JP2001087744A - Waste treating device - Google Patents

Waste treating device

Info

Publication number
JP2001087744A
JP2001087744A JP26690899A JP26690899A JP2001087744A JP 2001087744 A JP2001087744 A JP 2001087744A JP 26690899 A JP26690899 A JP 26690899A JP 26690899 A JP26690899 A JP 26690899A JP 2001087744 A JP2001087744 A JP 2001087744A
Authority
JP
Japan
Prior art keywords
screw
extruder
crushing
barrel
extruded
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
JP26690899A
Other languages
Japanese (ja)
Other versions
JP3683752B2 (en
Inventor
Akiyoshi Kobayashi
昭美 小林
Masaya Shinozaki
賢哉 篠崎
Yoshiyuki Sakai
良幸 酒井
Katsuichi Tanaka
勝一 田中
Tomiaki Furuya
富明 古屋
Terunobu Hayata
輝信 早田
Yutaka Kawamura
豊 河村
Toshio Ichihashi
利夫 市橋
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.)
Toshiba Corp
Shibaura Machine Co Ltd
Original Assignee
Toshiba Corp
Toshiba Machine Co 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 Toshiba Corp, Toshiba Machine Co Ltd filed Critical Toshiba Corp
Priority to JP26690899A priority Critical patent/JP3683752B2/en
Publication of JP2001087744A publication Critical patent/JP2001087744A/en
Application granted granted Critical
Publication of JP3683752B2 publication Critical patent/JP3683752B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
    • 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
    • Y02W30/20Waste processing or separation
    • 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
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
    • 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
    • Y02W30/62Plastics recycling; Rubber recycling
    • 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
    • Y02W30/82Recycling of waste of electrical or electronic equipment [WEEE]

Landscapes

  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Screw Conveyors (AREA)
  • Processing Of Solid Wastes (AREA)
  • Crushing And Pulverization Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a waste treating device which is capable of simultaneously executing the crushing, volume reducing and fluorocarbon recovering of thermal insulating materials which are wastes, is high in safety and may be downsized and suppressed in an equipment cost by integrating plural functions. SOLUTION: The waste treating device 1 which is disposed with a crushing machine 7 for crushing the pulverized goods of the wastes in a material supply section 5 of an extruder 2 is provided with a controller 30 which controls the feed rate of an extrusion material in the extruder 2 to a constant rate by controlling a drive motor 31 of a screw 4 of the extruder 2 in accordance with the detection signal from a load cell 32 mounted at a revolving shaft 13 of the crushing machine 7 and regulating the rotating speed of the screw 4.

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、例えば冷蔵庫のよ
うな家電製品などの廃棄物を破砕して処理する廃棄物処
理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste treatment apparatus for crushing and treating waste such as household appliances such as refrigerators.

【0002】[0002]

【従来の技術】一般に、過去に生産された古い冷蔵庫、
冷凍庫などの家電製品には冷媒としてフロンが使用され
ている。さらに、冷蔵庫、冷凍庫などの庫内の断熱材と
して使用されているポリウレタンフォームなどの発泡材
中には例えば冷媒として使用されるフロンの4倍程度の
多量のフロンガスが混入されている。そのため、冷蔵庫
のような家電製品などの廃棄物を破砕して処理する場合
には断熱材の発泡材中に含まれているフロンガスが外部
側に流出し、大気中に放出される問題がある。
2. Description of the Related Art Generally, an old refrigerator manufactured in the past,
Freon is used as a refrigerant in home electric appliances such as freezers. Further, a foam material such as polyurethane foam used as a heat insulating material in a refrigerator or a freezer contains a large amount of Freon gas, for example, about four times as large as Freon used as a refrigerant. Therefore, when crushing and treating waste such as home electric appliances such as refrigerators, there is a problem that CFCs contained in the foamed material of the heat insulating material flow out to the outside and are released into the atmosphere.

【0003】そこで、例えば特開平5−147039号
公報には冷蔵庫のような家電製品などの廃棄物を処理す
る際に放出されるフロンガスを同時に回収するようにし
た処理装置が示されている。ここでは、冷蔵庫のような
家電製品などの廃棄物を常温下で破砕し、破砕片中の発
泡材を風力選別によって回収したのち、次に発泡材であ
るフロンの発泡セルを開放系でさらに微粉砕するように
なっている。このとき、微細に破砕された発泡セル中の
固体の樹脂部分からガス成分が分離されて放出され、こ
こで放出されるフロンガスが回収されるようになってい
る。さらに、フロンガスが分離された発泡材の粉体は別
置きの押出機で圧縮されて固められた減容状態で取出さ
れるようになっている。
[0003] For example, Japanese Patent Application Laid-Open No. Hei 5-147039 discloses a processing apparatus for simultaneously recovering Freon gas released when processing waste such as home electric appliances such as refrigerators. Here, waste such as household appliances such as refrigerators is crushed at room temperature, and the foamed material in the crushed pieces is collected by wind power separation. It is designed to be crushed. At this time, the gas component is separated and released from the solid resin portion in the finely crushed foam cell, and the Freon gas released here is collected. Further, the foamed material powder from which the chlorofluorocarbon gas has been separated is taken out in a compacted and compacted state by a separate extruder.

【0004】また、特開平5−147039号公報には
粉砕前に所定の温度まで加熱された発泡ポリウレタンを
スクリュコンベア装置で粉砕装置に送り、この粉砕装置
で粉砕するようにした装置が示されている。ここでは、
粉砕前に所定の温度まで加熱することにより、発泡ポリ
ウレタンの気泡内に含まれるフロンをガス状に変化させ
て気泡内の圧力を上昇させ、気泡が破壊し易い状態で、
粉砕することにより、気泡内のフロンガスを粉砕された
発泡ポリウレタンの粉体から分離する構成になってい
る。そして、この装置では分離されたフロンガスはフロ
ン回収装置で回収され、残りのポリウレタンの粉体はそ
のまま粉末貯留タンク内に溜められるようになってい
る。
Further, Japanese Patent Application Laid-Open No. 5-147039 discloses an apparatus in which foamed polyurethane heated to a predetermined temperature before pulverization is sent to a pulverizer by a screw conveyor device and pulverized by the pulverizer. I have. here,
By heating to a predetermined temperature before pulverization, the fluorocarbon contained in the foamed polyurethane foam is changed into a gaseous state and the pressure in the foam is increased, and in a state where the foam is easily broken,
By crushing, the chlorofluorocarbon gas in the bubbles is separated from the crushed foamed polyurethane powder. In this apparatus, the separated Freon gas is recovered by a Freon recovery apparatus, and the remaining polyurethane powder is stored in a powder storage tank as it is.

【0005】[0005]

【発明が解決しようとする課題】上記従来構成の廃棄物
処理装置のシステムではポリウレタンフォームの破砕片
を微粉砕して超微細に粉状にすることにより、フロンの
発泡セルを砕き、内部のフロンを開放系の中で取り出す
ようにしているので、粉砕装置の中では超微細なウレタ
ン粉が舞い、フロンガスが充満し、粉塵爆発のおそれが
ある。そのため、粉砕装置の中に不燃性の窒素ガスなど
を充填させたり、周辺装置を防爆構造にする必要がある
ので、廃棄物処理装置のシステム全体の設備費が高くな
る問題がある。
In the above-mentioned conventional waste treatment system, the crushed pieces of polyurethane foam are finely pulverized into ultrafine powder, thereby crushing the freon foam cells, thereby reducing the internal freon. Is taken out in an open system, so that ultra-fine urethane powder flutters in the pulverizer, which is filled with Freon gas, and there is a risk of dust explosion. For this reason, it is necessary to fill the crushing device with nonflammable nitrogen gas or the like or to make the peripheral device have an explosion-proof structure, which causes a problem that the equipment cost of the entire system of the waste treatment device is increased.

【0006】また、上記従来構成の廃棄物処理装置では
廃棄物の破砕装置、発泡材粉砕装置、フロンガス回収装
置および発泡材の粉体を取出すための押出機などのすべ
ての機能が分離されているため、廃棄物処理装置のシス
テム全体が大型化し、設備費が一層高くなる問題もあ
る。
Further, in the conventional waste treatment apparatus, all functions such as a waste crushing apparatus, a foam material crushing apparatus, a CFC gas recovery apparatus, and an extruder for removing foam material powder are separated. Therefore, there is also a problem that the entire system of the waste disposal apparatus becomes large, and the equipment cost is further increased.

【0007】本発明は上記事情に着目してなされたもの
で、その目的は、冷蔵庫のような家電製品などの廃棄物
の断熱剤(ポリウレタンフォーム)の破砕、減容化とフ
ロン回収を同時に行え、かつ安全性が高く、さらに複数
の機能を一体化して小型化し、設備費を抑制することが
できる廃棄物処理装置を提供することにある。
The present invention has been made in view of the above circumstances, and an object thereof is to simultaneously crush and reduce the volume of a heat insulating agent (polyurethane foam) of waste such as home appliances such as refrigerators and collect Freon. It is another object of the present invention to provide a waste treatment apparatus which is highly safe, has a plurality of functions integrated, can be reduced in size, and can reduce equipment costs.

