JPH07276364A - Separation device of surface coating of resin waste matter - Google Patents

Separation device of surface coating of resin waste matter

Info

Publication number
JPH07276364A
JPH07276364A JP7693094A JP7693094A JPH07276364A JP H07276364 A JPH07276364 A JP H07276364A JP 7693094 A JP7693094 A JP 7693094A JP 7693094 A JP7693094 A JP 7693094A JP H07276364 A JPH07276364 A JP H07276364A
Authority
JP
Japan
Prior art keywords
peeling
coating film
cylinder
pulverized body
resin
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.)
Pending
Application number
JP7693094A
Other languages
Japanese (ja)
Inventor
Tadaaki Kawai
忠彰 川合
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.)
YAKUSHIN KIKAI SEISAKUSHO KK
Original Assignee
YAKUSHIN KIKAI SEISAKUSHO KK
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 YAKUSHIN KIKAI SEISAKUSHO KK filed Critical YAKUSHIN KIKAI SEISAKUSHO KK
Priority to JP7693094A priority Critical patent/JPH07276364A/en
Publication of JPH07276364A publication Critical patent/JPH07276364A/en
Pending 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
    • 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

Abstract

PURPOSE:To contrive easy separation and removal of a coating, by a method wherein a peeling roll is arranged between a peeling cylinder and its inner wall surface, a coarse pulverized body is passed through between both of them and the coating of the coarse pulverized body is peeled and removed from the surface by a shock and agitating actions. CONSTITUTION:A coarse pulverized body enters a gap between a peeling cylinder 30 and peeling roll 40 through a receiving side 33 of a polygonal peeling cylinder 30, the gap between both of them is narrowed greatly by a rotation of a projected line 42 of the peeling roll 40 and since compression and scattering of the coarse pulverized body are repeated and shock and agitation actions are generated. Then frictional heat is generated by a method wherein the coarse pulverized bodies are either adjoin to each other or rub against the projected line and a coating is peeled off. Then a direction of the coarse pulverized body is changed by the scattering by the projected line 42, chances colliding with a front wall 43 of the projected line 42 become equal and the coating is peeled off. Then a temperature of an article is adjusted by preparation of a press plate 52 and the pulverized body whose coating is peeled off is discharged through a discharge side. Therefore, the higher the temperature of the article becomes, the better peeling efficiency becomes, separation efficiency of the coating is improved and separation and removal of the coating can be performed easily.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、ポリプロピレン製の廃
棄物を破砕して粒状の粗粉砕体とし、該粗粉砕体の表面
を擦って、該粗粉砕体の表面の樹脂製塗膜を剥離し、樹
脂材料を再生するようにした樹脂製廃棄物の表面塗膜分
離装置に関し、廃棄物としては、例えば、廃棄バンパー
があり、樹脂製の塗膜としては、例えば、アクリル系樹
脂製、または、ポリウレタン系樹脂製の塗膜がある。
BACKGROUND OF THE INVENTION The present invention relates to a crushed polypropylene waste material to form a granular coarsely pulverized body, rubbing the surface of the coarsely pulverized body, and peeling a resin coating film on the surface of the coarsely pulverized body. However, the present invention relates to a surface coating film separation device for a resin waste that is made to regenerate a resin material, and the waste includes, for example, a waste bumper, and the resin coating includes, for example, an acrylic resin, or , There is a coating film made of polyurethane resin.

【0002】[0002]

【従来の技術】近年、資源の有効利用の観点から、例え
ば、ポリプロピレン樹脂製の廃棄バンパーを回収して、
スペアタイヤバケットやウオータースクリーンなどのバ
ンパー以外の樹脂部品に再生することが行なわれてい
る。一般的にバンパーは衝撃特性などの高い機械的特性
を高品質の外観が要求され、バンパーに再利用するため
には、廃棄バンパーに塗布された塗膜を完全に除去する
必要がある。
2. Description of the Related Art In recent years, from the viewpoint of effective use of resources, for example, a waste bumper made of polypropylene resin is collected,
Recycled into resin parts other than bumpers such as spare tire buckets and water screens. Generally, bumpers are required to have high mechanical properties such as impact characteristics and high quality appearance, and in order to reuse them in the bumper, it is necessary to completely remove the coating film applied to the waste bumper.

【0003】樹脂製廃棄物の表面塗膜分離装置として
は、例えば、廃棄バンパーを破砕して粒状の粗粉砕体と
し、粗粉砕体を化学的処理して、表面塗膜を剥離した後
に、洗浄および乾燥するようにしたものが考えられる。
As an apparatus for separating a surface coating film of a resin waste, for example, a waste bumper is crushed into a granular coarsely pulverized body, the coarsely pulverized body is chemically treated, and the surface coating film is peeled off, followed by washing. And it is considered that it is dried.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、このよ
うな前の技術では、粗破砕体を再生材とするまでに多く
の工程を要し、再生材のコストアップの要因となり、ま
た、粗破砕体にするまでにも、廃棄バンパーの回収から
分別までに多くの工数を要するとともに、化学的処理す
るものにあっては処理剤の処分という新たな課題も生じ
るため、樹脂製廃棄物のリサイクルは経済的にそぐわな
いという問題点があった。
However, in such a prior art, many steps are required until a coarsely crushed body is made into a recycled material, which causes an increase in the cost of the recycled material. However, the recycling of resin waste is economical because it requires a lot of man-hours from the collection of waste bumpers to the separation of waste bumpers, and in the case of chemical treatment, there is a new issue of disposal of treatment agents. There was a problem that it did not fit the purpose.

【0005】本発明は、このような前の技術の問題点に
着目してなされたもので、多くの工数を要しないで、樹
脂製廃棄物の表面塗膜を除去することができ、コストを
低減することができ、また、広い設置スペースを要しな
い樹脂製廃棄物の表面塗膜分離装置を提供することを目
的としている。
The present invention has been made by paying attention to the problems of the above prior arts, and the surface coating film of the resin waste can be removed without requiring a lot of man-hours, and the cost can be reduced. It is an object of the present invention to provide a surface coating film separation device for resin waste that can be reduced and does not require a large installation space.

【0006】[0006]

【課題を解決するための手段】かかる目的を達成するた
めの本発明の要旨とするところは、 1 ポリプロピレン樹脂製の廃棄物を破砕して粒状の粗
粉砕体とし、該粗粉砕体の表面を擦って、該粗粉砕体の
表面に塗布された樹脂製の塗膜を剥離し、樹脂材料を再
生するようにした樹脂製廃棄物の表面塗膜分離装置であ
って、一端が粗粉砕体の受入側で他端が吐出側である剥
離筒(30)と、複数の緩傾斜した突条を外周に有して
おり、前記剥離筒(30)の内壁面(32)との間に粗
粉砕体処理用の間隙を形成するよう配設された剥離ロー
ル(40)とにより粗粉砕体の塗膜の剥離装置(10)
を構成し、前記剥離筒(30)の吐出側に吐出口(3
6)を臨んで設けられるとともに、該吐出口(36)を
塞ぐようにして配設された押え板(52)を有し、該押
え板(52)の押し付け力を加減して粗粉状体の流出量
を調整し、前記剥離筒(30)内の圧力を調整して、前
記剥離筒(30)内の圧力、前記剥離ロール(40)の
回転数および粗粉砕体の投入量に起因する前記剥離筒
(30)内の粗粉砕体の品温を80℃〜115℃に調整
可能な圧力調節部(50)を設けたことを特徴とする樹
脂製廃棄物の表面塗膜分離装置。
Means for Solving the Problems The gist of the present invention for attaining the above-mentioned object is to: 1 waste material made of polypropylene resin is crushed into granular coarsely pulverized bodies, and the surface of the coarsely pulverized bodies is An apparatus for separating a surface coating film of a resin waste, in which a resin coating film applied on the surface of the coarsely pulverized body is peeled off to regenerate a resin material, one end of which is a coarse pulverized body. Coarse crushing is performed between the peeling cylinder (30) having the receiving side and the other end being the discharging side, and a plurality of gently inclined projections on the outer circumference, and the inner wall surface (32) of the peeling cylinder (30). Peeling device (10) for a coating film of a coarsely pulverized body by a peeling roll (40) arranged so as to form a gap for body treatment
And a discharge port (3) on the discharge side of the peeling cylinder (30).
6) has a holding plate (52) provided so as to face the discharge port (36) and adjusts the pressing force of the holding plate (52) to give a coarse powder. And the pressure in the peeling cylinder (30) to adjust the pressure in the peeling cylinder (30), the number of revolutions of the peeling roll (40), and the amount of the coarsely pulverized body charged. An apparatus for separating a surface coating film of a resin waste, comprising a pressure adjusting section (50) capable of adjusting the temperature of the coarsely pulverized body in the peeling cylinder (30) to 80 ° C to 115 ° C.

