JP2001030244A - Regeneration treatment apparatus for resin part having coating film - Google Patents

Regeneration treatment apparatus for resin part having coating film

Info

Publication number
JP2001030244A
JP2001030244A JP20442999A JP20442999A JP2001030244A JP 2001030244 A JP2001030244 A JP 2001030244A JP 20442999 A JP20442999 A JP 20442999A JP 20442999 A JP20442999 A JP 20442999A JP 2001030244 A JP2001030244 A JP 2001030244A
Authority
JP
Japan
Prior art keywords
coating film
processing tank
crushed pieces
crushed
powder
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
JP20442999A
Other languages
Japanese (ja)
Other versions
JP4073580B2 (en
Inventor
Tomomi Takase
朋視 高瀬
Taiichi Hijikata
泰一 土方
Toshinao Komori
俊尚 小森
Yukio Okada
行雄 岡田
Atsushi Mizutani
篤 水谷
Tsutomu Nishida
勉 西田
Hiroo Onodera
弘男 小野寺
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.)
TAKASE GOSEI KAGAKU KK
Sintokogio Ltd
Nissan Motor Co Ltd
Original Assignee
TAKASE GOSEI KAGAKU KK
Sintokogio Ltd
Nissan Motor 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 TAKASE GOSEI KAGAKU KK, Sintokogio Ltd, Nissan Motor Co Ltd filed Critical TAKASE GOSEI KAGAKU KK
Priority to JP20442999A priority Critical patent/JP4073580B2/en
Publication of JP2001030244A publication Critical patent/JP2001030244A/en
Application granted granted Critical
Publication of JP4073580B2 publication Critical patent/JP4073580B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B17/0412Disintegrating plastics, e.g. by milling to large particles, e.g. beads, granules, flakes, slices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B2017/0424Specific disintegrating techniques; devices therefor
    • B29B2017/048Cutter-compactors, e.g. of the EREMA type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2009/00Layered products
    • B29L2009/005Layered products coated
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

PROBLEM TO BE SOLVED: To enhance the peeling treatment efficiency of a coating film by preventing re-adhesion of an once peeled coating film powder. SOLUTION: Crushed pieces P charged in a treatment tank 1 are stirred to be raised in temp. by the mutual friction and collision thereof and the coating films on the surfaces of the crushed pieces P are peeled while crushed. A powder discharge port 8 having a reticulated structure 7 is formed to the part always coming into contact with the crushed pieces P of a buffle duct 6 for altering the flow direction of the crushed pieces P during stirring to be connected to an exhaust device 2. The crushed pieces P during stirring and flowing impinge against the reticulated structure 7 and only a powder component such as a peeled coating film powder is discharged to the outside.

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、塗装が施された熱
可塑性樹脂部品の再生処理装置に関し、さらに詳しく
は、自動車のバンパーのごとき加飾塗装が施された樹脂
部品廃材を再利用するにあたってその表面の塗膜を剥離
させるための装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for reprocessing a coated thermoplastic resin part, and more particularly to a method for reusing a decorative resin coated waste material such as an automobile bumper. The present invention relates to an apparatus for removing a coating film on the surface.

【0002】[0002]

【従来の技術】自動車用バンパーに代表されるような熱
可塑性樹脂部品の再生処理技術としては、金属その他の
異材質部品を除去したのちに塗膜を剥がすことなくその
まま例えば一辺が10mm程度の大きさに粉砕した上で
造粒し、外観品質がそれほど問題とならない下級部品の
原材料として再利用する方法のほか、その再生品質の向
上を図るために、上記粉砕片をアルカリあるいは有機塩
酸等の溶剤に浸漬させて塗膜を剥離させる方法や、上記
粉砕片を所定の処理槽に入れて高速にて撹拌させること
により塗膜を剥離させる方法がある(例えば特開平11
−58383号公報)。
2. Description of the Related Art As a technique for regenerating a thermoplastic resin part represented by an automobile bumper, a metal having a size of, for example, about 10 mm on a side without removing a coating film after removing a metal or other dissimilar parts is used. In addition to the method of re-grinding and granulating, and reusing it as a raw material for lower-grade parts whose appearance quality is not so problematic, in order to improve the reclaim quality, the above-mentioned crushed pieces are treated with a solvent such as alkali or organic hydrochloric acid. And a method in which the crushed pieces are put into a predetermined treatment tank and stirred at high speed to peel the coating film (for example, Japanese Patent Laid-Open No.
-58383).

【0003】そして、撹拌によって塗膜を剥離させる上
記の方法では、その撹拌に伴う粉砕片同士の相互摩擦あ
るいは相互衝突熱によって樹脂自体が軟化もしくは溶融
する直前の温度近くまで昇温させ、その昇温によって表
面の塗膜が剥離しやすくなった粉砕片同士をバレル仕上
研磨のごとき形態で相互に接触させることで塗膜を剥離
させることを基本としている。
[0003] In the above-mentioned method of peeling a coating film by stirring, the temperature of the resin itself is raised to a temperature close to a temperature immediately before the resin itself softens or melts due to mutual friction or mutual collision heat of the crushed pieces accompanying the stirring, and the temperature is raised. Basically, the coating film is peeled off by bringing the crushed pieces, whose surface coating film is easily peeled off by temperature, into contact with each other in a form such as barrel finish polishing.

【0004】[0004]

【発明が解決しようとする課題】溶剤を使って塗膜を剥
離させる方法では、処理後の溶剤の処理が問題となるほ
か、塗膜剥離後に水洗が必須となるために、処理設備全
体が大型化することとなって好ましくない。
In the method of peeling a coating film using a solvent, the treatment of the solvent after the treatment becomes a problem, and washing with water is necessary after the coating film is peeled off. This is undesirable.

【0005】また、撹拌のみによって塗膜を剥離させる
方法では、剥離された塗膜と樹脂とを処理槽内で完全に
分別することができないため、処理後に別工程において
塗膜と樹脂との分別作業を行わなければならず、工数の
増加とコストアップが余儀なくされる。
In the method of peeling the coating film only by stirring, the peeled coating film and the resin cannot be completely separated in the treatment tank. Therefore, after the treatment, the coating film and the resin are separated in a separate step. Work must be performed, which increases man-hours and costs.

【0006】その上、一旦剥離された塗膜も処理時間中
は粉砕片とともに継続して撹拌されることになるため、
その一旦剥離した塗膜がクッションとなって未剥離の粉
砕片の塗膜剥離を妨げるだけでなく、一旦剥離した塗膜
が粉砕片に再度付着してしまうことが予想され、結果と
して塗膜剥離効率が悪くなり、処理時間が無用に長くな
って好ましくない。
[0006] In addition, the coating film once peeled is continuously stirred together with the crushed pieces during the processing time.
It is expected that the peeled coating film not only prevents the unpeeled crushed pieces from peeling off as a cushion but also causes the once peeled coating film to adhere to the crushed pieces again. Efficiency deteriorates and the processing time becomes unnecessarily long, which is not preferable.

【0007】さらに、上記のように処理時間が長くなる
と、粉砕片の表面の塗膜だけでなく樹脂層自体までもが
粉状に破砕される度合いが大きくなり、本来の目的であ
る樹脂の回収効率が低下することになる。
Further, when the treatment time is long as described above, the degree of crushing not only the coating film on the surface of the crushed pieces but also the resin layer itself into a powdery form increases, and the original purpose of resin recovery is Efficiency will be reduced.

【0008】本発明は以上のような課題に着目してなさ
れたもので、その目的とするところは、設備の大型化や
廃液の二次処理問題を招くことなく、しかも短時間のう
ちに効率よく塗膜を剥離させることができるようにした
再生処理装置を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and has as its object to reduce the efficiency in a short period of time without incurring the problem of upsizing of equipment and secondary treatment of waste liquid. It is an object of the present invention to provide a reprocessing apparatus capable of removing a coating film.

