JP2004210832A - Recycling system of waste foamed synthetic resin - Google Patents

Recycling system of waste foamed synthetic resin Download PDF

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Publication number
JP2004210832A
JP2004210832A JP2002378897A JP2002378897A JP2004210832A JP 2004210832 A JP2004210832 A JP 2004210832A JP 2002378897 A JP2002378897 A JP 2002378897A JP 2002378897 A JP2002378897 A JP 2002378897A JP 2004210832 A JP2004210832 A JP 2004210832A
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Prior art keywords
solvent
synthetic resin
waste
tank
recycling system
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JP4105946B2 (en
Inventor
Munehiro Miyake
宅 宗 宏 三
Tatsue Edamura
村 達 衛 枝
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NISSHIN JAPAN KK
POROUS JAPAN KK
TEI SHOTA
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NISSHIN JAPAN KK
POROUS JAPAN KK
TEI SHOTA
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    • 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

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  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a recycling system of waste foamed synthetic resins, capable of performing treating works quickly, without causing deterioration of working environment with a solvent by installing a peculiar dissolving treatment constitution, also improving a recovery efficiency by using a peculiar conveying means and producing a high quality regenerated raw material. <P>SOLUTION: This device for the recycling system consists of a dissolving vessel containing a solvent sealed with water for dissolving the waste foamed synthetic resin by throwing it into the water-sealed solvent, a heating and separating device for separating a mixed solution obtained by dissolving the waste in the dissolving vessel to a resin portion and solvent portion, a solvent liquid tank for recovering and storing the separated solvent and a solidifying device for solidifying the separated resin portion. The method for recycling the waste foamed synthetic resin is characterized by heating the mixed solution of the waste foamed synthetic resin obtained by putting the waste into the solvent in the dissolving vessel and dissolving, in the heating and separating device to separate into the resin portion and solvent portion, storing the separated solvent in the solvent liquid tank for reuse, and also solidifying the separated resin portion in the solidifying device for reuse. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、廃棄合成樹脂製品の再資源化のためのリサイクルシステムに関し、特にスチロール系樹脂製品を有機溶剤に溶解してスチロール系合成樹脂と溶剤の両方を回収するリサイクルシステムに関する。
【0002】
【従来の技術】
使用済みの発泡スチロールなどの合成樹脂を回収してリサイクルする方法として、合成樹脂を熱で溶解して再生する方法と、合成樹脂を溶剤に溶解して合成樹脂を回収する方法などが検討されている。