【0007】2 ポリプロピレン樹脂製の廃棄バンパー
を破砕して粒状の粗粉砕体とし、該粗粉砕体の表面を擦
って、該粗粉砕体の表面に塗布された樹脂製の塗膜を剥
離し、バンパーの材料を再生するようにした樹脂製廃棄
物の表面塗膜分離装置であって、断面が非円形をしてお
り、一端が粗粉砕体の受入側で他端が吐出側である剥離
筒(30)と、複数の緩傾斜した突条を外周に有してお
り、前記剥離筒(30)の内壁面(32)との間に粗粉
砕体処理用の間隙を形成するよう配設された剥離ロール
(40)とにより粗粉砕体の塗膜の剥離装置(10)を
構成し、前記剥離筒(30)の吐出側に吐出口(36)
を臨んで設けられるとともに、該吐出口(36)を塞ぐ
ようにして配設された押え板(52)を有し、該押え板
(52)の押し付け力を加減して粗粉状体の流出量を調
整し、前記剥離筒(30)内の圧力を調整して、前記剥
離筒(30)内の圧力、前記剥離ロール(40)の回転
数および粗粉砕体の投入量に起因する前記剥離筒(3
0)内の粗粉砕体の品温を80℃〜115℃に調整可能
な圧力調節部(50)を設けたことを特徴とする樹脂製
廃棄物の表面塗膜分離装置。
2 A waste bumper made of polypropylene resin is crushed into a granular coarse pulverized body, the surface of the coarse pulverized body is rubbed, and the resin coating film applied to the surface of the coarse pulverized body is peeled off. A surface coating film separation device for resin waste, which is designed to recycle the material of a bumper, and has a non-circular cross section, with one end being the receiving side of the coarsely crushed body and the other end being the discharge side. (30) and a plurality of gently sloping ridges on the outer circumference, and are arranged so as to form a gap for coarsely crushed body treatment between the inner wall surface (32) of the peeling cylinder (30). The peeling roll (40) constitutes a peeling device (10) for the coating film of the coarsely pulverized body, and the discharge port (36) is provided on the discharge side of the peeling cylinder (30).
And a pressing plate (52) arranged so as to block the discharge port (36) and adjust the pressing force of the pressing plate (52) to flow out the coarse powder. The amount in the peeling cylinder (30) is adjusted, and the peeling is caused by the pressure in the peeling cylinder (30), the number of revolutions of the peeling roll (40), and the amount of the coarsely pulverized material charged. Tube (3
A surface coating film separating apparatus for resin waste, characterized in that a pressure adjusting section (50) capable of adjusting the temperature of the coarsely pulverized product in 0) to 80 ° C to 115 ° C is provided.

【0008】3 前記剥離装置(10)を複数の処理段
にして組み合わせ、各処理段に初期剥離から最終剥離ま
での各種段階を設定して割り当てたことを特徴とする1
または2項記載の樹脂製廃棄物の表面塗膜分離装置。
3. The peeling device (10) is combined into a plurality of processing stages, and various stages from initial peeling to final peeling are set and assigned to each processing stage.
Alternatively, the apparatus for separating surface coating film of resin waste according to the item 2.

【0009】4 前記各処理段における数個の剥離筒
(30)を、その各筒軸が水平方向に向き、かつ、各筒
軸が上下方向で並ぶように並設して一連の剥離装置(1
0)を構成したことを特徴とする3項記載の樹脂製廃棄
物の表面塗膜分離装置。
4 A series of peeling devices (30) are arranged side by side so that the peeling cylinders (30) in each processing stage are arranged so that their cylinder axes are oriented in the horizontal direction and the cylinder axes are aligned in the vertical direction. 1
0) is constituted, The surface coating film separation device of the resin waste as described in 3 above.

【0010】5 各処理段は、前段の吐出側を後段の受
入側にスクリューコンベア(65)を介して接続したこ
とを特徴とする3または4項記載の樹脂製廃棄物の表面
塗膜分離装置。
5. In each treatment stage, the discharge side of the former stage is connected to the receiving side of the latter stage via a screw conveyor (65), and the apparatus for separating surface coating film of resin waste according to the item 3 or 4 is characterized. .

【0011】6 前記剥離装置(10)の剥離筒(3
0)に剥離成分のみが通過可能な排出孔(32c)を多
数穿設し、剥離ロール(40)内に噴風流路(45a)
を設けるとともに、該噴風流路(45a)から剥離ロー
ル(40)の外周に連通する噴風口(46)を設けたこ
とを特徴とする1、2、3、4または5項記載の樹脂製
廃棄物の表面塗膜分離装置。
6 The peeling cylinder (3) of the peeling device (10)
No. 0) is provided with a large number of discharge holes (32c) through which only the peeling component can pass, and the blowing flow path (45a) is provided in the peeling roll (40).
And a blowout port (46) communicating from the blowout flow path (45a) to the outer periphery of the peeling roll (40). The resin waste according to any one of claims 1, 2, 3, 4 or 5. Surface coating film separation device.

【0012】7 各処理段は同一の駆動源を共用してい
ることを特徴とする3、4、5または6項記載の樹脂製
廃棄物の表面塗膜分離装置。
7. The apparatus for separating a surface coating film of resin waste according to item 3, 4, 5 or 6, wherein each processing stage shares the same drive source.

【0013】8 前記剥離筒(30)に、内壁面(3
2)から外に連通し、筒の周方向に細長であって、分離
された塗膜のみが通過可能な幅を有する排出孔(32
c)を周方向へ多数連設するとともに、筒軸方向と平行
方向に多数連設したことを特徴とする1、2、3、4、
5、6または7項記載の樹脂製廃棄物の表面塗膜分離装
置に存する。
8 An inner wall surface (3
A discharge hole (32) communicating with the outside from 2) and elongated in the circumferential direction of the cylinder and having a width through which only the separated coating film can pass.
c) are arranged in a large number in the circumferential direction and are also arranged in a direction parallel to the cylinder axis direction.
The present invention resides in the apparatus for separating a surface coating film of resin waste as described in 5, 6, or 7.

【0014】[0014]

【作用】先ず剥離装置(10)の一般的動作を説明す
る。粗粉砕体はポリプロピレン樹脂製の廃棄物を粒状に
破砕したものが用いられる。粗破砕体は、剥離筒(3
0)の受入側から剥離筒(30)と剥離ロール(40)
との間の間隙に連続的に入り、剥離ロール(40)の突
条(42)の回転にしたがって、突条(42)と剥離筒
(30)の内周面との空間は広くなったり狭くなったり
し、粗粉砕体は圧縮と拡散を繰り返して衝撃作用と攪拌
作用とを受ける。圧縮された状態で突条に衝突した粗粉
砕体には、衝突による衝撃圧と粗粉砕体相互間の圧力を
合わせた圧力が働き、突条の回転方向に粗粉砕体が移送
しようとする。このとき、粗粉砕体が相互に擦り合った
り、突条に擦れたりして、摩擦熱が生じ、主に摩擦熱に
よって粗粉砕体の塗膜が剥離される。
First, the general operation of the peeling device (10) will be described. As the coarsely crushed body, a waste product made of polypropylene resin is crushed into particles. The coarsely crushed body is
0) from the receiving side of the peeling cylinder (30) and peeling roll (40)
The space between the ridge (42) and the inner peripheral surface of the peeling cylinder (30) becomes wider or narrower as the ridge (42) of the peeling roll (40) rotates continuously. The coarsely pulverized body is repeatedly compressed and diffused and is subjected to an impact action and a stirring action. The coarse crushed body that collides with the ridges in a compressed state is subjected to a pressure that is a combination of the impact pressure due to the collision and the pressure between the coarse crushed bodies, and the coarse crushed body tries to be transferred in the rotation direction of the ridges. At this time, the coarsely pulverized bodies rub against each other or rub against the ridges to generate frictional heat, and the coating film of the coarsely pulverized body is mainly peeled off by the frictional heat.