【0008】[0008]

【課題を解決するための手段】請求項1の発明は、廃棄
物の粉砕品を破砕する破砕機が押出機の材料供給部に配
設された廃棄物処理装置であって、前記破砕機から前記
材料供給部に供給される破砕材料の供給圧力状態に応じ
て前記押出機のスクリュ回転速度を調整して前記押出機
における押出材料の送り量を一定に制御する制御手段を
設けたことを特徴とする廃棄物処理装置である。そし
て、本請求項1の発明では、押出機の材料供給部に破砕
機を配設して破砕機と押出機を一体化し、破砕機と押出
スクリュを接近させることにより、破砕機による破砕片
の送り力で押出スクリュ内に破砕片を充満させる。この
とき、破砕機から材料供給部には発泡材、鉄板などの金
属片、ABSなどのプラスチックシート、アルミ箔、モ
ータの電線などが混入された破砕材料が供給される。そ
して、この破砕材料の供給圧力状態に応じて押出機のス
クリュ回転速度を調整して押出機における押出材料の送
り量を一定に制御することにより、スクリュ内の押出材
料のカサ密度を上昇させ、押出材料の供給を安定化でき
るようにしたものである。
According to the first aspect of the present invention, there is provided a waste treatment apparatus in which a crusher for crushing crushed waste is provided in a material supply section of an extruder. Control means for adjusting the screw rotation speed of the extruder according to the supply pressure state of the crushed material supplied to the material supply unit and controlling the feed rate of the extruded material in the extruder to be constant is provided. Waste treatment equipment. According to the first aspect of the present invention, the crusher is arranged in the material supply section of the extruder, the crusher and the extruder are integrated, and the crusher and the extruding screw are brought close to each other, so that the crushed pieces by the crusher are removed. The extruded screw is filled with crushed pieces by the feeding force. At this time, the crushing machine supplies a crushing material into which a foam material, a metal piece such as an iron plate, a plastic sheet such as ABS, an aluminum foil, an electric wire of a motor, and the like are mixed. Then, by adjusting the screw rotation speed of the extruder according to the supply pressure state of the crushed material and controlling the feed amount of the extruded material in the extruder to be constant, the bulk density of the extruded material in the screw is increased, The supply of the extruded material can be stabilized.

【0009】請求項2の発明は、請求項1に記載の廃棄
物処理装置の前記破砕機を平行に配置された複数の回転
軸にそれぞれ取付けられた破砕具と、各回転軸の破砕具
をそれぞれ回転駆動する駆動手段とを具備する構成と
し、前記制御手段を前記回転軸に取付けた軸荷重検出用
のロードセルからの検出信号に基いて前記押出機のスク
リュ回転速度を調整する調整手段を備える構成としたも
のである。そして、本請求項2の発明では、破砕機の運
転中、破砕具の回転軸に取付けた軸荷重検出用のロード
セルからの検出信号に基いて調整手段によって押出機の
スクリュ回転速度を調整することにより、押出機におけ
る押出材料の送り量を一定に制御するようにしたもので
ある。
According to a second aspect of the present invention, there is provided a waste treatment apparatus according to the first aspect, wherein the crusher is attached to a plurality of rotating shafts arranged in parallel with each other and a crushing device for each rotating shaft. A drive means for driving each of the extruders, and an adjusting means for adjusting the screw rotation speed of the extruder based on a detection signal from a load cell for shaft load detection attached to the rotating shaft. It is configured. According to the second aspect of the present invention, during the operation of the crusher, the screw rotation speed of the extruder is adjusted by the adjusting means based on a detection signal from a load cell for detecting a shaft load attached to the rotating shaft of the crusher. Thus, the feed amount of the extruded material in the extruder is controlled to be constant.

【0010】請求項3の発明は、請求項1に記載の廃棄
物処理装置の前記押出機のバレル孔の内周面に前記スク
リュの回転軸方向に沿って延設されたバレル溝が形成さ
れる構成にしたものである。そして、本請求項3の発明
では、破砕機で破砕された破砕材料が押出機の材料供給
部に供給されると、押出機のバレルのバレル孔内で回転
する押出機のスクリュ回転にともないこの破砕材料がス
クリュとバレル孔の内周面との間の空間内を通り、下流
側に順次押出される。このとき、破砕材料の一部は押出
機のバレルのバレル孔の内周面のバレル溝に挿入され、
スクリュとバレル孔の内周面のバレル溝との間でこの破
砕材料が引き千切られることよって、材料の送り効率を
上げ、かつ安定化をもたらすようにしたものである。さ
らに、押出機内での圧縮作用と混練作用とにより破砕材
料中の発泡材の一部で、発泡セルを破壊し、発泡セル中
の固体の樹脂部分からガス成分が分離されて放出され
る。
According to a third aspect of the present invention, a barrel groove extending along the rotation axis direction of the screw is formed on an inner peripheral surface of a barrel hole of the extruder of the waste treatment apparatus according to the first aspect. The configuration is as follows. According to the third aspect of the present invention, when the crushed material crushed by the crusher is supplied to the material supply section of the extruder, the crushed material is rotated by the rotation of the screw of the extruder rotating in the barrel hole of the barrel of the extruder. The crushed material passes through the space between the screw and the inner peripheral surface of the barrel hole and is sequentially extruded downstream. At this time, part of the crushed material is inserted into the barrel groove on the inner peripheral surface of the barrel hole of the barrel of the extruder,
The crushed material is shredded between the screw and the barrel groove on the inner peripheral surface of the barrel hole, thereby increasing the material feeding efficiency and stabilizing the material. Further, the foaming cell is broken by a part of the foaming material in the crushed material by the compressing action and the kneading action in the extruder, and the gas component is separated and released from the solid resin portion in the foaming cell.

【0011】請求項4の発明は、請求項1に記載の廃棄
物処理装置の前記押出機をバレル内で回転駆動されるス
クリュの回転によって押出される押出材料の搬送路の途
中に配設された第1のベント口と、前記押出材料の搬送
路に沿って前記材料供給部に対して前記第1のベント口
とは反対側に配置された第2のベント口とを連結させて
前記押出機内に供給される押出材料中から放出されるガ
ス成分を回収するガス成分回収手段を備える構成にした
ものである。そして、本請求項4の発明では、押出機か
ら押出される押出材料は押出機のスクリュ回転にともな
い圧縮作用と混練作用とを受ける。これにより、押出材
料中の発泡材の発泡セルが破壊され、発泡セル中の固体
の樹脂部分からガス成分が分離されて放出され、残りの
押出材料は圧縮されて減容化された状態で下流側に押出
される。このとき、押出機のバレル内で回転駆動される
スクリュの回転によって押出される押出材料中から放出
されるガス成分を押出材料の搬送路の途中に配設された
第1のベント口と、材料供給部に対して第1のベント口
とは反対側に配置された第2のベント口とからそれぞれ
外部側に吸引し、これらの第1のベント口と第2のベン
ト口とからガス成分回収手段に回収するようにしたもの
である。
According to a fourth aspect of the present invention, the extruder of the waste disposal apparatus according to the first aspect is disposed in the middle of a conveying path of an extruded material extruded by rotation of a screw driven to rotate in a barrel. The first vent port is connected to a second vent port disposed on the opposite side to the first vent port with respect to the material supply unit along the conveying path of the extruded material, and the extrusion is performed. The apparatus is provided with a gas component collecting means for collecting gas components emitted from the extruded material supplied into the machine. According to the fourth aspect of the present invention, the extruded material extruded from the extruder undergoes a compression action and a kneading action as the screw of the extruder rotates. As a result, the foam cell of the foam material in the extruded material is destroyed, the gas component is separated and released from the solid resin portion in the foam cell, and the remaining extruded material is compressed and reduced in volume downstream. Extruded to the side. At this time, a gas component released from the extruded material extruded by the rotation of the screw rotationally driven in the barrel of the extruder is supplied to a first vent port provided in the middle of the extruded material conveying path; Suction to the outside from the second vent port disposed on the side opposite to the first vent port with respect to the supply unit, and gas component recovery from the first vent port and the second vent port It is intended to be collected by means.

【0012】請求項5の発明は、請求項4に記載の廃棄
物処理装置の前記ガス成分回収手段を前記押出機内に供
給される押出材料中から放出されるフロンガスを回収す
るフロンガス回収手段で構成したものである。そして、
本請求項5の発明では、押出機内の圧縮作用と混練作用
とにより発泡セルを破壊し、発泡セル中の固体の樹脂部
分から分離されて放出されるフロンガスを押出材料の搬
送路の途中に配設された第1のベント口と、材料供給部
に対して第1のベント口とは反対側に配置された第2の
ベント口とからそれぞれ外部側に吸引し、これらの第1
のベント口と第2のベント口とからガス成分回収手段に
回収するようにしたものである。
According to a fifth aspect of the present invention, the gas component collecting means of the waste treatment apparatus according to the fourth aspect is constituted by a CFC gas collecting means for collecting CFCs discharged from the extruded material supplied into the extruder. It was done. And
According to the fifth aspect of the present invention, the foaming cell is destroyed by the compression action and the kneading action in the extruder, and the CFC gas separated and released from the solid resin portion in the foaming cell is distributed in the middle of the extruded material conveying path. The first vent port provided and the second vent port disposed on the side opposite to the first vent port with respect to the material supply unit are respectively suctioned to the outside, and these first vent ports are sucked.
And the second vent port collects the gas component in the gas component collecting means.

【0013】請求項6の発明は、請求項4に記載の廃棄
物処理装置の前記押出機を前記第1のベント口と前記材
料供給部との間の部分に、前記スクリュにおけるねじ山
の向きが正回転方向の正スクリュ部が前記材料供給部
側、前記スクリュにおけるねじ山の向きが逆回転方向の
逆スクリュ部が前記第1のベント口側にそれぞれ配置さ
れ、かつ前記正スクリュ部と前記逆スクリュ部との間に
前記ねじ山がない平滑なリングによって形成される滞留
防止部が配設される構成にしたものである。そして、本
請求項6の発明では、材料供給部から押出機内に供給さ
れた押出材料が押出機のバレル内でスクリュの回転によ
り、圧縮作用と混練作用とを受ける。このとき、押出材
料は材料供給部側の正スクリュ部を通る際に徐々に高圧
状態に圧縮され、滞留防止部の平滑なリングの直前で最
大圧力状態になる。さらに、高圧状態に圧縮されている
押出材料は正スクリュ部から滞留防止部を経て第1のベ
ント口側の逆スクリュ部側に押出されると圧力が解放さ
れる。これにより、高圧状態に圧縮されている押出材料
中のガス成分が急激に膨張し、押出材料中の発泡材の発
泡セルを破って、発泡セル中の固体の樹脂部分から分離
されて放出される。このとき、正スクリュ部と逆スクリ
ュ部との間の滞留防止部のねじ山がない平滑なリングに
よって正スクリュ部と逆スクリュ部との間の境界部分に
押出材料中の金属材料などが滞留して押出材料の流れが
塞き止められることを防止するようにしたものである。
According to a sixth aspect of the present invention, the extruder of the waste disposal apparatus according to the fourth aspect is arranged such that a direction of a screw thread in the screw is provided at a portion between the first vent port and the material supply section. The positive screw part in the forward rotation direction is disposed on the material supply part side, the reverse screw part in the direction of the screw thread in the reverse rotation direction on the screw is disposed on the first vent port side, and the forward screw part and the A stagnation preventing portion formed by a smooth ring having no thread is provided between the reverse screw portion and the reverse screw portion. According to the sixth aspect of the present invention, the extruded material supplied from the material supply unit into the extruder undergoes a compression action and a kneading action by rotation of the screw in the barrel of the extruder. At this time, the extruded material is gradually compressed to a high pressure state when passing through the positive screw section on the material supply section side, and reaches the maximum pressure state immediately before the smooth ring of the stagnation prevention section. Furthermore, when the extruded material compressed to a high pressure state is extruded from the main screw portion to the reverse screw portion side of the first vent port side via the stagnation preventing portion, the pressure is released. As a result, the gas component in the extruded material that has been compressed to a high pressure state expands rapidly, breaks the foam cells of the foam material in the extruded material, and is separated and released from the solid resin portion in the foam cells. . At this time, the metal material etc. in the extruded material stays at the boundary between the forward screw section and the reverse screw section due to the smooth ring having no thread of the stagnation prevention section between the forward screw section and the reverse screw section. Thus, the flow of the extruded material is prevented from being blocked.