【0009】[0009]

【課題を解決するための手段】請求項1に記載の発明
は、予め所定の大きさに粉砕した塗膜付き熱可塑性樹脂
部品の粉砕片を処理槽内に収容するとともに、その処理
槽底部に配置した回転部材により粉砕片を撹拌して粉砕
片同士の相互摩擦衝突により塗膜を剥離させるようにし
た塗膜付き樹脂部品の再生処理装置であって、前記処理
槽の胴部内周に、撹拌に伴う遠心力によって槽内外周部
に寄せ集められた粉砕片の流動方向を上向き方向から下
向き方向に積極的に変更する返し部材を設ける一方、こ
の返し部材のうち流動粉砕片が直接的に接する部分に、
粉砕片自体の通過を阻止しつつその粉砕片から剥離した
粉体成分の通過を許容する粉体排出口を形成するととも
に、この粉体排出口を処理槽外部に臨ませ、前記遠心力
による粉砕片自体の流動により該粉砕片から粉体成分を
積極的に分離させて処理槽外部に排出するようにしたこ
とを特徴としている。
According to the first aspect of the present invention, a crushed piece of a thermoplastic resin part having a coating film, which has been crushed to a predetermined size in advance, is accommodated in a processing tank, and the crushed piece is placed on the bottom of the processing tank. An apparatus for regenerating a resin part with a coating film in which a crushed piece is agitated by an arranged rotating member and a coating film is peeled off by mutual frictional collision between the crushed pieces. While a return member is provided to positively change the flow direction of the crushed pieces gathered at the outer peripheral portion of the tank by the centrifugal force accompanying the above from the upward direction to the downward direction, the flowing crushed pieces of the return members are in direct contact with each other. In part,
While forming a powder outlet which allows the passage of the powder component separated from the crushed piece while preventing the passage of the crushed piece itself, the powder outlet is exposed to the outside of the treatment tank, and the pulverization by the centrifugal force is performed. It is characterized in that the powder component is positively separated from the crushed pieces by the flow of the pieces themselves and discharged to the outside of the treatment tank.

【0010】この場合、請求項2に記載の発明のよう
に、前記粉体排出口が処理槽外部の吸引手段に接続され
ていて、粉砕片から分離した粉体成分が粉体排出口から
強制的に吸引排出されるようになっていることが粉体成
分の分離効率の上で好ましい。
In this case, the powder discharge port is connected to suction means outside the processing tank, and the powder component separated from the crushed pieces is forcibly discharged from the powder discharge port. It is preferable from the viewpoint of the efficiency of separation of the powder component that the liquid be sucked and discharged.

【0011】また、上記粉砕片自体の通過を阻止しつつ
その粉砕片から剥離した粉体成分の通過を許容する粉体
排出口としては、例えば金網のごとき網目状のものやパ
ンチングメタル等をもって構成するのが望ましい。特に
その粉体排出口の網目の大きさ次第では粉体成分の付着
によって目詰まりを起こしやすいので、例えばその網目
部分にフッ素樹脂コーティングを施したり、あるいはそ
の網目部分に微振動を与えるようにするのがより望まし
い。
The powder discharge port for preventing the passage of the above-mentioned crushed pieces themselves and allowing the passage of the powder component peeled from the crushed pieces is constituted by, for example, a mesh-like one such as a wire mesh or a punching metal. It is desirable to do. In particular, depending on the size of the mesh of the powder discharge port, clogging is likely to occur due to the adhesion of the powder component. For example, a fluororesin coating is applied to the mesh portion, or fine vibration is applied to the mesh portion. Is more desirable.

【0012】したがって、この請求項1,2に記載の発
明では、撹拌による相互摩擦衝突等によって粉砕片の表
面の塗膜が粉状に破砕されながら徐々に剥離されてその
粉砕片とともに撹拌されることになるものの、粉砕片が
撹拌による流動を続ける過程で返し部材と衝突すること
により、塗膜粉や樹脂層の一部までもが粉状となった粉
体成分は比重が小さい故に粉砕片から離れて、金網もし
くはパンチングメタル等をもって形成された粉体排出口
から処理槽の外部に排出される。これにより、一旦剥離
した塗膜粉等の粉体成分が再度粉砕片に付着するような
事態はなくなる。
Therefore, according to the first and second aspects of the present invention, the coating film on the surface of the crushed piece is gradually peeled off while being crushed into a powder due to mutual frictional collision or the like caused by stirring, and is stirred together with the crushed piece. However, since the crushed pieces collide with the return member in the process of continuing the flow by stirring, the powder component in which even a part of the coating film powder and the resin layer has become powdery has a small specific gravity, so that the crushed pieces are small. Away from the processing tank through a powder outlet formed by a wire mesh or punched metal. As a result, a situation in which the powder components such as the coating film powder once peeled adhere to the crushed pieces again does not occur.

【0013】請求項3に記載の発明は、予め所定の大き
さに粉砕した塗膜付き熱可塑性樹脂部品の粉砕片を処理
槽内に収容するとともに、その処理槽底部に配置した回
転部材により粉砕片を撹拌して粉砕片同士の相互摩擦衝
突により塗膜を剥離させるようにした塗膜付き樹脂部品
の再生処理装置であって、撹拌に伴う遠心流動によって
槽内外周部に寄せ集められた粉砕片に向けて斜め方向か
ら空気を噴射し、処理槽内を周回しつつその処理槽内を
下方から上方に向かって流れる旋回空気流を生じさせる
ことにより、前記粉砕片から剥離した粉体成分を積極的
に処理槽内の上部空間に浮遊させ、この浮遊している粉
体成分を処理槽の上部に開口形成した排出口から外部に
吸引排出するようにしたことを特徴としている。
According to a third aspect of the present invention, a crushed piece of a thermoplastic resin part having a coating film, which has been crushed to a predetermined size in advance, is accommodated in a processing tank, and crushed by a rotating member disposed at the bottom of the processing tank. This is a device for regenerating a coated resin part in which pieces are agitated so that the coating film is peeled off by mutual frictional collision between the crushed pieces. By injecting air from the oblique direction toward the pieces, and by generating a swirling air flow that flows upward from below in the processing tank while circling in the processing tank, the powder component separated from the crushed pieces is removed. It is characterized in that it is positively suspended in the upper space in the processing tank, and the suspended powder component is sucked and discharged to the outside from a discharge opening formed in the upper part of the processing tank.

【0014】この場合、粉砕片に吹き付ける空気として
は予め湿度を除去したいわゆるドライエアを使用するの
が望ましく、こうすることにより粉砕片自体を乾燥させ
やすく、また粉砕片に付着している粉体成分を分離させ
やすくなる。
In this case, it is desirable to use so-called dry air from which humidity has been removed in advance as the air to be blown on the crushed pieces, so that the crushed pieces themselves can be easily dried, and the powder component adhering to the crushed pieces can be used. Can be easily separated.

【0015】したがって、この請求項3に記載の発明で
は、撹拌による相互摩擦衝突等によって粉砕片の表面の
塗膜が粉状に破砕されながら徐々に剥離されてその粉砕
片とともに撹拌されることになるものの、粉砕片が撹拌
による流動を続ける過程で空気噴射を受けることから、
塗膜粉や樹脂層の一部までもが粉状となった粉体成分は
比重が小さい故に粉砕片から吹き飛ばされて、処理槽内
の旋回空気流に乗ってその槽内の上部空間へと浮遊す
る。そして、処理槽の上部空間には排出口が開口してい
て、しかもその排出口には吸引力が作用していることか
ら、上記粉体成分は処理槽の外部に排出される。
Therefore, according to the third aspect of the present invention, the coating film on the surface of the crushed piece is gradually peeled off while being crushed into powder due to mutual frictional collision or the like caused by stirring, and is stirred together with the crushed piece. However, since the crushed pieces receive air injection in the process of continuing the flow by stirring,
The powder component in which even the coating film powder and even a part of the resin layer became powdery is blown off from the crushed pieces due to its low specific gravity, and rides on the swirling air flow in the processing tank to the upper space in the tank. Float. The outlet is opened in the upper space of the processing tank, and the suction force acts on the outlet, so that the powder component is discharged to the outside of the processing tank.

