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JPH0558792B2 - - Google Patents
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JPH0558792B2 - - Google Patents

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Publication number
JPH0558792B2
JPH0558792B2 JP62191213A JP19121387A JPH0558792B2 JP H0558792 B2 JPH0558792 B2 JP H0558792B2 JP 62191213 A JP62191213 A JP 62191213A JP 19121387 A JP19121387 A JP 19121387A JP H0558792 B2 JPH0558792 B2 JP H0558792B2
Authority
JP
Japan
Prior art keywords
hot air
waste plastics
outlet
air stove
heated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP62191213A
Other languages
Japanese (ja)
Other versions
JPS6434482A (en
Inventor
Shigeru Yaguchi
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.)
MORUTON KK
Original Assignee
MORUTON 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 MORUTON KK filed Critical MORUTON KK
Priority to JP19121387A priority Critical patent/JPS6434482A/en
Publication of JPS6434482A publication Critical patent/JPS6434482A/en
Publication of JPH0558792B2 publication Critical patent/JPH0558792B2/ja
Granted 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
    • 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)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

(発明の利用分野) この発明は、廃プラスチツク類の減容処理装置
に関する。 (背景技術) 一口に廃プラスチツクと言つても、その中には
ポリエチレン、ポリプロピレン、ポリ塩化ビニー
ル、ポリエスチレン等の熱可塑性樹脂と、フエノ
ール樹脂、尿素樹脂のような熱硬化性樹脂が混在
して含まれている他、多くの場合、土砂、紙屑、
木片、布、生ゴミといつたその他の廃棄物をも含
まれているので、本願明細書においてはこれらの
ものが含まれている種々雑多な廃プラスチツクと
いうことで廃プラスチツク類と称する。 これらの廃プラスチツク類を減容処理する装置
としては従来、該廃プラスチツク類を常温状態で
圧縮させ、これに誘導加熱を加えて熱可塑性樹脂
を溶融軟化させ、これを接着剤として用いて減容
処理する方式のものと、該廃プラスチツク類を熱
風炉内に収容させて熱風を吹きつけ熱可塑性樹脂
を軟化溶融させた後、この軟化溶融樹脂を接着剤
替わりにして熱硬化性樹脂及びその他の廃棄物と
共に圧縮成型させて減容処理する方式のものとが
あるが、この発明は後者に属する。 この場合処理後の処理物の圧縮成型状態を維持
させるために低温で溶融する熱可塑性樹脂が均一
に混入させると共に、処理物に対して温度が均一
に加わるように配慮することが必要である他、熱
によつて軟化しない熱硬化性樹脂が口径を絞つた
排出口によりスムースに排出されるよう配慮する
ことが必要であつた。 また、廃プラスチツク類の大きさは、大小一定
するものではないので、漏斗状の熱風炉で下部に
排出口を設けたものは、特別な工夫を凝らさない
と、小さな廃プラスチツク類は加熱されることな
く排出口よりこぼれ落ちてしまう場合を生じた。
それではといつて、排出口の口径を小さくする
と、比較的大型の熱硬化性樹脂からなる廃プラス
チツクは、排出口に詰まつてしまい排出できない
場合を生ずるという問題があつた。 (技術的課題) この発明の目的は、熱風炉内に収容された廃プ
ラスチツク類を炉内で撹拌させて良く混合させる
ことができ、熱風が均一に加えられるように工夫
すると共に、縦型漏斗状の熱風炉を用いても大小
さまざまな形状と熱特性をもつ廃プラスチツク類
を効率よく減容処理することのできる、廃プラス
チツク類の減容処理装置を提供せんとするにあ
る。 (技術的手段) 上述した技術的課題を達成するためにこの発明
は、外周に複数のノズルを設けた漏斗状の熱風炉
を熱風滞溜室内に設け、この熱風炉の大径の上部
に投入口を小径の下部に排出口を設け、前記熱風
炉の軸心方向に前記排出口の内径と略一致する外
径を有するスクリユー羽根を備えた回転軸を前記
排出口にその一部を臨ませて設置すると共に、前
記排出口に前記熱風炉内の処理物のこぼれ落ちを
防止するシヤツター板を開閉自在に設け、もつて
前記熱風炉を外側より加熱させる一方前記ノズル
を介して熱風を前記熱風炉内に送り込み該熱風炉
内に収容させた熱可塑性樹脂と熱硬化性樹脂、及
びその他の廃棄物を含む種々雑多な廃プラスチツ
ク類を加熱させて前記熱可塑性樹脂を軟化溶融さ
せると共に、この軟化溶融の最中に前記スクリユ
ー羽根を適宜正方向或は逆方向へ回転させて収容
廃プラスチツク類の前記熱風炉内での撹拌と前記
シヤツター板を開いて処理物の前記排出口からの
強制排出を行なうものである。 (作用) 上述したように構成することにより、熱風炉内
で加熱の最中に回転軸を正方向、或は逆方向へ回
転させることによりスクリユー羽根によつて廃プ
ラスチツク類を撹拌させ、熱風の通りを良くして
廃プラスチツク類を均一に加熱することができ、
排出時には正方向へ回転させることにより半溶融
状態の処理物を排出口へ向けて強制的に送り出す
ことができる上に、大型の熱硬化性樹脂及びその
他の廃棄物の排出を容易にするために、熱風炉の
口径を大きくしても、小さな廃プラスチツク類が
熱処理されることなく、排出口よりこぼれ落ちて
しまうことを防止することができるものである。 (実施例) 以下にこの発明の一実施例を図面に基づいて詳
細に説明すると、1は外気取入用のブロワーであ
り、例えば灯油を燃料とするオイルバーナー2を
取りつけた熱風発生炉3に、通風管4を介して接
続されている。 この熱風発生炉3に隣接して、断熱壁で構築さ
れた熱風滞溜室5が設けられている。この熱風滞
溜室5内部には、漏斗状の熱風炉6が縦方向に収
納されている。この熱風炉6の大径の上部には投
入口7が、小径の下部には排出口8が設けられて
おり、上部にはさらに排気管9が取り付けられて
いる。熱風炉6はさらに外周に複数のノズル6
a,6a……がランダムに取り付けられている。 この熱風炉6内部には、上部から排出口8の内
