JP2961293B2 - Plastic separation and recovery equipment - Google Patents
Plastic separation and recovery equipmentInfo
- Publication number
- JP2961293B2 JP2961293B2 JP28840893A JP28840893A JP2961293B2 JP 2961293 B2 JP2961293 B2 JP 2961293B2 JP 28840893 A JP28840893 A JP 28840893A JP 28840893 A JP28840893 A JP 28840893A JP 2961293 B2 JP2961293 B2 JP 2961293B2
- Authority
- JP
- Japan
- Prior art keywords
- plastic
- tank
- separation
- specific gravity
- separation tank
- 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 - Fee Related
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Processing Of Solid Wastes (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (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
【0001】[0001]
【産業上の利用分野】この発明は、廃プラスチックから
油化に適したプラスチックだけを回収するさいなどに使
用されるプラスチックの分離回収装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for separating and recovering plastic used for recovering only plastic suitable for oiling from waste plastic.
【0002】[0002]
【従来の技術】例えば都市分別ごみ中の廃プラスチック
を再利用するためには、油化に適しない塩化ビニルを除
去して油化に適した廃プラスチックを回収することが必
要であり、このためにプラスチックの分離回収装置が使
用されている。2. Description of the Related Art For example, in order to reuse waste plastic in municipal waste, it is necessary to remove vinyl chloride that is not suitable for oiling and recover waste plastic suitable for oiling. A plastic separation and recovery device is used.
【0003】従来、この種のプラスチックの分離回収装
置としては、図2に示すように、プラスチックの混合物
を低比重物と高比重物とに分離する分離槽(21)と、撹拌
機(23)が配置された投入槽(22)とを備え、分離槽(21)の
底部と投入槽(22)の底部とが連通されているものが知ら
れている。Conventionally, as this kind of plastic separation and recovery apparatus, as shown in FIG. 2, a separation tank (21) for separating a mixture of plastics into a low specific gravity substance and a high specific gravity substance, and a stirrer (23) And a charging tank (22) in which the bottom of the separating tank (21) is communicated with the bottom of the charging tank (22).
【0004】この装置では、投入槽(22)開口から適当に
粉砕されたプラスチックを投入するとともに、撹拌機(2
3)によって投入槽(22)内に循環流を作り、この循環流に
プラスチックをのせてほとんど流れの無い分離槽(21)に
移動させる。分離槽(21)内では、油化に適するポリエチ
レン等の低比重物(28)が浮上し、油化に不適な塩化ビニ
ル等の高比重物(29)が沈下し、浮上した分だけを回収す
ることにより油化に適したものだけが得られる。In this apparatus, appropriately pulverized plastic is charged from the opening of a charging tank (22) and a stirrer (2) is used.
A circulation flow is created in the charging tank (22) by 3), and plastic is placed on the circulation flow and moved to the separation tank (21) where there is almost no flow. In the separation tank (21), low-density substances (28) such as polyethylene suitable for oiling float up, and high-gravity substances (29) such as vinyl chloride unsuitable for oiling settle down and only the floating amount is collected. By doing so, only those suitable for oiling can be obtained.
【0005】[0005]
【発明が解決しようとする課題】上記従来のプラスチッ
クの分離回収装置では、投入槽(22)でプラスチック中の
発泡スチロールのような特に比重が小さいものが水面に
浮かび、以降に投入されるプラスチックの邪魔になると
いう問題があった。In the above-mentioned conventional apparatus for separating and recovering plastic, in the charging tank (22), a substance having a particularly low specific gravity, such as styrene foam, in the plastic floats on the water surface and obstructs the plastic that is subsequently charged. There was a problem of becoming.
【0006】さらに、塩化ビニルのように疎水性プラス
チックのものでは、撹拌によりできた泡がプラスチック
表面に付着しやすく、そのため本来沈下すべき高比重の
塩化ビニルの一部が分離槽内で浮上し、油化に適する低
比重物に油化に適しない塩化ビニルが多く含まれて回収
されるという問題があった。Further, in the case of a hydrophobic plastic such as vinyl chloride, bubbles formed by stirring tend to adhere to the surface of the plastic, so that a part of the high specific gravity vinyl chloride, which should originally settle, floats in the separation tank. However, there is a problem that a low specific gravity material suitable for oiling contains a large amount of vinyl chloride unsuitable for oiling and is recovered.