【0016】請求項4に記載の発明は、請求項3に記載
の発明における処理槽内の上部に棚状部を形成し、処理
槽内の上部空間に浮遊している粉体成分の一部をこの棚
状部にて自然落下により集めるようにしたことを特徴と
している。
According to a fourth aspect of the present invention, there is provided the processing tank according to the third aspect, wherein a shelf-like portion is formed in an upper portion in the processing tank, and a part of the powder component floating in the upper space in the processing tank. Are collected by natural fall on the shelf.

【0017】したがって、この請求項4に記載の発明で
は、旋回空気流に乗って処理槽内の上部空間まで浮遊し
ながら強制排出によって排出されなかった粉体成分の一
部は棚状部に自然落下により集められて捕集される。
Therefore, in the invention according to the fourth aspect, part of the powder component which is not discharged by the forced discharge while floating to the upper space in the processing tank while riding on the swirling airflow is naturally deposited on the shelf. Collected by falling and collected.

【0018】この場合、請求項5に記載の発明のよう
に、処理槽の上端部内径を大径化し、この大径部に棚状
部を形成しておくと、その大径部材では相対的に旋回空
気流の流れが緩やかなものとなることから、棚状部での
自然落下による粉体成分の捕集効率が一段と向上するこ
とになる。
In this case, if the inner diameter of the upper end portion of the processing tank is increased and a shelf-like portion is formed in the large-diameter portion, the large-diameter member has a relatively large diameter. Since the flow of the swirling air flow becomes gentler, the collection efficiency of the powder component by the natural fall on the shelf portion is further improved.

【0019】請求項6に記載の発明は、予め所定の大き
さに粉砕した塗膜付き熱可塑性樹脂部品の粉砕片を処理
槽内に収容するとともに、その処理槽底部に配置した回
転部材により粉砕片を撹拌して粉砕片同士の相互摩擦衝
突により塗膜を剥離させるようにした塗膜付き樹脂部品
の再生処理装置であって、前記処理槽内のうち回転部材
よりも上方位置であって且つ撹拌に伴う遠心流動によっ
て槽内外周部に寄せ集められた粉砕片と接する位置に空
気噴射用配管を配置して、この空気噴射用配管に接続し
た噴射ノズルから粉砕片に向けて空気を噴射するととも
に、旋回空気流生成用の噴射ノズルから空気を噴射して
処理槽内を周回しつつその処理槽内を下方から上方に向
かって流れる旋回空気流を生じさせることにより、前記
粉砕片から剥離した粉体成分を積極的に処理槽内の上部
空間に浮遊させ、この浮遊している粉体成分を処理槽の
上部に開口形成した排出口から外部に吸引排出するよう
にしたことを特徴としている。
According to a sixth aspect of the present invention, a crushed piece of a thermoplastic resin part having a coating film, which has been crushed to a predetermined size in advance, is accommodated in a processing tank, and crushed by a rotating member disposed at the bottom of the processing tank. An apparatus for regenerating a coated resin part in which the pieces are agitated to peel off the coating by mutual frictional collision between the crushed pieces, wherein the apparatus is located above a rotating member in the processing tank and An air injection pipe is arranged at a position in contact with the crushed pieces gathered in the outer peripheral portion of the tank by centrifugal flow accompanying stirring, and air is jetted toward the crushed pieces from an injection nozzle connected to the air injection pipe. At the same time, by injecting air from an injection nozzle for swirling air flow generation to generate a swirling air flow that flows upward from below in the processing tank while circulating in the processing tank, the air is separated from the crushed pieces. It is characterized in that the powder component is positively suspended in the upper space in the processing tank, and the floating powder component is sucked and discharged to the outside from a discharge opening formed in the upper part of the processing tank. .

【0020】この場合、空気噴射用配管を流れる空気を
予め冷却しておくことにより、配管壁面の温度上昇を抑
制して、溶融温度近くまで昇温している粉砕片が配管外
周面に付着するのを未然に防止することができる。
In this case, by cooling the air flowing through the air injection pipe in advance, the rise in the temperature of the pipe wall is suppressed, and the crushed pieces that have been heated to near the melting temperature adhere to the outer peripheral surface of the pipe. Can be prevented beforehand.

【0021】したがって、この請求項6に記載の発明で
は、空気噴射用配管を撹拌中の粉砕片と繰り返し衝突す
るように配置してあるので、この空気噴射用配管と粉砕
片との衝突による粉砕片表面の塗膜の剥離効率および粉
砕片と塗膜粉等の粉体成分との分離効率が一段と促進さ
れる。そして、粉砕片から分離した粉体成分は空気噴射
を受けることにより粉砕片から吹き飛ばされた上、旋回
空気流に乗って処理槽内の上部空間へと浮遊し、最終的
にはその処理槽上部の排出口から強制的に吸引排出され
ることになる。
Therefore, in the invention according to the sixth aspect, the air injection pipe is arranged so as to repeatedly collide with the crushed pieces during stirring. Therefore, the pulverization by collision between the air injection pipe and the pulverized pieces is performed. Separation efficiency of the coating film on one surface and separation efficiency of the pulverized pieces and powder components such as coating film powder are further promoted. Then, the powder component separated from the crushed pieces is blown off from the crushed pieces by receiving an air jet, and then floats in the upper space in the processing tank by riding a swirling air flow, and finally the upper part of the processing tank. Is forcibly sucked and discharged from the discharge port.

【0022】[0022]

【発明の効果】請求項1に記載の発明によれば、一旦粉
砕片から剥離した塗膜粉等の粉体成分が、処理槽内の返
し部材に設けた粉体排出口にて粉砕片から分離されて速
やか処理槽の外部に排出されるので、その一旦分離した
塗膜が再度粉砕片に付着することがなく塗膜剥離効率が
向上するほか、従来では必須とされた塗膜剥離処理後の
剥離塗膜と粉砕片との分別作業を廃止もしくは大幅に簡
略化することができるので、工程数の削減とコストダウ
ンを図ることができる。また、上記塗膜剥離効率の向上
により処理時間が短くて済むので、樹脂層の一部までも
粉状に破砕してしまう度合いが著しく小さくなり、本来
の目的である樹脂の回収効率が一段と向上する効果があ
る。
According to the first aspect of the present invention, the powder components such as the coating film powder once peeled from the crushed pieces are removed from the crushed pieces at the powder discharge port provided in the return member in the processing tank. Separated and quickly discharged to the outside of the processing tank, the once separated coating film does not adhere to the crushed pieces again, improving the coating film stripping efficiency. Since the work of separating the peeled coating film from the crushed pieces can be abolished or greatly simplified, the number of steps and the cost can be reduced. In addition, since the processing time can be shortened by improving the above-mentioned coating film peeling efficiency, the degree of crushing even a part of the resin layer into a powdery form is significantly reduced, and the original purpose of resin recovery efficiency is further improved. Has the effect of doing

【0023】請求項2に記載の発明によれば、上記粉体
排出口から塗膜粉等の粉体成分を強制的に吸引排出する
ことから、請求項1に記載の発明と同様の効果に加え
て、粉砕片と塗膜粉等の粉体成分との分離効率が一段と
向上する効果がある。
According to the second aspect of the present invention, since the powder component such as the coating film powder is forcibly sucked and discharged from the powder discharge port, the same effect as the first aspect of the present invention can be obtained. In addition, there is an effect that the separation efficiency between the crushed pieces and the powder components such as the coating film powder is further improved.

