JP3187724B2 - Mixed oversized garbage sorting equipment - Google Patents

Mixed oversized garbage sorting equipment

Info

Publication number
JP3187724B2
JP3187724B2 JP28021096A JP28021096A JP3187724B2 JP 3187724 B2 JP3187724 B2 JP 3187724B2 JP 28021096 A JP28021096 A JP 28021096A JP 28021096 A JP28021096 A JP 28021096A JP 3187724 B2 JP3187724 B2 JP 3187724B2
Authority
JP
Japan
Prior art keywords
magnetic
collected
impurities
mixed
separator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP28021096A
Other languages
Japanese (ja)
Other versions
JPH1099783A (en
Inventor
恭輔 園
充良 辻本
博嗣 野口
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.)
Kurimoto Ltd
Original Assignee
Kurimoto Ltd
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 Kurimoto Ltd filed Critical Kurimoto Ltd
Priority to JP28021096A priority Critical patent/JP3187724B2/en
Publication of JPH1099783A publication Critical patent/JPH1099783A/en
Application granted granted Critical
Publication of JP3187724B2 publication Critical patent/JP3187724B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • 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】この発明は混合系粗大ごみ選
別処理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 an apparatus for sorting large-sized waste.

【0002】[0002]

【従来の技術】従来より採用されている可燃性粗大ご
み、不燃性粗大ごみおよび不燃ごみを含む混合系粗大ご
みの選別処理装置(廃棄物を流動床焼却する場合の前処
理用破砕選別装置)として、この発明の出願人による特
開平1−11938号公報のものを挙げることができ
る。図3において、ごみ運搬車等によって運ばれてきた
粗大ごみはホッパ1に投入され、供給コンベヤ2、フィ
−ダ3を経て、破砕機4にて破砕される。破砕された破
砕物は排出コンベヤ5、破砕物搬送コンベヤ6で搬送さ
れ、同コンベヤ6の終端部に設けられたベルト型の一次
磁選機7にて、金属片等の磁性物が回収除去され、残つ
た破砕物は回転篩型選別機(トロンメル)8にて不燃物
と可燃物に分けられ、不燃物は回収され、可燃物は可燃
物コンベヤ9にて搬送され、可燃物コンベヤ9の端部に
組込まれたドラム型の二次磁選機10により磁性物が回
収され、磁性物が除去された可燃物は流動床焼却炉11
にて焼却されるのである。12,13はそれぞれ磁性物
ホッパ、不燃物ホッパで、14,15および16はそれ
ぞれサイクロン,集塵機および排風機である。
2. Description of the Related Art Conventionally used sorting equipment for combustible oversized refuse, non-combustible oversized refuse, and mixed oversized refuse including non-combustible refuse (crushing and sorting apparatus for pretreatment when waste is incinerated in a fluidized bed). Japanese Patent Application Laid-Open No. 1-1938, filed by the applicant of the present invention, may be mentioned. In FIG. 3, oversized garbage transported by a garbage truck or the like is put into a hopper 1, passed through a supply conveyor 2, a feeder 3, and crushed by a crusher 4. The crushed crushed material is transported by a discharge conveyor 5 and a crushed material transport conveyor 6, and a belt-type primary magnetic separator 7 provided at the end of the conveyor 6 collects and removes magnetic substances such as metal pieces. The remaining crushed material is separated into incombustibles and combustibles by a rotary sieve type sorter (Trommel) 8, the incombustibles are collected, and the combustibles are conveyed by a combustible conveyor 9. The magnetic material is collected by a drum-type secondary magnetic separator 10 incorporated in the furnace, and the combustible material from which the magnetic material has been removed is supplied to a fluidized bed incinerator 11.
It is incinerated at. Numerals 12 and 13 denote a magnetic material hopper and a non-combustible material hopper, respectively. Numerals 14, 15 and 16 denote a cyclone, a dust collector and an exhaust fan, respectively.

