JP3300652B2 - Method for recovering expanded polystyrene - Google Patents
Method for recovering expanded polystyreneInfo
- Publication number
- JP3300652B2 JP3300652B2 JP33357297A JP33357297A JP3300652B2 JP 3300652 B2 JP3300652 B2 JP 3300652B2 JP 33357297 A JP33357297 A JP 33357297A JP 33357297 A JP33357297 A JP 33357297A JP 3300652 B2 JP3300652 B2 JP 3300652B2
- Authority
- JP
- Japan
- Prior art keywords
- expanded polystyrene
- shrunk
- crushed
- pieces
- volume
- 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)
- 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]
【発明の属する技術分野】本発明は、梱包材等として多
用される発泡ポリスチレン成形体をペレットに加工して
回収する発泡ポリスチレンの回収方法に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recovering expanded polystyrene, which is obtained by processing an expanded polystyrene molded article frequently used as a packing material or the like into pellets and recovering the pellet.
【0002】[0002]
【従来の技術】発泡ポリスチレン成形体は、牛乳パッ
ク、段ボール、新聞紙等を再生利用したパルプモールド
材料に比較して、外観が良好で衝撃緩和性に優れるとと
もに任意の形状に容易に加工できることから、家電製
品、AV機器はいうにおよばず各種製品の梱包材等とし
て多用されているが、その反面、焼却時に高熱を発生し
て焼却炉の寿命を縮めることや土壌中で分解しないこと
等により、環境汚染の要因にもなっている。2. Description of the Related Art Compared with pulp molding materials made from recycled milk cartons, cardboards, newsprints, etc., foamed polystyrene moldings have good appearance, excellent impact relaxation properties, and can be easily processed into arbitrary shapes. Not to mention products and AV equipment, they are often used as packing materials for various products, but on the other hand, they generate high heat during incineration, shorten the life of the incinerator, and do not decompose in the soil. It is also a cause of pollution.
【0003】そこで、次に説明するような、発泡ポリス
チレン成形体を回収して再利用する発泡ポリスチレンの
回収方法が提案されている。[0003] Therefore, there has been proposed a method for recovering expanded polystyrene in which the expanded polystyrene molded body is recovered and reused as described below.
【0004】(イ) 発泡ポリスチレン成形体を加熱・
溶融して体積を収縮させたブロックにし、前記ブロック
をペレタイザーによってペレットに加工して回収する加
熱収縮方法。(A) Heating the expanded polystyrene molded body
A heat shrinking method in which a block is melted and reduced in volume, and the block is processed into pellets by a pelletizer and collected.
【0005】(ロ) 発泡ポリスチレン成形体を、ベン
ゼン系、ケトン系等の汎用の有機溶媒に溶解させたの
ち、有機溶媒とポリスチレンとを分離させて回収する方
法。(B) A method in which a foamed polystyrene molded body is dissolved in a general-purpose organic solvent such as a benzene-based or ketone-based solvent, and then the organic solvent and the polystyrene are separated and recovered.
【0006】(ハ) 発泡ポリスチレン成形体を、リモ
ネン、酢酸イソアミル、プロピオン酸ベンジル、酪酸エ
チルから選ばれた少なくとも1種類からなる収縮剤に接
触させてその体積を収縮させたのち、収縮剤とポリスチ
レンとを分離して回収する方法(特開平5−26306
5号公報参照)。(C) The expanded polystyrene molded body is brought into contact with a shrinking agent comprising at least one selected from limonene, isoamyl acetate, benzyl propionate, and ethyl butyrate to shrink the volume thereof, and then the shrinking agent and polystyrene And separating and recovering the same (JP-A-5-26306)
No. 5).
【0007】[0007]
【発明が解決しようとする課題】上記従来の技術のう
ち、(イ)の加熱収縮方法は、発泡ポリスチレン成形体
を加熱・溶融する際に、高温で加熱するため、ポリスチ
レンが熱分解を起こして悪臭を生じたり、回収されたポ
リスチレンの分子量が低下してしまい再利用が困難であ
る。Among the above prior arts, the heat shrinking method (a) involves heating at a high temperature when heating and melting the expanded polystyrene molded body, so that the polystyrene is thermally decomposed. Odor is generated and the molecular weight of the recovered polystyrene is reduced, making it difficult to reuse.