【0024】請求項3に記載の発明によれば、粉砕片に
付着している塗膜粉等の粉体成分を空気噴射により吹き
飛ばした上で旋回空気流に乗せて上方に浮遊させて処理
槽の上部から強制的に吸引排出するようにしたために、
請求項1に記載の発明と同様の効果が得られる。
According to the third aspect of the present invention, the processing tank is formed by blowing off powder components such as coating powder adhering to the crushed pieces by air jetting, and then placing them on a swirling air stream to float upward. To forcibly eject and discharge from the top of the
An effect similar to that of the first aspect is obtained.

【0025】請求項4に記載の発明によれば、粉体成分
を上方に浮遊させて強制的に吸引排出する方式に加え
て、棚状部での自然落下による粉体成分の捕集方式を併
用したため、請求項3に記載の発明と同様の効果に加え
て、塗膜粉等の粉体成分の分離捕集効率が一段と向上す
る効果がある。
According to the fourth aspect of the invention, in addition to the method of forcibly sucking and discharging the powder component by floating the powder component upward, the method of collecting the powder component by natural fall on the shelf portion is used. Since they are used together, in addition to the same effect as the invention described in claim 3, there is an effect that the efficiency of separating and collecting powder components such as coating film powder is further improved.

【0026】請求項5に記載の発明によれば、棚状部で
の自然落下による粉体成分の捕集方式の採用にあたり、
その棚状部を処理槽よりも大径化したため、その大径化
した部分では旋回空気流の流れが緩やかなものとなるた
めに、請求項4に記載の発明と同様の効果に加えて、棚
状部での粉体成分の捕集効率が一段と向上する効果があ
る。
According to the fifth aspect of the present invention, in adopting a method of collecting powder components by natural fall on a shelf,
Since the diameter of the shelf portion is larger than that of the processing tank, the swirling air flow is gentle in the portion having the larger diameter. In addition to the same effect as the invention described in claim 4, There is an effect that the collection efficiency of the powder component in the shelf portion is further improved.

【0027】請求項6に記載の発明によれば、粉体成分
を上方に浮遊させて強制的に吸引排出する方式を前提と
しつつも、空気噴射用配管を積極的に撹拌流動中の粉砕
片と衝突させるようにしたため、請求項1に記載の発明
と同様の効果のほかに、上記の衝突作用による塗膜の剥
離効率はもちろんのこと、その剥離した塗膜粉等の粉体
成分と粉砕片との分離効率が一段と向上する効果があ
る。
According to the sixth aspect of the present invention, it is assumed that the powder component is suspended upward and the suction and discharge of the powder component is forcibly performed. In addition to the same effect as the first aspect of the present invention, not only the peeling efficiency of the coating film due to the above-mentioned collision action but also the powder component such as the peeled coating film powder and the pulverization This has the effect of further improving the efficiency of separation from the pieces.

【0028】[0028]

【発明の実施の形態】図1,2は本発明に係る処理装置
の好ましい第1の実施の形態を示す図であって、1は図
示しない投入口から所定の塗膜付き熱可塑性樹脂部品の
粉砕片Pが投入されることによりその粉砕片Pの塗膜剥
離処理を行う略円筒状をなす密閉式の処理槽、2は処理
槽1の側部に付設された排気ダクト3に接続された排気
装置である。
1 and 2 show a first preferred embodiment of a processing apparatus according to the present invention, in which a numeral 1 designates a thermoplastic resin part having a predetermined coating film through an inlet (not shown). A substantially cylindrical hermetic treatment tank 2 for performing the coating film peeling treatment of the crushed pieces P by being supplied with the crushed pieces P was connected to an exhaust duct 3 attached to the side of the processing tank 1. Exhaust device.

【0029】例えば、ポリプロピレン製の自動車用バン
パーに代表されるような所定の加飾塗装が施された熱可
塑性の樹脂部品廃材は、前工程である破砕工程にて塗膜
付きのまま一辺が5〜30mm程度の大きさの粉砕片P
に粉砕された上で、図示外の空気輸送式やスクリュー式
のコンベヤあるいはベルトコンベヤ等にて所定量ずつ処
理槽1内に投入される。
For example, a thermoplastic resin component waste material which has been subjected to a predetermined decorative coating such as a polypropylene automobile bumper has a side with a coating film of 5 mm in a previous crushing step. Pulverized pieces P about 30mm in size
After being pulverized into the processing tank 1, a predetermined amount is charged by a pneumatic transport type or screw type conveyor or a belt conveyor (not shown).

【0030】前記処理槽1の内底部には図2に示すよう
にその底面全域を覆うような大きさの回転円板4が設け
られているとともに、粉砕片Pの撹拌を効率的に行うた
めにその回転円板4の上面には複数の羽根4aが取り付
けられていて、回転円板4はモータ5にて回転駆動され
るようになっている。
As shown in FIG. 2, a rotating disk 4 is provided at the inner bottom of the processing tank 1 so as to cover the entire bottom surface thereof. A plurality of blades 4a are attached to the upper surface of the rotating disk 4, and the rotating disk 4 is driven to rotate by a motor 5.

【0031】そして、処理槽1に所定量の粉砕片Pが投
入されると回転円板4が回転駆動されて、粉砕片Pが撹
拌される。この撹拌に伴い粉砕片P,P同士の相互摩擦
衝突もしくは槽内壁面や回転円板4との摩擦衝突等によ
り各粉砕片Pが溶融する直前の温度まで加熱され、その
表面での塗膜接着力が低下した塗膜が樹脂層の一部とと
もに細かく破砕されながら粉体成分となって樹脂層その
ものから剥離されるようになっている。
When a predetermined amount of the crushed pieces P is put into the processing tank 1, the rotary disk 4 is driven to rotate, and the crushed pieces P are stirred. Due to the agitation, the crushed pieces P are heated to a temperature immediately before melting due to mutual frictional collision between the pieces P or frictional collision with the inner wall surface of the tank or the rotating disk 4, etc., and adhesion of the coating film on the surface thereof The coating film having reduced force becomes a powder component while being finely crushed together with a part of the resin layer, and is peeled off from the resin layer itself.

【0032】また、上記処理槽1の内周面のうちその胴
部1aの高さ方向中央部には断面が略中空三角形状をな
す返し部材としてのバッフルダクト6が配設されてい
る。このバッフルダクト6は処理槽1の内周全周もしく
はその内周に部分的に設けられていて、回転円板4によ
って撹拌された粉砕片Pはその遠心力によって槽内外周
部に寄せ集められるようにして下方から上方に流動する
ことから、バッフルダクト6はその流動粉砕片Pの動き
を妨げつつその流動方向を図1に矢印Qで示すように上
向き方向から下向き方向に積極的に変更する役目を有し
ている。
A baffle duct 6 as a return member having a substantially hollow triangular cross section is disposed at the center in the height direction of the body 1a of the inner peripheral surface of the processing tank 1. The baffle duct 6 is provided on the entire inner circumference of the processing tank 1 or partially on the inner circumference thereof, so that the crushed pieces P stirred by the rotating disk 4 are gathered to the outer circumference inside the tank by the centrifugal force. As a result, the baffle duct 6 serves to actively change the flow direction from the upward direction to the downward direction as shown by the arrow Q in FIG. have.

【0033】このバッフルダクト6のうちその下面部す
なわち撹拌流動する粉砕片Pが常に当たる部分は金網や
スクリーンあるいはパンチングメタル等の網状構造物7
をもって形成されていて、この網状構造物7は実質的に
粉体排出口8として処理槽1内部に開口していると同時
に、バッフルダクト6自体は排気ダクト3に接続されて
いる。
The lower surface of the baffle duct 6, that is, the portion always contacted by the crushed pieces P, which is agitated and flown, is a mesh structure 7 such as a wire mesh, a screen or a punched metal.
The net-like structure 7 is opened substantially as a powder discharge port 8 inside the processing tank 1, and the baffle duct 6 itself is connected to the exhaust duct 3.