【0003】[0003]

【発明が解決しようとする課題】そこで、前記可燃物を
流動床焼却炉で処理する場合、この可燃物中に金属片が
存在することがある。その理由として、破砕物中の磁性
体は前記一次磁選機7にて大半は回収除去されるのであ
るが、破砕機4から排出される破砕ごみの量は一定では
なく相当の変動巾があること、また種々雑多なごみが混
り合っていることから、これら破砕物の通過を容易にす
るため、一次磁選機として通常はベルト型の磁選機7が
多用されている。この磁選機を設置する場合、前記した
如く破砕物中に100〜200m/m程度(長さ方向で
300m/m位)のサイズの大きい比較的嵩高な破砕物
が混入していることが多いため、これらの破砕物が容易
に搬送されるように破砕物コンベヤ6と磁選機7の間隔
は250m/m〜300m/m程度に設定される。この
ように設定されると、磁石から離れた位置(コンベヤ
側)における磁束密度が急激に低下し、磁着力が落ち
る。そこで強い磁石にすることも考えられるが、あまり
強くすると、急激な吸着によりベルトが早期に破損する
こととなるため、結局磁性物の回収率は十分とはいえ
ず、未回収のものが可燃物中に混入することとなる。未
回収の鉄類としては比較的重いもの例えばワウヤ状のも
の、冷蔵庫等のモ―タ類、鉄筋、平鋼部材が多いことが
判った。
Therefore, when the combustibles are treated in a fluidized bed incinerator, metal pieces may be present in the combustibles. The reason is that most of the magnetic material in the crushed material is collected and removed by the primary magnetic separator 7, but the amount of crushed waste discharged from the crusher 4 is not constant but has a considerable fluctuation range. In addition, since various kinds of garbage are mixed, a belt-type magnetic separator 7 is usually often used as a primary magnetic separator in order to facilitate passage of these crushed materials. When this magnetic separator is installed, a relatively bulky crushed material having a large size of about 100 to 200 m / m (about 300 m / m in the length direction) is often mixed in the crushed material as described above. The distance between the crushed material conveyor 6 and the magnetic separator 7 is set to about 250 m / m to 300 m / m so that these crushed materials are easily transported. With this setting, the magnetic flux density at a position distant from the magnet (on the side of the conveyor) rapidly decreases, and the magnetic adhesion decreases. Therefore, it is conceivable to use a strong magnet.However, if it is too strong, the belt will be damaged at an early stage due to sudden adsorption, so that the recovery rate of magnetic substances is not sufficient, and the unrecovered ones are flammable substances. It will be mixed in. It has been found that many uncollected irons are relatively heavy, for example, wowers, motors such as refrigerators, reinforcing bars, and flat steel members.

【0004】次いで、一次磁選機7で磁性物の大半は回
収除去されるも、未回収の鉄類を含む破砕物を回転篩型
選別機8に投入して篩下の不燃物と篩上の可燃物に篩分
けし、篩上の可燃物は残存する鉄類とともにオ―バ―サ
イズとして排出され、可燃物コンベヤ9にて搬送され、
可燃物コンベヤ9の終端部の回転篩型二次磁選機10に
て磁性物が確実に磁着除去され、純度の高いものとな
る。なお、一次選別機7の下方付近および選別機8内に
図示しない送風機から送風して選別効果を上げるように
なっているが、磁性物に不純物例えばビニールシートや
布などが絡んだ状態となっているため、一次磁選機7か
らいきよいよく落下する磁性物の落下途中で、該磁性物
から不純物を分離することははなはだ困難である。した
がって、磁性物中に不純物が含まれたまま回収されるこ
ととなり、それだけ磁性物の純度が低下する。さらに、
磁性物に絡まった不純物は回転篩型磁選機8内で解され
て分離するものもあるが、十分に分離されることなく磁
性物に付着したまま回収されることが多い。
The primary magnetic separator 7 recovers and removes most of the magnetic material, but the unrecovered crushed material containing iron is put into a rotary sieve-type separator 8 so that the incombustible material under the sieve and the unburned material on the sieve are removed. The mixture is sieved into combustibles, and the combustibles on the sieve are discharged as oversize together with the remaining irons, and are conveyed by the combustibles conveyor 9;
The magnetic material is reliably magnetized and removed by the rotary sieve type secondary magnetic separator 10 at the end of the combustible material conveyor 9, resulting in high purity. It should be noted that the air is blown from a blower (not shown) near the lower part of the primary sorter 7 and inside the sorter 8 to increase the sorting effect. However, impurities such as a vinyl sheet or cloth are entangled with the magnetic substance. Therefore, it is extremely difficult to separate impurities from the magnetic substance during the fall of the magnetic substance that falls well from the primary magnetic separator 7. Therefore, the magnetic substance is recovered while containing impurities, and the purity of the magnetic substance is reduced accordingly. further,
Impurities entangled with the magnetic substance are sometimes separated in the rotary sieve magnetic separator 8 and separated, but are often collected without being sufficiently separated and attached to the magnetic substance.