径と略一致する外径を有するスクリユー羽根10
を備えた回転軸11が、該スクリユー羽根10を
排出口8に臨ませて軸心方向に回転自在に垂下さ
れており、この回転軸11はモータ12によつて
正逆方向に回転させられる。そして、熱風炉6の
排出口8には、例えば油圧駆動させられるシヤツ
ター板13が開閉自在に取り付けられると共に、
この排出口8に面してバケツト14が置かれてい
る。 次に、作用効果について説明すると、灯油等を
燃料とするバーナー2に点火がなされ、ブロワー
1がONされると、バーナー2によつて発生した
高温の燃焼ガスは、ブロワー1によつて取り入れ
られた外気によつて稀釈、温度低下させられて熱
風発生炉3より熱風滞溜室5へ導入され、熱風炉
6の外周に設けたノズル6a,6a……より炉内
部へ吹き込まれる。 これに前後してモータ12をONさせ、スクリ
ユー羽根10を適当な速度で逆方向に回転をさ
せ、熱風炉6内部がほぼ180℃〜200℃に達したの
を確認した後、投入口7より例えば装入コンベヤ
ー15を介してモルトプレン、発泡スチロール、
ポリエチレン等の熱可塑性樹脂やフエノール樹
脂、尿素樹脂のような熱硬化性樹脂及びその他の
廃棄物を含む種々雑多な廃プラスチツク類の混合
物を投入させてやると、比較的低い温度で軟化溶
融する熱可塑性樹脂が溶けて他の軟化溶融しない
樹脂その他の廃棄物の間に浸透しつつ、処理物全
体を接着させる。 この際、回転しているスクリユー羽根10によ
つて投入廃プラスチツク類が撹拌される結果、当
該炉内温度で軟化溶融する熱可塑性樹脂と軟化溶
融しない熱硬化性樹脂及びその他の廃棄物がよく
混ざり合う他、熱風が処理物に対して均一に通る
ことになるので、温度ムラが生ずることがなくほ
ぼ均一に加熱されることになるものである。 また、熱風炉6内に収納された廃プラスチツク
類のうち小さなものは、加熱される間もなくその
ままスクリユー羽根10と排出口8との間の間隙
を通つてバケツト14内へこぼれ落ちようとする
が、シヤツター板13によつて阻止され、該シヤ
ツター板13上部に溜り、ノズル6a,6a……
を介して吹き込まれてくる熱風によつて加熱され
軟化溶融させられる。 スクリユー羽根10の回転は場合によつては正
方向、或は逆方向へと交互になされる場合もある
し、回転が適宜間欠的になされる場合もある。 このようにして、投入から約3〜6分前後経過
すると、融点の低い樹脂が溶けて他の樹脂及びそ
の他の廃棄物の間に浸透するので、シヤツター板
13を開いてモーター12の回転方向を正方向に
させると、スクリユー羽根10によつて廃プラス
チツク類は排出口8へ送られ、ここよりバケツト
14内部へ排出される。 同時に投入口7からは、新たに廃プラスチツク
類が投入され、再び上述したような処理が行われ
排出口8より排出され、このようにして連続して
廃プラスチツク類の減容処理を行うことができる
ものである。スクリユー羽根10を用いると、こ
のような連続処理を行うのに便利であるが、この
ことはこのスクリユー羽根10を用いてバツチ処
理ができないことを意味するものではない。 第2図は連続処理とバツチ処理との処理能力を
比較したものであり、熱風炉の容積が増大するに
つれて、連続処理の方がバツチ処理の場合よりも
処理能力が飛躍的に増大することが解る。 いずれによる場合でも、排出された廃プラスチ
ツク類の処理物が適宜量になつた時にバケツト1
4を引き出して内容物を取り出すか、或はバケツ
ト14の代りに該バケツト14の位置か、別の場
所に設置した図示してない成型機で圧縮成型さ
せ、さらになる減容処理を行うものである。 成型機によらない場合でも、溶けた樹脂が溶け
ない樹脂その他の廃棄物の間に浸透して両者を接
着させるので、最初の状態よりも体積を約10分の
1程度に減少させることができる。上記いずれの
場合にも、溶けた熱可塑性樹脂が冷却することに
よつて、溶けていない熱硬化性樹脂及びその他の
廃棄物を接着させるので、処理物がバラバラにな
つて分解しまうことはない。 廃プラスチツク類中に紙、布、木片といつた、
発火し易い廃棄物が混入している場合には、熱風
炉6内で発火する場合を生ずるが、この場合には
図示してない噴霧器を用いて炉内部に水を噴霧さ
せて消火させたり、或は予め熱風を加湿させて熱
風炉6内へ吹き込むという手段によつて発火を防
止することもできよう。 熱風炉6内における処理温度は、廃プラスチツ
ク類の減容性能に大きな影響を及ぼすが、以下の
表に示されたように熱可塑性樹脂のほとんどは、
150℃〜160℃で軟化し、都市ゴミ系の廃プラスチ
ツク類の主成分である、ポリエチレン、ポリプロ
ピレン、ポリ塩化ビニール、及ポリスチレン等は
180℃までに溶融状態になるので、処理温度は150
℃以上にすることが望ましいことが解つた。
(Field of Application of the Invention) The present invention relates to a volume reduction treatment device for waste plastics. (Background technology) Waste plastics are a mixture of thermoplastic resins such as polyethylene, polypropylene, polyvinyl chloride, and polyethylene, and thermosetting resins such as phenolic resins and urea resins. In addition, in many cases, it contains earth and sand, waste paper,
Since it also includes other waste materials such as wood chips, cloth, and food scraps, in this specification, it is referred to as "waste plastics" to refer to the miscellaneous waste plastics that include these materials. Conventionally, equipment for reducing the volume of these waste plastics compresses the waste plastics at room temperature, applies induction heating to melt and soften the thermoplastic resin, and uses this as an adhesive to reduce the volume. In some cases, the waste plastics are placed in a hot air oven and hot air is blown to soften and melt the thermoplastic resin, and then this softened molten resin is used as an adhesive to produce thermosetting resins and other materials. There is a method in which the volume is reduced by compression molding together with the waste, and