【0034】ここで、上記網状構造物7は、後述するよ
うに粉砕片Pそのものの通過を阻止しつつその粉砕片P
から剥離した塗膜粉等の粉体成分のみを通過させるもの
であるから、そのメッシュの大きさは例えば1〜5mm
程度とするのが望ましい。また、網状構造物7に粉体成
分が付着するのを防止するため、網状構造物7自体にフ
ッ素樹脂をコーティングしたり、あるいは網状構造物7
に微振動を与えるようにするとよい。
Here, the mesh structure 7 prevents the crushed pieces P from passing while preventing the crushed pieces P from passing through, as described later.
Since only the powder component such as the coating film powder peeled off from the substrate is passed through, the size of the mesh is, for example, 1 to 5 mm.
It is desirable to be about. In order to prevent the powder component from adhering to the network structure 7, the network structure 7 itself is coated with a fluororesin,
It is good to give a slight vibration to.

【0035】一方、上記排気装置2は集塵装置9と排気
ブロワ10および排気筒11とから構成されているとと
もに、この排気装置2による排気のための吸引力がバッ
フルダクト6の粉体排出口8に作用するようになってい
て、後述するように処理槽1内での塗膜剥離処理と並行
して排気装置2による排気が行われるようになってい
る。
On the other hand, the exhaust device 2 is composed of a dust collecting device 9, an exhaust blower 10 and an exhaust tube 11, and the suction force for exhausting by the exhaust device 2 is applied to the powder discharge port of the baffle duct 6. 8, the exhaust device 2 is evacuated in parallel with the coating film peeling process in the processing tank 1 as described later.

【0036】したがって、本実施の形態によれば、先に
述べたように、処理槽1内に所定量の粉砕片Pが投入さ
れると回転円板4が駆動されて、粉砕片Pが撹拌されな
がら流動するようになる。この撹拌に伴い、粉砕片Pは
その遠心力により処理槽1内の外周部に寄せ集められな
がら下方から上方に向かって隆起しようと流動するもの
の、図1に示すようにバッフルダクト6によってその粉
砕片Pの流動方向が変更される。
Therefore, according to the present embodiment, as described above, when a predetermined amount of the crushed pieces P is put into the processing tank 1, the rotating disk 4 is driven, and the crushed pieces P are stirred. It will flow while being played. Along with the stirring, the crushed pieces P are gathered at the outer peripheral portion in the processing tank 1 by the centrifugal force and flow so as to rise upward from below, but as shown in FIG. The flow direction of the piece P is changed.

【0037】そして、この撹拌に伴う流動により粉砕片
P,P同士もしくは粉砕片Pと槽内壁面あるいは回転円
板4との相互摩擦衝突等によりそれらの粉砕片Pが溶融
する直前の温度まで加熱され、粉砕片P表面での接着力
が低下した塗膜が細かく破砕されながら樹脂層そのもの
から剥離されるとともに、樹脂層そのものの表面の一部
も粉状に破砕されて粉体成分となり、この粉体成分は粉
砕片Pとともに撹拌される。
Then, the crushed pieces P are heated to a temperature just before the crushed pieces P are melted due to mutual frictional collision between the crushed pieces P, or between the crushed pieces P and the inner wall surface of the tank or the rotating disk 4 due to the flow accompanying the stirring. Then, the coating film having a reduced adhesive force on the surface of the crushed piece P is peeled off from the resin layer itself while being finely crushed, and a part of the surface of the resin layer itself is also crushed into a powder form to become a powder component. The powder component is stirred together with the crushed pieces P.

【0038】同時に、処理槽1での塗膜剥離処理と並行
して排気ブロワ10が運転されていることから、この排
気ブロワ10による吸引排気力が排気ダクト3を通して
バッフルダクト6の粉体排気口8まで及んでいる。これ
により、塗膜剥離処理によって発生した塗膜粉や樹脂粉
等の粉体成分が撹拌流動を繰り返す過程で粉砕片Pとと
もにバッフルダクト6の粉体排気口8である網状構造物
7に当たると、その粉体成分のみは網目を通過不能な粉
砕片Pを残して直ちに排気ダクト3側に吸引され、最終
的には集塵装置9によって集塵されることになる。
At the same time, since the exhaust blower 10 is operated in parallel with the coating film peeling treatment in the processing tank 1, the suction exhaust force of the exhaust blower 10 is applied to the powder exhaust port of the baffle duct 6 through the exhaust duct 3. Up to eight. As a result, when the powder components such as the coating powder and the resin powder generated by the coating peeling process hit the mesh structure 7 which is the powder exhaust port 8 of the baffle duct 6 together with the crushed pieces P in the process of repeating the stirring and flowing, Only the powder component is immediately sucked into the exhaust duct 3 while leaving the crushed pieces P that cannot pass through the mesh, and finally collected by the dust collecting device 9.

【0039】こうして処理槽1内での塗膜剥離処理が終
了すると粉砕片Pは処理槽1から取り出され、後工程に
てなおも表面に付着している塗膜粉や樹脂粉等の粉体成
分と分別されたのちに回収されて、そのままの状態もし
くはペレット化されて所定の樹脂材料として再利用され
る。
When the coating film peeling treatment in the processing tank 1 is completed in this way, the crushed pieces P are taken out of the processing tank 1, and powders such as coating film powder and resin powder still adhered to the surface in a later step. After being separated from the components, they are collected and reused as they are or as pellets after being pelletized.

【0040】このように本実施の形態によれば、処理槽
1内にて粉砕片Pから剥離した塗膜粉等の粉体成分を速
やかに処理槽1外に排出することができるため、一旦剥
離した塗膜粉等が粉砕片Pに再付着することがなく、塗
膜剥離効率が飛躍的に向上することになる。
As described above, according to the present embodiment, the powder components such as the coating film powder peeled off from the crushed pieces P in the processing tank 1 can be quickly discharged out of the processing tank 1. The peeled coating film powder and the like do not adhere to the crushed pieces P, and the coating film peeling efficiency is dramatically improved.

【0041】図3,4は本発明に係る処理装置の好まし
い第2の実施の形態を示す図であって、図1に示した第
1の実施の形態と共通する部分には同一符号を付してあ
る。
FIGS. 3 and 4 are views showing a second preferred embodiment of the processing apparatus according to the present invention, in which parts common to those of the first embodiment shown in FIG. I have.

【0042】この第2の実施の形態では、処理槽1の上
部に排出口12が形成されていて、この上部の排出口1
2に排気装置2が接続されている一方、処理槽1のうち
胴部1aとなるべき部分の高さ方向中央部には空気圧力
源13に接続された一対の空気噴射ノズル14が設けら
れている。これらの空気噴射ノズル14は槽内にて互い
に逆向きで正対するような位置関係のもとに配置され、
図4の平面視ではその軸線が内部の撹拌流動方向Rのほ
ぼ接線方向を指向しつつも、図3の断面図示状態ではそ
の軸線が斜め下方を指向するように設定されている。
In the second embodiment, a discharge port 12 is formed in the upper part of the processing tank 1, and the discharge port 1 in the upper part is formed.
2, a pair of air injection nozzles 14 connected to an air pressure source 13 is provided at the center in the height direction of a portion of the processing tank 1 that is to become the body 1a. I have. These air injection nozzles 14 are arranged in a positional relationship such that they face each other in opposite directions in the tank,
In the plan view of FIG. 4, the axis is set to point substantially obliquely to the tangential direction of the internal stirring and flowing direction R, but in the cross-sectional view of FIG. 3, the axis is set to point diagonally downward.

