JP2001062333A - Method and apparatus for separating and recovering polyethylene resin and vinyl chloride resin from nugget refuse - Google Patents
Method and apparatus for separating and recovering polyethylene resin and vinyl chloride resin from nugget refuseInfo
- Publication number
- JP2001062333A JP2001062333A JP23900399A JP23900399A JP2001062333A JP 2001062333 A JP2001062333 A JP 2001062333A JP 23900399 A JP23900399 A JP 23900399A JP 23900399 A JP23900399 A JP 23900399A JP 2001062333 A JP2001062333 A JP 2001062333A
- Authority
- JP
- Japan
- Prior art keywords
- kiln
- water
- polyethylene resin
- vinyl chloride
- nugget
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/28—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
- B03B5/30—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions
- B03B5/36—Devices therefor, other than using centrifugal force
- B03B5/42—Devices therefor, other than using centrifugal force of drum or lifting wheel type
Landscapes
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ナゲット屑と呼ば
れるポリエチレン樹脂と塩化ビニール樹脂との混合物か
らポリエチレン樹脂及び塩化ビニール樹脂を分離し、回
収する方法及び装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for separating and recovering polyethylene resin and vinyl chloride resin from a mixture of polyethylene resin and vinyl chloride resin, which is called nugget waste.
【0002】[0002]
【従来の技術】配電盤の配線などに使用される銅電線
は、使用済み後においては、粉砕して比重選別によりコ
アと外被とが分離され、コアは銅材として再利用され
る。外被は、コアから分離された後粉砕され、ポリエチ
レン樹脂と塩化ビニール樹脂との混合物であるナゲット
屑とされ、廃棄されるか、或は、焼却される。2. Description of the Related Art After being used, a copper wire used for wiring of a switchboard or the like is crushed and separated into a core and a jacket by specific gravity sorting, and the core is reused as a copper material. The jacket is pulverized after being separated from the core, turned into nugget waste, which is a mixture of polyethylene resin and vinyl chloride resin, and discarded or incinerated.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、ポリエ
チレン樹脂と塩化ビニール樹脂との混合物であるナゲッ
ト屑を廃棄したり、或は、焼却することは、環境上問題
がある。又、このようなポリエチレン樹脂及び塩化ビニ
ール樹脂は、回収して再利用することが望ましい。However, disposal or incineration of nugget waste, which is a mixture of a polyethylene resin and a vinyl chloride resin, has environmental problems. It is desirable that such polyethylene resin and vinyl chloride resin be collected and reused.
【0004】従って、本発明の目的は、ナゲット屑と呼
ばれるポリエチレン樹脂と塩化ビニール樹脂との混合物
からポリエチレン樹脂及び塩化ビニール樹脂を、簡単に
且つ有効に分離し、回収することのできる分離、回収方
法及び装置を提供することである。Accordingly, it is an object of the present invention to provide a method for separating and recovering polyethylene resin and vinyl chloride resin easily and effectively from a mixture of polyethylene resin and vinyl chloride resin called nugget waste. And an apparatus.
【0005】[0005]
【課題を解決するための手段】上記目的は本発明に係る
ナゲット屑からポリエチレン樹脂と塩化ビニール樹脂を
分離し、回収する方法及び装置にて達成される。要約す
れば、本発明の一態様によると、(a)長手軸線方向両
端部に入口及び出口を備え、且つ内壁面に螺旋手段を形
成した円筒状回転体を、入口側が低くなるように傾斜さ
せて長手軸線の回りに回転させ、且つ入口側に堰を設け
て前記円筒状回転体内に水を貯溜可能に構成し、(b)
前記円筒状回転体入口側からポリエチレン樹脂破砕物と
塩化ビニル樹脂破砕物との混合物からなるナゲット屑を
前記円筒状回転体内へと装入して、ポリエチレン樹脂破
砕物を水面上に浮上させ、且つ、塩化ビニル樹脂破砕物
は沈降させ、(c)前記円筒状回転体出口側から水を円
筒状回転体内へと噴霧し、前記水面上に浮上したポリエ
チレン樹脂破砕物を前記円筒状回転体入口側から水と共
に前記堰を越えて前記円筒状回転体外へと流出させてポ
リエチレン樹脂破砕物を回収し、そして、(d)前記円
筒状回転体底部に沈降した塩化ビニル樹脂破砕物は、前
記螺旋手段により前記円筒状回転体出口側から水と共に
前記円筒状回転体外へと流出させて回収する、ことを特
徴とするナゲット屑からポリエチレン樹脂と塩化ビニル
樹脂とを分離し、回収する方法が提供される。本発明の
一実施態様によると、前記螺旋手段は、前記円筒状回転
体の内壁面に設けた螺旋羽根であるか、又は、前記円筒
状回転体の内面に形成した螺旋溝である。The above object is achieved by a method and apparatus for separating and recovering polyethylene resin and vinyl chloride resin from nugget waste according to the present invention. In summary, according to one embodiment of the present invention, (a) a cylindrical rotating body having an inlet and an outlet at both ends in the longitudinal axis direction and having a spiral means formed on an inner wall surface is inclined so that the inlet side is lowered. (B) rotating around the longitudinal axis and providing a weir on the inlet side so that water can be stored in the cylindrical rotating body.