【0015】また、圧縮された粗粉砕体群が再び拡散す
る際に、突条による拡散作用を受けて前後左右の粗粉砕
体が激しく入れ替わり、粗粉砕体の向きが変わり、どの
粗粉砕体も突条の正面壁と衝突する機会が均等になり、
粗粉砕体の塗膜が剥離される。剥離筒(30)内の粗粉
砕体の品温は、粗粉砕体の投入量、剥離ロール(4
0)、吐出口(36)を押える押え板(52)の押し付
け力などにより変化するが、主に、押え板(52)の押
し付け力を調整することにより、粗粉砕体の品温は80
℃〜115℃の中で調整される。塗膜が剥離された粗粉
砕体は剥離筒(30)の吐出側から吐出される。樹脂製
廃棄物の表面塗膜分離装置では、剥離は同一の段で完全
な剥離作業が行なってもよく、複数の段に分けて行なっ
てもよい。
Further, when the compressed coarse crushed body group diffuses again, the rough crushed bodies on the front, rear, right and left are violently exchanged by the diffusion action of the projections, the direction of the coarse crushed body changes, and any coarse crushed body is changed. Opportunity to collide with the front wall of the ridge is even,
The coating film of the coarsely pulverized body is peeled off. The product temperature of the coarsely pulverized body in the peeling cylinder (30) depends on the amount of the coarsely pulverized body charged, the peeling roll (4
0) and the pressing force of the pressing plate (52) that presses the discharge port (36), etc., but mainly by adjusting the pressing force of the pressing plate (52), the product temperature of the coarsely pulverized body is 80%.
It is adjusted in the range of ℃ to 115 ℃. The coarsely pulverized body with the coating film peeled off is discharged from the discharge side of the peeling cylinder (30). In the surface coating film separating apparatus for resin waste, the peeling may be carried out by the complete peeling work in the same stage, or in a plurality of stages.

【0016】前記剥離装置(10)を複数の処理段にし
て組み合わせ、各処理段に初期剥離から最終剥離までの
各種段階を設定して割り当てたものでは、第1段の剥離
装置(10)に粗粉砕体を投入して処理を進める。第1
段は初期の剥離に適した仕様になるよう、剥離筒(3
0),剥離ロール(40)の形態や間隙が設定され、ま
た、剥離ロール(40)の回転数も適切に設定されてお
り、剥離ロール(40)が粗粉砕体に当って塗膜が除か
れる。前記各処理段における数個の剥離筒(30)を、
その各筒軸が水平方向に向き、かつ、各筒軸が上下方向
で並ぶように並設して一連の剥離装置(10)を構成し
たものでは、粗粉砕体が上流側の剥離筒(30)から下
流側の剥離筒(30)へと円滑に流れ、剥離処理がし易
く、狭いスペースでも本装置を据付けることが可能にな
る。各処理段は、前段の吐出側を後段の受入側にスクリ
ューコンベア(65)を介して接続したものでは、ある
処理段を通過して粗破砕体はタンク等に貯留されること
なく、次段に受け入れられ、迅速に処理することができ
る。
In the case where the peeling device (10) is combined into a plurality of processing stages and various stages from the initial peeling to the final peeling are set and assigned to each processing stage, the first peeling device (10) is assigned. The coarsely pulverized material is put in to proceed with the treatment. First
Make sure that the step has a stripping cylinder (3
0), the form and gap of the peeling roll (40) are set, and the rotation speed of the peeling roll (40) is also set appropriately. The peeling roll (40) hits the coarsely pulverized body to remove the coating film. Get burned. Several peeling cylinders (30) in each of the processing stages are
In the one in which the cylinder shafts are oriented in the horizontal direction and the cylinder shafts are arranged side by side in the vertical direction to form a series of separation devices (10), the coarsely pulverized body has the upstream separation pipe (30). ) To the peeling cylinder (30) on the downstream side, the peeling process is easy, and the present apparatus can be installed even in a narrow space. In each processing stage, the discharge side of the former stage is connected to the receiving side of the latter stage via the screw conveyor (65), and the coarse crushed body is not stored in the tank or the like after passing through a certain treatment stage, Accepted and can be processed quickly.

【0017】前記剥離装置(10)の剥離筒(30)に
剥離成分のみが通過可能な排出孔(32c)を多数穿設
し、剥離ロール(40)内に噴風流路(45a)を設け
るとともに、該噴風流路(45a)から剥離ロール(4
0)の外周に連通する噴風口(46)を設けたもので
は、各段において、塗膜が粉状になった剥離成分は、剥
離ロール(40)内の噴風流路(45a)を通って噴風
口(46)から噴出された噴風により吹き飛ばされ、剥
離筒(30)の排出孔(32c)から外部に排出される
ようにすることもできる。また、噴風の風量を調整する
ことにより、剥離筒(30)内の粗粉砕体の品温を調節
することが可能になる。各処理段は同一の駆動源を共用
しているものでは、各処理段を同一の駆動源で駆動して
いるため、構造が簡単化し、全体を調和させて駆動する
ことができる。
The stripping cylinder (30) of the stripping device (10) is provided with a large number of discharge holes (32c) through which only stripping components can pass, and a jet flow path (45a) is provided in the stripping roll (40). , The peeling roll (4
In the one in which the blowout port (46) communicating with the outer periphery of (0) is provided, the release component whose coating film becomes powdery passes through the blowout flow channel (45a) in the release roll (40) in each stage. It is also possible that the air is blown off by the air blown from the air blow port (46) and is discharged to the outside from the discharge hole (32c) of the peeling cylinder (30). In addition, the product temperature of the coarsely pulverized body in the peeling cylinder (30) can be adjusted by adjusting the amount of jet air. In the case where each processing stage shares the same driving source, since each processing stage is driven by the same driving source, the structure is simplified and the entire driving can be performed in harmony.

【0018】[0018]