this invention belongs to the latter. In this case, in order to maintain the compression molded state of the processed material after treatment, it is necessary to mix the thermoplastic resin that melts at low temperatures uniformly, and to ensure that the temperature is uniformly applied to the processed material. It was necessary to ensure that the thermosetting resin, which does not soften with heat, can be smoothly discharged through a narrowed discharge port. In addition, the size of waste plastics is not constant, so if you use a funnel-shaped hot air stove with an outlet at the bottom, small waste plastics will be heated unless special measures are taken. There were cases where the liquid spilled out from the outlet without any problem.
However, if the diameter of the discharge port is made small, there is a problem in that relatively large waste plastics made of thermosetting resin may clog the discharge port and cannot be discharged. (Technical Problem) The purpose of this invention is to make it possible to stir the waste plastics stored in the hot air furnace and mix it well, and to make it possible to add hot air uniformly. It is an object of the present invention to provide a waste plastics volume reduction processing apparatus which can efficiently reduce the volume of waste plastics having various sizes and shapes and thermal characteristics even when using a hot blast furnace. (Technical Means) In order to achieve the above-mentioned technical problem, the present invention provides a funnel-shaped hot air stove with a plurality of nozzles on the outer periphery in a hot air storage chamber, and injects air into the upper part of the large diameter of this hot air stove. A discharge port is provided at the bottom with a small diameter, and a rotating shaft having a screw blade having an outer diameter that substantially matches the inner diameter of the discharge port is provided in the axial direction of the hot air stove, with a part of the rotating shaft facing the discharge port. At the same time, a shutter plate is provided at the discharge port so as to be openable and closable to prevent the material to be processed in the hot air stove from spilling out. A variety of miscellaneous waste plastics including thermoplastic resins, thermosetting resins, and other wastes are fed into the hot air oven and housed in the hot blast furnace, and the thermoplastic resins are heated to soften and melt the thermoplastic resins, and the softened and melted During this process, the screw blades are rotated in the forward or reverse direction as appropriate to stir the stored waste plastics in the hot blast furnace, and the shutter plate is opened to forcefully discharge the treated materials from the discharge port. It is something. (Function) By configuring as described above, by rotating the rotating shaft in the forward or reverse direction during heating in the hot air stove, the screw blades agitate the waste plastics, and the hot air is heated. Improves circulation and allows waste plastics to be heated evenly.