【0014】[0014]

【発明の実施の形態】以下、本発明の第1の実施の形態
を図1(A),(B)乃至図5を参照して説明する。図
1(A),(B)は本実施の形態の廃棄物処理装置1を
示すものである。本実施の形態の廃棄物処理装置1には
単軸押出機2が設けられている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a first embodiment of the present invention will be described with reference to FIGS. 1 (A), 1 (B) and 5. FIG. 1A and 1B show a waste treatment apparatus 1 according to the present embodiment. A single-screw extruder 2 is provided in the waste treatment apparatus 1 of the present embodiment.

【0015】また、図2は単軸押出機2の内部構成を示
すものである。なお、図2中で、参照符号3は本実施の
形態の単軸押出機2のバレル、4はこのバレル3のスク
リュ挿通孔3a内に配設された単軸のスクリュである。
ここで、バレル3の一端部側には材料供給部5、他端部
側には押出製品の吐出部6がそれぞれ配置されている。
そして、本実施の形態の単軸押出機2の材料供給部5に
は廃棄物の粉砕品を破砕する破砕機7、吐出部6にはペ
レタイザ8がそれぞれ配設されている。
FIG. 2 shows the internal structure of the single screw extruder 2. In FIG. 2, reference numeral 3 denotes a barrel of the single-screw extruder 2 according to the present embodiment, and reference numeral 4 denotes a single-screw screw provided in the screw insertion hole 3a of the barrel 3.
Here, a material supply section 5 is arranged on one end side of the barrel 3 and a discharge section 6 for extruded products is arranged on the other end side.
A crusher 7 for crushing the crushed waste is provided in the material supply section 5 of the single-screw extruder 2 of the present embodiment, and a pelletizer 8 is provided in the discharge section 6.

【0016】また、図3(A)は破砕機7の横断面図、
図3(B)は押出機2の材料供給部5と破砕機7との連
結部を示す要部の縦断面図、図4は図3(B)のIV−
IV線断面図である。この破砕機7には例えば冷蔵庫の
ような家電製品などの廃棄物を粉砕した粉砕品が投入さ
れるホッパ9と、このホッパ9の下側に配設された破砕
機構部10とが設けられている。ここで、破砕機構部1
0は押出機2の材料供給部5に一体的に取付けられてい
る。
FIG. 3A is a cross-sectional view of the crusher 7.
FIG. 3B is a longitudinal sectional view of a main part showing a connecting portion between the material supply unit 5 and the crusher 7 of the extruder 2, and FIG.
FIG. 4 is a sectional view taken along line IV. The crusher 7 is provided with a hopper 9 into which pulverized products obtained by pulverizing waste such as household appliances such as refrigerators, and a crushing mechanism 10 disposed below the hopper 9 are provided. I have. Here, the crushing mechanism 1
Numeral 0 is integrally attached to the material supply section 5 of the extruder 2.

【0017】また、破砕機構部10にはハウジング11
内に2本の回転軸12,13が平行に配置されている。
これらの回転軸12,13は軸受部材14を介してそれ
ぞれ回転自在に軸支されている。
The crushing mechanism 10 includes a housing 11.
Inside, two rotating shafts 12 and 13 are arranged in parallel.
These rotating shafts 12 and 13 are rotatably supported by bearings 14 respectively.

【0018】さらに、各回転軸12,13には図3
(A),(B)に示すように多数の破砕具15が各回転
軸12,13の軸方向に並設されている。各破砕具15
には図4に示すように円板状のベース部材15aの外周
面に複数、本実施の形態では8つの回転刃15bが等間
隔で並設されている。ここで、2本の回転軸12,13
の各破砕具15は互いの回転刃15bがそれぞれ噛み合
うように配置されている。
Further, each of the rotating shafts 12 and 13 has a structure shown in FIG.
As shown in (A) and (B), a large number of crushers 15 are arranged in the axial direction of each of the rotating shafts 12 and 13. Each crushing tool 15
As shown in FIG. 4, a plurality of, in this embodiment, eight rotary blades 15b are juxtaposed at equal intervals on the outer peripheral surface of a disk-shaped base member 15a. Here, the two rotating shafts 12 and 13
The crushing tools 15 are arranged such that the rotary blades 15b of the crushing tools 15 mesh with each other.

【0019】また、図1(A)に示すように単軸押出機
2の近傍には破砕機7の駆動モータ(駆動手段)16が
配設されている。この駆動モータ16の駆動力は例えば
ベルト機構などの動力伝達機構を介して破砕機7側に伝
達され、2本の回転軸12,13がそれぞれ逆方向、例
えば図4中に矢印で示すように、左側の回転軸12は時
計回り方向、右側の回転軸13は反時計回り方向にそれ
ぞれ回転駆動されるようになっている。そして、破砕機
7の駆動時にはホッパ9に例えば冷蔵庫のような家電製
品などの廃棄物を粉砕した粉砕品が投入され、各回転軸
12,13と一緒に回転する各破砕具15の回転にとも
ないこの廃棄物の粉砕品がさらに細かく破砕されて押出
機2の材料供給部5に強制的に詰め込まれるようになっ
ている。
As shown in FIG. 1A, a drive motor (drive means) 16 for the crusher 7 is disposed near the single screw extruder 2. The driving force of the driving motor 16 is transmitted to the crusher 7 via a power transmission mechanism such as a belt mechanism, and the two rotating shafts 12 and 13 are moved in opposite directions, for example, as shown by arrows in FIG. The left rotating shaft 12 is driven to rotate clockwise, and the right rotating shaft 13 is driven to rotate counterclockwise. When the crushing machine 7 is driven, crushed products obtained by crushing waste such as household appliances such as refrigerators are put into the hopper 9, and the crushing tools 15 that rotate together with the rotary shafts 12 and 13 rotate. The waste pulverized product is further finely crushed and compulsorily packed into the material supply section 5 of the extruder 2.

【0020】また、単軸押出機2のバレル3には材料供
給部5と押出製品の吐出部6との間でスクリュ4の回転
によって押出される押出材料の搬送路の途中に第1のベ
ント口17が配設されている。さらに、バレル3内の押
出材料の搬送路の上流側には材料供給部5に対して第1
のベント口17とは反対側に配置された第2のベント口
(リアベント口)18が配設されている。
In the barrel 3 of the single-screw extruder 2, a first vent is provided in the conveying path of the extruded material extruded by the rotation of the screw 4 between the material supply section 5 and the extruded product discharge section 6. A mouth 17 is provided. Further, the first side of the material supply unit 5 is provided on the upstream side of the conveying path of the extruded material in the barrel 3.
A second vent port (rear vent port) 18 disposed on the opposite side of the vent port 17 is provided.

【0021】これらの第1のベント口17と第2のベン
ト口18との間は吸引用連結管路19を介して連結され
ている。さらに、この連結管路19には吸引管路20の
一端が連結されている。この吸引管路20の他端は押出
機2内に供給される押出材料中から放出されるフロンガ
スなどのガス成分を回収するガス成分回収手段であるガ
ス回収装置(フロンガス回収手段)21に連結されてい
る。
The first vent port 17 and the second vent port 18 are connected to each other via a connection pipe 19 for suction. Further, one end of a suction pipe 20 is connected to the connection pipe 19. The other end of the suction pipe 20 is connected to a gas recovery device (Freon gas recovery means) 21 which is a gas component recovery means for recovering gas components such as CFCs discharged from the extruded material supplied into the extruder 2. ing.

【0022】また、本実施の形態の単軸押出機2のスク
リュ4には押出材料の搬送路の上流側および下流側にス
クリュ4におけるねじ山(スクリュフライト)4aの向
きが正回転方向の正スクリュ部22,23がそれぞれ配
置されている。ここで、材料供給部5側に配置される正
スクリュ部22の上流側のスクリュ溝4bは破砕機7で
細かく破砕された破砕品(押出材料)が搬送できる程度
に十分に大きくなるように設定されている。
In the screw 4 of the single-screw extruder 2 of this embodiment, the direction of the screw thread (screw flight) 4a of the screw 4 in the forward rotation direction is on the upstream side and the downstream side of the conveying path of the extruded material. Screw parts 22 and 23 are arranged, respectively. Here, the screw groove 4b on the upstream side of the main screw part 22 disposed on the material supply part 5 side is set to be large enough to carry the crushed product (extruded material) finely crushed by the crusher 7. Have been.

【0023】さらに、下流側の正スクリュ部23の直前
にはスクリュ4におけるねじ山(スクリュフライト)4
aの向きが逆回転方向の逆スクリュ部24が配置されて
いる。
Further, just before the downstream positive screw portion 23, a screw thread (screw flight) 4 of the screw 4 is formed.
A reverse screw portion 24 in which the direction a is in the reverse rotation direction is arranged.