【実施例】以下、図面に基づき本発明の各種実施例を説
明する。図1〜図3は本発明の一実施例を示している。
図3に示すように、粗粉砕体供給部Aと、塗膜剥離装置
Dと、砕粒除去機Cとにより剥離ラインが構成されてい
る。前処理において、ポリプロピレン樹脂製の廃棄バン
パーは、ハンマーミル等で粒状に破砕され、その粒径が
1から6mmの粗粉砕体になっている。粗粉砕体の表面
には、廃棄バンパーの表面塗膜であるアクリル系樹脂ま
たはポリウレタン系樹脂の塗膜が付着している。粗粉砕
体供給部Aは、荷受けホッパA1に供給された粗粉砕体
が、粗選別機A2,計量器A3を経て粗粉砕体タンクA
4に溜められ、塗膜剥離装置Dに送り込まれるようにな
っている。粗粉砕体等を移送するための昇降機a1,a
2,a3…が各所に配設されている。粗粉砕体の処理装
置は塗膜剥離装置Dに設置されており、図1に示すよう
に同様の構成をした粗粉砕体の塗膜の剥離装置10a,
10b,10cを複数の処理段にして組み合わせ、各処
理段に初期剥離から最終剥離までの各種段階を設定して
割り当ててある。塗膜剥離装置Dで処理された粗粉砕体
は完全に塗膜が剥離されたものとなり、微細に砕けた砕
粒が砕粒除去機Cで除去され、剥離済タンクへ送られる
ようになっている。粗粉砕体の処理装置は、3段の剥離
装置10a,10b,10cを一連にしたものから構成
されているが、これらを二連以上のものにしてもよし、
剥離装置10a,10b,10cを4段以上に構成して
もよい。さらに、粗粉砕体を直接剥離装置10a,10
b,10cに供給するようにしてもよく、その際には、
前述した一連のシステム装置とする必要はない。剥離装
置10a,10b,10cは、処理段階に応じた仕様に
なっているがいずれも同様の構成をしており、共通の部
位に同一符号を付し重複した説明を省略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Various embodiments of the present invention will be described below with reference to the drawings. 1 to 3 show an embodiment of the present invention.
As shown in FIG. 3, the coarsely pulverized body supply unit A, the coating film peeling device D, and the crushed particle removing machine C constitute a peeling line. In the pretreatment, the waste bumper made of polypropylene resin is crushed into particles with a hammer mill or the like to form a coarse crushed body having a particle size of 1 to 6 mm. A coating film of acrylic resin or polyurethane resin, which is the surface coating film of the waste bumper, is attached to the surface of the coarsely pulverized body. In the coarse pulverized body supply unit A, the coarse pulverized body supplied to the load receiving hopper A1 is passed through the coarse sorter A2 and the weighing machine A3, and the coarse pulverized body tank A is supplied.
4 and is sent to the coating film peeling device D. Elevators a1 and a for transferring coarsely crushed bodies
2, a3 ... Are arranged at various places. The processing device for the coarsely crushed body is installed in the coating film peeling device D, and as shown in FIG.
10b and 10c are combined into a plurality of processing stages, and various stages from initial peeling to final peeling are set and assigned to each processing stage. The coarsely pulverized body treated by the coating film peeling device D has the coating film completely peeled off, and finely crushed crushed particles are removed by the crushed particle removing machine C and sent to the peeled tank. The apparatus for treating coarsely pulverized bodies is composed of a series of three-stage stripping devices 10a, 10b, 10c, but these may be two or more in series,
The peeling devices 10a, 10b, 10c may be configured in four or more stages. Further, the coarsely crushed body is directly removed from the peeling device 10a
b, 10c may be supplied, in which case
The series of system devices described above need not be used. The peeling devices 10a, 10b, and 10c have specifications according to the processing stages, but all have the same configuration, and common portions are denoted by the same reference numerals and duplicate description will be omitted.

【0019】図1および図2に示すように、粗粉砕体の
塗膜の剥離装置10a,10b,10cは、粗粉砕体供
給部20と、剥離筒30と、剥離筒30内で水平な枢軸
41まわりに回転駆動される剥離ロール40と、圧力調
節部50とを備えて成る。剥離筒30は剥離装置10の
ハウジング11に一体的に形成されている。
As shown in FIGS. 1 and 2, the apparatus 10a, 10b, 10c for removing the coating film of the coarsely pulverized body comprises a coarsely pulverized body supply section 20, a stripping cylinder 30, and a horizontal axis inside the stripping cylinder 30. The peeling roll 40 is driven to rotate around 41, and the pressure adjusting unit 50 is provided. The peeling cylinder 30 is formed integrally with the housing 11 of the peeling device 10.

【0020】粗粉砕体供給部20は粗粉砕体を受け入れ
て剥離筒30の内壁と剥離筒30の外周との間の間隙1
5に送出するものであり、受入口22に対応して送りロ
ール25を配設し、送りロール25を囲繞して送出室1
2をハウジング11に形成して成る。送りロール25は
粗粉砕体の流れの上流になるよう剥離ロール40と同心
に一体的に装着され、外周に送り螺旋26が設けられて
いる。送りロール25の枢軸41にはプーリ27が固設
され、プーリ27に巻き掛るベルト28から駆動力が入
力するようになっている。図2でわかるように、剥離筒
30は断面が半径一定でない非円形の多角形である8角
形断面をしており、内壁面32は面部32a,32a…
と角部32b,32b…とが交互になって外円周に連続
している。剥離筒30の一端は粗粉砕体の受入側33で
粗粉砕体供給部20に接続し、他端が吐出側34で圧力
調節部50に接続している。
The coarsely pulverized body supply unit 20 receives the coarsely pulverized body and a gap 1 between the inner wall of the peeling cylinder 30 and the outer periphery of the peeling cylinder 30.
5, the feed roll 25 is disposed in correspondence with the receiving port 22, and the feed roll 25 is surrounded so that the feed chamber 1
2 is formed in the housing 11. The feed roll 25 is integrally mounted concentrically with the peeling roll 40 so as to be upstream of the flow of the coarsely pulverized body, and a feed spiral 26 is provided on the outer circumference. A pulley 27 is fixedly mounted on a pivot shaft 41 of the feed roll 25, and a driving force is input from a belt 28 wound around the pulley 27. As can be seen in FIG. 2, the peeling cylinder 30 has an octagonal cross section that is a non-circular polygon whose cross section is not constant in radius, and the inner wall surface 32 has surface portions 32a, 32a ...
And the corner portions 32b, 32b ... Alternately and continuously on the outer circumference. One end of the peeling cylinder 30 is connected to the coarse pulverized body supply section 20 at the receiving side 33 of the coarse pulverized body, and the other end is connected to the pressure adjusting section 50 at the discharge side 34.

【0021】剥離筒30の内壁面32から外に連通して
剥離成分のみが通過可能な排出孔32c,32c…が多
数穿設されている。剥離ロール40は、その外径が5
7.5mmのものが用いられ、その先端部に同じく底面
の外径が62mmの切頭円錐形状の抵抗部材41が取り
付けられている。剥離ロール40は、軸方向に延びる複
数の鋸歯形の突条42,42…を外周に有する鋸歯車形
断面をしており、ハウジング11の前壁13と後壁14
との間に架設された枢軸41aにより枢支され、剥離筒
30の内壁面32との間に粗粉砕体処理用の間隙15を
形成するよう配設されている。抵抗部材の底面の外径と
剥離筒30の内壁面32との隙間は約9mmに設定され
ている。突条42の高さは4〜10mm程度、正面壁43
の角度βは30〜85度程度である。剥離ロール40の
突条42,42…の本数は、多いほど粗粉砕体との衝突
機会が増えるが、一方、圧縮時と拡散時との圧力差が小
さくなり攪拌力が低下するため、通常2〜6本程度が望
ましく、例えば4本としたとき粗粉砕体が投入されてか
ら排出されるまでに100〜200回の突条42との衝
突機会があった。
A large number of discharge holes 32c, 32c, ... Which communicate with the outside from the inner wall surface 32 of the peeling cylinder 30 and through which only peeling components can pass are provided. The peeling roll 40 has an outer diameter of 5
A 7.5 mm-thick resistance member 41 having a frustoconical shape with a bottom surface having an outer diameter of 62 mm is attached to the tip of the resistance member 41. The peeling roll 40 has a saw-tooth-shaped cross section having a plurality of saw-tooth-shaped protrusions 42, 42 ...
It is pivotally supported by a pivot 41a that is installed between and, and is disposed so as to form a gap 15 for treating the coarsely pulverized body with the inner wall surface 32 of the peeling cylinder 30. The gap between the outer diameter of the bottom surface of the resistance member and the inner wall surface 32 of the peeling cylinder 30 is set to about 9 mm. The height of the ridge 42 is about 4 to 10 mm, the front wall 43
Angle β is about 30 to 85 degrees. The larger the number of the ridges 42, 42 ... Of the peeling roll 40, the greater the chance of collision with the coarsely pulverized body, but on the other hand, the pressure difference between the time of compression and the time of diffusion decreases and the stirring force decreases. Approximately 6 pieces are desirable, and when the number is 4, for example, there were 100 to 200 opportunities to collide with the ridges 42 from the time when the coarsely pulverized body was introduced to the time when it was discharged.

【0022】これは、衝撃圧を利用しているために粗粉
砕体相互間の圧力が低くても剥離が可能であるからであ
る。
This is because the impact pressure is utilized, and therefore the peeling is possible even if the pressure between the coarsely pulverized bodies is low.