【0007】この発明の目的は、発泡スチロール等が投
入路内に浮かんで以降に投入されるプラスチックの邪魔
になることがなく、しかも油化に適する低比重物と油化
に適しない塩化ビニルとを極めて精度よく分離して回収
できるプラスチックの分離回収装置を提供することにあ
る。[0007] An object of the present invention is to prevent low-density substances suitable for oiling and vinyl chloride not suitable for oiling, without styrofoam or the like floating in the charging path and obstructing plastics to be charged thereafter. An object of the present invention is to provide an apparatus for separating and collecting plastics which can be separated and collected with extremely high accuracy.
【0008】[0008]
【課題を解決するための手段】この発明によるプラスチ
ックの分離回収装置は、プラスチックの混合物を低比重
物と高比重物とに分離する分離槽(1) と、分離槽(1) 底
部に通じる垂下状投入路(2) と、分離槽(1) 外に設けら
れかつ撹拌機(7) を有しプラスチック粉砕物をスラリー
状に調整するスラリー調整槽(4) と、スラリー調整槽
(4) からスラリー状プラスチック粉砕物を抜き出して投
入路(2) に下向きに送り込むポンプ(6) と、分離槽(1)
底部に沈下した高比重物(9) を循環流(3) により系外に
抜き出す高比重物回収装置とを備えているものである。Means for Solving the Problems] separation and recovery device of a plastic according to the invention, the separation tank for separating a mixture of plastic and low density material and high specific gravity equivalent to (1), leads to the separation tank (1) bottom droop Jo turned path and (2), the separation tank (1) et provided on the outer
A slurry adjusting tank (4) having a stirrer (7) for adjusting the plastic pulverized material to a slurry state; and a slurry adjusting tank.
(4) or lath projecting an extracted slurry-like plastic pulverized product
Pump (6) feeding downward into the inlet (2) and separation tank (1)
High specific gravity material (9) settled to the bottom is circulated out of the system by circulation (3).
And a high-specific-gravity substance recovery device to be extracted .
【0009】[0009]
【作用】この発明のプラスチックの分離回収装置による
と、ポンプによりプラスチック粉砕物がスラリー状で投
入路に送り込まれる。このさい、発泡スチロールのよう
に比重が小さいものもポンプ圧によって強制的に分離槽
底部まで移動させられ、投入路内で浮かんで滞留するこ
とはない。また、撹拌機によりプラスチックを分離槽に
送るための循環流を作る必要がないので、撹拌によりで
きた泡がプラスチック表面に付着することがなく、本来
沈下すべき高比重の塩化ビニルの一部が付着した泡のた
めに分離槽内で浮上させられることがない。According to the apparatus for separating and recovering plastics of the present invention, the pulverized plastics are fed into the charging path in the form of slurry by the pump. At this time, even a material having a small specific gravity, such as styrene foam, is forcibly moved to the bottom of the separation tank by the pump pressure and does not float and stay in the charging path. In addition, there is no need to create a circulating flow to send the plastic to the separation tank using a stirrer, so that the foam created by the stirring does not adhere to the plastic surface, and some of the high specific gravity vinyl chloride, which should originally settle, is eliminated. It does not float in the separation tank due to attached bubbles.
【0010】[0010]
【実施例】この発明の実施例を、以下図面を参照して説
明する。Embodiments of the present invention will be described below with reference to the drawings.