【0024】ここで、上流側の正スクリュ部22および
逆スクリュ部24はバレル3における第1のベント口1
7と材料供給部5との間の部分と対応する部分にそれぞ
れ配置されている。さらに、これらの上流側の正スクリ
ュ部22と逆スクリュ部24との間にはねじ山(スクリ
ュフライト)がない平滑なリングによって形成される滞
留防止部25が配設されている。
Here, the upstream front screw portion 22 and the reverse screw portion 24 are connected to the first vent port 1 in the barrel 3.
7 and a portion corresponding to a portion between the material supply unit 5. Further, between the upstream front screw portion 22 and the reverse screw portion 24, a stagnation prevention portion 25 formed of a smooth ring having no screw thread (screw flight) is provided.

【0025】また、本実施の形態の単軸押出機2のバレ
ル3には材料供給部5の近傍部位に溝付きバレル26が
配設されている。この溝付きバレル26には図4に示す
ようにスクリュ4を収容するバレル孔26aの内周面に
複数のバレル溝27がスクリュ4の軸方向に沿って延設
されている。ここで、複数のバレル溝27はバレル孔2
6aの内周面に周方向に沿って並設されている。
The barrel 3 of the single-screw extruder 2 of this embodiment is provided with a grooved barrel 26 at a position near the material supply section 5. As shown in FIG. 4, a plurality of barrel grooves 27 extend in the grooved barrel 26 along the axial direction of the screw 4 on the inner peripheral surface of a barrel hole 26a for accommodating the screw 4. Here, the plurality of barrel grooves 27 are formed in the barrel hole 2.
6a are arranged side by side in the circumferential direction on the inner peripheral surface.

【0026】さらに、溝付きバレル26の外周面には水
冷ジャケット28が形成されている。そして、この水冷
ジャケット28に冷却水を流すことにより、常に冷却さ
れ、押出機2の材料供給部5での発熱を防止して材料供
給部5に供給される押出材料がこの材料供給部5の部分
で溶融することが防止されている。
Further, a water cooling jacket 28 is formed on the outer peripheral surface of the grooved barrel 26. Then, by flowing cooling water through the water cooling jacket 28, the extruded material that is constantly cooled and is supplied to the material supply unit 5 while preventing heat generation in the material supply unit 5 of the extruder 2 is supplied to the material supply unit 5. Melting is prevented at the part.

【0027】また、押出機2のバレル3における下流側
には温度調整用のバレルヒータ29などが装着されてい
る。そして、押出機2の運転中、押出機2内の温度を供
給材料の一部である熱硬化性のウレタンフォームを考慮
し、150℃〜250℃前後程度で一定に制御する温度
コントロールが行なわれるようになっている。
A barrel heater 29 for adjusting the temperature and the like are mounted on the downstream side of the barrel 3 of the extruder 2. During the operation of the extruder 2, temperature control is performed to control the temperature inside the extruder 2 to be constant at about 150 to 250 ° C. in consideration of the thermosetting urethane foam which is a part of the feed material. It has become.

【0028】また、本実施の形態の廃棄物処理装置1に
は破砕機7から材料供給部5に供給される破砕材料の供
給圧力状態に応じて押出機2のスクリュ4の回転速度を
調整して押出機2における押出材料の送り量を一定に制
御する図5に示すコントローラ(制御手段)30が設け
られている。このコントローラ30には押出機2のスク
リュ4の駆動モータ31が接続されている。
Further, in the waste treatment apparatus 1 of the present embodiment, the rotation speed of the screw 4 of the extruder 2 is adjusted according to the supply pressure state of the crushed material supplied from the crusher 7 to the material supply section 5. A controller (control means) 30 shown in FIG. 5 for controlling the feed amount of the extruded material in the extruder 2 to be constant is provided. The drive motor 31 of the screw 4 of the extruder 2 is connected to the controller 30.

【0029】さらに、破砕機7の一方の回転軸13には
軸荷重検出用のロードセル32が取付けられている。こ
のロードセル32はコントローラ30に接続されてい
る。そして、このロードセル32からの検出信号に基い
てコントローラ30によってスクリュ4の駆動モータ3
1を制御することにより、押出機2のスクリュ4の回転
速度を調整し、押出機2における押出材料の送り量を一
定に制御するようになっている。
Further, a load cell 32 for detecting a shaft load is attached to one rotating shaft 13 of the crusher 7. The load cell 32 is connected to the controller 30. The controller 30 controls the drive motor 3 of the screw 4 based on the detection signal from the load cell 32.
By controlling 1, the rotation speed of the screw 4 of the extruder 2 is adjusted, and the feed amount of the extruded material in the extruder 2 is controlled to be constant.

【0030】次に、上記構成の作用について説明する。
本実施の形態の廃棄物処理装置1の運転時には破砕機7
のホッパ9に例えば冷蔵庫のような家電製品などの廃棄
物を粉砕した粉砕品が投入される。ここで、投入される
廃棄物の粉砕品は予め風選される。この風選作業は廃棄
物の粉砕品に下から一定速度の風を送った際に、落下す
る重い粉砕品と、落下しない軽い粉砕品とに選別して回
収するものである。そして、本実施の形態の破砕機7の
ホッパ9にはここで風選された軽い粉砕品が投入され
る。
Next, the operation of the above configuration will be described.
During operation of the waste treatment apparatus 1 of the present embodiment, the crusher 7
A crushed product obtained by crushing waste such as household appliances such as a refrigerator is put into the hopper 9. Here, the pulverized product of the waste to be input is selected in advance by air. In this wind selection operation, when a constant-speed wind is sent from below to the waste pulverized product, a heavy pulverized product that falls and a light pulverized product that does not fall are sorted and collected. Then, the lightly pulverized product selected here is put into the hopper 9 of the crusher 7 of the present embodiment.

【0031】なお、風選された軽い粉砕品の中には熱硬
化性樹脂であるポリウレタンフォームなどの発泡材、熱
可塑性樹脂であるABSシート、PS片などのプラスチ
ックシートの他、鉄板などの金属片、アルミ箔、モータ
の電線、針金などが混入されている。ここで、ポリウレ
タンフォームの破砕片はカサ密度ρがρ=0.03程度
と小さい。そして、破砕機7のホッパ9に投入された廃
棄物の粉砕品はホッパ9の下の破砕機構部10に導かれ
る。
In addition, among the lightly pulverized products selected in the wind, foamed materials such as polyurethane foam which is a thermosetting resin, ABS sheets and PS sheets which are thermoplastic resins, and metal sheets such as iron plates are included. Pieces, aluminum foil, motor wires, wires, etc. are mixed. Here, the crushed pieces of the polyurethane foam have a small bulk density ρ of about 0.03. Then, the crushed product of the waste put into the hopper 9 of the crusher 7 is guided to the crushing mechanism 10 below the hopper 9.

【0032】また、破砕機7の駆動時には破砕機構部1
0の2本の回転軸12,13がそれぞれ逆方向、例えば
図4中に矢印で示すように、左側の回転軸12は時計回
り方向、右側の回転軸13は反時計回り方向にそれぞれ
回転駆動される。そして、各回転軸12,13と一緒に
回転する各破砕具15の回転にともない廃棄物の粉砕品
がさらに細かく破砕されて押出機2の材料供給部5に強
制的に詰め込まれる。なお、破砕機7による廃棄物の粉
砕品の破砕時に押出材料中の発泡材の一部の発泡セルが
破壊され、発泡セル中の固体の樹脂部分からガス成分で
あるフロンガスが分離されて放出される。このフロンガ
スは第2のベント口18側に吸引されて回収される。
When the crusher 7 is driven, the crushing mechanism 1
The two rotating shafts 12 and 13 are driven to rotate in opposite directions, for example, as shown by arrows in FIG. 4, the left rotating shaft 12 rotates clockwise and the right rotating shaft 13 rotates counterclockwise. Is done. Then, with the rotation of each crushing tool 15 that rotates together with each of the rotating shafts 12 and 13, the crushed waste product is further finely crushed and forcibly packed into the material supply unit 5 of the extruder 2. During the crushing of the crushed waste product by the crusher 7, a part of the foaming cells of the foaming material in the extruded material is destroyed, and the fluorocarbon gas, which is a gas component, is separated and released from the solid resin part in the foaming cells. You. This Freon gas is sucked and collected by the second vent port 18 side.

【0033】さらに、破砕機7から押出機2の材料供給
部5に送られた細い破砕品の押出材料はバレル3の内部
に供給される。ここで、バレル3の内部に供給された押
出材料はスクリュ4の回転にともないこのスクリュ4の
正スクリュ部22におけるねじ山(スクリュフライト)
4a間のスクリュ溝4bとバレル3のスクリュ挿通孔3
aの内周面との間で囲まれた空間内を通り、このスクリ
ュ4の正スクリュ部22から下流側の滞留防止部25、
逆スクリュ部24、正スクリュ部23側に順次移送され
る。
Further, the extruded material of the fine crushed product sent from the crusher 7 to the material supply section 5 of the extruder 2 is supplied into the barrel 3. Here, the extruded material supplied to the inside of the barrel 3 is screwed (screw flight) in the positive screw portion 22 of the screw 4 as the screw 4 rotates.
Screw groove 4b between barrel 4a and screw insertion hole 3 of barrel 3
a through the space surrounded by the inner peripheral surface of the screw 4, the stagnation prevention portion 25 on the downstream side from the normal screw portion 22 of the screw 4,
It is sequentially transferred to the reverse screw part 24 and the forward screw part 23 side.