【0023】剥離ロール40は芯筒45に外嵌され、芯
筒45の中心孔は噴風流路45aをなしており、噴風流
路45aと、移動方向で正面壁43の後になる急傾斜し
た鋸歯形の突条42の裏面壁44との間に剥離成分排出
用の噴風口46が開設されている。圧力調節部50は、
剥離筒30の吐出側34に設けられた排出路35の末端
の吐出口36を臨んで設けられ、押し付けアーム51に
より支持され吐出口36を塞ぐようにして配設された押
え板52を有し、押し付けアーム51は付勢ばね53で
吐出口36に当接する方向に付勢されている。
The peeling roll 40 is externally fitted to the core cylinder 45, and the central hole of the core cylinder 45 forms a blast flow passage 45a. The blast flow passage 45a and the sawtooth which is steeply inclined behind the front wall 43 in the moving direction. A jet port 46 for discharging the peeling component is formed between the rear surface 44 and the rear wall 44 of the shaped ridge 42. The pressure adjusting unit 50
The pressing plate 52 is provided so as to face the discharge port 36 at the end of the discharge path 35 provided on the discharge side 34 of the peeling cylinder 30, and is supported by the pressing arm 51 and arranged so as to close the discharge port 36. The pressing arm 51 is urged by the urging spring 53 in the direction of coming into contact with the discharge port 36.

【0024】押し付けアーム51は付勢ばね53の後端
を押すねじ54による調節機構により押え板52の押圧
力を変え、あるいは吐出口36と押え板52との距離を
変えることができる。剥離筒30内の粗粉砕体の品温
は、押え板52の押圧力を上げると高くなり、粗粉砕体
の投入量が多ければ粗粉砕体の品温上昇を招き、剥離ロ
ール40の回転速度を上げると圧力が下がっての粗粉砕
体の品温が下がり、噴風口46を通る噴風量が多くなれ
ば粗粉砕体の品温が下がるが、その粗粉砕体の品温調整
は、主に押え板52の押圧力の調整により行われ、80
℃〜115℃に設定されている。図1でわかるように、
剥離装置10a,10b,10cは段階的な処理段をな
すよう上下に重畳して装置ボディ60に支持されてい
る。剥離装置10a,10b,10cの各剥離筒30を
囲繞してダクトボックス61a,61b,61cが装置
ボディ60に形成され、ダクトボックス61a,61
b,61cにそれぞれ集塵口62が設けられている。第
1段の剥離装置10aの受入口22はホッパ21に接続
し、ホッパ21の流路には流量を調節して粗粉砕体を流
下させる送り装置23が設けられている。
The pressing arm 51 can change the pressing force of the pressing plate 52 or the distance between the discharge port 36 and the pressing plate 52 by an adjusting mechanism using a screw 54 that presses the rear end of the biasing spring 53. The product temperature of the coarsely pulverized body in the peeling cylinder 30 increases as the pressing force of the pressing plate 52 is increased, and if the amount of the coarsely pulverized body added is large, the product temperature of the coarsely pulverized body rises, and the rotation speed of the peeling roll 40 is increased. When the pressure is raised, the product temperature of the coarsely pulverized body is lowered and the product temperature of the coarsely pulverized body is lowered as the amount of the air blown through the air blow port 46 is increased. It is performed by adjusting the pressing force of the holding plate 52.
It is set to ℃ -115 ℃. As you can see in Figure 1,
The peeling devices 10a, 10b, and 10c are vertically stacked and supported by the device body 60 so as to form a stepwise processing stage. Duct boxes 61a, 61b, 61c are formed in the device body 60 so as to surround the peeling cylinders 30 of the peeling devices 10a, 10b, 10c.
A dust collecting port 62 is provided on each of b and 61c. The receiving port 22 of the first-stage peeling apparatus 10a is connected to the hopper 21, and a flow path of the hopper 21 is provided with a feeding device 23 for adjusting the flow rate to flow down the coarsely pulverized body.

【0025】第3段の剥離装置10cの枢軸41に入力
用プーリ27aがプーリ27に並設され、駆動源により
回転駆動される駆動軸29の駆動プーリ29aとの間に
駆動ベルト29bが巻き掛けられている。剥離装置10
a,10bの間と剥離装置10b,10cの間には前段
の吐出口36から後段の受入口22に処理対象を搬送す
るスクリュ−コンベア65,65が配設されている。
An input pulley 27a is arranged in parallel with the pulley 27 on the pivot 41 of the third-stage peeling device 10c, and a drive belt 29b is wound around the drive pulley 29a of the drive shaft 29 which is rotationally driven by a drive source. Has been. Peeling device 10
Between the a and 10b and between the stripping devices 10b and 10c, screw conveyors 65 and 65 that convey the processing target from the discharge port 36 in the front stage to the inlet 22 in the rear stage are arranged.

【0026】剥離ロール40の枢軸41およびスクリュ
−コンベア65の回転軸65aは装置ボディ60の支持
ブロック66に枢支され、回転軸65aに固設されたプ
ーリ65bと枢軸41に固設されたプーリ41aとの間
に伝動ベルト67が巻き掛けられている。また、送り装
置23の駆動軸23aに固設されたプーリ23bと第1
段の剥離装置10aの枢軸41に固設されたプーリ41
bとの間には伝動ベルト67aが巻き掛けられている。
剥離装置10a,10b,10cの各剥離ロール40の
枢軸41の内部を通っている噴風流路45aは枢軸41
の端部に開口し、枢軸41の端部に接続して圧搾空気を
送る噴風供給管68が設けられ、噴風供給管68の分岐
管68a,68b,68cは回転カップラ69を介して
剥離装置10a,10b,10cの各剥離ロール40の
枢軸41の端部から噴風流路45aに接続している。
A pivot shaft 41 of the peeling roll 40 and a rotary shaft 65a of the screw conveyor 65 are pivotally supported by a support block 66 of the apparatus body 60, and a pulley 65b fixed to the rotary shaft 65a and a pulley fixed to the pivot shaft 41 are provided. The transmission belt 67 is wound around 41a. Also, the pulley 23b fixed to the drive shaft 23a of the feeding device 23 and the first
A pulley 41 fixedly mounted on a pivot 41 of the step peeling device 10a
A transmission belt 67a is wound around b.
The blast flow passage 45a passing through the inside of the pivot 41 of each peeling roll 40 of the peeling devices 10a, 10b, 10c is the pivot 41.
Is provided with a blast supply pipe 68 that is connected to the end of the pivot 41 and sends compressed air. The branch pipes 68a, 68b, 68c of the blast supply pipe 68 are separated via the rotary coupler 69. Each of the peeling rolls 40 of the devices 10a, 10b, and 10c is connected to the blast flow passage 45a from the end of the pivot 41.