【0011】図1は、この発明のプラスチックの分離回
収装置を示しており、同装置は、プラスチックの混合物
を低比重物と高比重物とに分離する分離槽(1) と、分離
槽(1) 底部に通じる投入路(2) と、プラスチック粉砕物
をスラリー状に調整するスラリー調整槽(4) と、スラリ
ー調整槽(4) から投入路(2) にスラリー状プラスチック
粉砕物を送り込むポンプ(6) とを備えており、例えば都
市分別ごみ中の廃プラスチックを再利用するに当たり、
廃プラスチックから油化に適しない塩化ビニルを分離し
て、油化に適したプラスチックを回収するものである。
分離槽(1) には水が入れられており、比重が1より大き
い塩化ビニルは沈下し、比重が1より小さいポリエチレ
ン、ポリプロピレン等の油化に適したプラスチックは浮
上するようになされている。FIG. 1 shows an apparatus for separating and recovering plastic according to the present invention. The apparatus comprises a separation tank (1) for separating a mixture of plastics into a low specific gravity substance and a high specific gravity substance, and a separation tank (1). ) A charging path (2) leading to the bottom, a slurry adjusting tank (4) for adjusting the plastic pulverized material into a slurry, and a pump () for feeding the pulverized slurry plastic from the slurry adjusting tank (4) to the charging path (2). 6) For example, in recycling waste plastic in municipal waste,
It separates vinyl chloride that is not suitable for oiling from waste plastic and recovers plastic that is suitable for oiling.
Water is contained in the separation tank (1), and vinyl chloride having a specific gravity of more than 1 sinks, and plastics suitable for oiling such as polyethylene and polypropylene having a specific gravity of less than 1 float.
【0012】スラリー調整槽(4) は、プラスチック粉砕
物を水と混合することにより、プラスチックをスラリー
状にするもので、スラリー調整槽(4) 内には撹拌機(7)
が配置されている。The slurry adjusting tank (4) is for mixing the pulverized plastic with water to make the plastic into a slurry. The slurry adjusting tank (4) contains a stirrer (7).
Is arranged.
【0013】投入路(2) は分離槽(1) 開口と同じ高さの
注入口を有しており、この注入口より管(5) によって送
られてきたスラリー状プラスチック粉砕物が注入される
ようになされている。なお、注入口は分離槽(1) の開口
の高さと同じでなくてもよい。The charging path (2) has an inlet at the same height as the opening of the separation tank (1), and the pulverized slurry-like plastic sent by the pipe (5) is injected from the inlet. It has been made like that. The inlet may not be at the same height as the opening of the separation tank (1).
【0014】投入路に送り込まれたスラリー状プラスチ
ック粉砕物は、ポンプ圧によって強制的に分離槽(1) 底
部まで移動させられる。このさい、発泡スチロールのよ
うに比重が小さいものも一緒に移動させられ、投入路
(2) 内で発泡スチロール等が浮かんで滞留することはな
い。The pulverized slurry-like plastic material sent into the charging path is forcibly moved to the bottom of the separation tank (1) by a pump pressure. At this time, materials with low specific gravity, such as styrofoam, are also moved together,
(2) Styrofoam etc. do not float and stay inside.
【0015】分離槽(1) 内では水の流れは少なく、各プ
ラスチックはそれぞれの比重に応じた特性を示すことに
なり、ポリエチレン等の低比重物(8) が浮上し、塩化ビ
ニル等の高比重物(9) が沈下することによってプラスチ
ックが分離させられる。浮上した低比重物(8) を回収す
ると、油化に不適な塩化ビニルを含まず非常に油化に適
したプラスチックが得られる。沈下した高比重物(9)
は、エアリフト、ポンプまたはスクリュー等により作り
出された循環流(3) にのせられて別途回収される。In the separation tank (1), the flow of water is small, and each plastic exhibits characteristics according to its specific gravity. A low specific gravity material (8) such as polyethylene floats, and The sedimentation of the specific gravity (9) separates the plastic. When the low specific gravity (8) that has floated is recovered, a plastic that is very suitable for oiling without containing vinyl chloride unsuitable for oiling can be obtained. Settled high specific gravity (9)
Is collected on a circulating flow (3) created by an air lift, a pump or a screw.