Nugget waste consisting of a mixture of the crushed polyethylene resin and the crushed vinyl chloride resin is charged into the cylindrical rotator from the inlet side of the cylindrical rotating body, and the polyethylene resin crushed material floats on the water surface, and The crushed polyvinyl chloride resin is allowed to settle, and (c) water is sprayed from the outlet side of the cylindrical rotator into the cylindrical rotator, and the crushed polyethylene resin material floating on the water surface is moved toward the inlet of the cylindrical rotator. From the cylindrical rotary body through the weir together with the water to collect the crushed polyethylene resin, and (d) the crushed polyvinyl chloride resin settled at the bottom of the cylindrical rotary body is removed by the helical means. By separating the polyethylene resin and the vinyl chloride resin from the nugget waste, which is collected by flowing out of the cylindrical rotary body with water from the outlet side of the cylindrical rotary body to the outside and recovering the same, How to yield is provided. According to one embodiment of the present invention, the spiral means is a spiral blade provided on an inner wall surface of the cylindrical rotating body, or a spiral groove formed on an inner surface of the cylindrical rotating body.
【0006】本発明の他の態様によると、(a)入口及
び出口を備え、内壁面には螺旋手段を設け、前記入口に
は堰を有し、内部に水を貯溜することのできるキルン
と、(b)前記キルンをキルン入口側が出口側より低く
なるようにして長手軸線方向に回転自在に保持する支持
手段と、(c)前記キルンを回転駆動する手段と、
(d)前記キルン入口側からポリエチレン樹脂破砕物と
塩化ビニル樹脂破砕物との混合物からなるナゲット屑を
前記キルン内へと装入するためのシュート手段と、
(e)前記キルン出口側から水を前記キルン内へと噴霧
する水噴射手段と、を備え、水面上に浮上したポリエチ
レン樹脂破砕物を前記キルン入口側から水と共に前記堰
を越えて前記キルン外へと流出させ、一方、前記キルン
底部に沈降した塩化ビニル樹脂破砕物は前記キルンと共
に回転する前記螺旋手段により前記キルン出口側から水
と共にキルン外へと流出させて回収する、ことを特徴と
するナゲット屑からポリエチレン樹脂と塩化ビニル樹脂
とを分離し、回収する装置が提供される。本発明の一実
施態様によると、前記螺旋手段は、前記キルンの内壁面
に配置した螺旋羽根であるか、或は、前記キルンの内壁
面に形成した螺旋溝とされる。又、本発明の他の実施態
様によると、前記キルンの入口に近接して、外部に脱水
装置が設けられる。好ましくは、前記脱水装置の上面に
網目スクリーンを設置し、更に好ましくは、前記脱水装
置の網目スクリーンを振動させることができる。According to another aspect of the present invention, there is provided (a) a kiln having an inlet and an outlet, a spiral means provided on an inner wall surface, a weir at the inlet, and capable of storing water therein. (B) support means for holding the kiln rotatably in the longitudinal axis direction such that the kiln inlet side is lower than the outlet side, and (c) means for rotationally driving the kiln;
(D) a chute means for charging nugget waste comprising a mixture of crushed polyethylene resin and crushed vinyl chloride resin into the kiln from the kiln inlet side;
(E) water jetting means for spraying water from the kiln outlet side into the kiln, wherein the polyethylene resin crushed material floating on the water surface passes through the weir together with the water from the kiln inlet side to the outside of the kiln. While the crushed vinyl chloride resin settled at the bottom of the kiln flows out of the kiln outlet along with the water by the spiral means rotating together with the kiln and is collected outside the kiln. An apparatus for separating and collecting polyethylene resin and vinyl chloride resin from nugget waste is provided. According to one embodiment of the present invention, the spiral means is a spiral blade disposed on an inner wall surface of the kiln, or a spiral groove formed on an inner wall surface of the kiln. According to another embodiment of the present invention, an external dewatering device is provided near the kiln inlet. Preferably, a mesh screen is installed on the upper surface of the dehydrator, and more preferably, the mesh screen of the dehydrator can be vibrated.