During discharge, by rotating in the forward direction, the semi-molten processed material can be forcibly sent toward the discharge port, and it also facilitates the discharge of large thermosetting resins and other waste. Even if the diameter of the hot air stove is increased, small waste plastics can be prevented from being heat-treated and falling out of the outlet. (Embodiment) An embodiment of the present invention will be described below in detail based on the drawings. Reference numeral 1 denotes a blower for taking in outside air, and a hot air generating furnace 3 equipped with an oil burner 2 that uses kerosene as fuel, for example. , are connected via a ventilation pipe 4. Adjacent to this hot air generating furnace 3, a hot air retention chamber 5 constructed with a heat insulating wall is provided. Inside this hot air storage chamber 5, a funnel-shaped hot air stove 6 is housed vertically. An input port 7 is provided at the large diameter upper portion of the hot air stove 6, an outlet port 8 is provided at the small diameter lower portion, and an exhaust pipe 9 is further provided at the upper portion. The hot air stove 6 further includes a plurality of nozzles 6 on the outer periphery.
a, 6a... are attached at random. Inside this hot air stove 6, screw blades 10 having an outer diameter substantially matching the inner diameter of the discharge port 8 are disposed from the top.
A rotary shaft 11 is rotatably suspended in the axial direction with the screw blade 10 facing the discharge port 8, and the rotary shaft 11 is rotated by a motor 12 in forward and reverse directions. For example, a hydraulically driven shutter plate 13 is attached to the discharge port 8 of the hot air stove 6 so as to be openable and closable.
A bucket 14 is placed facing this discharge port 8. Next, to explain the function and effect, when the burner 2, which uses kerosene as fuel, is ignited and the blower 1 is turned on, the high temperature combustion gas generated by the burner 2 is taken in by the blower 1. The hot air is diluted and the temperature is lowered by the outside air, and then introduced from the hot air generating furnace 3 into the hot air storage chamber 5, and then blown into the inside of the furnace through nozzles 6a, 6a, . . . provided on the outer periphery of the hot air furnace 6. Around this time, the motor 12 is turned on, the screw blade 10 is rotated in the opposite direction at an appropriate speed, and after confirming that the temperature inside the hot blast stove 6 has reached approximately 180°C to 200°C, the inlet port 7 is For example, maltprene, styrofoam,
When a mixture of various waste plastics including thermoplastic resins such as polyethylene, thermosetting resins such as phenolic resins and urea resins, and other waste materials is introduced, the heat that softens and melts at a relatively low temperature is generated. The plastic resin melts and penetrates between the other softened and unmelted resins and other waste materials, thereby bonding the entire treated object. At this time, as the input waste plastics are stirred by the rotating screw blade 10, thermoplastic resins that soften and melt at the temperature inside the furnace, thermosetting resins that do not soften and melt, and other wastes are well mixed. In addition to this, the hot air passes through the object uniformly, so there is no temperature unevenness and the object is heated almost uniformly. Furthermore, small pieces of waste plastic stored in the hot air stove 6 tend to spill into the bucket 14 through the gap between the screw blade 10 and the discharge port 8 before being heated; It is blocked by the plate 13 and accumulates on the upper part of the shutter plate 13, and the nozzles 6a, 6a...