【0043】すなわち、各空気噴射ノズル14の指向方
向としては、撹拌流動中の粉砕片Pの隆起部に向けて斜
め上方から空気を吹き付けた場合に、二つの空気噴射ノ
ズル14からの空気流の相乗作用により、槽内を周回し
つつその下方から上方に向かう螺旋状の旋回空気流Fが
生成されるように設定されている。
That is, when the air is blown obliquely from above toward the protruding portion of the crushed pieces P during the stirring and flowing, the air flow from the two air injection nozzles 14 By the synergistic action, it is set so as to generate a spiral swirling airflow F that goes upward from below and circulates in the tank.

【0044】したがって、この第2の実施の形態によれ
ば、回転円板4による粉砕片Pの撹拌動作と並行して排
気装置2の排気ブロワ10を運転する一方、二つの空気
噴射ノズル14から撹拌流動している粉砕片Pに向けて
空気を噴射して、図3に矢印で示すように槽内を下方か
ら上方に向かう螺旋状の旋回空気流Fを生成する。
Therefore, according to the second embodiment, the exhaust blower 10 of the exhaust device 2 is operated in parallel with the stirring operation of the crushed pieces P by the rotating disk 4 while the two air injection nozzles 14 Air is jetted toward the stirring and flowing pulverized pieces P to generate a spiral swirling airflow F that flows upward from below in the tank as shown by arrows in FIG.

【0045】この状態では、撹拌に伴う流動に基づいて
粉砕片P,P同士もしくは粉砕片Pと槽内壁面あるいは
回転円板4との相互摩擦衝突等により剥離された塗膜粉
あるいは樹脂粉等の粉体成分は粉砕片Pとともに撹拌さ
れていて、上記隆起部の表面に表れるようになると比重
の小さい粉体成分は空気噴射により吹き飛ばされるとと
もに、旋回空気流Fに乗って槽内の下方から上方に向か
って浮遊しつつ上昇する。そして、槽内の上部空間にて
浮遊している粉体成分は排気装置2の強制吸引力によっ
て排出口12から速やかに排出されることになる。この
第2の実施の形態においても基本的に第1の実施の形態
のものと同様の効果が得られる。
In this state, based on the flow accompanying the stirring, the coating powder or the resin powder, etc., which have been separated due to mutual frictional collision between the crushed pieces P, or between the crushed pieces P or between the crushed pieces P and the inner wall surface of the tank or the rotating disk 4 or the like. Is stirred together with the crushed pieces P, and when it comes to appear on the surface of the above-mentioned raised portion, the powder component having a small specific gravity is blown off by air jetting and rides on the swirling air flow F from below in the tank. It rises while floating upward. Then, the powder component floating in the upper space in the tank is quickly discharged from the discharge port 12 by the forced suction force of the exhaust device 2. In the second embodiment, basically, the same effects as those of the first embodiment can be obtained.

【0046】ここで、空気噴射ノズル14から噴射する
空気として予め湿度を除去したドライエアを使用する
と、粉砕片P自体の乾燥とその粉砕片Pからの粉体成分
の分離とが一段と促進される。また、空気噴射ノズル1
4の形態としては、粉砕片Pに向けて空気を直接吹き付
けるノズルと、旋回空気流Fを生成するためのノズルと
を相互に独立させても同様の機能が発揮される。
Here, when dry air from which humidity has been removed in advance is used as the air injected from the air injection nozzle 14, the drying of the crushed pieces P itself and the separation of the powder component from the crushed pieces P are further promoted. In addition, the air injection nozzle 1
In the fourth embodiment, the same function is exhibited even when the nozzle for directly blowing air toward the crushed pieces P and the nozzle for generating the swirling airflow F are made independent of each other.

【0047】図5は本発明に係る処理装置の好ましい第
3の実施の形態を示す図であって、図3に示す第2の実
施の形態と共通する部分には同一符号を付してある。
FIG. 5 is a view showing a third preferred embodiment of the processing apparatus according to the present invention, and portions common to those of the second embodiment shown in FIG. 3 are denoted by the same reference numerals. .

【0048】すなわち、この第3の実施の形態では、処
理槽1の上端部を部分的に大径化して、その大径部15
とそれより下方の一般部たる胴部1aとの境界部に両者
の径差に相当する棚状部16を形成するとともに、この
棚状部16の一部に図示外のシャッター等にて開閉可能
な粉体取出口17を形成してある。
That is, in the third embodiment, the upper end portion of the processing tank 1 is partially enlarged, and the large diameter portion 15 is formed.
A shelf 16 corresponding to the difference in diameter between the two is formed at the boundary between the main body 1a and the lower part of the body 1a, and a part of the shelf 16 can be opened and closed by a shutter or the like (not shown). A powder outlet 17 is formed.

【0049】この第3の実施の形態によれば、槽内に生
成されている旋回空気流Fは、その大径部15に相当す
る部分では相対的にその流れが緩やかになることから、
旋回空気流Fに乗って槽内上部で浮遊している粉体成分
の一部はそのまま自重により棚状部16に落下して捕集
されることになる。したがって、排気口12からの強制
吸引との併用のためにその粉体成分の捕集効率が一段と
向上することになる。なお、棚状部16で捕集された粉
体成分は、粉体取出口17を適宜開くことでその取り出
しを容易に行える。
According to the third embodiment, the swirling air flow F generated in the tank has a relatively gentle flow in a portion corresponding to the large diameter portion 15.
A part of the powder component floating in the upper part of the tank on the swirling air flow F falls on the shelf 16 by its own weight and is collected. Therefore, the combined use with the forced suction from the exhaust port 12 further improves the collection efficiency of the powder component. The powder component collected by the shelf 16 can be easily removed by opening the powder outlet 17 as appropriate.

【0050】ここで、大径部15を形成せずに棚状部1
6を設けることも可能ではあるが、上記のように旋回空
気流Fの流れを緩やかにして粉体成分の捕集効率を高め
る上では、大径部15を形成した方が有利となる。
Here, without forming the large diameter portion 15,
Although it is possible to provide the large-diameter portion 15, it is advantageous to form the large-diameter portion 15 in order to reduce the flow of the swirling air flow F and increase the efficiency of collecting the powder component as described above.

【0051】図6,7は本発明に係る処理装置の好まし
い第4の実施の形態を示す図であって、図3に示した第
2の実施の形態と共通する部分には同一符号を付してあ
る。
FIGS. 6 and 7 are views showing a fourth preferred embodiment of the processing apparatus according to the present invention, in which parts common to those of the second embodiment shown in FIG. I have.

【0052】この第4の実施の形態では、処理槽1の下
端部のうち回転円板4よりも上方位置に、空気圧力源1
3に接続された空気噴射用配管18を槽自体の直径方向
に貫通するようにして横架する一方、この空気噴射用配
管18には撹拌流動中の粉砕片Pに向けて空気を直接的
に噴射する一対の空気噴射ノズル19を互いに逆向きに
接続してある。この空気噴射用配管18の設置位置とし
ては、撹拌流動中の粉砕片Pと常に接触し且つその接触
効率が最も高い位置が選定される。また、上記空気噴射
用配管18よりも上方位置には、粉砕片Pの撹拌方向R
の接線方向を指向するように一対の旋回空気流生成用の
空気噴射ノズル20を互いに逆向きに配置してある。
In the fourth embodiment, the air pressure source 1 is located above the rotary disk 4 at the lower end of the processing tank 1.
3 is pierced so as to penetrate in the diametrical direction of the tank itself, while the air is directly supplied to the crushed pieces P during the stirring flow. A pair of air jet nozzles 19 for jetting are connected in opposite directions. As the installation position of the air injection pipe 18, a position that is always in contact with the crushed pieces P during the stirring flow and has the highest contact efficiency is selected. Further, the stirring direction R of the crushed pieces P is located above the air injection pipe 18.
The pair of swirling air flow generating air jet nozzles 20 are arranged in opposite directions so as to be directed in the tangential direction of the swirling air flow.