【0005】他方、図示省略したが、前記ベルト型磁選
機に変えて破砕物コンベヤ6のプ―リ(終端側)に磁石
を組み込んだプ―リ型(ドラム型)の磁選機を採用する
こともあるが、この場合比較的重い磁性物は確実に回収
されるが、破砕ごみ量の変動などでごみ層厚が一定でな
いため、やはりごみ中の鉄片が残ることが多い。この場
合、特に上層に存在する小片の鉄片類の残存が多く、前
記ベルト型に比べて回収率が低いとされいる。また、比
較的重い磁性物中にも不純物が絡まったまま回収される
ことがある。
On the other hand, although not shown, a pull-type (drum-type) magnetic separator in which magnets are incorporated in the pulley (end side) of the crushed material conveyor 6 instead of the belt-type magnetic separator is used. In this case, a relatively heavy magnetic substance is reliably recovered in this case. However, since the thickness of the refuse layer is not constant due to fluctuations in the amount of crushed refuse, iron pieces in the refuse often remain. In this case, particularly, small pieces of iron pieces existing in the upper layer often remain, and the collection rate is said to be lower than that of the belt type. Further, impurities may be collected in a relatively heavy magnetic substance while being entangled.

【0006】この発明は、一次磁選機での回収もれの磁
性物、すなわち鉄類を確実に除去し、可燃物中の鉄類の
残存を無くすとともに磁性物の純度をも上げることがで
きる混合系粗大ごみ選別処理装置を提供するものであ
る。
According to the present invention, there is provided a mixing device capable of reliably removing magnetic materials, that is, irons, which have been recovered from a primary magnetic separator and eliminating irons remaining in combustible materials and increasing the purity of the magnetic materials. An object of the present invention is to provide a system oversized trash sorting apparatus.

【0007】[0007]

【課題を解決するための手段】前記課題を達成するため
に、この発明の混合系粗大ごみ選別処理装置は、混合系
粗大ごみの破砕物を搬送用ベルトコンベヤの終端部に内
蔵された回転ドラム型一次磁選機で磁性物と不純物とに
選別し、前記磁性物と一部混入する不純物を風力併用型
振動フィーダに供給して該磁性物に混入する不純物中の
軽量可燃物を該風力併用型振動フィーダへ導入される空
気により浮上分離させて捕集機により吸引回収し、前記
風力併用型振動フィーダの終端部に所定の隙間を設けて
配設した回転ドラム型二次磁選機の回転ドラムに磁性物
を磁着させ、かつ、前記軽量可燃物が取り除かれた比較
的重い可燃物からなる不純物を前記隙間から落下させる
ことで、両者をそれぞれ選別回収するとともに、前記回
転ドラム型一次磁選機からの不純物を回転篩型選別機に
供給して不燃物と可燃物とに篩分け回収するようにした
ことである。これにより、可燃物は磁性物が確実に回収
除去されて純度の高いものとなり、また磁性物も純度の
高い可燃物をものとなる。
In order to achieve the above-mentioned object, the present invention provides a mixed-system bulky waste sorting apparatus, comprising: a rotary drum built in a terminal end portion of a conveyor belt conveyor for crushed mixed-size bulky waste; The magnetic primary material is separated into magnetic substances and impurities by a primary magnetic separator, and the impurities which are partially mixed with the magnetic substances are supplied to a wind-powered type vibration feeder, and the lightweight combustible substances in the impurities which are mixed into the magnetic substances are mixed with the wind-powered type. floated separated by air introduced into the vibration feeder suction collected by the collecting machine, the
Provide a predetermined clearance at the end of the vibrating feeder with wind power.
Magnetic material on the rotating drum of the installed rotating drum type secondary magnetic separator
And the lightweight combustible material is removed.
Drops impurities composed of heavy combustibles from the gap
Thus, both of them are sorted and collected , and the impurities from the rotary drum type primary magnetic separator are supplied to a rotary sieve type sorter to be separated into incombustibles and combustibles and collected. As a result, the combustibles are reliably recovered and removed from the magnetic substances, and the combustibles have a high purity, and the magnetic substances also have a high purity combustibles.