【0027】次に作用を説明する。粗粉砕体供給部Aの
粗粉砕体タンクA4から昇降機a4により揚穀された粗
粉砕体はホッパ21に投入され、送り装置23により第
1段の剥離装置10aの受入口22に連続的に送入され
る。駆動軸29に固設された駆動プーリ29aから駆動
ベルト29bにより駆動力が第3段の剥離装置10cの
入力用プーリ27aに伝達される。入力用プーリ27a
により枢軸41が回転するとプーリ27が回転し、この
回転がベルト28を介して各段のプーリ27に伝達さ
れ、剥離装置10a,10b,10cがいずれも回転駆
動される。第1段および第2段の剥離装置10a,10
bの剥離ロール40の枢軸41にそれぞれプーリ41a
が固設されているので、プーリ41aから伝動ベルト6
7によりプーリ65bに回転力が伝達され、各スクリュ
−コンベア65が回転駆動される。第1段の剥離装置1
0aの枢軸41に固設されたプーリ41bから伝動ベル
ト67aを介してプーリ23bに回転駆動力が伝達さ
れ、駆動軸23aが回転して送り装置23が動作する。
第1段の剥離装置10aの粗粉砕体供給部20に受け入
れられた粗粉砕体は、送出室12内で送りロール25に
より剥離筒30,剥離ロール40側へ押し出され、剥離
筒30の受入側33から剥離筒30と剥離ロール40と
の間の間隙15に連続的に送り出される。
Next, the operation will be described. The coarsely pulverized body fried by the elevator a4 from the coarsely pulverized body tank A4 of the coarsely pulverized body supply section A is put into the hopper 21, and continuously fed by the feeder 23 to the inlet 22 of the first stage peeling apparatus 10a. Be entered. The driving force is transmitted from the driving pulley 29a fixed to the driving shaft 29 to the input pulley 27a of the third-stage peeling device 10c by the driving belt 29b. Input pulley 27a
As a result, when the pivot shaft 41 rotates, the pulley 27 rotates, and this rotation is transmitted to the pulleys 27 at each stage via the belt 28, and the peeling devices 10a, 10b, 10c are all driven to rotate. First-stage and second-stage peeling devices 10a, 10
The peeling roll 40 of FIG.
Is fixed, the transmission belt 6 is pulled from the pulley 41a.
Rotating force is transmitted to the pulley 65b by 7 and each screw conveyor 65 is rotationally driven. First stage peeling device 1
The rotational driving force is transmitted from the pulley 41b fixed to the shaft 41 of 0a to the pulley 23b through the transmission belt 67a, the driving shaft 23a rotates, and the feeding device 23 operates.
The coarsely pulverized body received in the coarsely pulverized body supply unit 20 of the first-stage peeling apparatus 10a is extruded in the delivery chamber 12 by the feed roll 25 toward the peeling cylinder 30 and the peeling roll 40, and the receiving side of the peeling cylinder 30. It is continuously fed from 33 to the gap 15 between the peeling cylinder 30 and the peeling roll 40.

【0028】粗粉砕体の流量は粗粉砕体供給部20にお
ける供給量と、剥離筒30の吐出側34に接続して設け
られた圧力調節部50とのバランスをとり、あるいは剥
離ロール40の回転数の設定を変えることにより剥離処
理に適したよう設定される。剥離処理においては、剥離
筒30内の粗粉砕体の品温は80℃〜115℃の中で調
整されている。剥離筒30内の粗粉砕体の品温は高くな
るにつれて、剥離効率が高まる傾向を示すが、120℃
以上になると、粗粉砕体同志が溶着し始める。また、8
0℃以下では、剥離効率が極めて良くない。送出室12
から押し出された粗粉砕体は剥離筒30と剥離ロール4
0との間の間隙15内に入り、衝撃作用と攪拌作用とを
受けながら通過する。
The flow rate of the coarsely pulverized body balances the supply amount in the coarsely pulverized body supply section 20 and the pressure adjusting section 50 connected to the discharge side 34 of the peeling cylinder 30, or the rotation of the peeling roll 40. It is set to be suitable for the peeling process by changing the setting of the number. In the peeling process, the product temperature of the coarsely pulverized body in the peeling cylinder 30 is adjusted to 80 ° C to 115 ° C. As the temperature of the coarsely pulverized body in the peeling cylinder 30 increases, the peeling efficiency tends to increase, but the temperature is 120 ° C.
When the above is reached, the coarsely crushed comrades start to weld. Also, 8
Below 0 ° C, the peeling efficiency is not very good. Delivery room 12
The coarsely crushed body extruded from the peeling cylinder 30 and peeling roll 4
It enters into the gap 15 between 0 and 0, and passes through it while being subjected to an impact action and a stirring action.

【0029】非円形の剥離筒30に対して剥離ロール4
0は鋸歯形の突条42の緩傾斜側である正面壁43を先
にして回転し、正面壁43と剥離ロール40の内周面と
の間の空間は剥離ロール40の回転にしたがって広くな
ったり狭くなったりし、粗粉砕体は圧縮と拡散を繰り返
してのように衝撃作用と攪拌作用とを受ける。
The peeling roll 4 is used for the non-circular peeling cylinder 30.
0 rotates first with respect to the front wall 43, which is the gently sloping side of the serrated protrusion 42, and the space between the front wall 43 and the inner peripheral surface of the peeling roll 40 becomes wider as the peeling roll 40 rotates. The coarsely pulverized body is subjected to an impact action and a stirring action as if it is repeatedly compressed and diffused.

【0030】衝撃作用と攪拌作用とを説明すると次のと
おりである。間隙15が最も狭くなった状態に移行する
に従い粗粉砕体の密度が高まって相互間の圧力が上昇す
る。圧縮された状態で突条42の正面壁43に衝突した
粗粉砕体には、衝突による衝撃圧と粗粉砕体相互間の圧
力を合わせた圧力が働き、粗粉砕体は衝撃作用を受け
る。このとき、粗粉砕体が相互に擦り合ったり、突条に
擦れたりして、摩擦熱が生じ、主に摩擦熱によって粗粉
砕体の塗膜が剥離される。剥離ロール40の突条42の
正面壁43と剥離筒30の内壁面32との間の間隙15
がもっとも広がった状態で、粗粉砕体である粗粉砕体相
互間の圧力は低く、突条42と衝突した粗粉砕体は自由
に跳ね返ることができるので、攪拌作用により前後左右
の粗粉砕体が激しく入れ替わり、粗粉砕体の向きが変わ
り、どの粗粉砕体も鋸歯形の突条42の正面壁43と衝
突する機会が均等になり、これによっても粗粉砕体の塗
膜が剥離される。衝撃圧を受けているので粗粉砕体相互
間の圧力は一般的な粒々摩擦式に比べて低くてもよく、
砕粒の発生を抑えることができる。
The impact action and the stirring action will be described below. As the gap 15 moves to the narrowest state, the density of the coarsely pulverized bodies increases and the pressure between them increases. The coarse crushed body that has collided with the front wall 43 of the ridge 42 in a compressed state is subjected to an impact pressure and the pressure between the coarse crushed bodies, and the coarse crushed body is impacted. At this time, the coarsely pulverized bodies rub against each other or rub against the ridges to generate frictional heat, and the coating film of the coarsely pulverized body is mainly peeled off by the frictional heat. The gap 15 between the front wall 43 of the ridge 42 of the peeling roll 40 and the inner wall surface 32 of the peeling cylinder 30
In the most spread state, the pressure between the coarse crushed bodies, which are coarse crushed bodies, is low, and the coarse crushed bodies that collide with the ridges 42 can freely bounce off, so that the front and rear, right and left coarse crushed bodies are stirred by the stirring action. The coarse crushing bodies are changed abruptly, the orientations of the coarse crushing bodies are changed, and the chances of any of the coarse crushing bodies colliding with the front wall 43 of the serrated ridges 42 are equalized, and the coating film of the coarse crushing bodies is also peeled off. Since it receives an impact pressure, the pressure between the coarsely crushed bodies may be lower than that of the general grain-friction system,
Generation of crushed particles can be suppressed.

【0031】塗膜が剥離された粗粉砕体は剥離筒30の
吐出側34から排出路35を通り、吐出口36で圧力調
節部50の押え板52により圧力の調節作用を受けなが
ら吐出され回収される。第1段で塗膜が剥離された粗粉
砕体は吐出口36からスクリュ−コンベア65の始端部
に吐出されて第2段の剥離装置10bの受入口22に送
られる。
The coarsely crushed body from which the coating film has been peeled off is discharged from the discharge side 34 of the peeling cylinder 30 through the discharge passage 35, and is discharged and collected at the discharge port 36 while being subjected to the pressure adjusting action by the holding plate 52 of the pressure adjusting section 50. To be done. The coarsely pulverized body from which the coating film has been peeled off in the first stage is discharged from the discharge port 36 to the starting end of the screw conveyor 65 and sent to the receiving port 22 of the peeling device 10b in the second stage.

【0032】第2段の剥離装置10bでも第1段の剥離
装置10aと同様に粗粉砕体はその塗膜が研削される。
各段の処理内容は適宜に設定されているが、例えば、第
1段で完全な塗膜の除去をさせない場合、第2段および
第3段で完全な塗膜の除去をする。
Even in the second-stage peeling device 10b, the coating film of the coarsely pulverized body is ground as in the first-stage peeling device 10a.
Although the processing contents of each stage are set appropriately, for example, when the first stage does not completely remove the coating film, the second stage and the third stage completely remove the coating film.