【0007】[0007]
【発明の実施の形態】以下、本発明に係るナゲット屑か
らポリエチレン樹脂と塩化ビニール樹脂を分離し、回収
する方法及び装置を図面に則して更に詳しく説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A method and an apparatus for separating and recovering a polyethylene resin and a vinyl chloride resin from nugget waste according to the present invention will be described in more detail with reference to the drawings.
【0008】実施例1 図1及び図2に、本発明に係る分離、回収装置の一実施
例を示す。本実施例にて、分離、回収装置1は、一端が
入口3とされ、他端が出口4とされる概略円筒形状とさ
れる回転体であるキルン2を有する。キルン2は、長手
方向軸線(O)の回りに回転し得るように軸受け手段5
を介して支持手段6にて担持されている。又、キルン2
は、入口3側が出口4側より低くなるように支持されて
いる。更に、キルン2は、駆動手段10にて所定の回転
速度にて回転される。駆動手段10としては、例えば、
図示するように、キルンの胴部に配置した被駆動歯車1
1と、この被駆動歯車11に噛合する駆動歯車12を備
えた電動機13とにて構成することができる。Embodiment 1 FIGS. 1 and 2 show an embodiment of a separation and recovery apparatus according to the present invention. In the present embodiment, the separation / recovery device 1 has a kiln 2 which is a rotating body having a substantially cylindrical shape, one end of which is an inlet 3 and the other end of which is an outlet 4. The kiln 2 is provided with bearing means 5 such that it can rotate about a longitudinal axis (O).
And supported by the support means 6. Also kiln 2
Are supported such that the inlet 3 side is lower than the outlet 4 side. Further, the kiln 2 is rotated by the driving means 10 at a predetermined rotation speed. As the driving means 10, for example,
As shown, the driven gear 1 disposed on the body of the kiln
1 and a motor 13 having a driving gear 12 meshed with the driven gear 11.
【0009】本実施例では、キルン2は、内径(D)が
700mm、長さ(L)が4mとされ、長手方向回転軸
線(O)は、水平に対して角度(α)4゜だけ傾斜して
配置された。又、キルン2は、通常、1〜10rpmに
て回転される。In this embodiment, the kiln 2 has an inner diameter (D) of 700 mm, a length (L) of 4 m, and a longitudinal rotation axis (O) inclined by an angle (α) 4 ° with respect to the horizontal. Was placed. The kiln 2 is normally rotated at 1 to 10 rpm.
【0010】本発明によると、キルン内壁面2Aには螺
旋手段20が形成される。螺旋手段20は、本実施例で
は、キルン2と共に回転する螺旋状の羽根20とされ
る。According to the present invention, the spiral means 20 is formed on the kiln inner wall surface 2A. In this embodiment, the spiral means 20 is a spiral blade 20 that rotates together with the kiln 2.
【0011】螺旋羽根20の形状、寸法は、所望に応じ
て任意に設計することができるが、キルン内壁面からの
高さ(h)が50〜300mmとなるように厚さ(t)
が3〜5mmの鋼板をピッチ(p)100〜400mm
にて螺旋状に形成して、キルン内壁面に取付けることに
より作製される。本実施例では、厚さ(t)3.2mm
の鋼板を使用し、高さ(h)を100mm、ピッチ
(P)を300mmとした螺旋羽根20をキルン内壁面
2Aに取付けることにより良好な結果を得ることができ
た。The shape and dimensions of the spiral blade 20 can be arbitrarily designed as desired, but the thickness (t) is such that the height (h) from the inner wall of the kiln is 50 to 300 mm.
Is 3-5mm steel plate pitch (p) 100-400mm
And formed on the inner wall of the kiln. In this embodiment, the thickness (t) is 3.2 mm.
Good results could be obtained by attaching the spiral blade 20 having a height (h) of 100 mm and a pitch (P) of 300 mm to the kiln inner wall surface 2A using the steel plate of No. 1 above.
【0012】キルン2の入口3には、傾斜したキルン内
部に水を保持するための堰7が設けられる。本実施例で
は、入口3に中心穴8を備えた端部壁を設けることによ
り、堰7を構成した。本実施例で、堰7の高さ(H)は
200mmとした。又、キルン入口3には、コンベアベ
ルトなどの搬送手段30により搬送されるナゲット屑1
00をキルン2内へと装入するシュート手段31が端部
壁中心穴8を貫通して配置され、更に、キルン入口3に
隣接した外側下方には、脱水装置32が配置される。At the entrance 3 of the kiln 2, there is provided a weir 7 for retaining water inside the inclined kiln. In this embodiment, the weir 7 is formed by providing an end wall having a center hole 8 at the entrance 3. In this embodiment, the height (H) of the weir 7 was set to 200 mm. In the kiln entrance 3, nugget waste 1 conveyed by conveying means 30 such as a conveyor belt is provided.