【0053】すなわち、この第4の実施の形態では、撹
拌流動中の粉砕片Pに向けて直接的に空気を噴射する空
気噴射ノズル19と、槽内を周回しつつその下方から上
方に向かう螺旋状の旋回空気流Fを生成するための空気
噴射ノズル20とを相互に独立させ、その上で空気噴射
用配管18を積極的に粉砕片Pと衝突させるようにした
点に特徴がある。
That is, in the fourth embodiment, the air injection nozzle 19 for directly injecting air toward the crushed pieces P during the stirring and flowing, and the spiral spiraling from the lower part to the upper part while circulating in the tank. It is characterized in that the air injection nozzle 20 for generating the swirling air flow F is made independent of each other, and the air injection pipe 18 is positively collided with the crushed pieces P.

【0054】したがって、この第4の実施の形態によれ
ば、旋回流動中の粉砕片Pに向けて空気噴射ノズル19
から直接的に空気が噴射され、この直接的な空気噴射に
よって、粉砕片Pとともに撹拌されている粉体成分が粉
砕片Pそのものから分離されるようにして吹き飛ばされ
て、この吹き飛ばされた粉体成分は旋回空気流Fに乗っ
て上方に浮遊するようになる。これらの挙動は基本的に
は第2,3の実施の形態と同様である。
Therefore, according to the fourth embodiment, the air injection nozzle 19 is directed
Air is directly injected from the crushed piece P, and the powder component being stirred together with the crushed piece P is blown off by the direct air injection so as to be separated from the crushed piece P itself. The component floats upward on the swirling airflow F. These behaviors are basically the same as in the second and third embodiments.

【0055】その一方、本実施の形態では撹拌流動中の
粉砕片Pは常に空気噴射用配管18と衝突を繰り返して
いることから、その分だけ粉砕片Pに与えられる衝撃力
が増加し、粉砕片Pそのものからの塗膜の剥離効率と、
粉砕片Pからの粉体成分の分離効率とが一段と高められ
る。
On the other hand, in the present embodiment, since the crushed pieces P which are being stirred and flowed repeatedly collide with the air injection pipe 18, the impact force applied to the crushed pieces P increases by that much, and the crushed pieces P The peeling efficiency of the coating film from the piece P itself,
The efficiency of separating the powder component from the crushed pieces P is further enhanced.

【0056】この場合、空気噴射用配管18内を通流す
る空気を予め冷却しておくことにより、粉砕片Pと直接
衝突することになる配管壁面の温度上昇を抑制して、溶
融温度近くまで昇温している粉砕片Pの配管への付着を
未然に防止することができる。
In this case, by cooling the air flowing through the air injection pipe 18 in advance, the temperature rise of the pipe wall that directly collides with the crushed pieces P is suppressed, and the temperature is increased to near the melting temperature. It is possible to prevent the rising of the crushed pieces P from adhering to the pipe.

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

【図1】本発明に係る処理装置の好ましい第1の実施の
形態を示す構成説明図。
FIG. 1 is a configuration explanatory view showing a first preferred embodiment of a processing apparatus according to the present invention.

【図2】図1の処理槽内に配置される回転円板の拡大斜
視図。
FIG. 2 is an enlarged perspective view of a rotating disk arranged in the processing tank of FIG. 1;

【図3】本発明に係る処理装置の好ましい第2の実施の
形態を示す構成説明図。
FIG. 3 is a configuration explanatory view showing a second preferred embodiment of the processing apparatus according to the present invention.

【図4】図3の平面説明図。FIG. 4 is an explanatory plan view of FIG. 3;

【図5】本発明に係る処理装置の好ましい第3の実施の
形態を示す構成説明図。
FIG. 5 is a configuration explanatory view showing a third preferred embodiment of the processing apparatus according to the present invention.

【図6】本発明に係る処理装置の好ましい第4の実施の
形態を示す構成説明図。
FIG. 6 is a configuration explanatory view showing a preferred fourth embodiment of a processing apparatus according to the present invention.

【図7】図6の平面説明図。FIG. 7 is an explanatory plan view of FIG. 6;

【符号の説明】[Explanation of symbols]

1…処理槽 2…排気装置 4…回転円板(回転部材) 6…バッフルダクト(返し部材) 7…網状構造物 8…粉体排出口 12…排出口 14…空気噴射ノズル 15…大径部 16…棚状部 18…空気噴射用配管 19…空気噴射ノズル 20…旋回空気流生成用空気噴射ノズル F…旋回空気流 P…粉砕片 DESCRIPTION OF SYMBOLS 1 ... Processing tank 2 ... Exhaust device 4 ... Rotating disk (rotating member) 6 ... Baffle duct (return member) 7 ... Net structure 8 ... Powder discharge port 12 ... Discharge port 14 ... Air injection nozzle 15 ... Large diameter part Reference Signs List 16: shelf portion 18: air injection pipe 19: air injection nozzle 20: air injection nozzle for generating swirling air flow F: swirling air flow P: crushed piece

───────────────────────────────────────────────────── フロントページの続き (72)発明者 高瀬 朋視 広島県加茂郡河内町大字河戸743 高瀬合 成化学株式会社内 (72)発明者 土方 泰一 愛知県豊川市穂ノ原3丁目1番 新東工業 株式会社内 (72)発明者 小森 俊尚 愛知県豊川市穂ノ原3丁目1番 新東工業 株式会社内 (72)発明者 岡田 行雄 神奈川県横浜市神奈川区宝町2番地 日産 自動車株式会社内 (72)発明者 水谷 篤 神奈川県横浜市神奈川区宝町2番地 日産 自動車株式会社内 (72)発明者 西田 勉 神奈川県横浜市神奈川区宝町2番地 日産 自動車株式会社内 (72)発明者 小野寺 弘男 神奈川県横浜市神奈川区宝町2番地 日産 自動車株式会社内 Fターム(参考) 4D004 AA07 AA26 CA15 CA50 CB09 CB50 4D075 BB20Z DC13 EA02 4F201 AA50 AC04 AD11 AH24 BA04 BC02 BC12 BC25 BC37 BN29 BP05 BP12 BP31 BQ18 BQ21 BQ40 BQ44 4F301 AA14 BC38 BC58 BF05  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Tomomi Takase Hirose Prefecture Kamo-gun Kawachi-machi Ogata Kawato 743 Takasego Seikagaku Co., Ltd. (72) Inventor Taiichi Hijikata 3-1-1 Honohara, Toyokawa City, Aichi Prefecture Shinto Industrial Co., Ltd. (72) Inventor Toshihisa Komori 3-1-1 Honohara, Toyokawa City, Aichi Prefecture Shinto Kogyo Co., Ltd. Inventor Atsushi Mizutani 2 Takara-cho, Kanagawa-ku, Yokohama-shi, Kanagawa Nissan Motor Co., Ltd. (72) Inventor Tsutomu Nishida 2 Takara-cho, Kanagawa-ku, Yokohama-shi, Kanagawa Nissan Motor Co., Ltd. (72) Hiroo Onodera Yokohama-shi, Kanagawa 2F, Takaracho, Kanagawa-ku Nissan Motor Co., Ltd. F-term (reference) 4D004 AA07 AA26 CA15 CA50 CB09 CB50 4D075 BB20 Z DC13 EA02 4F201 AA50 AC04 AD11 AH24 BA04 BC02 BC12 BC25 BC37 BN29 BP05 BP12 BP31 BQ18 BQ21 BQ40 BQ44 4F301 AA14 BC38 BC58 BF05