【0033】噴風供給管68には噴風用の圧搾空気が図
外の空気源から送られており、噴風供給管68a,68
b,68cから各処理段の枢軸41内の噴風流路45a
に噴風が送られる。剥離ロール40の突条42の裏面壁
44に噴風口46を開設したものでは、この噴風口46
から風を噴出して剥離成分を吹き出し、剥離成分は剥離
筒30の排出孔32cからダクトボックス61a,61
b,61cに排出される。粗粉砕体から削り取られる塗
膜は僅かづつであるので容易に吹き飛ばすことができ、
塗膜は集塵口62を通って排出され、回収して処理され
る。第3段の剥離装置10cから吐出された粗粉砕体は
塗膜は除去されているが、砕粒が混在しているので、砕
粒除去機Cで砕粒を除去してから図外の剥離済タンクへ
送られる。砕粒除去機Cの後に直ちに袋詰めしても良
い。
Compressed air for blast is sent to the blast supply pipe 68 from an air source (not shown), and the blast supply pipes 68a, 68 are provided.
b, 68c to the jet flow passage 45a in the shaft 41 of each processing stage
A blast is sent to. In the case where the blowout port 46 is opened on the back wall 44 of the ridge 42 of the peeling roll 40, this blowout port 46
From the exhaust holes 32c of the separating cylinder 30, the separating components are discharged from the duct boxes 61a, 61a.
b, 61c is discharged. Since the coating film scraped from the coarsely crushed body is only a few, it can be easily blown off,
The coating film is discharged through the dust collecting port 62, collected, and processed. The coating is removed from the coarsely pulverized body discharged from the third-stage peeling device 10c, but since crushed particles are mixed, the crushed particles are removed by the crushed particle removing machine C before being transferred to the peeled tank (not shown). Sent. The bag may be immediately packed after the crushing machine C.

【0034】なお、剥離筒30の断面形状は多角形が通
常であるが、外周が円形であっても、内壁面に抵抗体な
どを取付けて剥離ロール40との間で圧縮と拡散の作用
が生じるようにしてもよい。同様に、剥離ロール40の
突条42は剥離ロール40本体に一体に形成するのが普
通であるが、所定形状の板を装着して突条としてもよ
い。また、剥離筒30あるいは剥離ロール40の寸法
や、突条42の高さ,本数等を変え、また、運転速度等
を変えることにより対応することができる。
The cross-sectional shape of the peeling cylinder 30 is usually polygonal, but even if the outer circumference is circular, a resistor or the like is attached to the inner wall surface so that the compression roll and the diffusion roll 40 can work together. It may occur. Similarly, the ridge 42 of the peeling roll 40 is generally formed integrally with the main body of the peeling roll 40, but a plate having a predetermined shape may be attached to form the ridge. Further, it is possible to deal with the problem by changing the size of the peeling cylinder 30 or the peeling roll 40, the height and the number of the ridges 42, and the operating speed.

【0035】[0035]

【発明の効果】本発明に係る樹脂製廃棄物の表面塗膜分
離装置によれば、剥離筒と剥離ロールとの間に粗粉砕体
を通し、衝撃作用,攪拌作用により粗粉砕体の表面塗膜
を擦りとって剥離するようにしたから、塗膜の分離処理
が簡略になり、コストを低減することができ、またスペ
ースも取らない。
According to the apparatus for separating a surface coating film of a resin waste according to the present invention, a coarsely pulverized body is passed between a stripping cylinder and a stripping roll, and the surface coating of the coarsely pulverized body is carried out by an impact action and a stirring action. Since the film is rubbed and peeled off, the separation process of the coating film is simplified, the cost can be reduced, and no space is required.

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

【図1】本発明の一実施例を示す樹脂製廃棄物の表面塗
膜分離装置の縦断面図である。
FIG. 1 is a vertical cross-sectional view of a surface coating film separation device for resin waste showing an embodiment of the present invention.

【図2】図1のII−II線断面図である。FIG. 2 is a sectional view taken along line II-II of FIG.

【図3】本発明の一実施例を示す剥離処理ラインの概念
面である。
FIG. 3 is a conceptual view of a peeling processing line showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10…剥離装置 11…ハウジング 20…粗粉砕体供給部 25…送りロール 30…剥離筒 32…内壁面 32c…排出孔 33…受入側 34…吐出側 36…吐出口 40…剥離ロール 42…突条 43…正面壁 45a…噴風流路 46…噴風口 50…圧力調節部 52…押え板 60…装置ボディ 61a,61b,61c…ダクトボックス 62…集塵口 65…スクリュ−コンベア 68…噴風供給管 DESCRIPTION OF SYMBOLS 10 ... Peeling device 11 ... Housing 20 ... Coarse crushed body supply part 25 ... Feed roll 30 ... Peeling cylinder 32 ... Inner wall surface 32c ... Discharge hole 33 ... Receiving side 34 ... Discharging side 36 ... Discharging port 40 ... Peeling roll 42 ... 43 ... Front wall 45a ... Jet flow channel 46 ... Jet port 50 ... Pressure adjusting part 52 ... Holding plate 60 ... Device body 61a, 61b, 61c ... Duct box 62 ... Dust collection port 65 ... Screw conveyor 68 ... Jet supply pipe