A chute means 31 for charging 00 into the kiln 2 is disposed through the center hole 8 of the end wall, and a dewatering device 32 is disposed below the outer side adjacent to the kiln inlet 3.
【0013】脱水装置32は、容器33を有する。容器
33は、例えば漏斗状とされ、底部に排水口34が形成
され、上部開口部には、網目スクリーン35が設けられ
る。容器上部開口部は、即ち、スクリーン35は、一方
向へと、本実施例では、図1にて左側方向へと傾斜して
設けられている。スクリーン35は適当なサイズのメッ
シュ(網目)を有し、本実施例では、ナゲット屑100
が2〜3mm程度の大きさとされたので、1m/m目の
スクリーン35を用いた。The dehydrator 32 has a container 33. The container 33 has, for example, a funnel shape, a drain port 34 is formed at the bottom, and a mesh screen 35 is provided at the upper opening. The container upper opening, that is, the screen 35 is provided so as to be inclined in one direction, and in this embodiment, to the left side in FIG. The screen 35 has a mesh (mesh) of an appropriate size, and in this embodiment, the nugget waste 100
Was about 2 to 3 mm, so a 1 m / m screen 35 was used.
【0014】一方、本発明によれば、キルン出口4に位
置してキルン内壁面へと水を噴射する水噴射(スプレ
ー)手段36を配置する。スプレー手段36としては、
例えば、株式会社ニイクラ製のEX2タイプ(商品名)
などを有効に使用することができる。On the other hand, according to the present invention, a water injection (spray) means 36 is provided at the kiln outlet 4 for injecting water to the kiln inner wall surface. As the spraying means 36,
For example, EX2 type (product name) manufactured by Niikura Co., Ltd.
Etc. can be used effectively.
【0015】次に、本発明に係る上記構成の分離、回収
装置1の作動について説明する。Next, the operation of the separation / recovery device 1 having the above-described structure according to the present invention will be described.
【0016】キルン2は駆動手段10により所定の回転
速度で、本実施例では4rpmで回転される。一方、キ
ルン出口4に配置したスプレー手段36からは、キルン
内壁へと8000L(リットル)/hrにて水が噴射さ
れる。従って、キルン内部には、水が溜まり、余分な水
は、入口3の堰7を越えて、更には、出口4からキルン
外へと流出する。The kiln 2 is rotated by the driving means 10 at a predetermined rotational speed, in this embodiment at 4 rpm. On the other hand, water is sprayed from the spray means 36 arranged at the kiln outlet 4 to the inner wall of the kiln at 8000 L (liter) / hr. Therefore, water accumulates inside the kiln, and excess water flows out of the kiln through the weir 7 at the inlet 3 and further from the outlet 4.
【0017】粉砕されて直径2〜3mmの破砕物とされ
たポリエチレン樹脂101と塩化ビニール樹脂102の
混合物からなるナゲット屑100が搬送手段30及びシ
ュート手段31によりキルン内部へと、例えば、150
kg/hrにて供給される。本実施例では、シュート手
段31により、ナゲット屑100は、キルン2の内方へ
と堰7より距離(L1)0.5〜1.0mの位置に供給
したが、この位置は、シュート手段31の長さを調整す
ることにより適宜位置決めされる。The nugget scrap 100 made of a mixture of the polyethylene resin 101 and the vinyl chloride resin 102 which has been pulverized into a crushed product having a diameter of 2 to 3 mm is introduced into the kiln by the conveying means 30 and the chute means 31, for example, 150 mm.
kg / hr. In this embodiment, the chute means 31 supplies the nugget debris 100 to the inside of the kiln 2 at a distance (L1) of 0.5 to 1.0 m from the weir 7. The position is appropriately determined by adjusting the length.
【0018】キルン2内へと装入されたナゲット屑10
0は、キルン内に貯溜した水中へと送給されることによ
り、ポリエチレン樹脂破砕物101は水面に浮き、塩化
ビニール樹脂破砕物102は沈降する。従って、水面に
浮いたポリエチレン樹脂破砕物101は、キルン内部を
流れる水と共に堰7を越えてキルン外へと溢流し、脱水
装置32へと流出する。Nugget waste 10 charged into kiln 2
When 0 is fed into the water stored in the kiln, the crushed polyethylene resin material 101 floats on the water surface, and the crushed vinyl chloride resin material 102 sinks. Therefore, the crushed polyethylene resin material 101 floating on the water surface flows over the weir 7 to the outside of the kiln together with the water flowing inside the kiln, and flows out to the dewatering device 32.