【0003】
ところで前述の前者の方法では、加熱により樹脂が変性するため品質の高い再生樹脂は得られない。また後者の方法では、一般に使用した溶剤は回収しないので、ランニングコストが高くつき、また溶剤の蒸発により作業環境が悪いなどの問題がある。
例えば、従来、廃発泡スチロールの再生処理方法として、溶剤を用いてこれに溶解し、これを分離して再生すると共に再原料化するという溶剤減容処理方法が知られている(例えば、特許文献1、特許文献2参照)。
また、スチレン系合成樹脂からなるプラスチック廃棄物の改良リサイクル法も開示されている(例えば、特許文献3参照)。
【0004】
【特許文献1】
特開平7−26057号公報
【特許文献2】
特開平7−62137号公報
【特許文献3】
特許第2819209号公報
【0005】
【発明が解決しようとする課題】
しかしながら、前記従来の溶剤減容処理方法には、次のような不都合な課題がある。
(1)溶剤は、有害物質で環境汚染物質として使用が禁止されている塩素化炭化水素類を用いている。
(2)溶解速度が遅いため、実用性に欠ける。
(3)溶剤の主成分が、引火・発火等の安全性に問題がある。
(4)溶剤の水封処理がなされていない。
(5)不純物の除去のためのろ過手段が必要である。
そこで、この発明は、前記のような課題を解決せんと提案されたものであり、その目的は、特有な溶解処理構成を備えることにより、溶解速度が速く、溶剤による作業環境の悪化がなく、特殊な輸送手段を用いることにより、回収効率も向上でき、かつ、再生原料、リサイクル製品も高品質なものが提供でき、その上、プラント構成がコンパクトで全体としてランニングコストが低く、しかも作業環境の良好な廃棄発泡合成樹脂のリサイクルシステムを提供することにある。
【0006】
【課題を解決するための手段】
前記課題を解決するため、この発明の廃棄発泡合成樹脂のリサイクルシステムは、溶剤が水封されて容入され、この水封されている溶剤中に廃棄発泡合成樹脂を投入して溶解する溶解槽と、この溶解槽で溶解された混溶液を樹脂分と溶剤分とに分離する加熱分離装置と、この分離された溶剤を回収して貯溜する溶剤液タンクと、分離された樹脂分を固化する固化装置とより成り、
溶解槽の溶剤中に投入して溶解した廃棄発泡合成樹脂の混溶液を、加熱分離装置で加熱して樹脂分と溶剤分に分離し、この分離された溶剤を溶剤液タンクに貯溜し再使用すると共に、分離された樹脂分を固化装置において固化し再使用することを特徴とする。
これにより廃棄発泡合成樹脂は、水封されている溶剤中に投入して液状に溶解させた後、この混溶液(溶解液)を分離装置で樹脂分(スチレン分)と溶剤分とに分離して回収し、再使用できる。この時、溶剤は水封層において揮散が防止されているので、環境を悪化させることもない。
【0007】
また、この発明の廃棄発泡合成樹脂のリサイクルシステムは、前記溶解槽と加熱分離装置との間に混溶液タンクを設け、溶解槽で溶解した混溶液を一旦混溶液タンクに貯溜し、この混溶液タンクから混溶液を加熱分離装置に導入することを特徴とする。
これにより溶解槽で溶解した廃棄発泡合成樹脂の混溶液は、一旦混溶液タンクに貯溜しておくことができる。
【0008】
また、この発明の廃棄発泡合成樹脂のリサイクルシステムは、前記溶解槽に容入された溶剤は、下層となって上層の水封層で水封されており、溶解槽には該下層の溶剤層にガイドする廃棄発泡合成樹脂の供給手段および水封層に浮上した異物を除去する異物除去手段が設けられていることを特徴とする。
これにより廃棄発泡合成樹脂は、溶剤中にガイドして溶解させることができるし、混入した異物も容易に除去することができる。
【0009】
また、この発明の廃棄発泡合成樹脂のリサイクルシステムは、前記廃棄発泡合成樹脂の供給手段は、筒体内に回転可能に設けられた押込スクリューが、溶剤層に到達して設けられていることを特徴とする。
これにより、廃棄発泡合成樹脂は、押込スクリューにガイドされて溶剤層中に到達させることができる。
【0010】
また、この発明の廃棄発泡合成樹脂のリサイクルシステムは、前記溶解槽には、異物除去手段で除去した異物を回収するゴミ容器が設けられていることを特徴とする。
これにより、除去した異物は、環境を汚すことなく回収することができる。
【0011】
また、この発明の廃棄発泡合成樹脂のリサイクルシステムは、前記加熱分離装置は、上部が気化した溶剤の通路となっている加熱筒内にスクリューが回転可能に設けられ、この加熱筒内に前記混溶液が供給され、加熱されつつスクリューで混練されて出口方向に送られる間に、溶剤は気化して通路を通って溶剤液タンクに排出され、樹脂分は出口より排出されることを特徴とする。
これにより容易に樹脂分と溶剤分とに分離することができる。
【0012】
また、この発明の廃棄発泡合成樹脂のリサイクルシステムは、前記固化装置は、押出機と、冷却手段と、切断機とよりなることを特徴とする。
これにより樹脂分は押出機で線条体に押出し、これを冷却した後、切断することによってペレット化することができる。
【0013】
また、この発明の廃棄発泡合成樹脂のリサイクルシステムは、前記溶解槽は走行体に搭載され、廃棄発泡合成樹脂は廃棄場所において該溶解槽に投入され、溶解して回収することを特徴とする。
これにより廃棄発泡合成樹脂は、廃棄場所において減容して回収することができる。
【0014】
さらに、この発明の廃棄発泡合成樹脂のリサイクルシステムは、前記溶剤としてノルマルプロピルブロマイド60%、プロピレンカーボネート35%、安定剤その他が5%より成る廃発泡スチロール系合成樹脂の溶剤であることを特徴とする。
【0015】
【発明の実施の形態】
以下、この発明を図面に示す実施の形態について詳細に説明する。図1はこの発明のリサイクルシステムを示す全体説明図である。