【0008】また、混合系粗大ごみの破砕物を搬送用ベ
ルトコンベヤの終端部に内蔵された回転ドラム型一次磁
選機で磁性物と不純物とに選別し、前記磁性物と一部混
入する不純物を風力併用型振動フィーダに供給して該磁
性物に混入する不純物中の軽量可燃物を該風力併用型振
動フィーダへ導入される空気により浮上分離させて捕集
機により吸引回収し、磁性物と、前記軽量可燃物が取り
除かれた比較的重い可燃物からなる不純物とを、前記風
力併用型振動フィーダの終端部に排出シュートを介して
配設した回転ドラム型二次磁選機によりそれぞれ選別回
収するとともに、前記回転ドラム型一次磁選機からの不
純物を回転篩型選別機に供給して不燃物と可燃物とに篩
分け回収するようにしたことである。
Further, the crushed material of the mixed bulky waste is separated into magnetic substances and impurities by a rotary drum type primary magnetic separator built in the end portion of the conveyor belt conveyor, and impurities mixed with the magnetic substances are mixed. The lightweight combustible material in the impurities mixed into the magnetic material supplied to the wind-powered vibration feeder is floated and separated by air introduced into the wind-powered vibration feeder, suction-collected by a collector, and the magnetic material, The lightweight combustible material is removed and impurities composed of relatively heavy combustible material are separately collected and collected by a rotary drum type secondary magnetic separator arranged at a terminal end of the combined use wind type vibration feeder via a discharge chute. In addition, the impurities from the rotary drum type primary magnetic separator are supplied to a rotary sieve type separator to be sieved and collected as incombustibles and combustibles.

【0009】[0009]

【発明の実施の形態】以下、この発明の実施の形態を図
面に基づいて説明する。なお、図3と同一のものは同一
符号を用いて説明する。図1は混合系粗大ごみ選別処理
装置の代表例を示すフロ―シ―トで、同図において、1
はホッパ、2は供給コンベヤ、3はフィ―ダ、4は破砕
機、5は排出コンベヤ、6は第1(破砕物)コンベヤ、
17はコンベヤ、18はコンベヤ17の端部に込み込ん
だドラム型の一次磁選機、8は回転篩型選別機(トロン
メル)で、篩網目の大きさは20〜30m/m 程度に
設定する。19は風力併用型振動フィーダで、多孔板2
0の下部から送風機21により空気を送り込むようにな
っている。22は排気口で、配管を介して捕集機14
(図示の場合はサイクロンであるが、サイクロンと集塵
機の組合わせでもよい)と吸引排風機16に接続する。
23はドラム型の二次磁選機で、風力併用型振動フィー
ダ19との間に所定の間隔dを開けて配設する。24,
25,26,27はホッパである。18はコンベヤ17
の終端側プ―リに代えた回転ドラムとこの回転ドラム内
に組込んだ回転磁石とからなるいわゆる回転ドラム型磁
選機である。23は、回転ドラムとこの回転ドラム内に
組み込んだ固定磁石とからなる回転ドラム型磁選機であ
る。
Embodiments of the present invention will be described below with reference to the drawings. In addition, the same thing as FIG. 3 is demonstrated using the same code | symbol. FIG. 1 is a flow chart showing a typical example of a mixed bulk waste sorting apparatus.
Is a hopper, 2 is a feed conveyor, 3 is a feeder, 4 is a crusher, 5 is a discharge conveyor, 6 is a first (crushed material) conveyor,
Reference numeral 17 denotes a conveyor, 18 denotes a drum-type primary magnetic separator incorporated in the end of the conveyor 17, 8 denotes a rotary sieve-type separator (Trommel), and the size of the sieve mesh is set to about 20 to 30 m / m 2. 19 is a vibrating feeder combined with wind power,
Air is blown in by a blower 21 from the lower part of 0. Reference numeral 22 denotes an exhaust port.
(In the illustrated case, it is a cyclone, but it may be a combination of a cyclone and a dust collector.)
Reference numeral 23 denotes a drum-type secondary magnetic separator, which is disposed at a predetermined interval d between the secondary magnetic separator and the vibrating feeder 19 combined with wind power. 24,
25, 26 and 27 are hoppers. 18 is a conveyor 17
A rotary drum type magnetic separator comprising a rotary drum instead of the pulley on the end side and a rotary magnet incorporated in the rotary drum. Reference numeral 23 denotes a rotary drum type magnetic separator including a rotary drum and a fixed magnet incorporated in the rotary drum.