【0019】脱水装置32の上面には、スクリーン35
が配置されているため、水だけが容器33内へと流れ、
底部の排出口34を介して排出される。一方、スクリー
ン35の上に残ったポリエチレン樹脂破砕物101は、
スクリーン35の傾斜面に沿って流下し、適当な網目と
される網籠37内に溜められる。スクリーン35の傾斜
面に沿ったポリエチレン樹脂破砕物101の脱水及び移
動を促進するために、振動篩を設置することができる。
振動篩は、例えば、古河金属機械株式会社製のリップル
フロ型(商品名)などを有効に使用することができる。On the upper surface of the dehydrator 32, a screen 35 is provided.
Is arranged, only water flows into the container 33,
It is discharged through the outlet 34 at the bottom. On the other hand, the crushed polyethylene resin material 101 remaining on the screen 35 is
It flows down along the inclined surface of the screen 35 and is stored in a mesh basket 37 which is an appropriate mesh. A vibrating sieve can be provided to facilitate dewatering and movement of the crushed polyethylene resin 101 along the inclined surface of the screen 35.
As the vibrating sieve, for example, a ripple flow type (trade name) manufactured by Furukawa Metal Machine Co., Ltd. can be effectively used.
【0020】本発明者らの実験によれば、網籠37内に
回収されたポリエチレン樹脂破砕物101中に塩化ビニ
ル樹脂破砕物102は全く含まれていなかった。又、網
籠37内に回収されたポリエチレン樹脂破砕物101中
の水分含有量は、22.6%であった。この回収された
ポリエチレン樹脂破砕物101は、更に、脱水機(図示
せず)にて水分含有量が4.4%程度にまで脱水するこ
とができる。回収されたポリエチレン樹脂破砕物101
は、通常、燃料として使用される。According to the experiments of the present inventors, the crushed polyethylene resin 101 collected in the net basket 37 did not contain the crushed vinyl chloride resin 102 at all. The water content in the crushed polyethylene resin material 101 collected in the net basket 37 was 22.6%. The collected crushed polyethylene resin 101 can be further dehydrated by a dehydrator (not shown) to a water content of about 4.4%. Recovered crushed polyethylene resin 101
Is usually used as fuel.
【0021】又、キルン底部へと沈降した塩化ビニール
樹脂破砕物102は、回転するキルン2の内壁に形成し
た螺旋羽根20によって、キルン出口4側へと案内さ
れ、キルン出口4から一部の水と共にキルン外へと流出
し、適当な網目とされる網籠38内に溜められる。この
とき、キルン内壁或は螺旋羽根20に付着してキルン出
口4へと搬送されてきたポリエチレン樹脂破砕物101
は、スプレー手段36にて洗浄され、水と共にキルン入
口3の方へと流動される。従って、網籠38内に回収さ
れた塩化ビニール樹脂破砕物102中のポリエチレン樹
脂破砕物101の含有量は、微量であり、本発明者らの
実験の結果によると、0.5%(重量)であった。又、
回収された塩化ビニール樹脂破砕物102中の水分含有
量は、35.0%であった。この回収された塩化ビニー
ル樹脂破砕物102は、更に、脱水機(図示せず)にて
水分含有量が24.0%程度にまで脱水することができ
る。回収された塩化ビニール樹脂破砕物102は、通
常、工業用原料として再利用される。The crushed vinyl chloride resin 102 settled to the bottom of the kiln is guided toward the kiln outlet 4 by the spiral blades 20 formed on the inner wall of the rotating kiln 2, and a part of the water is discharged from the kiln outlet 4. Along with this, it flows out of the kiln and is stored in a mesh basket 38 which is an appropriate mesh. At this time, the crushed polyethylene resin material 101 adhered to the kiln inner wall or the spiral blade 20 and conveyed to the kiln outlet 4.
Are washed by the spray means 36 and flow toward the kiln inlet 3 together with water. Therefore, the content of the crushed polyethylene resin 101 in the crushed vinyl chloride resin 102 recovered in the net basket 38 is very small, and according to the results of the experiments of the present inventors, 0.5% (weight). Met. or,
The water content in the recovered crushed vinyl chloride resin 102 was 35.0%. The collected crushed vinyl chloride resin 102 can be further dehydrated to a water content of about 24.0% by a dehydrator (not shown). The collected crushed vinyl chloride resin 102 is usually reused as an industrial raw material.