同図に示すリサイクルシステムは、溶剤が水封されて容入され、この水封されている溶剤中に廃棄発泡合成樹脂(以下、単に発泡樹脂という)を投入して溶解する溶解槽1と、この溶解槽1で溶解された混溶液を貯溜する混溶液タンク11と、この混溶液タンク11の混溶液を樹脂分と溶剤分とに分離する加熱分離装置12と、この加熱分離装置12で分離された溶剤を回収して貯留する溶剤液タンク23と、分離された樹脂分を固化する固化装置16とより大略構成され、溶解槽1の溶剤中に投入して溶解された発泡樹脂の混溶液は、一旦混溶液タンク11に貯溜され、ここから加熱分離装置12に注入されて樹脂分と溶剤分に分離され、この分離された溶剤は溶解液タンク23に回収されて再使用され、分離された樹脂分は固化装置16に移動して固化され再使用される。
【0016】
図2は溶解槽の拡大概略説明図であり、同図に示すように溶解槽1に容入された溶剤は、下層Aとなって上層の水封層Bで水封されている。これにより溶剤が不用意に気化逃逸しないようになっている。
なお、溶剤は、スチロールを溶解できて比重が水よりも大きいものであれば、一応使用できるが、環境を破壊したり、汚染するものは好ましくなく、この実施の形態では、安全性の高いノルマルプロピルブロマイド60%、プロピレンカーボネート35%、安定剤その他が5%より成る溶剤を使用した。
【0017】
この溶解槽1には、該下層の溶剤層A中にガイドする発泡樹脂の供給手段3および水封層Bの界面に浮上してきた異物を除去する異物除去手段28が設けられている。本例の供給手段3は、筒体4内にスクリュー5が回転可能に設けられ、図示しないモータで回転される。図2に示すようにコンベア2で搬送されてきた発泡樹脂は、羽根の付いた回転ローラ6で供給手段3に投入され、回転するスクリュー5で溶剤層A中にガイドされ、溶解される。この投入される発泡樹脂は、粉砕して投入することが好ましい。
【0018】
また、異物除去手段28は水封層Bの界面に浮上したラベル等の夾雑物(異物)を除去するもので、スクリュー羽根を備えた除去管で構成されている。これは吸い込み式であってもよい。この異物除去手段28の排出口には、除去した異物を回収するゴミ容器8が備えられている。
【0019】
なお、溶解槽1の上部には、揮発溶媒を焼却用燃焼器(図示省略)へ排出する排出路10がブロワー9を備えて設けられている。即ち、溶剤層Aで発泡樹脂中の気泡中の空気が上昇し水封層Bを経て溶解槽1上のカバー内に充満し、排出路10内に流出できるようになっており、この排出路10内の空気分はブロア9により燃焼器(図示省略)内に送給され、この燃焼器のバーナにより空気内に含まれる溶剤分などを焼却除去できるようになっている。なお焼却された気体は燃焼筒と接続される排管を経て、さらに中和槽(図示省略)内に送給され、燃焼ガス中の有害気化分を中和させ、該槽内に貯留させた水中に溶解されると共に、冷却して常温に近い無害の空気として煙突(図示省略)より大気へ放出できるようになっている。
【0020】
溶解槽1の下部側面と混溶液タンク11との間にはポンプP3が設けられた排出管7が連結され、溶解槽1で溶解された発泡樹脂の混溶液が、混溶液タンク11に排出されて貯溜されるようになっている。この混溶液タンク11の下部には、ポンプPを備える配管が設けられ、加熱分離装置12に連結されている。
【0021】
加熱分離装置12は、上部が気化した溶剤の通路14となっている加熱筒12a内にスクリュー13が回転可能に設けられ、前記混溶液タンク11からこの加熱筒12a内に供給口を介して供給された混溶液は、加熱されつつスクリュー13で混練されて出口方向に送られる。この間に混溶液の溶剤分は気化して通路14を通って排出部15を介し溶解液タンク23に回収され、樹脂分は出口より固化装置16に排出される。前記排出部15は冷却手段を具備し、気化して排出されてきた溶剤を冷却し液状に戻して溶解液タンク23に回収する。
【0022】
固化装置16は、押出機17と、冷却手段18と、水切り手段19と、切断機20とを具備する。前記加熱分離装置12で分離されて排出された樹脂分は、押出機17で加熱されつつ線状体に押し出され、この押出しされた樹脂分は冷却手段18で冷却され、水切り手段19で水切りされた後、切断機20で切断されペレット化される。この切断機20で切断されたペレットは、ペレット選別機21にかけられ選別されてキャッチャータンク22に収集される。図3は、この固化装置の部分拡大説明図である。
【0023】
また、図4は溶解槽の供給手段を示す変形例であり、前記実施の形態と同一要素には同一符号を付して詳細な説明は省略する。本例によれば発泡樹脂が確実に溶剤層A中に供給される。
なお、符号24は加熱分離装置12に熱媒を供給する加熱手段、例えばボイラーであり、25は排気部15の冷却手段としての水冷チラーであり、26は排気を浄化するクリーニングタワーである。
【0024】
更に、この発明では、溶解槽1を走行体(タンクローリー)27に搭載して、発泡樹脂を廃棄場所や回収場所において該溶解槽1に投入して溶解して回収するようにしてもよい。例えば敷地に余裕がない小規模スーパー、家電販売店などから、鮮魚や青果の容器や家電製品やOA機器の包装材、緩衝材などとして利用された用済みの発泡スチロールを回収し乍ら、同時にタンク内で回収発泡スチロールを運搬中に溶剤で溶解し、この樹脂溶解液を混溶液タンク11へ供給する機能を有するものである。
この実施の形態で用いられる二液混合の溶剤は、気化温度が約66℃であるので蒸留分離処理温度は100℃以下の低温で処理可能であると共に、この溶剤自体発火点は660℃であるため、通常作業における引火事故などの不都合を回避できる。
【0025】
なお、タンクローリー27は、供給輸送手段として再生溶剤とは別に新規なバージンの溶剤を充填運搬して同様に溶解層1内に補給することができることは勿論である。
ことに反復利用するときは、溶剤自体の移送過程での損失や気化による損失などにより次第に使用量が減少して行くため、減量状態に達した場合とか、減量の恐れのある場合には、新規なバージンの溶剤を不足分に応じて補給する必要がある。
さらに、水と溶剤との容積の配合割合は7:3程度が好ましく、これにより臭気もウォーターシールでき実用に支障を生じないで実施できる。
【0026】
ここで廃棄発泡合成樹脂としては、廃棄発泡スチロール、廃棄ABS樹脂および廃発泡AS樹脂、等を例示できる。
なお、前記実施の形態は、この発明を制限するものではなく、この発明の要旨を逸脱しない範囲において種々の変形が許容される。例えば、混溶液タンク11は必ずしも必要ではなく、溶解槽1から直接加熱分離装置12に導入するようにしてもよい。