It is heated by the hot air blown through it and is softened and melted. Depending on the situation, the screw blade 10 may be rotated alternately in the forward direction or in the reverse direction, or may be rotated intermittently as appropriate. In this way, after approximately 3 to 6 minutes have elapsed since the injection, the resin with a low melting point melts and permeates between other resins and other waste, so the shutter plate 13 is opened and the direction of rotation of the motor 12 is adjusted. When turned in the forward direction, the waste plastics are sent to the discharge port 8 by the screw blade 10, and are discharged from there into the interior of the bucket 14. At the same time, new waste plastics are inputted from the input port 7, subjected to the above-described treatment, and then discharged from the discharge port 8. In this way, the volume of waste plastics can be continuously reduced. It is possible. Although the screw blade 10 is convenient for performing such continuous processing, this does not mean that batch processing cannot be performed using the screw blade 10. Figure 2 compares the processing capacity of continuous processing and batch processing, and shows that as the volume of the hot blast stove increases, the processing capacity of continuous processing increases dramatically compared to batch processing. I understand. In either case, when the amount of waste plastics to be processed reaches an appropriate amount, one bucket is
4 to take out the contents, or instead of the bucket 14, compression molding is performed using a molding machine (not shown) installed at the location of the bucket 14 or at a different location to further reduce the volume. be. Even if a molding machine is not used, the molten resin penetrates between the unmelted resin and other waste and bonds them together, making it possible to reduce the volume to about one-tenth of the original size. . In any of the above cases, as the melted thermoplastic resin cools, it adheres the unmelted thermosetting resin and other waste materials, so that the material to be treated does not fall apart and decompose. Paper, cloth, and wood chips were found in the waste plastics.
If ignitable waste is mixed in, a fire may occur inside the hot blast furnace 6, but in this case, a sprayer (not shown) may be used to spray water into the inside of the furnace to extinguish the fire. Alternatively, ignition could be prevented by humidifying the hot air beforehand and blowing it into the hot air stove 6. The processing temperature in the hot air stove 6 has a large effect on the volume reduction performance of waste plastics, but as shown in the table below, most of the thermoplastic resins
Polyethylene, polypropylene, polyvinyl chloride, polystyrene, etc., which soften at 150℃ to 160℃ and are the main components of municipal waste plastics,
Since it becomes molten by 180℃, the processing temperature is 150℃.
It was found that it is desirable to keep the temperature above ℃.