【0022】実施例2 実施例1では、キルン2の内壁に設ける螺旋手段は、キ
ルン内壁面2Aに取付けられた螺旋状の羽根20である
として説明したが、本実施例では、図3に示すように、
螺旋手段20は、キルン内壁面2Aに形成された溝とす
ることができる。分離、回収装置1のその他の構成は実
施例1と同様に構成されるので、同じ構成及び機能をな
す部材には同じ参照番号を付し、詳しい説明は省略す
る。Second Embodiment In the first embodiment, the spiral means provided on the inner wall of the kiln 2 has been described as the spiral blade 20 attached to the inner wall surface 2A of the kiln, but in this embodiment, it is shown in FIG. like,
The spiral means 20 can be a groove formed in the kiln inner wall surface 2A. Other configurations of the separation / collection apparatus 1 are the same as those of the first embodiment, and therefore, members having the same configuration and function are denoted by the same reference numerals, and detailed description is omitted.
【0023】螺旋溝20の形状、寸法は、所望に応じて
任意に設計することができるが、実施例1で説明したキ
ルン2と同じキルンを使用したとき、溝幅(W)は50
〜100mm、深さ(T)は100〜200mm、ピッ
チ(P)は100〜400mmとされ、本実施例では、
溝幅(W)を70mm、深さ(T)を150mm、ピッ
チ(P)を300mmとすることにより良好な結果を得
ることができ、実施例1と同様の作用効果を達成するこ
とができた。The shape and dimensions of the spiral groove 20 can be arbitrarily designed as desired, but when the same kiln as the kiln 2 described in the first embodiment is used, the groove width (W) becomes 50.
100100 mm, depth (T) is 100-200 mm, and pitch (P) is 100-400 mm. In this embodiment,
By setting the groove width (W) to 70 mm, the depth (T) to 150 mm, and the pitch (P) to 300 mm, good results could be obtained, and the same function and effect as in Example 1 could be achieved. .
【0024】[0024]
【発明の効果】以上説明したように、本発明は、例えば
キルンのような円筒状回転体に水を貯溜し、この水中に
ナゲット屑を送給し、水面上に浮上したポリエチレン樹
脂破砕物を円筒状回転体入口側から水と共に円筒状回転
体外へと流出させてポリエチレン樹脂破砕物を回収し、
そして、円筒状回転体底部に沈降した塩化ビニル樹脂破
砕物は、円筒状回転体の内壁に設けた螺旋手段により円
筒状回転体出口側から水と共に円筒状回転体外へと流出
させて回収する構成とされるので、ポリエチレン樹脂と
塩化ビニール樹脂との混合物からなるナゲット屑から、
ポリエチレン樹脂及び塩化ビニール樹脂を、簡単に且つ
有効に分離し、回収することができる。As described above, according to the present invention, water is stored in a cylindrical rotating body such as a kiln, nugget debris is fed into the water, and the polyethylene resin crushed material floating on the water surface is removed. Collected crushed polyethylene resin by flowing out of the cylindrical rotary body with water from the cylindrical rotary body inlet side,
Then, the crushed vinyl chloride resin settled at the bottom of the cylindrical rotating body is recovered by flowing out of the cylindrical rotating body together with water from the outlet side of the cylindrical rotating body to the outside by the spiral means provided on the inner wall of the cylindrical rotating body. So, from nugget waste consisting of a mixture of polyethylene resin and vinyl chloride resin,
Polyethylene resin and vinyl chloride resin can be easily and effectively separated and recovered.
【図1】本発明に係るナゲット屑からポリエチレン樹脂
と塩化ビニル樹脂とを分離し、回収する装置の一実施例
の概略構成図である。FIG. 1 is a schematic configuration diagram of an embodiment of an apparatus for separating and collecting polyethylene resin and vinyl chloride resin from nugget waste according to the present invention.
【図2】キルンの内壁面に設置される螺旋羽根の一実施
例の形状を説明する概略説明図である。FIG. 2 is a schematic explanatory view illustrating a shape of an embodiment of a spiral blade installed on an inner wall surface of a kiln.
【図3】本発明に係るナゲット屑からポリエチレン樹脂
と塩化ビニル樹脂とを分離し、回収する装置の他の実施
例の概略構成図である。FIG. 3 is a schematic configuration diagram of another embodiment of an apparatus for separating and collecting polyethylene resin and vinyl chloride resin from nugget waste according to the present invention.