【0010】上記において、ホッパ1に投入された粗大
ごみはコンベヤ2により搬送され、フィーダ3を経て破
砕機4に押込まれ、破砕機4にて破砕され、破砕物はコ
ンベヤ6で搬送され、コンベヤ17の終端で、一次磁選
機18で磁性体が磁着除去される。この際一次磁選機は
ドラム型であるので、大小を問わず磁性物(鉄類)が磁
着回収される。特にモータやコンプレッサーなどの塊状
磁性物も確実に吸着される。残った破砕物(不純物)は
回転篩型選別機8に投入され、ここで篩上の可燃物と篩
下の不燃物とに篩分され、篩上の可燃物はホッパ24
へ、篩下の不燃物はホッパ25に収容される。前記一次
磁選機18で磁着された磁性物は風力併用型振動フィー
ダ19に送られる。このとき磁性物に絡まった不純物す
なわち軽量な可燃物や紛れ込んだ一部の可燃物(不純
物)がある。これらの磁性物や可燃物は風力併用型振動
フィーダ19の振動による搬送過程で、送風機21から
送られる空気が多孔板20を噴き上げにより、軽量な可
燃物が磁性物から離脱浮上し、排風機16の運転により
排気口22を経て吸引され、捕集機14に捕集される。
軽量な可燃物が取り除かれた磁性物はドラム型の二次磁
選機23により磁着回収される。このとき、吸着されな
い不純物すなわち比較的重い可燃物は間隙dをそのまま
落下する。したがって、可燃物および磁性物は何れも極
めて純度の高いものとなる。さらに、回転篩型選別機に
供給される不純物中に磁性物がほとんど混入されないた
め、該回転篩型選別機の篩に磁性物が引っ掛かることが
無い。
In the above, the oversized refuse introduced into the hopper 1 is conveyed by the conveyor 2, pushed into the crusher 4 via the feeder 3, crushed by the crusher 4, and the crushed material is conveyed by the conveyor 6 to be conveyed by the conveyor 6. At the end of 17, the magnetic material is demagnetized by the primary magnetic separator 18. At this time, since the primary magnetic separator is of a drum type, magnetic substances (irons) regardless of size are magnetically collected. In particular, massive magnetic substances such as motors and compressors are also reliably adsorbed. The remaining crushed material (impurities) is put into a rotary sieve-type sorter 8, where it is sieved into combustibles on the sieve and incombustibles below the sieve.
The incombustible material below the sieve is stored in the hopper 25. The magnetic material magnetized by the primary magnetic separator 18 is sent to a vibrating feeder 19 combined with wind power. At this time, there are impurities entangled with the magnetic material, that is, light combustibles and some combustibles (impurities) that have entered. In the process of transporting these magnetic and combustible materials by the vibration of the wind power type vibrating feeder 19, the air sent from the blower 21 blows up the perforated plate 20, so that lightweight combustible materials are separated from the magnetic material and float, and the air Is sucked through the exhaust port 22 and collected by the collector 14.
The magnetic material from which the light combustible material has been removed is magnetically collected by a drum-type secondary magnetic separator 23. At this time, impurities that are not adsorbed, that is, relatively heavy combustibles, fall directly through the gap d. Therefore, both the combustible material and the magnetic material have extremely high purity. Furthermore, since a magnetic substance is hardly mixed in impurities supplied to the rotary sieve type sorter, the magnetic substance does not catch on the sieve of the rotary sieve type sorter.

【0011】また、図2に示すように、風力併用型振動
フィーダ19とドラム型の二次磁選機23との間にシュ
ート28を設けることもできる。この場合、隙間dがな
いので磁性物を含む全量がドラム型の二次磁選機23上
に落下し、ここで磁性物と不純物である比較的重い可燃
物とに選別される。この方式は比較的重い可燃物が少な
い場合に、二次磁選機23を小容量化できる。
As shown in FIG. 2, a chute 28 may be provided between the vibrating feeder 19 combined with wind power and the secondary magnetic separator 23 of a drum type. In this case, since there is no gap d, the entire amount including the magnetic substance falls onto the drum-type secondary magnetic separator 23, where it is separated into the magnetic substance and the relatively heavy combustible substances as impurities. This method can reduce the capacity of the secondary magnetic separator 23 when relatively heavy combustible materials are small.