【0034】また、押出材料は材料供給部5の正スクリ
ュ部22から滞留防止部25に移送される過程で、徐々
に圧縮されるとともに、その間にバレル3の外部からの
加熱と、スクリュ4の回転による剪断作用に基く内部発
熱とによって加熱された状態で、混練される。このと
き、押出材料中の発泡材のウレタンフォームは熱硬化性
樹脂で溶融し難いため、そのまま圧縮される。このと
き、発泡材以外の残りの押出材料も圧縮された状態で下
流側に押出される。
The extruded material is gradually compressed in the process of being transferred from the main screw section 22 of the material supply section 5 to the stagnation preventing section 25, and during this time, the barrel 3 is heated from the outside and the screw 4 is heated. The mixture is kneaded in a state of being heated by internal heat generated by a shearing action due to rotation. At this time, the urethane foam of the foamed material in the extruded material is compressed as it is because it is difficult to melt with the thermosetting resin. At this time, the remaining extruded material other than the foamed material is also extruded downstream in a compressed state.

【0035】さらに、スクリュ4の正スクリュ部22を
通る押出材料の一部は押出機2の溝付きバレル26のバ
レル孔26aの内周面のバレル溝27に挿入され、スク
リュ4とバレル孔26aの内周面のバレル溝27との間
でこの押出材料が引き千切られる。これにより、押出材
料の送り効率を上げ、かつ押出材料の送り動作の安定化
が図れる。なお、このとき、押出材料中の発泡材の一部
で発泡セルの破壊が促進され、フロンガスが若干分離さ
れて放出される。
Further, a part of the extruded material passing through the front screw portion 22 of the screw 4 is inserted into the barrel groove 27 on the inner peripheral surface of the barrel hole 26a of the grooved barrel 26 of the extruder 2, and the screw 4 and the barrel hole 26a are formed. The extruded material is cut between the inner peripheral surface and the barrel groove 27. Thereby, the feeding efficiency of the extruded material can be increased, and the feeding operation of the extruded material can be stabilized. At this time, the destruction of the foam cells is promoted by a part of the foam material in the extruded material, and the CFC gas is slightly separated and released.

【0036】また、スクリュ4の上流側の正スクリュ部
22から下流側に押出された押出材料は滞留防止部25
を経て逆スクリュ部24側に送り込まれる。このとき、
スクリュ4の正スクリュ部22を通る押出材料は徐々に
高圧状態に圧縮され、滞留防止部25の平滑なリングの
直前で最大圧力状態になる。ここでは、圧縮された押出
材料中の発泡材のウレタンフォームの発泡セル内のフロ
ンガスも圧縮される。
The extruded material extruded downstream from the front screw portion 22 on the upstream side of the screw 4 is retained by the stagnation preventing portion 25.
And is sent to the reverse screw portion 24 side. At this time,
The extruded material passing through the positive screw portion 22 of the screw 4 is gradually compressed to a high pressure state, and reaches a maximum pressure state immediately before the smooth ring of the stagnation prevention section 25. Here, the CFCs in the foamed cells of the urethane foam of the foamed material in the compressed extruded material are also compressed.

【0037】なお、熱硬化性樹脂であるウレタンフォー
ムは、圧縮されたものと、圧縮されずに材料供給部5に
投入されたままの状態で送られるものとが混在し、ボソ
ボソの状態になっている。そして、これらウレタンフォ
ームや、熱可塑性樹脂等が混練された状態で、下流側に
押出される。
As for the urethane foam which is a thermosetting resin, a compressed one and a urethane foam which is sent in a state of being supplied to the material supply unit 5 without being compressed are mixed, resulting in a state of warping. ing. Then, the urethane foam, the thermoplastic resin, and the like are extruded downstream in a kneaded state.

【0038】このとき、正スクリュ部22と逆スクリュ
部24との間の滞留防止部25のねじ山がない平滑なリ
ングによって樹脂シールが形成され、圧縮されずにボソ
ボソの状態の発泡材がそのまま圧縮されることなく逆ス
クリュ部24側に送り込まれることが防止される。
At this time, a resin seal is formed by a smooth ring having no thread of the stagnation preventing portion 25 between the forward screw portion 22 and the reverse screw portion 24, and the foamed material in a warped state is directly compressed without being compressed. It is prevented from being sent to the reverse screw portion 24 side without being compressed.

【0039】さらに、正スクリュ部22の下流部分で高
圧状態に圧縮されている押出材料は正スクリュ部22か
ら滞留防止部25を経て第1のベント口17側の逆スク
リュ部24側に押出されると圧力が解放される。これに
より、高圧状態に圧縮されている押出材料における発泡
材の発泡セル中に残留しているガス成分であるフロンガ
スが急激に膨張し、発泡材の発泡セルを破って飛び出
し、発泡セル中の固体の樹脂部分から分離されて放出さ
れる。このフロンガスは第1のベント口17側に吸引さ
れて回収される。
Further, the extruded material which has been compressed to a high pressure state in the downstream portion of the main screw portion 22 is extruded from the main screw portion 22 through the stagnation prevention portion 25 to the reverse screw portion 24 side of the first vent port 17 side. Pressure is released. As a result, the CFC, which is a gas component remaining in the foam cells of the foam material in the extruded material that has been compressed to a high pressure, rapidly expands and breaks out of the foam cells of the foam material, jumps out, and solids in the foam cells. Is separated and released from the resin part. This Freon gas is sucked into the first vent port 17 and collected.

【0040】また、正スクリュ部22と逆スクリュ部2
4との間の滞留防止部25のねじ山がない平滑なリング
によって正スクリュ部24と逆スクリュ部25との間の
境界部分に押出材料中の金属材料などが滞留して押出材
料の流れが塞き止められることが防止される。
The forward screw portion 22 and the reverse screw portion 2
The metal material in the extruded material stays at the boundary between the forward screw portion 24 and the reverse screw portion 25 by the smooth ring having no thread of the stay preventing portion 25 between the extruded material and the flow of the extruded material. Blocking is prevented.

【0041】なお、第1のベント口17側に吸引されて
回収されるフロンガスは第2のベント口18側に吸引さ
れて回収されるフロンガスと一緒に吸引用連結管路1
9、吸引管路20を順次介してガス回収装置21に送ら
れて液化回収される。このように、第1のベント口17
側と、第2のベント口18側の真空系を合流することに
より、完全な密閉系で略100%フロンガスの回収がで
きる。
The Freon gas sucked and collected by the first vent port 17 is collected together with the Freon gas sucked and collected by the second vent port 18 together with the suction connecting pipe 1.
9. The liquid is sequentially sent to the gas recovery device 21 via the suction pipe 20 and liquefied and recovered. Thus, the first vent port 17
By joining the vacuum system on the side of the second vent port 18 with the vacuum system on the side of the second vent port 18, it is possible to collect approximately 100% of CFC gas in a completely closed system.

【0042】また、ガス回収装置21は真空ポンプでフ
ロンガスを吸引し、吸引管路20の途中に設置した図示
しない液化装置で、−20°以下程度にガスを冷却して
凝固回収する構成になっている。さらに、この凝縮回収
システムには、真空コールドトラップを使用し、冷媒に
は高濃度食塩水や、エチルアルコール等にドライアイス
を投入し、−20℃以下に保持し、フロンガスを凝縮さ
せ、液体として回収する方法が採用されている。
The gas recovery device 21 sucks Freon gas by a vacuum pump, and is a liquefaction device (not shown) installed in the middle of the suction line 20 to cool the gas to about -20 ° or less and collect and coagulate it. ing. Furthermore, a vacuum cold trap is used for this condensation and recovery system, and high-concentration saline solution or dry ice is put into ethyl alcohol or the like as a refrigerant, kept at -20 ° C or lower, and condenses Freon gas to form a liquid. The method of collecting is adopted.

【0043】また、逆スクリュ部24を通過した押出材
料は下流側の正スクリュ部23側に流入される。この正
スクリュ部23ではフロンガスが除去された発泡材の発
泡セル中の固体の樹脂部分が発泡材以外の残りの押出材
料とともに圧縮された状態で下流側に押出される。この
とき、押出材料中の熱可塑性樹脂は溶融され、他の押出
材料の成分とともに混練される。これにより、正スクリ
ュ部23で押出材料はさらに圧縮され、減容化された状
態で下流側に押出される。そして、吐出部6からペレタ
イザ8に供給され、押出製品としての火力発電所用の固
形燃料であるロッド状のRDFが製造される。ここで、
本実施の形態の廃棄物処理装置1によれば、破砕品のフ
ロン含有量を0.1%にまで低下できるとともに、破砕
品におけるポリウレタンフォームなどの発泡材を処理前
のカサ密度ρがρ=0.03程度であったものを、カサ
密度ρがρ=0.9程度に減容化することができる。
The extruded material having passed through the reverse screw portion 24 flows into the downstream front screw portion 23. In this positive screw portion 23, the solid resin portion in the foam cell of the foam material from which the chlorofluorocarbon gas has been removed is extruded downstream while being compressed together with the remaining extruded material other than the foam material. At this time, the thermoplastic resin in the extruded material is melted and kneaded with other components of the extruded material. As a result, the extruded material is further compressed in the main screw portion 23 and extruded downstream in a reduced volume state. Then, the rod-shaped RDF is supplied from the discharge unit 6 to the pelletizer 8 and is a solid fuel for a thermal power plant as an extruded product. here,
According to the waste treatment apparatus 1 of the present embodiment, the CFC content of the crushed product can be reduced to 0.1%, and the bulk density ρ of the crushed product before processing the foamed material such as polyurethane foam is ρ = From about 0.03, the bulk density ρ can be reduced to about 0.9.

【0044】また、本実施の形態では廃棄物処理装置1
の運転中、破砕機7の破砕具15の回転軸13に取付け
た軸荷重検出用のロードセル32からの検出信号がコン
トローラ30に入力されている。そして、このコントロ
ーラ30によってロードセル32からの検出信号に基い
て押出機2のスクリュ4の駆動モータ31が制御され、
押出機2のスクリュ4の回転速度が調整される。
In the present embodiment, the waste treatment apparatus 1
During the operation of, the detection signal from the load cell 32 for detecting the axial load attached to the rotating shaft 13 of the crusher 15 of the crusher 7 is input to the controller 30. The drive motor 31 of the screw 4 of the extruder 2 is controlled by the controller 30 based on the detection signal from the load cell 32,
The rotation speed of the screw 4 of the extruder 2 is adjusted.