1 分離、回収装置 2 円筒状回転体(キルン) 3 キルン入口 4 キルン出口 5 軸受け手段 6 支持手段 7 堰 10 キルン駆動手段 20 螺旋手段(螺旋羽根、螺旋溝) 30 搬送手段 31 シュート手段 32 脱水装置 35 網目スクリーン 36 水噴射手段 100 ナゲット屑 101 ポリエチレン樹脂破砕物 102 塩化ビニル樹脂破砕物 DESCRIPTION OF SYMBOLS 1 Separation and collection apparatus 2 Cylindrical rotating body (kiln) 3 Kiln inlet 4 Kiln outlet 5 Bearing means 6 Support means 7 Weir 10 Kiln drive means 20 Spiral means (spiral blade, spiral groove) 30 Transport means 31 Chute means 32 Dehydrator 35 mesh screen 36 water injection means 100 nugget waste 101 crushed polyethylene resin 102 crushed vinyl chloride resin
───────────────────────────────────────────────────── フロントページの続き (72)発明者 東川 憲兒 北海道苫小牧市字勇払152番地 苫小牧ケ ミカル株式会社内 Fターム(参考) 4D071 AA02 AA06 AA65 AB03 AB14 AB43 CA03 DA15 4F301 AA13 AA17 BA10 BA13 BA15 BA17 BA21 BE32 BF02 BF03 BF09 BF12 BF26 BF27 ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Kenji Higashikawa 152 Yufutsu, Tomakomai City, Hokkaido Tomakomai Chemical Co., Ltd. F-term (reference) 4D071 AA02 AA06 AA65 AB03 AB14 AB43 CA03 DA15 4F301 AA13 AA17 BA10 BA13 BA15 BA17 BA21 BE32 BF02 BF03 BF09 BF12 BF26 BF27
Claims (7)
口を備え、且つ内壁面に螺旋手段を形成した円筒状回転
体を、入口側が低くなるように傾斜させて長手軸線の回
りに回転させ、且つ入口側に堰を設けて前記円筒状回転
体内に水を貯溜可能に構成し、(b)前記円筒状回転体
入口側からポリエチレン樹脂破砕物と塩化ビニル樹脂破
砕物との混合物からなるナゲット屑を前記円筒状回転体
内へと装入して、ポリエチレン樹脂破砕物を水面上に浮
上させ、且つ、塩化ビニル樹脂破砕物は沈降させ、
(c)前記円筒状回転体出口側から水を円筒状回転体内
へと噴霧し、前記水面上に浮上したポリエチレン樹脂破
砕物を前記円筒状回転体入口側から水と共に前記堰を越
えて前記円筒状回転体外へと流出させてポリエチレン樹
脂破砕物を回収し、そして、(d)前記円筒状回転体底
部に沈降した塩化ビニル樹脂破砕物は、前記螺旋手段に
より前記円筒状回転体出口側から水と共に前記円筒状回
転体外へと流出させて回収する、ことを特徴とするナゲ
ット屑からポリエチレン樹脂と塩化ビニル樹脂とを分離
し、回収する方法。(A) A cylindrical rotary body having an inlet and an outlet at both ends in a longitudinal axis direction and having spiral means formed on an inner wall surface is rotated around the longitudinal axis by being inclined so that the inlet side is lowered. And a weir is provided on the inlet side so that water can be stored in the cylindrical rotating body, and (b) a mixture of the crushed polyethylene resin and the crushed vinyl chloride resin from the inlet side of the cylindrical rotating body. Nugget waste is charged into the cylindrical rotating body, the polyethylene resin crushed material floats on the water surface, and the vinyl chloride resin crushed material is settled,
(C) water is sprayed from the outlet side of the cylindrical rotating body into the cylindrical rotating body, and the crushed polyethylene resin floating on the water surface passes through the weir together with the water from the cylindrical rotating body inlet side to the cylindrical body. (D) the crushed polyvinyl chloride resin settled at the bottom of the cylindrical rotator is drained from the outlet of the cylindrical rotator by the spiral means. And separating and collecting the polyethylene resin and the vinyl chloride resin from the nugget waste.
壁面に設けた螺旋羽根であるか、又は、前記円筒状回転
体の内面に形成した螺旋溝であることを特徴とする請求
項1のナゲット屑からポリエチレン樹脂と塩化ビニル樹
脂とを分離し、回収する方法。2. The apparatus according to claim 1, wherein said spiral means is a spiral blade provided on an inner wall surface of said cylindrical rotating body or a spiral groove formed on an inner surface of said cylindrical rotating body. 1. A method for separating and collecting polyethylene resin and vinyl chloride resin from nugget waste.