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】ポリプロピレン樹脂製の廃棄物を破砕して
粒状の粗粉砕体とし、該粗粉砕体の表面を擦って、該粗
粉砕体の表面に塗布された樹脂製の塗膜を剥離し、樹脂
材料を再生するようにした樹脂製廃棄物の表面塗膜分離
装置であって、 一端が粗粉砕体の受入側で他端が吐出側である剥離筒
と、複数の緩傾斜した突条を外周に有しており、前記剥
離筒の内壁面との間に粗粉砕体処理用の間隙を形成する
よう配設された剥離ロールとにより粗粉砕体の塗膜の剥
離装置を構成し、 前記剥離筒の吐出側に吐出口を臨んで設けられるととも
に、該吐出口を塞ぐようにして配設された押え板を有
し、該押え板の押し付け力を加減して粗粉状体の流出量
を調整し、前記剥離筒内の圧力を調整して、前記剥離筒
内の圧力、前記剥離ロールの回転数および粗粉砕体の投
入量に起因する前記剥離筒内の粗粉砕体の品温を80℃
〜115℃に調整可能な圧力調節部を設けたことを特徴
とする樹脂製廃棄物の表面塗膜分離装置。
1. A waste product made of polypropylene resin is crushed into a granular coarsely pulverized body, the surface of the coarsely pulverized body is rubbed, and the resin coating film applied to the surface of the coarsely pulverized body is peeled off. A surface coating film separation device for resin waste, which is adapted to regenerate a resin material, comprising a peeling cylinder having one end on the receiving side of the coarsely crushed body and the other end on the discharging side, and a plurality of gently inclined projections. Having an outer periphery, and a peeling roll arranged so as to form a gap for the coarse pulverized body treatment between the inner wall surface of the peeling cylinder and a peeling device for the coating film of the coarse pulverized body, The peeling cylinder has a discharge port facing the discharge port, and has a holding plate arranged so as to close the discharge port, and the pressing force of the holding plate is adjusted to flow out the coarse powder. Adjusting the amount, adjusting the pressure in the peeling cylinder, the pressure in the peeling cylinder, the rotation speed of the peeling roll and The product temperature of the coarse grinding bodies within the release cylinder due to input of grinding bodies 80 ° C.
An apparatus for separating a surface coating film of a resin waste, which is provided with a pressure adjusting section which can be adjusted to ˜115 ° C.
【請求項2】ポリプロピレン樹脂製の廃棄バンパーを破
砕して粒状の粗粉砕体とし、該粗粉砕体の表面を擦っ
て、該粗粉砕体の表面に塗布された樹脂製の塗膜を剥離
し、バンパーの材料を再生するようにした樹脂製廃棄物
の表面塗膜分離装置であって、 断面が非円形をしており、一端が粗粉砕体の受入側で他
端が吐出側である剥離筒と、複数の緩傾斜した突条を外
周に有しており、前記剥離筒の内壁面との間に粗粉砕体
処理用の間隙を形成するよう配設された剥離ロールとに
より粗粉砕体の塗膜の剥離装置を構成し、 前記剥離筒の吐出側に吐出口を臨んで設けられるととも
に、該吐出口を塞ぐようにして配設された押え板を有
し、該押え板の押し付け力を加減して粗粉状体の流出量
を調整し、前記剥離筒内の圧力を調整して、前記剥離筒
内の圧力、前記剥離ロールの回転数および粗粉砕体の投
入量に起因する前記剥離筒内の粗粉砕体の品温を80℃
〜115℃に調整可能な圧力調節部を設けたことを特徴
とする樹脂製廃棄物の表面塗膜分離装置。
2. A waste bumper made of polypropylene resin is crushed into a granular coarsely pulverized body, the surface of the coarsely pulverized body is rubbed, and the resin coating film applied to the surface of the coarsely pulverized body is peeled off. , A surface coating film separation device for resin waste that is designed to recycle the material of the bumper, having a non-circular cross section, one end being the receiving side of the coarsely crushed body and the other end being the discharge side Coarse crushed body having a cylinder and a plurality of gently inclined projections on the outer circumference, and a peeling roll arranged so as to form a gap for processing the coarsely crushed body between the inner wall surface of the peeling cylinder. And a pressing plate that is provided so as to face the discharge port on the discharge side of the peeling cylinder and that is arranged so as to close the discharge port, and the pressing force of the pressing plate. To adjust the outflow amount of the coarse powder, adjust the pressure in the peeling cylinder, Pressure, the peeling roll speed and coarse grinding of product temperature to 80 ° C. of the release cylinder due to input of the coarse grinding bodies
An apparatus for separating a surface coating film of a resin waste, which is provided with a pressure adjusting section which can be adjusted to ˜115 ° C.
【請求項3】前記剥離装置を複数の処理段にして組み合
わせ、各処理段に初期剥離から最終剥離までの各種段階
を設定して割り当てたことを特徴とする請求項1または
2記載の樹脂製廃棄物の表面塗膜分離装置。
3. The resin product according to claim 1, wherein the stripping apparatus is combined into a plurality of processing stages, and various stages from initial stripping to final stripping are set and assigned to each processing stage. Waste surface coating film separation device.
【請求項4】前記各処理段における数個の剥離筒を、そ
の各筒軸が水平方向に向き、かつ、各筒軸が上下方向で
並ぶように並設して一連の剥離装置を構成したことを特
徴とする請求項3記載の樹脂製廃棄物の表面塗膜分離装
置。
4. A series of peeling devices are formed by arranging several peeling cylinders in each processing stage side by side so that each cylinder axis is oriented in the horizontal direction and each cylinder axis is aligned in the vertical direction. The surface coating film separation device for resin waste according to claim 3, wherein
【請求項5】各処理段は、前段の吐出側を後段の受入側
にスクリューコンベアを介して接続したことを特徴とす
る請求項3または4記載の樹脂製廃棄物の表面塗膜分離
装置。
5. The surface coating film separating apparatus for resin waste according to claim 3 or 4, wherein in each processing stage, the discharge side of the former stage is connected to the receiving side of the latter stage via a screw conveyor.
【請求項6】前記剥離装置の剥離筒に剥離成分のみが通
過可能な排出孔を多数穿設し、剥離ロール内に噴風流路
を設けるとともに、該噴風流路から剥離ロールの外周に
連通する噴風口を設けたことを特徴とする請求項1、
2、3、4または5記載の樹脂製廃棄物の表面塗膜分離
装置。
6. A stripping cylinder of the stripping device is provided with a large number of discharge holes through which only stripping components can pass, a jet flow channel is provided in the stripping roll, and the jet flow channel communicates with the outer periphery of the stripping roll. 2. A blast opening is provided,
The surface coating film separation device for resin waste according to 2, 3, 4 or 5.
【請求項7】各処理段は同一の駆動源を共用しているこ
とを特徴とする請求項3、4、5または6記載の樹脂製
廃棄物の表面塗膜分離装置。
7. The surface coating film separating apparatus for resin waste according to claim 3, 4, 5 or 6, wherein each processing stage shares the same drive source.
【請求項8】前記剥離筒に、内壁面から外に連通し、筒
の周方向に細長であって、分離された塗膜のみが通過可
能な幅を有する排出孔を周方向へ多数連設するととも
に、筒軸方向と平行方向に多数連設したことを特徴とす
る請求項1、2、3、4、5、6または7記載の樹脂製
廃棄物の表面塗膜分離装置。
8. A large number of discharge holes, which communicate with the outside from the inner wall surface and are elongated in the circumferential direction of the cylinder and have a width that allows only the separated coating film to pass therethrough, are connected in the circumferential direction to the peeling cylinder. In addition, the apparatus for separating a surface coating film of a resin waste according to claim 1, 2, 3, 4, 5, 6 or 7, wherein a plurality of them are continuously provided in a direction parallel to the cylinder axis direction.
JP7693094A 1994-04-15 1994-04-15 Separation device of surface coating of resin waste matter Pending JPH07276364A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7693094A JPH07276364A (en) 1994-04-15 1994-04-15 Separation device of surface coating of resin waste matter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7693094A JPH07276364A (en) 1994-04-15 1994-04-15 Separation device of surface coating of resin waste matter

Publications (1)

Publication Number Publication Date
JPH07276364A true JPH07276364A (en) 1995-10-24

Family

ID=13619450

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7693094A Pending JPH07276364A (en) 1994-04-15 1994-04-15 Separation device of surface coating of resin waste matter

Country Status (1)

Country Link
JP (1) JPH07276364A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000271932A (en) * 1999-03-29 2000-10-03 Hitachi Ltd Peeling device of plastic resin surface
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US6672523B2 (en) 2000-01-18 2004-01-06 Fuji Jukogyo Kabushiki Kaisha Method and apparatus for peeling a coating film of a coated resin product
US7204260B2 (en) 2001-11-21 2007-04-17 Techno Polymer Co., Ltd. Apparatus for cleaning polymeric pieces
JP2008080679A (en) * 2006-09-28 2008-04-10 Kurimoto Ltd Cleaning apparatus for waste plastics
JP2008080680A (en) * 2006-09-28 2008-04-10 Kurimoto Ltd Cleaning apparatus of waste plastics
KR100869820B1 (en) * 2007-12-18 2008-11-21 강성윤 Separation device of resin coated with metal
JP2010179603A (en) * 2009-02-06 2010-08-19 Satake Corp Releasing device for resin paint film
JP2011148166A (en) * 2010-01-20 2011-08-04 Satake Corp Resin coating film peeling system

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000271932A (en) * 1999-03-29 2000-10-03 Hitachi Ltd Peeling device of plastic resin surface
JP2001088128A (en) * 1999-09-24 2001-04-03 Dic Plastics Inc Coated film separating apparatus
US6672523B2 (en) 2000-01-18 2004-01-06 Fuji Jukogyo Kabushiki Kaisha Method and apparatus for peeling a coating film of a coated resin product
US6702211B2 (en) 2000-01-18 2004-03-09 Fuji Jukogyo Kabushiki Kaisha Method and apparatus for peeling a coating film of a coated resin product
US7204260B2 (en) 2001-11-21 2007-04-17 Techno Polymer Co., Ltd. Apparatus for cleaning polymeric pieces
JP2008080679A (en) * 2006-09-28 2008-04-10 Kurimoto Ltd Cleaning apparatus for waste plastics
JP2008080680A (en) * 2006-09-28 2008-04-10 Kurimoto Ltd Cleaning apparatus of waste plastics
KR100869820B1 (en) * 2007-12-18 2008-11-21 강성윤 Separation device of resin coated with metal
JP2010179603A (en) * 2009-02-06 2010-08-19 Satake Corp Releasing device for resin paint film
US8469075B2 (en) 2009-02-06 2013-06-25 Satake Corporation Coating film peeling apparatus for resin material
JP2011148166A (en) * 2010-01-20 2011-08-04 Satake Corp Resin coating film peeling system

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