【0027】
【発明の効果】
以上詳細に説明したとおり、この発明の廃棄発泡合成樹脂のリサイクルシステムによれば、次のような効果を奏する。
(1)廃棄発泡合成樹脂は、水封されている溶剤中に投入して液状に溶解させた後、この混溶液(溶解液)を分離装置で樹脂分(スチレン分)と溶剤分とに分離して回収し、再使用できる。この時、溶剤は水封層において揮散が防止されているので、環境を悪化させることもない。
(2)処理作業が容易で短時間で可能であり、ランニングコストも低い。
(3)再生原料、リサイクル製品も高品質なものが提供できる。
(4)作業環境も悪化させない。
【0028】
(5)廃棄発泡合成樹脂は、溶剤層中にガイドされ確実に溶解されるし、溶解速度も速い。
(6)異物が除去されるし、異物の除去も容易となり、他の濾過装置は不要となる。
【0029】
(7)異物はゴミ容器に回収され、他の炭化装置で処理できる。
(8)合成樹脂を有効に、しかも樹脂に変性を生じることなく回収することができる。
(9)特殊な輸送手段を用いることにより廃棄発泡合成樹脂の回収効率を向上することができる。
【図面の簡単な説明】
【図1】この発明の実施の形態を示すリサイクルシステムの全体説明図である。
【図2】溶解槽の拡大説明図である。
【図3】固化装置の部分拡大説明図である。
【図4】溶解槽の変形例を示す拡大説明図である。
【符号の説明】
1 溶解槽
3 供給手段
4 円筒
5 スクリュー
11 混溶液タンク
12 加熱分離装置
12a 加熱筒
13 スクリュー
14 通路
16 固化装置
17 押出機
18 冷却手段
20 切断機
23 溶剤液タンク
27 走行体
28 異物除去手段
A 下層(溶剤層)
B 上層(水封層)
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a recycling system for recycling waste synthetic resin products, and more particularly to a recycling system for dissolving a styrene resin product in an organic solvent to recover both the styrene synthetic resin and the solvent.
[0002]
[Prior art]
As a method of collecting and recycling used synthetic resin such as styrene foam, a method of dissolving the synthetic resin by heat and a method of recovering the synthetic resin by dissolving the synthetic resin in a solvent are being studied. .
[0003]
By the way, in the former method, since the resin is denatured by heating, a high-quality regenerated resin cannot be obtained. In the latter method, since generally used solvents are not recovered, there are problems such as high running cost and poor working environment due to evaporation of the solvents.
For example, conventionally, as a method of regenerating waste styrofoam, there has been known a solvent volume reduction method in which a solvent is dissolved in a solvent, separated, regenerated, and recycled. , Patent Document 2).
Also, an improved recycling method for plastic waste made of a styrene-based synthetic resin is disclosed (for example, see Patent Document 3).
[0004]
[Patent Document 1]
JP-A-7-26057 [Patent Document 2]
JP-A-7-62137 [Patent Document 3]
Japanese Patent No. 2819209 [0005]
[Problems to be solved by the invention]
However, the conventional solvent volume reduction method has the following disadvantages.
(1) Chlorinated hydrocarbons, which are harmful substances and whose use is prohibited as environmental pollutants, are used as the solvent.
(2) Poor practicality due to low dissolution rate.
(3) The main component of the solvent has a problem in safety such as ignition or ignition.
(4) The solvent has not been water-sealed.
(5) Filtration means for removing impurities is required.