【表】【table】

【表】 他方、処理温度をあげすぎると、廃プラスチツ
ク類の熱分解が起り、煙や臭気を発生させるの
で、処理温度の上限は200℃程度とし、結局のと
ころ上述した都市ゴミ系の廃プラスチツク類は
180℃〜200℃程度の処理温度が最も望ましいこと
が解つた。 この処理温度は当然のことながら、減容処理さ
せる廃プラスチツク類の種類、配分割合等によつ
て変動し、一定するものではない。 次に減容性能についても、廃プラスチツク類の
組成によつて種々に異なるが、上述した都市ゴミ
系のものでは、熱風炉6内での減容率は約10分の
1で成型プレスによる成型後では40分の1程度に
なつた。他方、発泡スチロールが主成分の場合
は、成型後で100分の1、異物や熱硬化性樹脂が
多く混入している場合には、成型後で20分の1な
いし30分の1程度であつた。 (効果) 以上詳細に説明したようにこの発明によれば、
熱風炉内にスクリユー羽根を設けた回転軸を設け
ることにより、加熱時には投入物の撹拌を行い均
一に加熱されるようにして処理効率及び熱効率を
上げることができる他、小さな処理物が減容、或
は溶融されることなく排出口よりこぼれ落ちてし
まうことを防止でき、さらに、大型のとくに熱硬
化性の廃プラスチツクその他の廃棄物を容易に排
出口より排出することができ、その上連続的に減
容処理を行うことができるという、効果を奏し得
る。
[Table] On the other hand, if the processing temperature is raised too high, the waste plastics will thermally decompose, producing smoke and odors. The kind is
It has been found that a treatment temperature of about 180°C to 200°C is most desirable. This treatment temperature naturally varies depending on the type of waste plastics to be subjected to volume reduction treatment, the distribution ratio, etc., and is not constant. Next, the volume reduction performance also varies depending on the composition of waste plastics, but in the case of the above-mentioned municipal waste, the volume reduction rate in the hot blast furnace 6 is about 1/10, and the volume reduction rate is about 1/10 when molded using a molding press. Later, it was reduced to about 1/40. On the other hand, when Styrofoam was the main component, the strength was 1/100 after molding, and when a large amount of foreign matter or thermosetting resin was mixed in, it was about 1/20 to 1/30 after molding. . (Effects) As explained in detail above, according to the present invention,
By installing a rotating shaft equipped with screw blades inside the hot blast furnace, the input material is stirred during heating to ensure uniform heating, increasing processing efficiency and thermal efficiency, as well as reducing the volume of small processed materials. Alternatively, it is possible to prevent spilling from the discharge port without being melted, and furthermore, large-sized waste plastics, especially thermosetting plastics, and other waste can be easily discharged from the discharge port, and furthermore, it can be continuously disposed of. The effect of being able to perform volume reduction processing can be achieved.

【図面の簡単な説明】[Brief explanation of the drawing]

図面はこの発明の一実施例を示し、第1図はこ
の発明を概略的に示す縦断面図、第2図はこの発
明に係る廃プラスチツク類の減容処理装置の処理
能力を示す図面である。 1……ブロワー、2……オイルバーナー、3…
…熱風発生炉、5……熱風滞溜室、6……熱風
炉、6a,6a……ノズル、7……投入口、8…
…排出口、10……スクリユー羽根、11……回
転軸、12……モーター、13……シヤツター
板。
The drawings show an embodiment of the present invention, FIG. 1 is a vertical sectional view schematically showing the invention, and FIG. 2 is a drawing showing the processing capacity of the waste plastics volume reduction processing apparatus according to the invention. . 1...Blower, 2...Oil burner, 3...
...Hot air generation furnace, 5...Hot air retention chamber, 6...Hot air furnace, 6a, 6a...Nozzle, 7...Inlet, 8...
...Discharge port, 10...Screw blade, 11...Rotating shaft, 12...Motor, 13...Shutter plate.