【0012】[0012]

【発明の効果】この発明は、以上のように構成したか
ら、次に述べるような効果を奏する。混合系粗大ごみの
破砕物を搬送用ベルトコンベヤの終端部に内蔵された回
転ドラム型一次磁選機で磁性物と不純物とに選別し、前
記磁性物と一部混入する不純物を風力併用型振動フィー
ダに供給して該磁性物に混入する不純物中の軽量可燃物
を該風力併用型振動フィーダへ導入される空気により浮
上分離させて捕集機により吸引回収し、前記風力併用型
振動フィーダの終端部に所定の隙間を設けて配設した回
転ドラム型二次磁選機の回転ドラムに磁性物を磁着さ
せ、かつ、前記軽量可燃物が取り除かれた比較的重い可
燃物からなる不純物を前記隙間から落下させることで、
両者をそれぞれ選別回収するとともに、前記回転ドラム
型一次磁選機からの不純物を回転篩型選別機に供給して
不燃物と可燃物とに篩分け回収するようにしたので、特
に可燃物又はプラスチック類中に残存する鉄類等の磁性
体を完全に除去することができる。このため、可燃物や
プラスチックを焼却処理或いは燃料化処理する際、該焼
却炉や成形機での不燃物の排出機構閉塞のトラブルなど
が激減し、安定した運転が可能となる。また、再資源と
なる磁性物の純度も極めて高いものとなる。
As described above, the present invention has the following advantages. A crushed material of the mixed bulky garbage is separated into a magnetic material and an impurity by a rotary drum type primary magnetic separator built in an end portion of a conveyor belt conveyor, and the magnetic material and an impurity partially mixed therein are combined with a wind power type vibration feeder. The light combustibles in the impurities supplied to the magnetic material and mixed into the magnetic material are floated and separated by air introduced into the combined use of the wind power type vibration feeder and collected by a collector, and are collected by suction.
A circuit provided with a predetermined gap at the end of the vibrating feeder
Magnetic material is magnetically attached to the rotating drum of a rotating drum type secondary magnetic separator.
And the relatively heavy combustible material has been removed.
By dropping impurities consisting of combustibles from the gap,
Both of them are separated and collected, and the impurities from the rotary drum type primary magnetic separator are supplied to a rotary sieve type sorter to be sieved and collected as incombustibles and combustibles. It is possible to completely remove magnetic substances such as irons remaining therein. Therefore, when combustibles and plastics are incinerated or converted to fuel, troubles such as the blockage of the incombustibles discharge mechanism in the incinerator or the molding machine are drastically reduced, and stable operation becomes possible. In addition, the purity of the magnetic substance that is to be recycled becomes extremely high.

【0013】また、混合系粗大ごみの破砕物を搬送用ベ
ルトコンベヤの終端部に内蔵された回転ドラム型一次磁
選機で磁性物と不純物とに選別し、前記磁性物と一部混
入する不純物を風力併用型振動フィーダに供給して該磁
性物に混入する不純物中の軽量可燃物を該風力併用型振
動フィーダへ導入される空気により浮上分離させて捕集
機により吸引回収し、磁性物と、前記軽量可燃物が取り
除かれた比較的重い可燃物からなる不純物とを、前記風
力併用型振動フィーダの終端部に排出シュートを介して
配設した回転ドラム型二次磁選機によりそれぞれ選別回
収するとともに、前記回転ドラム型一次磁選機からの不
純物を回転篩型選別機に供給して不燃物と可燃物とに篩
分け回収するようにしたので、可燃物および磁性物の純
度を大幅に上げることができるとともに二次磁選機を
容量化できる。
Further, the crushed material of the mixed bulky waste is separated into magnetic substances and impurities by a rotary drum type primary magnetic separator built in the end portion of the conveyor belt conveyor, and impurities mixed partially with the magnetic substances are removed. The lightweight combustible material in the impurities mixed into the magnetic material supplied to the wind-powered vibration feeder is floated and separated by air introduced into the wind-powered vibration feeder, suction-collected by a collector, and the magnetic material, The lightweight combustible material is removed and impurities composed of relatively heavy combustible material are separately collected and collected by a rotary drum type secondary magnetic separator arranged at a terminal end of the combined use wind type vibration feeder via a discharge chute. Since the impurities from the rotary drum type primary magnetic separator are supplied to a rotary sieve type separator to be sieved and collected as incombustibles and combustibles, the purity of combustibles and magnetics is greatly increased. Door can be small the capacity of the secondary magnetic separator is possible.