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 予め所定の大きさに粉砕した塗膜付き熱
可塑性樹脂部品の粉砕片を処理槽内に収容するととも
に、その処理槽底部に配置した回転部材により粉砕片を
撹拌して粉砕片同士の相互摩擦衝突により塗膜を剥離さ
せるようにした塗膜付き樹脂部品の再生処理装置であっ
て、 前記処理槽の胴部内周に、撹拌に伴う遠心力によって槽
内外周部に寄せ集められた粉砕片の流動方向を上向き方
向から下向き方向に積極的に変更する返し部材を設ける
一方、 この返し部材のうち流動粉砕片が直接的に接する部分
に、粉砕片自体の通過を阻止しつつその粉砕片から剥離
した粉体成分の通過を許容する粉体排出口を形成すると
ともに、この粉体排出口を処理槽外部に臨ませ、 前記遠心力による粉砕片自体の流動により該粉砕片から
粉体成分を積極的に分離させて処理槽外部に排出するよ
うにしたことを特徴とする塗膜付き樹脂部品の再生処理
装置。
A crushed piece of a thermoplastic resin part with a coating film, which has been crushed to a predetermined size in advance, is accommodated in a processing tank, and the crushed piece is stirred by a rotating member disposed at the bottom of the processing tank. An apparatus for regenerating a resin part with a coating film in which a coating film is peeled off by mutual frictional collision between each other, wherein the resin part is gathered on the inner periphery of the body of the treatment tank by a centrifugal force caused by stirring. While providing a return member that positively changes the flow direction of the crushed pieces from the upward direction to the downward direction, the portion of the return member that is directly in contact with the flow crushed pieces is prevented while the crushed pieces themselves pass through. A powder outlet is formed to allow the passage of the powder component peeled from the crushed pieces, and the powder outlet is exposed to the outside of the treatment tank, and the powder from the crushed pieces flows by the flow of the crushed pieces themselves due to the centrifugal force. Aggressive body components A recycling apparatus for a resin part with a coating film, wherein the resin part is separated and discharged outside the processing tank.
【請求項2】 前記粉体排出口が処理槽外部の吸引手段
に接続されていて、粉砕片から分離した粉体成分が粉体
排出口から吸引排出されるようになっていることを特徴
とする請求項1に記載の塗膜付き樹脂部品の再生処理装
置。
2. The method according to claim 1, wherein the powder outlet is connected to suction means outside the processing tank, and the powder component separated from the crushed pieces is sucked and discharged from the powder outlet. The apparatus for reprocessing a resin part with a coating film according to claim 1.
【請求項3】 予め所定の大きさに粉砕した塗膜付き熱
可塑性樹脂部品の粉砕片を処理槽内に収容するととも
に、その処理槽底部に配置した回転部材により粉砕片を
撹拌して粉砕片同士の相互摩擦衝突により塗膜を剥離さ
せるようにした塗膜付き樹脂部品の再生処理装置であっ
て、 撹拌に伴う遠心流動によって槽内外周部に寄せ集められ
た粉砕片に向けて斜め方向から空気を噴射し、処理槽内
を周回しつつその処理槽内を下方から上方に向かって流
れる旋回空気流を生じさせることにより、前記粉砕片か
ら剥離した粉体成分を積極的に処理槽内の上部空間に浮
遊させ、 この浮遊している粉体成分を処理槽の上部に開口形成し
た排出口から外部に吸引排出するようにしたことを特徴
とする塗膜付き樹脂部品の再生処理装置。
3. A crushed piece of a thermoplastic resin part with a coating film, which has been crushed in advance to a predetermined size, is accommodated in a processing tank, and the crushed piece is stirred by a rotating member arranged at the bottom of the processing tank. This is a reprocessing device for resin parts with a coating film, in which the coating film is peeled off by mutual frictional collision between the two. By injecting air and generating a swirling airflow that flows upward from below in the processing tank while circulating in the processing tank, the powder component separated from the crushed pieces is positively in the processing tank. An apparatus for regenerating a resin part with a coating film, wherein the resin component is floated in an upper space, and the suspended powder component is sucked and discharged to the outside from a discharge port formed in an upper portion of a processing tank.
【請求項4】 前記処理槽内の上部に棚状部を形成し、
処理槽内の上部空間に浮遊している粉体成分の一部をこ
の棚状部にて自然落下により集めるようにしたことを特
徴とする請求項3に記載の塗膜付き樹脂部品の再生処理
装置。
4. A shelf-shaped part is formed in an upper part in the processing tank,
4. The resin part with a coating according to claim 3, wherein a part of the powder component floating in the upper space in the processing tank is collected by natural fall on the shelf. apparatus.
【請求項5】 前記処理槽の上端部内径を大径化し、こ
の大径部に棚状部を形成したことを特徴とする請求項4
に記載の塗膜付き樹脂部品の再生処理装置。
5. The process tank according to claim 4, wherein the inner diameter of the upper end portion of the processing tank is increased, and a shelf portion is formed in the large diameter portion.
A reprocessing apparatus for a resin part with a coating film according to item 1.
【請求項6】 予め所定の大きさに粉砕した塗膜付き熱
可塑性樹脂部品の粉砕片を処理槽内に収容するととも
に、その処理槽底部に配置した回転部材により粉砕片を
撹拌して粉砕片同士の相互摩擦衝突により塗膜を剥離さ
せるようにした塗膜付き樹脂部品の再生処理装置であっ
て、 前記処理槽内のうち回転部材よりも上方位置であって且
つ撹拌に伴う遠心流動によって槽内外周部に寄せ集めら
れた粉砕片と接する位置に空気噴射用配管を配置して、
この空気噴射用配管に接続した噴射ノズルから粉砕片に
向けて空気を噴射するとともに、 旋回空気流生成用の噴射ノズルから空気を噴射して処理
槽内を周回しつつその処理槽内を下方から上方に向かっ
て流れる旋回空気流を生じさせることにより、前記粉砕
片から剥離した粉体成分を積極的に処理槽内の上部空間
に浮遊させ、 この浮遊している粉体成分を処理槽の上部に開口形成し
た排出口から外部に吸引排出するようにしたことを特徴
とする塗膜付き樹脂部品の再生処理装置。
6. A pulverized piece of a thermoplastic resin part with a coating film, which has been pulverized to a predetermined size in advance, is accommodated in a processing tank, and the pulverized piece is stirred by a rotating member disposed at the bottom of the processing tank. A reprocessing apparatus for a resin part with a coating film, wherein the coating film is peeled off by mutual frictional collision between each other. Arrange the air injection pipe at the position in contact with the crushed pieces gathered at the inner and outer circumferences,
In addition to injecting air toward the crushed pieces from the injection nozzle connected to this air injection pipe, air is injected from the injection nozzle for swirling air flow generation, and the inside of the processing tank is circulated from below while rotating around the processing tank. By generating a swirling airflow that flows upward, the powder components separated from the crushed pieces are positively floated in the upper space in the processing tank, and the floating powder components are removed from the upper part of the processing tank. An apparatus for regenerating a resin part with a coating film, wherein the resin part is sucked and discharged to the outside from a discharge port formed in the opening.
JP20442999A 1999-07-19 1999-07-19 Recycling equipment for resin parts with coating film Expired - Fee Related JP4073580B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20442999A JP4073580B2 (en) 1999-07-19 1999-07-19 Recycling equipment for resin parts with coating film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20442999A JP4073580B2 (en) 1999-07-19 1999-07-19 Recycling equipment for resin parts with coating film

Publications (2)

Publication Number Publication Date
JP2001030244A true JP2001030244A (en) 2001-02-06
JP4073580B2 JP4073580B2 (en) 2008-04-09

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ID=16490401

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Country Link
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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011127507A1 (en) * 2010-04-16 2011-10-20 Erema Engineering Recycling Maschinen Und Anlagen Gesellschaft M.B.H. Lance
US9216522B2 (en) 2011-10-14 2015-12-22 Erema Engineering Recycling Maschinen Und Anlagen Gesellschaft M.B.H. Apparatus for the pretreatment and subsequent plastification of plastic material with melt filter
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