【0045】そこで、上記構成のものにあっては次の効
果を奏する。すなわち、本実施の形態の廃棄物処理装置
1では押出機2の材料供給部5に破砕機7を配設して破
砕機7と押出機2を一体化したので、これらの破砕機7
と押出機2の押出スクリュ4を接近させて配置すること
ができる。そのため、破砕機7による破砕片の送り力で
押出機2の押出スクリュ4内に熱硬化性樹脂であるポリ
ウレタンフォームなどの発泡材、熱可塑性樹脂であるA
BSシート、PS片などのプラスチックシートの他、鉄
板などの金属片、アルミ箔、モータの電線、針金などが
混入されている破砕片を充満させることができるので、
スクリュ4内のカサ密度を上昇させ、押出材料の供給を
安定化できる。
Therefore, the above configuration has the following effects. That is, in the waste treatment apparatus 1 of the present embodiment, the crusher 7 is disposed in the material supply section 5 of the extruder 2 and the crusher 7 and the extruder 2 are integrated.
And the extrusion screw 4 of the extruder 2 can be arranged close to each other. Therefore, a foaming material such as polyurethane foam which is a thermosetting resin and A which is a thermoplastic resin are formed in the extrusion screw 4 of the extruder 2 by a feed force of the crushed pieces by the crushing machine 7.
In addition to plastic sheets such as BS sheets and PS pieces, metal pieces such as iron plates, aluminum foil, motor wires, wires and other crushed pieces mixed with wire can be filled,
The bulk density in the screw 4 can be increased, and the supply of the extruded material can be stabilized.

【0046】さらに、本実施の形態では廃棄物処理装置
1の運転中、破砕機7の破砕具15の回転軸13に取付
けた軸荷重検出用のロードセル32からの検出信号をコ
ントローラ30に入力させ、このコントローラ30によ
ってロードセル32からの検出信号に基いて押出機2の
スクリュ4の駆動モータ31を制御して押出機2のスク
リュ4の回転速度を調整するようにしている。そのた
め、従来では押出機2の押出スクリュ4内に供給するこ
とが困難であった上記押出材料を本実施の形態の廃棄物
処理装置1の押出機2に安定に供給して熱硬化性樹脂で
あるポリウレタンフォームなどの発泡材からフロンガス
を回収する処理を安定に大量に行うことができるので、
従来のように粉砕装置の中に不燃性の窒素ガスなどを充
填させたり、周辺装置を防爆構造にする必要がなく、廃
棄物処理装置のシステム全体の設備費を低く抑制するこ
とができる。
Further, in this embodiment, during operation of the waste treatment apparatus 1, a detection signal from a load cell 32 for detecting a shaft load attached to the rotating shaft 13 of the crushing tool 15 of the crusher 7 is input to the controller 30. The controller 30 controls the drive motor 31 of the screw 4 of the extruder 2 based on the detection signal from the load cell 32 to adjust the rotation speed of the screw 4 of the extruder 2. For this reason, the above-mentioned extruded material, which was conventionally difficult to be supplied into the extruding screw 4 of the extruder 2, is stably supplied to the extruder 2 of the waste treatment apparatus 1 of the present embodiment, and a thermosetting resin is used. Since the process of recovering CFCs from foam materials such as polyurethane foam can be performed stably in large quantities,
It is not necessary to fill the non-combustible nitrogen gas or the like in the pulverizing apparatus as in the related art, and it is not necessary to make peripheral devices have an explosion-proof structure.

【0047】また、本実施の形態では単軸押出機2のバ
レル3における材料供給部5の近傍部位に溝付きバレル
26を配設したので、スクリュ4の正スクリュ部22を
通る押出材料の一部を押出機2の溝付きバレル26のバ
レル孔26aの内周面のバレル溝27に挿入させ、スク
リュ4とバレル孔26aの内周面のバレル溝27との間
でこの押出材料を引き千切ることができる。これによ
り、押出材料中の発泡材の一部で、発泡セルの破壊を促
進させ、発泡材中のフロンガスを若干分離させて放出さ
せることができるとともに、材料の送り効率を上げ、か
つ送りの安定化をもたらす。
In this embodiment, since the grooved barrel 26 is provided in the barrel 3 of the single-screw extruder 2 in the vicinity of the material supply section 5, one of the extruded materials passing through the front screw section 22 of the screw 4 can be used. The extruded material is inserted into the barrel groove 27 on the inner peripheral surface of the barrel hole 26a of the grooved barrel 26 of the extruder 2, and the extruded material is drawn between the screw 4 and the barrel groove 27 on the inner peripheral surface of the barrel hole 26a. Can be cut. As a result, a part of the foam material in the extruded material promotes the destruction of the foam cells, and the fluorocarbon gas in the foam material can be slightly separated and released, while increasing the material feeding efficiency and stabilizing the feeding. Bring about.

【0048】また、本実施の形態の単軸押出機2のスク
リュ4には押出材料の搬送路の上流側および下流側にス
クリュ4におけるねじ山(スクリュフライト)4aの向
きが正回転方向の正スクリュ部22,23をそれぞれ配
置し、下流側の正スクリュ部23の直前にはスクリュ4
におけるねじ山(スクリュフライト)4aの向きが逆回
転方向の逆スクリュ部24を配置するとともに、上流側
の正スクリュ部22と逆スクリュ部24との間にはねじ
山(スクリュフライト)がない平滑なリングによって形
成される滞留防止部25を配設している。そして、スク
リュ4の正スクリュ部22を通る押出材料を徐々に高圧
状態に圧縮させたのち、高圧状態に圧縮されている押出
材料が正スクリュ部22から滞留防止部25を経て第1
のベント口17側の逆スクリュ部24側に押出される際
に圧力が解放されることにより、高圧状態に圧縮されて
いる押出材料における発泡材の発泡セル中に残留してい
るガス成分であるフロンガスを急激に膨張させ、発泡材
の発泡セルを破って飛び出させることができる。そのた
め、この押出材料の圧力変化によって発泡材の発泡セル
中の固体の樹脂部分からフロンガスを確実に分離させて
放出させることができ、効果的にフロンガスを回収する
ことができる。
In the screw 4 of the single-screw extruder 2 of this embodiment, the direction of the screw thread (screw flight) 4a of the screw 4 in the forward rotation direction is on the upstream side and the downstream side of the extruded material conveying path. The screw parts 22 and 23 are respectively arranged, and the screw 4 is disposed immediately before the downstream positive screw part 23.
In this example, the reverse screw portion 24 having the reverse rotation direction of the screw thread (screw flight) 4a is arranged, and there is no screw thread (screw flight) between the upstream normal screw portion 22 and the reverse screw portion 24. A stagnation preventing portion 25 formed by a simple ring is provided. Then, after the extruded material passing through the positive screw portion 22 of the screw 4 is gradually compressed to a high pressure state, the extruded material that has been compressed to a high pressure state passes through the first screw portion 22 via the stagnation preventing portion 25 and the first material.
Is a gas component remaining in the foam cell of the foam material in the extruded material that has been compressed to a high pressure state by releasing the pressure when the material is extruded to the reverse screw portion 24 side of the vent port 17 side. The freon gas can be rapidly expanded to break the foamed cells of the foamed material and cause the foamed cells to fly out. Therefore, due to the change in pressure of the extruded material, the fluorocarbon gas can be reliably separated and released from the solid resin portion in the foam cell of the foam material, and the fluorocarbon gas can be effectively recovered.

【0049】さらに、正スクリュ部22と逆スクリュ部
24との間の滞留防止部25のねじ山がない平滑なリン
グによって正スクリュ部24と逆スクリュ部25との間
の境界部分に押出材料中の金属材料などが滞留して押出
材料の流れが塞き止められることを防止することができ
る。なお、正スクリュ部24と逆スクリュ部25との間
の境界部分に滞留防止部25の平滑なリングがない場合
には正スクリュ部24と逆スクリュ部25との間の境界
部分に押出材料中の金属材料などが滞留して堆積し、時
間経過と共に完全に押出材料の流れを塞き止めてしまう
ことになる。そのため、本実施の形態では正スクリュ部
24と逆スクリュ部25との間の境界部分に滞留防止部
25の平滑なリングによって押出材料の流れを円滑に保
持することができ、単軸押出機2を安定に運転させるこ
とができる。
Further, a boundary between the forward screw portion 24 and the reverse screw portion 25 is formed on the boundary between the forward screw portion 24 and the reverse screw portion 25 by a smooth ring having no thread of the stagnation preventing portion 25 between the forward screw portion 22 and the reverse screw portion 24. Of the extruded material can be prevented from being blocked by the stagnation of the metal material. If there is no smooth ring of the stagnation preventing portion 25 at the boundary between the forward screw portion 24 and the reverse screw portion 25, the boundary between the forward screw portion 24 and the reverse screw portion 25 has The metal material or the like stays and accumulates, and the flow of the extruded material is completely blocked with the passage of time. Therefore, in the present embodiment, the flow of the extruded material can be smoothly held by the smooth ring of the stagnation preventing portion 25 at the boundary between the forward screw portion 24 and the reverse screw portion 25, and the single-screw extruder 2 Can be operated stably.

【0050】また、本実施の形態では正スクリュ部22
と逆スクリュ部24との間の滞留防止部25のねじ山が
ない平滑なリングによって樹脂送りにブレーキがかか
り、樹脂シールが形成されるので、圧縮されずにボソボ
ソの状態の発泡材がそのまま圧縮されることなく逆スク
リュ部24側に送り込まれることが防止される。そのた
め、圧縮されずにボソボソの状態の発泡材がそのまま圧
縮されることなく第1のベント口17側に吸引され、フ
ロンガスの回収が妨害されることを防止することができ
る。
In this embodiment, the main screw portion 22
Since the resin feed is braked by a smooth ring having no thread of the stagnation preventing portion 25 between the screw portion 24 and the reverse screw portion 24 and a resin seal is formed, the foamed material in a loose state is compressed without being compressed. It is prevented from being fed to the reverse screw part 24 side without being performed. For this reason, it is possible to prevent the foam material in a loose state without being compressed from being sucked into the first vent port 17 side without being compressed as it is, thereby preventing the recovery of the CFC gas from being hindered.