Claims (1)

【特許請求の範囲】[Claims] 1 外周に複数のノズルを設けた漏斗状の熱風炉
を熱風滞溜室内に設け、この熱風炉の大径の上部
に投入口を小径の下部に排出口を設け、前記熱風
炉の軸心方向に前記排出口の内径と略一致する外
径を有するスクリユー羽根を備えた回転軸を前記
排出口にその一部を臨ませて設置すると共に、前
記排出口に前記熱風炉内の処理物のこぼれ落ちを
防止するシヤツター板を開閉自在に設け、もつて
前記熱風炉を外側より加熱させる一方前記ノズル
を介して熱風を前記熱風炉内に送り込み該熱風炉
内に収容させた熱可塑性樹脂と熱硬化性樹脂、及
びその他の廃棄物を含む種々雑多な廃プラスチツ
ク類を加熱させて前記熱可塑性樹脂を軟化溶融さ
せると共に、この軟化溶融の最中に前記スクリユ
ー羽根を適宜正方向或は逆方向へ回転させて収容
廃プラスチツク類の前記熱風炉内での撹拌と前記
シヤツター板を開いて処理物の前記排出口からの
強制排出を行なうことを特徴とする、廃プラスチ
ツク類の減容処理装置。
1. A funnel-shaped hot air stove with a plurality of nozzles on the outer periphery is provided in a hot air storage chamber, an inlet is provided at the upper part of the large diameter of this hot air stove, and an outlet is provided at the lower part of the small diameter, and A rotary shaft equipped with a screw blade having an outer diameter that substantially matches the inner diameter of the outlet is installed with a part thereof facing the outlet, and a rotary shaft is installed with a part thereof facing the outlet, and the material to be processed in the hot blast furnace is not spilled into the outlet. A shutter plate is provided that can be opened and closed to prevent the hot air from burning, and the hot air stove is heated from the outside, while hot air is sent into the hot air stove through the nozzle, and the thermoplastic resin and thermosetting resin accommodated in the hot air stove are heated. Various miscellaneous waste plastics including resins and other wastes are heated to soften and melt the thermoplastic resin, and during this softening and melting, the screw blade is rotated in the forward or reverse direction as appropriate. A volume reduction processing apparatus for waste plastics, characterized in that the collected waste plastics are agitated in the hot blast furnace, and the waste plastics to be treated are forcibly discharged from the discharge port by opening the shutter plate.
JP19121387A 1987-07-30 1987-07-30 Apparatus for volume reduction treatment of waste plastic Granted JPS6434482A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19121387A JPS6434482A (en) 1987-07-30 1987-07-30 Apparatus for volume reduction treatment of waste plastic

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19121387A JPS6434482A (en) 1987-07-30 1987-07-30 Apparatus for volume reduction treatment of waste plastic

Publications (2)

Publication Number Publication Date
JPS6434482A JPS6434482A (en) 1989-02-03
JPH0558792B2 true JPH0558792B2 (en) 1993-08-27

Family

ID=16270789

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19121387A Granted JPS6434482A (en) 1987-07-30 1987-07-30 Apparatus for volume reduction treatment of waste plastic

Country Status (1)

Country Link
JP (1) JPS6434482A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108556166B (en) * 2018-01-26 2020-06-02 重庆市长寿区分素装饰工程有限责任公司 Coating grinding and stirring device

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5117253U (en) * 1974-07-25 1976-02-07
JPS59159313A (en) * 1983-03-01 1984-09-08 Moruton Hanbai Kk Apparatus for melting treatment of foamed waste plastic
JPS59159312A (en) * 1983-03-01 1984-09-08 Moruton Hanbai Kk Apparatus for melting treatment of waste plastic

Also Published As

Publication number Publication date
JPS6434482A (en) 1989-02-03

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