Therefore, the present invention has been proposed to solve the above problems, the purpose of which is to provide a unique dissolution processing configuration, the dissolution speed is fast, there is no deterioration of the working environment due to the solvent, By using special transportation means, recovery efficiency can be improved, and high-quality recycled materials and recycled products can be provided. Furthermore, the plant configuration is compact, running costs are low as a whole, and work environment An object of the present invention is to provide a good waste foam synthetic resin recycling system.
[0006]
[Means for Solving the Problems]
In order to solve the above-mentioned problem, a waste foam synthetic resin recycling system according to the present invention includes a dissolving tank in which a solvent is sealed by being filled with water, and the waste foamed synthetic resin is charged and dissolved in the water-sealed solvent. And a heating / separating device for separating the mixed solution dissolved in the dissolving tank into a resin component and a solvent component, a solvent liquid tank for collecting and storing the separated solvent, and solidifying the separated resin component. Solidification device,
The mixed solution of waste foamed synthetic resin put into and dissolved in the solvent in the dissolving tank is heated and separated by a heating and separating device into a resin component and a solvent component, and the separated solvent is stored in a solvent liquid tank and reused. In addition, the separated resin component is solidified in a solidifying device and reused.
Thus, the waste foamed synthetic resin is put into a water-sealed solvent and dissolved in a liquid state. Then, the mixed solution (solution) is separated into a resin component (styrene component) and a solvent component by a separator. Can be collected and reused. At this time, since the solvent is prevented from volatilizing in the water seal layer, the environment does not deteriorate.
[0007]
Further, the waste foaming synthetic resin recycling system of the present invention is provided with a mixed solution tank between the dissolving tank and the heating and separating device, and temporarily stores the mixed solution dissolved in the dissolving tank in the mixed solution tank. The mixed solution is introduced from the tank to the heat separation device.
Thus, the mixed solution of the waste foamed synthetic resin dissolved in the dissolving tank can be temporarily stored in the mixed solution tank.
[0008]
Further, in the recycling system for waste foamed synthetic resin of the present invention, the solvent contained in the dissolving tank is water-sealed as a lower layer with an upper water-sealing layer, and the lower solvent layer is formed in the dissolving tank. And a foreign matter removing means for removing foreign matter floating on the water sealing layer.
As a result, the waste foamed synthetic resin can be guided and dissolved in the solvent, and the mixed foreign matter can be easily removed.
[0009]
Further, the waste foam synthetic resin recycling system of the present invention is characterized in that the waste foam synthetic resin supply means is provided with a push screw rotatably provided in the cylindrical body reaching the solvent layer. And
Thereby, the waste foamed synthetic resin can be guided into the solvent layer by being guided by the pushing screw.
[0010]
Further, the waste foaming synthetic resin recycling system of the present invention is characterized in that the dissolving tank is provided with a trash container for collecting the foreign matter removed by the foreign matter removing means.
Thus, the removed foreign matter can be collected without polluting the environment.
[0011]
Further, in the waste foaming synthetic resin recycling system of the present invention, the heating / separating device is provided such that a screw is rotatably provided in a heating cylinder having an upper portion serving as a passage for a vaporized solvent. While the solution is supplied, kneaded with a screw while being heated and sent toward the outlet, the solvent is vaporized and discharged to the solvent liquid tank through the passage, and the resin component is discharged from the outlet. .
Thereby, it can be easily separated into a resin component and a solvent component.
[0012]
Further, the waste foam synthetic resin recycling system according to the present invention is characterized in that the solidifying device includes an extruder, a cooling means, and a cutting machine.
Thus, the resin component can be extruded into a filament by an extruder, cooled, and then cut into pellets.
[0013]
Further, the waste foam synthetic resin recycling system according to the present invention is characterized in that the dissolving tank is mounted on a traveling body, and the waste foam synthetic resin is put into the dissolving tank at a disposal place, and is dissolved and collected.
As a result, the waste foamed synthetic resin can be collected at a disposal place with a reduced volume.
[0014]
Further, the recycling system for waste foamed synthetic resin according to the present invention is characterized in that the solvent is a solvent for waste foamed styrene-based synthetic resin comprising 60% of normal propyl bromide, 35% of propylene carbonate, 5% of stabilizer and the like. .
[0015]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings. FIG. 1 is an overall explanatory view showing a recycling system of the present invention.
The recycling system shown in FIG. 1 includes a dissolving tank 1 in which a solvent is sealed in a water bath and a waste foamed synthetic resin (hereinafter, simply referred to as a foamed resin) is injected into the water-sealed solvent and dissolved therein. A mixed solution tank 11 for storing the mixed solution dissolved in the dissolving tank 1, a heating separation device 12 for separating the mixed solution in the mixed solution tank 11 into a resin component and a solvent component, and separation by the heating separation device 12. A solvent solution tank 23 for collecting and storing the separated solvent, and a solidifying device 16 for solidifying the separated resin component, which is roughly composed of a mixed solution of the foamed resin dissolved in the solvent in the dissolving tank 1 Is temporarily stored in the mixed solution tank 11 and then injected into the heating / separating device 12 to be separated into a resin component and a solvent component. The separated solvent is collected in the solution tank 23, reused and separated. The solidified resin is separated into Be re-used is solidified to move.