【0051】さらに、本実施の形態では破砕機7と押出
機2を一体化した廃棄物処理装置1によって冷蔵庫のよ
うな家電製品などの廃棄物の断熱剤である発泡材(ポリ
ウレタンフォーム)の破砕、減容化とフロン回収を同時
に行えるので、複数の機能を一体化して廃棄物処理装置
1のシステム全体を小型化し、設備費を抑制することが
できる。
Further, in this embodiment, the crusher 7 and the extruder 2 are integrated into a waste treatment apparatus 1 to crush a foam material (polyurethane foam) which is a heat insulating agent for waste such as household appliances such as refrigerators. Since the volume reduction and the CFC recovery can be performed at the same time, a plurality of functions can be integrated to reduce the size of the entire system of the waste disposal apparatus 1 and reduce the equipment cost.

【0052】また、本実施の形態では押出機2は、温度
調節を行なっているため、押出機2内の温度を150℃
〜250℃前後の適正範囲の温度で制御することができ
る。そのため、上記適正範囲以上に上昇した場合のよう
にウレタンフォームの分解が進行し、塩化水素、シア
ン、アンモニアなどのガスの発生を防止することができ
るとともに、適正範囲以下の低温状態で保持される場合
のように充分なフロンガスの回収が困難となることを防
止することができる。
In the present embodiment, since the temperature of the extruder 2 is adjusted, the temperature inside the extruder 2 is set to 150 ° C.
It can be controlled at a temperature in an appropriate range of about 250 ° C. Therefore, the decomposition of the urethane foam proceeds as in the case where the temperature rises above the appropriate range, and the generation of gases such as hydrogen chloride, cyan, and ammonia can be prevented, and the temperature is kept at a low temperature within the appropriate range. It is possible to prevent a situation in which it is difficult to recover a sufficient amount of CFC gas as in the case.

【0053】また、図6は本発明の第2の実施の形態を
示すものである。本実施の形態は第1の実施の形態(図
1(A),(B)乃至図5参照)の廃棄物処理装置1の
構成を次の通り変更したものである。
FIG. 6 shows a second embodiment of the present invention. In the present embodiment, the configuration of the waste disposal apparatus 1 of the first embodiment (see FIGS. 1A, 1B and 5) is changed as follows.

【0054】すなわち、本実施の形態では押出機2の材
料供給部5における溝付きバレル26の内周面に圧力セ
ンサ41を設け、この圧力センサ41によって検出され
る検出信号に基いて第1の実施の形態と同様にコントロ
ーラ30によってスクリュ4の駆動モータ31を制御す
ることにより、押出機2のスクリュ4の回転速度を調整
し、押出機2における押出材料の送り量を一定に制御す
る構成にしたものである。
That is, in this embodiment, a pressure sensor 41 is provided on the inner peripheral surface of the grooved barrel 26 in the material supply section 5 of the extruder 2, and the first pressure sensor 41 is provided based on a detection signal detected by the pressure sensor 41. By controlling the drive motor 31 of the screw 4 by the controller 30 in the same manner as in the embodiment, the rotation speed of the screw 4 of the extruder 2 is adjusted, and the feed amount of the extruded material in the extruder 2 is controlled to be constant. It was done.

【0055】そこで、本実施の形態でも第1の実施の形
態と同様に破砕機7による破砕片の送り力で押出機2の
押出スクリュ4内に熱硬化性樹脂であるポリウレタンフ
ォームなどの発泡材、熱可塑性樹脂であるABSシー
ト、PS片などのプラスチックシートの他、鉄板などの
金属片、アルミ箔、モータの電線、針金などが混入され
ている破砕片を充満させることができるので、スクリュ
4内のカサ密度を上昇させ、押出材料の供給を安定化で
きる。
Therefore, in this embodiment, as in the first embodiment, a foaming material such as polyurethane foam, which is a thermosetting resin, is placed in the extrusion screw 4 of the extruder 2 by the feed force of the crushed pieces by the crusher 7. In addition to plastic sheets such as ABS sheets and PS pieces which are thermoplastic resins, metal pieces such as iron plates, aluminum foil, motor wires, wires and the like, can be filled with crushed pieces. The bulk density in the inside can be increased, and the supply of the extruded material can be stabilized.

【0056】なお、本発明は上記実施の形態に限定され
るものではない。例えば、フロン以外の他のガス気体を
内包するウレタンフォームなどの発泡材を含む廃棄物処
理も行える。さらに、その他、本発明の要旨を逸脱しな
い範囲で種々変形実施できることは勿論である。
The present invention is not limited to the above embodiment. For example, waste treatment including a foaming material such as urethane foam containing gaseous gases other than CFCs can be performed. Further, it goes without saying that various modifications can be made without departing from the spirit of the present invention.

【0057】[0057]

【発明の効果】請求項1の発明によれば、廃棄物の粉砕
品を破砕する破砕機が押出機の材料供給部に配設された
廃棄物処理装置における破砕機から材料供給部に供給さ
れる破砕材料の供給圧力状態に応じて押出機のスクリュ
回転速度を調整して押出機における押出材料の送り量を
一定に制御する制御手段を設けたので、冷蔵庫のような
家電製品などの廃棄物の断熱剤(ポリウレタンフォー
ム)の破砕、減容化とフロン回収を同時に行え、かつ安
全性が高く、さらに複数の機能を一体化して小型化し、
設備費を抑制することができる。
According to the first aspect of the present invention, a crusher for crushing a crushed waste product is supplied from the crusher of the waste treatment apparatus provided in the material supply section of the extruder to the material supply section. Control means for controlling the screw rotation speed of the extruder in accordance with the supply pressure of the crushed material to control the feed rate of the extruded material in the extruder to a constant value. Simultaneous crushing, volume reduction, and chlorofluorocarbon recovery of heat insulating agent (polyurethane foam), high safety, and miniaturization by integrating multiple functions.
Equipment costs can be reduced.

【0058】請求項2の発明によれば、破砕機の運転
中、破砕具の回転軸に取付けた軸荷重検出用のロードセ
ルからの検出信号に基いて調整手段によって押出機のス
クリュ回転速度を調整することにより、押出機における
押出材料の送り量を一定に制御することができる。
According to the invention of claim 2, during the operation of the crusher, the screw rotation speed of the extruder is adjusted by the adjusting means based on the detection signal from the load cell for detecting the shaft load attached to the rotary shaft of the crusher. By doing so, the feed amount of the extruded material in the extruder can be controlled to be constant.

【0059】請求項3の発明によれば、破砕機で破砕さ
れた破砕材料が押出機の材料供給部に供給された際に、
破砕材料の一部が押出機のバレルのバレル孔の内周面の
バレル溝に挿入され、スクリュとバレル孔の内周面のバ
レル溝との間でこの破砕材料が引き千切られることよっ
て、材料の送り効率を上げ、かつ安定化をもたらすこと
ができる。
According to the third aspect of the present invention, when the crushed material crushed by the crusher is supplied to the material supply section of the extruder,
A part of the crushed material is inserted into the barrel groove on the inner peripheral surface of the barrel hole of the extruder barrel, and the crushed material is cut apart between the screw and the barrel groove on the inner peripheral surface of the barrel hole, whereby the material is cut. Feed efficiency and stabilization can be achieved.

【0060】請求項4の発明によれば、押出機のバレル
内で回転駆動されるスクリュの回転によって押出される
押出材料中から放出されるガス成分を押出材料の搬送路
の途中に配設された第1のベント口と、材料供給部に対
して第1のベント口とは反対側に配置された第2のベン
ト口とからそれぞれ外部側に吸引し、これらの第1のベ
ント口と第2のベント口とからガス成分回収手段に回収
することができる。
According to the fourth aspect of the present invention, the gas component discharged from the extruded material extruded by the rotation of the screw rotationally driven in the barrel of the extruder is disposed in the middle of the extruded material conveying path. The first vent port and the second vent port disposed on the side opposite to the first vent port with respect to the material supply unit are respectively sucked to the outside, and these first vent port and the first vent port are sucked. 2 and can be collected by the gas component collection means.

【0061】請求項5の発明によれば、押出機内の圧縮
作用と混練作用とにより発泡セルを破壊し、発泡セル中
の固体の樹脂部分から分離されて放出されるフロンガス
を押出材料の搬送路の途中に配設された第1のベント口
と、材料供給部に対して第1のベント口とは反対側に配
置された第2のベント口とからそれぞれ外部側に吸引
し、これらの第1のベント口と第2のベント口とからガ
ス成分回収手段に回収することができる。
According to the fifth aspect of the present invention, the foaming cell is destroyed by the compressing action and the kneading action in the extruder, and the CFC gas separated and released from the solid resin portion in the foaming cell is transferred to the extruded material conveying path. A first vent port provided in the middle of the first supply port and a second vent port disposed on the opposite side to the first vent port with respect to the material supply section respectively suck out to the outside. The gas can be recovered by the gas component recovery means from the first vent port and the second vent port.

【0062】請求項6の発明によれば、材料供給部から
押出機内に供給された押出材料が押出機のバレル内でス
クリュの回転により、圧縮作用と混練作用とを受け、押
出材料が材料供給部側の正スクリュ部を通る際に徐々に
高圧状態に圧縮され、滞留防止部の平滑なリングの直前
で最大圧力状態になる。さらに、高圧状態に圧縮されて
いる押出材料は正スクリュ部から滞留防止部を経て第1
のベント口側の逆スクリュ部側に押出されると圧力が解
放される。これにより、高圧状態に圧縮されている押出
材料中のガス成分が急激に膨張し、押出材料中の発泡材
の発泡セルを破って、発泡セル中の固体の樹脂部分から
分離されて放出される。このとき、正スクリュ部と逆ス
クリュ部との間の滞留防止部のねじ山がない平滑なリン
グによって正スクリュ部と逆スクリュ部との間の境界部
分に押出材料中の金属材料などが滞留して押出材料の流
れが塞き止められることを防止することができる。
According to the sixth aspect of the present invention, the extruded material supplied from the material supply unit into the extruder is subjected to a compressing action and a kneading action by the rotation of the screw in the barrel of the extruder, and the extruded material is supplied to the extruder. The pressure is gradually compressed to a high pressure state when passing through the positive screw section on the side, and reaches the maximum pressure state immediately before the smooth ring of the stagnation prevention section. Further, the extruded material that has been compressed to a high pressure state passes through the first screw portion, passes through the stagnation prevention portion, and then enters the first material.
The pressure is released when it is pushed out to the reverse screw part side of the vent port side. As a result, the gas component in the extruded material that has been compressed to a high pressure state expands rapidly, breaks the foam cells of the foam material in the extruded material, and is separated and released from the solid resin portion in the foam cells. . At this time, the metal material etc. in the extruded material stays at the boundary between the forward screw section and the reverse screw section due to the smooth ring having no thread of the stagnation prevention section between the forward screw section and the reverse screw section. Thus, the flow of the extruded material can be prevented from being blocked.