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

【図1】この発明の実施の形態に係る混合系粗大ごみ選
別処理装置を示す全体構成図。
FIG. 1 is an overall configuration diagram showing a mixed-system bulky waste sorting apparatus according to an embodiment of the present invention.

【図2】この発明の実施の形態に係る混合系粗大ごみ選
別処理装置の他の例を示す部分拡大断面図。
FIG. 2 is a partially enlarged cross-sectional view showing another example of the mixed bulky waste sorting apparatus according to the embodiment of the present invention.

【図3】従来例を示す全体構成図。FIG. 3 is an overall configuration diagram showing a conventional example.

【符号の説明】[Explanation of symbols]

6 搬送コンベヤ 8 回転篩型選別機 14 捕集機 16 吸引排風機 17 コンベヤ 18 回転ドラム型の一次磁選機 19 風力併用型振動フィーダ 20 多孔板 21 送風機 22 排気口 23 回転ドラム型の二次磁選機 Reference Signs List 6 Conveyor 8 Rotating sieve sorter 14 Collector 16 Suction exhauster 17 Conveyor 18 Rotary drum type primary magnetic separator 19 Combined wind power type vibratory feeder 20 Perforated plate 21 Blower 22 Exhaust port 23 Rotary drum type secondary magnetic separator

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI B07B 1/22 B07B 1/22 Z 4/08 4/08 Z B09B 5/00 ZAB B09B 5/00 ZABL (56)参考文献 特開 平6−23341(JP,A) 特開 平8−173908(JP,A) 特開 平5−7796(JP,A) (58)調査した分野(Int.Cl.7,DB名) B07B 1/00 - 15/00 ────────────────────────────────────────────────── ─── Continued on the front page (51) Int.Cl. 7 Identification symbol FI B07B 1/22 B07B 1/22 Z 4/08 4/08 Z B09B 5/00 ZAB B09B 5/00 ZABL (56) References Special JP-A-6-23341 (JP, A) JP-A-8-173908 (JP, A) JP-A-5-7796 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B07B 1 / 00-15/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 混合系粗大ごみの破砕物を搬送用ベルト
コンベヤの終端部に内蔵された回転ドラム型一次磁選機
で磁性物と不純物とに選別し、前記磁性物と一部混入す
る不純物を風力併用型振動フィーダに供給して該磁性物
混入する不純物中の軽量可燃物を該風力併用型振動フ
ィーダへ導入される空気により浮上分離させて捕集機に
より吸引回収し、前記風力併用型振動フィーダの終端部
に所定の隙間を設けて配設した回転ドラム型二次磁選機
の回転ドラムに磁性物を磁着させ、かつ、前記軽量可燃
物が取り除かれた比較的重い可燃物からなる不純物を前
記隙間から落下させることで、両者をそれぞれ選別回収
するとともに、前記回転ドラム型一次磁選機からの不純
物を回転篩型選別機に供給して不燃物と可燃物とに篩分
け回収するようにしたことを特徴とする混合系粗大ごみ
選別処理装置。
1. A crushed mixed bulk waste is separated into magnetic substances and impurities by a rotary drum type primary magnetic separator built in the end of a conveyor belt conveyor, and impurities mixed with the magnetic substances are partially mixed. The light combustibles in the impurities mixed into the magnetic material supplied to the wind-powered vibration feeder are floated and separated by air introduced into the wind- powered vibration feeder, collected by a collector, and collected by suction. End of vibration feeder
Drum type secondary magnetic separator with a predetermined gap
Magnetic material is magnetically attached to the rotating drum, and the lightweight flammable
To remove impurities consisting of relatively heavy combustibles
Both are sorted and collected by dropping from the gap
And an impurity from the rotary drum type primary magnetic separator is supplied to a rotary sieve type separator to be sieved and collected as incombustibles and combustibles.
【請求項2】 混合系粗大ごみの破砕物を搬送用ベルト
コンベヤの終端部に内蔵された回転ドラム型一次磁選機
で磁性物と不純物とに選別し、前記磁性物と一部混入す
る不純物を風力併用型振動フィーダに供給して該磁性物
混入する不純物中の軽量可燃物を該風力併用型振動フ
ィーダへ導入される空気により浮上分離させて捕集機に
より吸引回収し、磁性物と、前記軽量可燃物が取り除か
れた比較的重い可燃物からなる不純物とを、前記風力併
用型振動フィーダの終端部に排出シュートを介して配設
した回転ドラム型二次磁選機によりそれぞれ選別回収す
るとともに、前記回転ドラム型一次磁選機からの不純物
を回転篩型選別機に供給して不燃物と可燃物とに篩分け
回収するようにしたことを特徴とする混合系粗大ごみ選
別処理装置。
2. A crushed material of the mixed bulky waste is separated into a magnetic material and an impurity by a rotary drum type primary magnetic separator built in an end portion of a conveyor belt conveyor, and an impurity partially mixed with the magnetic material is removed. The lightweight combustible material in the impurities mixed into the magnetic material supplied to the wind-powered vibration feeder is floated and separated by air introduced into the wind-powered vibration feeder, suction-collected by a collector, and the magnetic material, The lightweight combustible material is removed and impurities composed of relatively heavy combustible material are separately collected and collected by a rotary drum type secondary magnetic separator arranged at a terminal end of the combined use wind type vibration feeder via a discharge chute. A mixing system for separating large-sized refuse, wherein impurities from the rotary drum-type primary magnetic separator are supplied to a rotary sifter-type separator and sieved and collected as incombustibles and combustibles.
JP28021096A 1996-09-30 1996-09-30 Mixed oversized garbage sorting equipment Expired - Fee Related JP3187724B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28021096A JP3187724B2 (en) 1996-09-30 1996-09-30 Mixed oversized garbage sorting equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28021096A JP3187724B2 (en) 1996-09-30 1996-09-30 Mixed oversized garbage sorting equipment