[0016]
FIG. 2 is an enlarged schematic explanatory view of the dissolving tank. As shown in FIG. 2, the solvent contained in the dissolving tank 1 becomes a lower layer A and is water-sealed by an upper water-sealing layer B. This prevents the solvent from inadvertently evaporating.
The solvent can be used as long as it can dissolve styrene and has a specific gravity greater than that of water.However, it is not preferable that the solvent destroys the environment or pollutes it. A solvent composed of 60% of propyl bromide, 35% of propylene carbonate, 5% of a stabilizer and the like was used.
[0017]
The dissolving tank 1 is provided with a foamed resin supply means 3 for guiding into the lower solvent layer A and a foreign matter removing means 28 for removing foreign matter floating on the interface of the water seal layer B. In the supply means 3 of this example, a screw 5 is rotatably provided in a cylindrical body 4 and is rotated by a motor (not shown). As shown in FIG. 2, the foamed resin conveyed on the conveyor 2 is fed into the supply means 3 by a rotating roller 6 having blades, guided by the rotating screw 5 into the solvent layer A, and dissolved. It is preferable that the foamed resin to be charged is pulverized and charged.
[0018]
The foreign matter removing means 28 removes foreign matters (foreign matter) such as labels floating on the interface of the water sealing layer B, and is constituted by a removing pipe having screw blades. This may be a suction type. A waste container 8 for collecting the removed foreign matter is provided at an outlet of the foreign matter removing means 28.
[0019]
In addition, a discharge path 10 for discharging a volatile solvent to an incinerator (not shown) is provided with a blower 9 at an upper portion of the dissolving tank 1. That is, the air in the bubbles in the foamed resin rises in the solvent layer A, fills the cover on the dissolving tank 1 via the water seal layer B, and can flow out into the discharge path 10. The air in 10 is fed into a combustor (not shown) by a blower 9, and the burner of the combustor can burn off and remove the solvent and the like contained in the air. The incinerated gas was sent through a discharge pipe connected to the combustion cylinder and further into a neutralization tank (not shown) to neutralize harmful vaporized components in the combustion gas and stored in the tank. As well as being dissolved in water, it can be cooled and released as harmless air near normal temperature from the chimney (not shown) to the atmosphere.
[0020]
A discharge pipe 7 provided with a pump P3 is connected between the lower side surface of the dissolving tank 1 and the mixed solution tank 11, and the mixed solution of the foamed resin dissolved in the dissolving tank 1 is discharged to the mixed solution tank 11. Are stored. A pipe provided with a pump P 1 is provided below the mixed solution tank 11, and is connected to the heat separation device 12.
[0021]
The heating / separating apparatus 12 has a screw 13 rotatably provided in a heating cylinder 12a having an upper portion serving as a passage 14 for a vaporized solvent, and is supplied from the mixed solution tank 11 to the heating cylinder 12a via a supply port. The heated mixed solution is kneaded by the screw 13 while being heated, and is sent toward the outlet. During this time, the solvent component of the mixed solution is vaporized and collected in the solution tank 23 through the discharge portion 15 through the passage 14, and the resin component is discharged to the solidification device 16 from the outlet. The discharge unit 15 is provided with a cooling means, and cools the solvent that has been vaporized and discharged, returns the liquid to a liquid state, and collects it in the solution tank 23.
[0022]
The solidifying device 16 includes an extruder 17, a cooling unit 18, a draining unit 19, and a cutting machine 20. The resin component separated and discharged by the heating separation device 12 is extruded into a linear body while being heated by an extruder 17, and the extruded resin component is cooled by a cooling unit 18 and drained by a draining unit 19. After that, it is cut by the cutting machine 20 and pelletized. The pellets cut by the cutter 20 are separated by a pellet sorter 21 and collected in a catcher tank 22. FIG. 3 is a partially enlarged explanatory view of the solidifying device.
[0023]
FIG. 4 is a modification showing the supply means of the dissolving tank, and the same elements as those in the above embodiment are denoted by the same reference numerals and detailed description thereof will be omitted. According to this example, the foamed resin is reliably supplied into the solvent layer A.
Reference numeral 24 denotes a heating unit for supplying a heat medium to the heating / separating device 12, for example, a boiler; 25, a water-cooled chiller as a cooling unit for the exhaust unit 15; and 26, a cleaning tower for purifying exhaust gas.