【0016】上記のプラスチックの分離回収装置では、
発泡スチロール等が投入路(2) 内で浮かんで滞留するこ
とがないので、以降に投入されるプラスチックの邪魔に
なることがなく、処理時間が短縮できる。また、従来の
装置のように投入槽内に撹拌機を配置する必要がないの
で、疎水性の塩化ビニルの表面に泡が付着して浮上する
ことが少なく、しかも装置が小型化できるというメリッ
トもある。In the above-mentioned plastic separation and recovery apparatus,
Since the styrofoam and the like do not float and stay in the charging path (2), the processing time can be shortened without obstructing the plastic to be charged thereafter. In addition, there is no need to dispose a stirrer in the charging tank as in the conventional device, so there is little chance that bubbles will adhere to the surface of hydrophobic vinyl chloride and float, and the device can be downsized. is there.
【0017】表1は、図2に示した従来のプラスチック
の分離回収装置と図1に示したこの発明によるプラスチ
ックの分離回収装置とについて、発泡スチロールを約1
0%含む廃プラスチックを用いてプラスチックの分離回
収実験を行った結果を示している。Table 1 shows that the conventional plastic separation and recovery apparatus shown in FIG. 2 and the plastic separation and recovery apparatus according to the present invention shown in FIG.
The result of performing a plastic separation and recovery experiment using waste plastic containing 0% is shown.
【0018】[0018]
【表1】 この表から分かるように、投入路(2) (従来装置では投
入槽(22))に浮かんで滞留する廃プラスチック、浮上回
収物中の塩化水素量(塩化ビニル量)および回収率のす
べてにおいて、この発明のプラスチックの分離回収装置
が優れている。なお、従来装置の投入槽(22)に浮く廃プ
ラスチックは、次に投入するプラスチックの邪魔になり
除去が必要な量であった。[Table 1] As can be seen from this table, the waste plastic floating and staying in the charging path (2) (the charging tank (22) in the conventional equipment), the amount of hydrogen chloride (vinyl chloride) in the floating recovered material, and the recovery rate were all The apparatus for separating and recovering plastic of the present invention is excellent. The amount of waste plastic floating in the charging tank (22) of the conventional apparatus was an amount that obstructed the next charging plastic and needed to be removed.
【0019】[0019]
【発明の効果】この発明のプラスチックの分離回収装置
によると、発泡スチロール等が投入路内で浮かんで滞留
することがないので、以降に投入されるプラスチックの
邪魔になることがなく、また、本来沈下すべき高比重の
塩化ビニルの一部が付着した泡のために分離槽内で浮上
させられることがないので、油化に適する低比重物と油
化に適しない塩化ビニルとを極めて精度よく分離して回
収することができる。さらに、プラスチック粉砕物がス
ラリー調整槽で洗浄されることにより、同槽に汚れが蓄
積されていくが、分離槽はこのスラリー調整槽の外に設
けられているので、汚れが分離槽に伝わりにくく、した
がって、汚れがプラスチックに付着することによる分離
効率の低下が防止できる。さらにまた、分離槽底部に沈
下した高比重物が循環流により系外に抜き出されること
により、分離槽内において、浮上分と沈降分とが混ざり
合うことがなく、したがって、分離効率が上がり、しか
も、沈降分を完全に抜き出すことができる。 According to the apparatus for separating and recovering plastics of the present invention, styrene foam and the like do not float and stay in the charging path, so that they do not hinder the plastics to be charged later, and they do not originally sink. Very high-density vinyl chloride, which is not suitable for oiling, is separated from vinyl chloride, which is not suitable for oiling, because it does not float in the separation tank due to foam to which part of high-density vinyl chloride to be attached has adhered. And can be collected. In addition, plastic crushed
Dirt accumulates in the tank after being cleaned in the rally adjustment tank.
The separation tank is installed outside this slurry adjustment tank.
Dirt is difficult to transfer to the separation tank.
Separation due to dirt sticking to plastic
A decrease in efficiency can be prevented. Furthermore, it is settled at the bottom of the separation tank.
High specific gravity dropped out of the system by circulating flow
Float and sediment mix in the separation tank
Does not fit, thus increasing the separation efficiency
However, the sediment can be completely extracted.
【図1】この発明によるプラスチックの分離回収装置を
概略的に示す正面図である。FIG. 1 is a front view schematically showing a plastic separation and recovery apparatus according to the present invention.