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

【図1】本発明の第1の実施の形態を示すもので、
(A)は廃棄物処理装置全体の概略構成を示す平面図、
(B)は同側面図。
FIG. 1 shows a first embodiment of the present invention;
(A) is a plan view showing a schematic configuration of the entire waste treatment apparatus,
(B) is the same side view.

【図2】第1の実施の形態の廃棄物処理装置の内部の概
略構成を示す縦断面図。
FIG. 2 is a longitudinal sectional view showing a schematic configuration inside the waste disposal apparatus according to the first embodiment.

【図3】第1の実施の形態の廃棄物処理装置における破
砕機を示すもので、(A)は破砕機の横断面図、(B)
は押出機の材料供給部と破砕機との連結部を示す要部の
縦断面図。
FIG. 3 shows a crusher in the waste treatment apparatus according to the first embodiment, where (A) is a cross-sectional view of the crusher and (B).
Fig. 3 is a longitudinal sectional view of a main part showing a connection part between a material supply unit of the extruder and a crusher.

【図4】図3(B)のIV−IV線断面図。FIG. 4 is a sectional view taken along line IV-IV of FIG.

【図5】第1の実施の形態の押出機のスクリュ回転速度
を調整するコントローラの接続状態を示す概略構成図。
FIG. 5 is a schematic configuration diagram illustrating a connection state of a controller that adjusts a screw rotation speed of the extruder according to the first embodiment.

【図6】本発明の第2の実施の形態の廃棄物処理装置の
要部構成を示す縦断面図。
FIG. 6 is a vertical cross-sectional view illustrating a main configuration of a waste disposal apparatus according to a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

2 単軸押出機 3 バレル 4 スクリュ 5 材料供給部 7 破砕機 30 コントローラ(制御手段) 2 Single screw extruder 3 Barrel 4 Screw 5 Material supply section 7 Crusher 30 Controller (control means)

───────────────────────────────────────────────────── フロントページの続き (72)発明者 篠崎 賢哉 静岡県沼津市大岡2068の3 東芝機械株式 会社内 (72)発明者 酒井 良幸 静岡県沼津市大岡2068の3 東芝機械株式 会社内 (72)発明者 田中 勝一 静岡県沼津市大岡2068の3 東芝機械株式 会社内 (72)発明者 古屋 富明 神奈川県横浜市磯子区新杉田町8番地 株 式会社東芝横浜事業所内 (72)発明者 早田 輝信 神奈川県横浜市磯子区新杉田町8番地 株 式会社東芝横浜事業所内 (72)発明者 河村 豊 東京都港区芝浦一丁目1番1号 株式会社 東芝本社事務所内 (72)発明者 市橋 利夫 神奈川県横浜市鶴見区末広町2丁目4番地 株式会社東芝京浜事業所内 Fターム(参考) 3F040 AA02 BA01 CA01 CA02 CA03 DA00 EA01 4D004 AA22 BA06 CA03 CA04 CA50 CB13 CB16 CB28 CB50 DA01 DA02 DA04 4D065 CA12 CB02 CC01 CC08 DD08 EB14 EC07 ED13 ED35 ED50 4F301 AA29 BA21 BE18 BE29 BF02 BF08 BF11 BF16  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Kenya Shinozaki 2068-3 Ooka, Numazu-shi, Shizuoka Pref. Toshiba Machine Co., Ltd. (72) Inventor Yoshiyuki Sakai 2068-3 Ooka, Numazu-shi, Shizuoka Pref. Toshiba Machine Co., Ltd. (72) Inventor Katsuichi Tanaka 2068-3 Ooka, Numazu-shi, Shizuoka Pref. Toshiba Machine Co., Ltd. (72) Inventor Tomiaki Furuya 8 Shinsugita-cho, Isogo-ku, Yokohama-shi, Kanagawa Pref. Toshiba Yokohama Works Co., Ltd. 8, Shinsugita-cho, Isogo-ku, Yokohama-shi, Japan Inside the Toshiba Yokohama Office (72) Inventor Yutaka Kawamura 1-1-1, Shibaura, Minato-ku, Tokyo Inside the head office of Toshiba Corporation (72) Inventor Toshio Ichihashi Yokohama, Kanagawa 2-4 Suehirocho, Tsurumi-ku, Ichiba F-term in Toshiba Keihin Works (reference) 3F040 AA02 BA01 CA01 CA02 CA03 DA00 EA01 4D0 04 AA22 BA06 CA03 CA04 CA50 CB13 CB16 CB28 CB50 DA01 DA02 DA04 4D065 CA12 CB02 CC01 CC08 DD08 EB14 EC07 ED13 ED35 ED50 4F301 AA29 BA21 BE18 BE29 BF02 BF08 BF11 BF16

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 廃棄物の粉砕品を破砕する破砕機が押出
機の材料供給部に配設された廃棄物処理装置であって、 前記破砕機から前記材料供給部に供給される破砕材料の
供給圧力状態に応じて前記押出機のスクリュ回転速度を
調整して前記押出機における押出材料の送り量を一定に
制御する制御手段を設けたことを特徴とする廃棄物処理
装置。
A crusher for crushing a crushed waste product is a waste treatment device provided in a material supply section of an extruder, wherein a crusher for crushing material supplied to the material supply section from the crusher is provided. A waste treatment apparatus comprising a control means for controlling a screw rotation speed of the extruder in accordance with a supply pressure state to control a feed rate of an extruded material in the extruder to be constant.
【請求項2】 前記破砕機は、平行に配置された複数の
回転軸にそれぞれ取付けられた破砕具と、 各回転軸の破砕具をそれぞれ回転駆動する駆動手段とを
具備し、 前記制御手段は、前記回転軸に取付けた軸荷重検出用の
ロードセルからの検出信号に基いて前記押出機のスクリ
ュ回転速度を調整する調整手段を備えていることを特徴
とする請求項1に記載の廃棄物処理装置。
2. The crushing machine includes a crushing tool attached to each of a plurality of rotating shafts arranged in parallel, and a driving unit that drives each of the crushing tools on each rotating shaft to rotate. 2. The waste treatment according to claim 1, further comprising adjusting means for adjusting a screw rotation speed of the extruder based on a detection signal from a load cell for shaft load detection attached to the rotating shaft. apparatus.
【請求項3】 前記押出機は、回転駆動されるスクリュ
を収容するバレルのバレル孔の内周面に前記スクリュの
回転軸方向に沿って延設されたバレル溝が形成されてい
ることを特徴とする請求項1に記載の廃棄物処理装置。
3. The extruder is characterized in that a barrel groove extending along the rotation axis direction of the screw is formed on an inner peripheral surface of a barrel hole of a barrel accommodating a screw driven to rotate. The waste disposal device according to claim 1, wherein
【請求項4】 前記押出機は、バレル内で回転駆動され
るスクリュの回転によって押出される押出材料の搬送路
の途中に配設された第1のベント口と、前記押出材料の
搬送路に沿って前記材料供給部に対して前記第1のベン
ト口とは反対側に配置された第2のベント口とを連結さ
せて前記押出機内に供給される押出材料中から放出され
るガス成分を回収するガス成分回収手段を備えているこ
とを特徴とする請求項1に記載の廃棄物処理装置。
4. An extruder comprising: a first vent port provided in the middle of a conveying path of an extruded material extruded by rotation of a screw rotationally driven in a barrel; Along with the material supply unit, the first vent port is connected to a second vent port disposed on the opposite side to connect the gas component released from the extruded material supplied into the extruder. The waste treatment apparatus according to claim 1, further comprising a gas component collecting means for collecting.
【請求項5】 前記ガス成分回収手段は、前記押出機内
に供給される押出材料中から放出されるフロンガスを回
収するフロンガス回収手段であることを特徴とする請求
項4に記載の廃棄物処理装置。
5. The waste treatment apparatus according to claim 4, wherein the gas component collecting means is a Freon gas collecting means for collecting Freon gas discharged from the extruded material supplied into the extruder. .
【請求項6】 前記押出機は、前記第1のベント口と前
記材料供給部との間の部分に、前記スクリュにおけるね
じ山の向きが正回転方向の正スクリュ部が前記材料供給
部側、前記スクリュにおけるねじ山の向きが逆回転方向
の逆スクリュ部が前記第1のベント口側にそれぞれ配置
され、かつ前記正スクリュ部と前記逆スクリュ部との間
に前記ねじ山がない平滑なリングによって形成される滞
留防止部が配設されていることを特徴とする請求項4に
記載の廃棄物処理装置。
6. The extruder further comprises a positive screw part having a screw thread in a forward rotation direction at a part between the first vent port and the material supply part, the screw part having a forward rotation direction. A reverse screw portion in which the direction of the screw thread in the screw is in the reverse rotation direction is arranged on the first vent port side, respectively, and the smooth screw ring having no screw thread between the forward screw portion and the reverse screw portion. The waste treatment device according to claim 4, further comprising a stagnation prevention unit formed by:
JP26690899A 1999-09-21 1999-09-21 Waste treatment equipment Expired - Fee Related JP3683752B2 (en)

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Application Number Priority Date Filing Date Title
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Publication Number Publication Date
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JP3683752B2 JP3683752B2 (en) 2005-08-17

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ID=17437343

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