[0024]
Further, in the present invention, the dissolving tank 1 may be mounted on the traveling body (tank lorry) 27, and the foamed resin may be introduced into the dissolving tank 1 at a disposal place or a collecting place to be dissolved and collected. For example, while collecting used polystyrene foam used as containers for fresh fish and fruits and vegetables, packaging materials for home appliances and OA equipment, cushioning materials, etc., from small supermarkets and home appliance stores where there is not enough room, It has a function of dissolving the recovered styrofoam with a solvent during transportation and supplying this resin solution to the mixed solution tank 11.
Since the two-component mixed solvent used in this embodiment has a vaporization temperature of about 66 ° C., it can be processed at a low distillation separation temperature of 100 ° C. or less, and the solvent itself has an ignition point of 660 ° C. Therefore, it is possible to avoid inconveniences such as a fire accident in normal work.
[0025]
The tank lorry 27 can of course be filled and transported with a new virgin solvent separately from the regenerated solvent as a supply and transport means, and can be similarly supplied into the dissolving layer 1.
In particular, when repeatedly used, the amount used gradually decreases due to the loss during the transfer of the solvent itself and the loss due to vaporization, so if the weight loss state is reached or if there is a risk of weight loss, a new It is necessary to replenish the necessary virgin solvent according to the shortage.
Furthermore, the mixing ratio of the volume of water and the solvent is preferably about 7: 3, whereby the odor can be sealed with water, so that it can be carried out without hindering practical use.
[0026]
Here, examples of the waste foam synthetic resin include a waste styrene foam, a waste ABS resin, a waste foam AS resin, and the like.
The above embodiment does not limit the present invention, and various modifications are allowed without departing from the gist of the present invention. For example, the mixed solution tank 11 is not always necessary, and the mixed solution tank 11 may be directly introduced from the dissolving tank 1 to the heat separation device 12.
[0027]
【The invention's effect】
As described in detail above, according to the waste foam synthetic resin recycling system of the present invention, the following effects can be obtained.
(1) The waste foamed synthetic resin is introduced into a water-sealed solvent and dissolved in a liquid state, and then the mixed solution (solution) is separated into a resin component (styrene component) and a solvent component by a separator. Can be collected and reused. At this time, since the solvent is prevented from volatilizing in the water seal layer, the environment does not deteriorate.
(2) The processing operation is easy and can be performed in a short time, and the running cost is low.
(3) High quality recycled materials and recycled products can be provided.
(4) The working environment is not deteriorated.
[0028]
(5) The waste foamed synthetic resin is reliably dissolved by being guided in the solvent layer, and has a high dissolution rate.
(6) Foreign matter is removed, foreign matter is easily removed, and another filtering device is not required.
[0029]
(7) Foreign matter is collected in a garbage container and can be treated by another carbonization device.
(8) Synthetic resin can be recovered effectively and without denaturation of the resin.
(9) The collection efficiency of the waste foamed synthetic resin can be improved by using a special transportation means.
[Brief description of the drawings]
FIG. 1 is an overall explanatory diagram of a recycling system showing an embodiment of the present invention.
FIG. 2 is an enlarged explanatory view of a melting tank.
FIG. 3 is a partially enlarged explanatory view of a solidifying device.
FIG. 4 is an enlarged explanatory view showing a modification of the melting tank.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Dissolution tank 3 Supply means 4 Cylinder 5 Screw 11 Mixed solution tank 12 Heat separation device 12a Heating cylinder 13 Screw 14 Passage 16 Solidification device 17 Extruder 18 Cooling means 20 Cutting machine 23 Solvent liquid tank 27 Running body 28 Foreign material removing means A Lower layer (Solvent layer)
B Upper layer (water sealing layer)

Claims (9)

溶剤が水封されて容入され、この水封されている溶剤中に廃棄発泡合成樹脂を投入して溶解する溶解槽と、この溶解槽で溶解された混溶液を樹脂分と溶剤分とに分離する加熱分離装置と、この分離された溶剤を回収して貯溜する溶剤液タンクと、分離された樹脂分を固化する固化装置とより成り、
溶解槽の溶剤中に投入して溶解した廃棄発泡合成樹脂の混溶液を、加熱分離装置で加熱して樹脂分と溶剤分に分離し、この分離された溶剤を溶剤液タンクに貯溜し再使用すると共に、分離された樹脂分を固化装置において固化し再使用することを特徴とする廃棄発泡合成樹脂のリサイクルシステム。
A solvent is filled in with a water seal, and a dissolving tank for dissolving the foamed synthetic resin by throwing it into the water-sealed solvent, and the mixed solution dissolved in the dissolving tank is converted into a resin component and a solvent component. It consists of a heat separation device for separating, a solvent liquid tank for collecting and storing the separated solvent, and a solidifying device for solidifying the separated resin component,
The mixed solution of waste foamed synthetic resin put into and dissolved in the solvent in the dissolving tank is heated and separated by a heating and separating device into a resin component and a solvent component, and the separated solvent is stored in a solvent liquid tank and reused. A recycling system for waste foamed synthetic resin, wherein the separated resin component is solidified in a solidifying device and reused.
