに応じて設けられた搬出路(60)を介して
これらを夫々収集する収集手段(C) とを有してなり、し
かも、前記収集手段(C) は、少なくとも二つの搬出路(6
0)に、紙等の不純物を除去すべく送風可能な風力選別手
段(67)を夫々設けてなることを特徴とするガラス粒分別
収集システム。
1. A crushing device (A) for crushing a crushed material such as a glass bottle having a label attached thereto, and a crushed material crushed by the crushing device (A) is separated according to a particle size and separated.
Two or more types of crushed material having a predetermined particle size or less according to the particle size
Fractionating fractionating means (B), and fractionated over the two broken to
Through the unloading route (60) provided for each of the crushed materials
These will have a collection means for each collected (C), moreover, the collector means (C) is at least two discharge paths (6
A glass particle sorting and collecting system characterized in that 0) is provided with a wind force sorting means (67) capable of blowing air to remove impurities such as paper.
【請求項2】 前記搬出路(60)は破砕物が自重により落
下する自重落下部(65b) を有し、且つ前記風力選別手段
(67)は該自重落下部(65b) を落下する破砕物の落下方向
と対向する対向風を送風可能に設けられてなる請求項1
記載のガラス粒分別収集システム。
2. The unloading path (60) has a dead weight drop section (65b) in which the crushed material falls by its own weight, and the wind separation means
(1) The air flow (67) is provided so as to be able to blow an opposing wind facing the falling direction of the crushed material falling on the dead weight dropping portion (65b).
The glass particle sorting and collecting system as described.
【請求項3】 前記風力選別手段(67)が、ガラス粒の粒
に応じて風力を調整可能に設けられてなる請求項1又
は2記載のガラス粒分別収集システム。
3. The method according to claim 2, wherein the wind sorting means (67) comprises a glass particle.
The glass particle sorting and collecting system according to claim 1 or 2, wherein a wind force is adjustable according to the diameter .
【請求項4】 前記分別手段(B) が、前記破砕装置(A)
により破砕された破砕物を所定粒径以下と所定粒径以上
の二種に分別可能な返送用分別機(25)と、該返送用分別
機(25)で分別された所定粒径以下の破砕物を受取る搬送
路(50)と、前記返送用分別機(25)で分別された所定粒径
以上の破砕物を破砕装置(A) に返送可能な返送路(29)
と、前記搬送路(50)により搬送される所定粒径以下の破
砕物を夫々粒径に応じて前記各搬出路(60)に搬出すべく
少なくとも二種以上に分別可能な収集用分別機(52)とを
具備してなる請求項1乃至3の何れかに記載のガラス粒
分別収集システム。
4. The crushing device (A), wherein the separating means (B) is
A return sorting machine (25) capable of separating the crushed material into two types having a predetermined particle size or less and a predetermined particle size or more, and a crushed product having a predetermined particle size or less separated by the return sorting machine (25). A transport path (50) for receiving materials, and a return path (29) capable of returning crushed materials having a predetermined particle size or more separated by the return separator (25) to the crusher (A).
And, a crushed material having a predetermined particle size or less which is conveyed by the conveyance path (50) is separated into at least two or more types of collection sorters for carrying out to each of the carry-out paths (60) according to the particle diameter ( 52) The system for separating and collecting glass particles according to any one of claims 1 to 3, comprising:
【請求項5】 ラベルの付着したガラス瓶等の被破砕物
を破砕する破砕工程と、該破砕工程で破砕された破砕物
を粒径に応じて二種の破砕物に分別して、所定粒径以上
の破砕物を前記破砕工程に返送する返送用分別工程と、
該返送用分別工程で分別された所定粒径以下の破砕物を
粒径に応じて二種以上に分別する収集用分別工程と、該
収集用分別工程によって分別された破砕物のそれぞれに
応じて設けられた搬出路(60)を介してこれらを夫々収集
する収集工程とからなり、且つ、前記収集工程において
少なくとも二種の破砕物の搬出路(60)で風力選別手段(6
7)によって紙等の不純物を除去することを特徴とするガ
ラス粒分別収集方法。
5. A crushing step of crushing an object to be crushed such as a glass bottle having a label attached thereto, and the crushed material crushed in the crushing step is separated into two types of crushed substances according to the particle size, and the crushed material is separated into a predetermined particle size or more. A return separation step of returning the crushed material to the crushing step,
A collection separation step of separating the two or more depending on the particle size of the crushed material having a predetermined particle diameter or less under fractionated in the return for fractionation step, each of the crushed material which has been fractionated by the collection for fractionation step
And a collecting step of collecting these through a discharge path (60) provided accordingly , and in the collecting step, at least two types of crushed materials are discharged through the wind separation means (6).
7. A method for separating and collecting glass particles, wherein impurities such as paper are removed by 7).
JP24185196A 1996-09-12 1996-09-12 Glass particle sorting and collecting system and method for collecting the same Expired - Lifetime JP3206884B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24185196A JP3206884B2 (en) 1996-09-12 1996-09-12 Glass particle sorting and collecting system and method for collecting the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24185196A JP3206884B2 (en) 1996-09-12 1996-09-12 Glass particle sorting and collecting system and method for collecting the same

Publications (2)

Publication Number Publication Date
JPH1085670A JPH1085670A (en) 1998-04-07
JP3206884B2 true JP3206884B2 (en) 2001-09-10

Family

ID=17080460

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24185196A Expired - Lifetime JP3206884B2 (en) 1996-09-12 1996-09-12 Glass particle sorting and collecting system and method for collecting the same

Country Status (1)

Country Link
JP (1) JP3206884B2 (en)

Also Published As

Publication number Publication date
JPH1085670A (en) 1998-04-07

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