Publications (2)

Publication Number Publication Date
JPH1099783A JPH1099783A (en) 1998-04-21
JP3187724B2 true JP3187724B2 (en) 2001-07-11

Family

ID=17621856

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28021096A Expired - Fee Related JP3187724B2 (en) 1996-09-30 1996-09-30 Mixed oversized garbage sorting equipment

Country Status (1)

Country Link
JP (1) JP3187724B2 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3632123B2 (en) * 2000-08-18 2005-03-23 佐藤 絢子 Empty can crushed material separation device
DE10146512C1 (en) * 2001-09-21 2002-10-02 Maier Zerkleinerungstech Gmbh Separation and sorting system for waste material containing old wood includes sifting station and magnetic separator for tramp iron and has vertical material separation channel
JP2005058858A (en) * 2003-08-08 2005-03-10 Kubota Corp Wind power sorting apparatus
CN102233331A (en) * 2010-04-26 2011-11-09 舒城圣桂食品有限公司 Wild vegetable sorting and selecting device
CN104384108B (en) * 2014-05-12 2016-04-06 深圳市龙吉顺环保科技有限公司 Compact sorting consumer waste production line
CN105289839B (en) * 2015-11-06 2017-01-25 沈阳隆基电磁科技股份有限公司 Dry magnetic sorting machine for mine magnetic sorting
CN105233982B (en) * 2015-11-06 2017-01-18 沈阳隆基电磁科技股份有限公司 Staged combined sorting machine for mine magnetic separation
CN109092868B (en) * 2018-10-30 2024-03-26 江西省庭发再生能源有限公司 Domestic garbage environment-friendly renewable energy source treatment system and process
CN109701877A (en) * 2019-03-16 2019-05-03 江苏长三角环境科学技术研究院有限公司 A kind of full-automatic soil screening pretreatment unit system
JP7172936B2 (en) * 2019-09-27 2022-11-16 Jfeエンジニアリング株式会社 Garbage sorting method and device

Also Published As

Publication number Publication date
JPH1099783A (en) 1998-04-21

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