前記溶解槽と加熱分離装置との間に混溶液タンクを設け、溶解槽で溶解した混溶液を一旦混溶液タンクに貯溜し、この混溶液タンクから混溶液を加熱分離装置に導入することを特徴とする請求項1記載の廃棄発泡合成樹脂のリサイクルシステム。A mixed solution tank is provided between the dissolving tank and the heat separation device, the mixed solution dissolved in the dissolution tank is temporarily stored in the mixed solution tank, and the mixed solution is introduced from the mixed solution tank to the heat separation device. The recycling system for waste foamed synthetic resin according to claim 1. 前記溶解槽に容入された溶剤は、下層となって上層の水封層で水封されており、溶解槽には該下層の溶剤層にガイドする廃棄発泡合成樹脂の供給手段および水封層に浮上した異物を除去する異物除去手段が設けられていることを特徴とする請求項1および2記載のリサイクルシステム。The solvent contained in the dissolving tank is water-sealed as a lower layer with an upper water-sealing layer. 3. A recycling system according to claim 1, further comprising a foreign matter removing means for removing foreign matter floating on the surface. 前記廃棄発泡合成樹脂の供給手段は、筒体内に回転可能に設けられた押込スクリューが、溶剤層に到達して設けられていることを特徴とする請求項3記載の廃棄発泡合成樹脂のリサイクルシステム。The waste foam synthetic resin recycling system according to claim 3, wherein the waste foam synthetic resin supply means is provided with a push screw rotatably provided in the cylinder so as to reach the solvent layer. . 前記溶解槽には、異物除去手段で除去した異物を回収するゴミ容器が設けられていることを特徴とする請求項3記載の廃棄発泡合成樹脂のリサイクルシステム。The recycling system for waste foamed synthetic resin according to claim 3, wherein a trash container for collecting the foreign matter removed by the foreign matter removing means is provided in the melting tank. 前記加熱分離装置は、上部が気化した溶剤の通路となっている加熱筒内にスクリューが回転可能に設けられ、この加熱筒内に前記混溶液が供給され、加熱されつつスクリューで混練されて出口方向に送られる間に、溶剤は気化して通路を通って溶剤液タンクに排出され、樹脂分は出口より排出されることを特徴とする請求項1乃至5のいずれかに記載の廃棄発泡合成樹脂のリサイクルシステム。The heating / separating apparatus is provided with a screw rotatable in a heating cylinder whose upper portion is a passage for a vaporized solvent, and the mixed solution is supplied into the heating cylinder, kneaded by the screw while being heated, and exited. The waste foam synthesis according to any one of claims 1 to 5, wherein the solvent is vaporized and discharged to the solvent liquid tank through the passage while being sent in the direction, and the resin component is discharged from the outlet. Resin recycling system. 前記固化装置は、押出機と、冷却手段と、切断機とより成る請求項1乃至6のいずれかに記載の廃棄発泡合成樹脂のリサイクルシステム。7. The recycling system for waste foamed synthetic resin according to claim 1, wherein the solidifying device includes an extruder, a cooling unit, and a cutter. 前記溶解槽は走行体に搭載され、廃棄発泡合成樹脂は廃棄場所において該溶解槽に投入され、溶解して回収することを特徴とする請求項1乃至7のいずれかに記載の廃棄発泡合成樹脂のリサイクルシステム。The waste foamed synthetic resin according to any one of claims 1 to 7, wherein the dissolving tank is mounted on a traveling body, and the waste foamed synthetic resin is put into the dissolving tank at a disposal place, and is dissolved and collected. Recycling system. 前記溶剤は、ノルマルプロピルブロマイド60%、プロピレンカーボネート35%、安定剤その他が5%より成る廃発泡スチロール系合成樹脂の溶剤であることを特徴とする請求項1乃至8のいずれかに記載の廃棄発泡合成樹脂のリサイクルシステム。The waste foam according to any one of claims 1 to 8, wherein the solvent is a solvent for waste foamed styrene-based synthetic resin comprising 60% of normal propyl bromide, 35% of propylene carbonate, and 5% of a stabilizer and the like. Synthetic resin recycling system.
JP2002378897A 2002-12-27 2002-12-27 Waste foaming synthetic resin recycling system Expired - Fee Related JP4105946B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102728584A (en) * 2012-06-12 2012-10-17 广州力宝珍科技有限公司 Depainting cleaning method and depainting cleaning agent thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102728584A (en) * 2012-06-12 2012-10-17 广州力宝珍科技有限公司 Depainting cleaning method and depainting cleaning agent thereof

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