螺旋手段を設け、前記入口には堰を有し、内部に水を貯
溜することのできるキルンと、(b)前記キルンをキル
ン入口側が出口側より低くなるようにして長手方向軸線
の回りに回転自在に保持する支持手段と、(c)前記キ
ルンを回転駆動する手段と、(d)前記キルン入口側か
らポリエチレン樹脂破砕物と塩化ビニル樹脂破砕物との
混合物からなるナゲット屑を前記キルン内へと装入する
ためのシュート手段と、(e)前記キルン出口側から水
を前記キルン内へと噴霧する水噴射手段と、を備え、水
面上に浮上したポリエチレン樹脂破砕物を前記キルン入
口側から水と共に前記堰を越えて前記キルン外へと流出
させ、一方、前記キルン底部に沈降した塩化ビニル樹脂
破砕物は前記キルンと共に回転する前記螺旋手段により
前記キルン出口側から水と共にキルン外へと流出させて
回収する、ことを特徴とするナゲット屑からポリエチレ
ン樹脂と塩化ビニル樹脂とを分離し、回収する装置。3. A kiln having an inlet and an outlet, a spiral means provided on an inner wall surface, a weir at the inlet, and capable of storing water therein, and (b) the kiln. Support means for holding the kiln at an inlet side lower than the outlet side so as to be rotatable about a longitudinal axis; (c) means for rotating and driving the kiln; and (d) crushed polyethylene resin from the kiln inlet side. A chute means for charging nugget waste consisting of a mixture of crushed vinyl chloride resin into the kiln; and (e) a water injection means for spraying water from the kiln outlet side into the kiln; The crushed polyethylene resin floating on the water surface flows out of the kiln through the weir from the kiln inlet side together with the water to the outside of the kiln, while the crushed polyvinyl chloride resin settled at the bottom of the kiln is the kiln An apparatus for separating and collecting polyethylene resin and vinyl chloride resin from nugget waste, wherein the spiral means rotates together with the water and flows out of the kiln from the kiln outlet to the outside of the kiln.
配置した螺旋羽根であるか、或は、前記キルンの内壁面
に形成した螺旋溝であることを特徴とする請求項3のナ
ゲット屑からポリエチレン樹脂と塩化ビニル樹脂とを分
離し、回収する装置。4. The nugget waste according to claim 3, wherein said spiral means is a spiral blade disposed on an inner wall surface of said kiln or a spiral groove formed on an inner wall surface of said kiln. For separating and recovering polyethylene resin and vinyl chloride resin from wastewater.
水装置を設けたことを特徴とする請求項3又は4のナゲ
ット屑からポリエチレン樹脂と塩化ビニル樹脂とを分離
し、回収する装置。5. The apparatus for separating and recovering polyethylene resin and vinyl chloride resin from nugget waste according to claim 3 or 4, wherein a dewatering device is provided outside near the inlet of the kiln.
設置したことを特徴とする請求項5のナゲット屑からポ
リエチレン樹脂と塩化ビニル樹脂とを分離し、回収する
装置。6. An apparatus for separating and collecting polyethylene resin and vinyl chloride resin from nugget waste according to claim 5, wherein a mesh screen is provided on an upper surface of said dehydrating apparatus.
せることを特徴とする請求項6のナゲット屑からポリエ
チレン樹脂と塩化ビニル樹脂とを分離し、回収する装
置。7. The apparatus for separating and collecting polyethylene resin and vinyl chloride resin from nugget waste according to claim 6, wherein the mesh screen of the dehydrating apparatus is vibrated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23900399A JP3973802B2 (en) | 1999-08-25 | 1999-08-25 | Equipment for separating and collecting polyethylene resin and vinyl chloride resin from nugget scrap |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23900399A JP3973802B2 (en) | 1999-08-25 | 1999-08-25 | Equipment for separating and collecting polyethylene resin and vinyl chloride resin from nugget scrap |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2001062333A true JP2001062333A (en) | 2001-03-13 |
JP3973802B2 JP3973802B2 (en) | 2007-09-12 |
Family
ID=17038460
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JP23900399A Expired - Fee Related JP3973802B2 (en) | 1999-08-25 | 1999-08-25 | Equipment for separating and collecting polyethylene resin and vinyl chloride resin from nugget scrap |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010000469A (en) * | 2008-06-23 | 2010-01-07 | Nakata Coating Co Ltd | Apparatus and method for recovery of plastic waste and separation recovery apparatus |
-
1999
- 1999-08-25 JP JP23900399A patent/JP3973802B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010000469A (en) * | 2008-06-23 | 2010-01-07 | Nakata Coating Co Ltd | Apparatus and method for recovery of plastic waste and separation recovery apparatus |
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