【図2】従来のプラスチックの分離回収装置を概略的に
示す正面図である。FIG. 2 is a front view schematically showing a conventional plastic separation and recovery device.
(1) 分離槽 (2) 投入路 (4) スラリー調整槽 (6) ポンプ (1) Separation tank (2) Input path (4) Slurry adjustment tank (6) Pump
フロントページの続き (56)参考文献 特開 昭48−100760(JP,A) 特開 平6−63944(JP,A) 特開 平6−114839(JP,A) 実開 昭57−183129(JP,U) (58)調査した分野(Int.Cl.6,DB名) B03B 1/00 - 13/06 B29B 17/00 Continuation of the front page (56) References JP-A-48-100760 (JP, A) JP-A-6-63944 (JP, A) JP-A-6-114839 (JP, A) Jpn. , U) (58) Fields investigated (Int. Cl. 6 , DB name) B03B 1/00-13/06 B29B 17/00
Claims (1)
重物とに分離する分離槽(1) と、分離槽(1) 底部に通じ
る垂下状投入路(2) と、分離槽(1) 外に設けられかつ撹
拌機(7) を有しプラスチック粉砕物をスラリー状に調整
するスラリー調整槽(4) と、スラリー調整槽(4) からス
ラリー状プラスチック粉砕物を抜き出して投入路(2) に
下向きに送り込むポンプ(6) と、分離槽(1) 底部に沈下
した高比重物(9) を循環流(3) により系外に抜き出す高
比重物回収装置とを備えているプラスチックの分離回収
装置。1. A separation tank (1) for separating a mixture of plastics into a low specific gravity substance and a high specific gravity substance, a hanging charging path (2) leading to the bottom of the separation tank (1), and an outside of the separation tank (1). Provided and stirred
Slurry adjusting tank for adjusting the plastic pulverized slurried have agitator (7) and (4), the slurry adjusting tank (4) or Las <br/> turned path extracted slurry-like plastic pulverized product (2 )
Pump (6) feeding downward and sinking at the bottom of the separation tank (1)
High-density material (9) drawn out of the system by circulating flow (3).
A separation and recovery device for plastics, comprising a specific gravity recovery device.
Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28840893A JP2961293B2 (en) | 1993-11-17 | 1993-11-17 | Plastic separation and recovery equipment |
| DK94117953T DK0662379T3 (en) | 1993-11-17 | 1994-11-14 | Process and apparatus for collecting plastic waste in sorted state |
| AT94117953T ATE177045T1 (en) | 1993-11-17 | 1994-11-14 | METHOD AND DEVICE FOR SORTING PLASTIC WASTE |
| EP19940117953 EP0662379B1 (en) | 1993-11-17 | 1994-11-14 | Process and apparatus for collecting waste plastics as separated |
| DE69416810T DE69416810T2 (en) | 1993-11-17 | 1994-11-14 | Method and device for sorting plastic waste |
| CA 2135959 CA2135959C (en) | 1993-11-17 | 1994-11-16 | Process and apparatus for collecting waste plastics as separated |
| KR1019940030193A KR950013671A (en) | 1993-11-17 | 1994-11-17 | Waste plastic separation and recovery apparatus and method |
| TW83110660A TW252945B (en) | 1993-11-17 | 1994-11-17 | |
| US08/638,866 US5667151A (en) | 1993-02-25 | 1996-04-29 | Process and apparatus for collecting waste plastics as separated |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28840893A JP2961293B2 (en) | 1993-11-17 | 1993-11-17 | Plastic separation and recovery equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07136546A JPH07136546A (en) | 1995-05-30 |
| JP2961293B2 true JP2961293B2 (en) | 1999-10-12 |
Family
ID=17729828
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28840893A Expired - Fee Related JP2961293B2 (en) | 1993-02-25 | 1993-11-17 | Plastic separation and recovery equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2961293B2 (en) |
-
1993
- 1993-11-17 JP JP28840893A patent/JP2961293B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07136546A (en) | 1995-05-30 |
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