【0008】他方、(ロ)の汎用の有機溶媒に溶解させ
る方法では、この有機溶媒が人体・環境に少なからず悪
影響を与えるものであるため、有機溶媒を分離・回収し
て再利用するための分離装置が不可欠であり、コスト高
を招く。また、(ハ)の発泡ポリスチレンを収縮剤に接
触させて体積を収縮させる方法では、収縮剤自体は人体
や環境に安全なものであるが、上記(ロ)と同様に収縮
剤を分離・回収して再利用するための分離装置が不可欠
であり、コスト高を招くという問題点がある。On the other hand, in the method (b) of dissolving in a general-purpose organic solvent, since this organic solvent has a considerable adverse effect on the human body and the environment, it is necessary to separate and recover the organic solvent for reuse. Separation equipment is indispensable, resulting in high costs. In the method (c), in which the expanded polystyrene is brought into contact with a shrinking agent to reduce the volume, the shrinking agent itself is safe for the human body and the environment. A separating device for reusing the waste is indispensable, and there is a problem that the cost is increased.
【0009】本発明は、上記従来の技術の有する問題点
に鑑みてなされたものであって、悪臭の発生やポリスチ
レンの分子量が低下するおそれがなく、しかも、回収コ
ストを低減することができる発泡ポリスチレンの回収方
法を実現することを目的とするものである。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems of the prior art, and has no fear of generating an odor or reducing the molecular weight of polystyrene, and can reduce the cost of recovery. It is intended to realize a method for recovering polystyrene.
【0010】[0010]
【課題を解決するための手段】上記目的を達成するため
に、本発明の発泡ポリスチレンの回収方法は、発泡ポリ
スチレン成形体を破砕機により所定の大きさの破砕片に
破砕したのち、前記破砕片を気流により気力輸送する配
管の一端側より他端側へ移送する間に、前記配管の外壁
に配設された加熱手段によって所定の温度に加熱して前
記破砕片の体積を収縮させ、体積が収縮した収縮済破砕
片を引き続いてスクリュ式押出機を備えたペレタイザー
によりペレットに加工することを特徴とするものであ
る。Means for Solving the Problems To achieve the above object, a method for recovering expanded polystyrene according to the present invention comprises the steps of: crushing a foamed polystyrene molded product into crushed pieces of a predetermined size by a crusher; For air transport by airflow
While transferring from one end of the pipe to the other end, the outer wall of the pipe
Before and heated to a predetermined temperature by the disposed a heating means
The volume of the shredded pieces is shrunk, and the shrunk shrunken pieces whose volume shrinks are subsequently processed into pellets by a pelletizer equipped with a screw type extruder.
【0011】[0011]
【発明の実施の形態】本発明の一実施の形態による発泡
ポリスチレンの回収方法を図1を参照しつつ説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS A method for recovering expanded polystyrene according to one embodiment of the present invention will be described with reference to FIG.
【0012】(1) 発泡ポリスチレン成形体1を、破
砕機供給口2を通して破砕機3へ供給して所定の大きさ
の破砕片18に破砕する。(1) The foamed polystyrene molded article 1 is supplied to a crusher 3 through a crusher supply port 2 and crushed into crushed pieces 18 of a predetermined size.
【0013】(2) 上記(1)により破砕された破砕
片18を、後述するスクリュ式押出機9へ気力輸送する
ための配管6の配管供給口4へ投入する。(2) The crushed pieces 18 crushed by the above (1) are fed into a pipe supply port 4 of a pipe 6 for pneumatically transporting the crushed pieces 18 to a screw type extruder 9 described later.
【0014】(3) 上記(2)ののち、破砕片18
は、配管6内において、配管6の一端に配設された送風
機5により発生された気流により気力輸送されて配管6
の他端側へ移送される間に、配管6の外壁に配設された
加熱手段7によって所定の温度に加熱されてその体積が
収縮し、体積が収縮した収縮済破砕片19は、配管6の
他端に配設された気固分離器21により分離されて引き
続き押出機供給口8よりスクリュ式押出機9に供給され
る。(3) After the above (2), the crushed pieces 18
Is pneumatically transported in the pipe 6 by the airflow generated by the blower 5 disposed at one end of the pipe 6,
While being transferred to the other end of the pipe 6, the volume is shrunk by heating to a predetermined temperature by the heating means 7 disposed on the outer wall of the pipe 6, and the shrunk crushed pieces 19 whose volume has shrunk are Are separated by a gas-solid separator 21 disposed at the other end of the extruder, and subsequently supplied to the screw type extruder 9 from the extruder supply port 8.
【0015】一方、気固分離器21によって分離された
気体は、大気中へ放出するか、あるいは送風機5の吸込
側へ返戻して循環させる。On the other hand, the gas separated by the gas-solid separator 21 is discharged into the atmosphere or returned to the suction side of the blower 5 and circulated.
【0016】[0016]
【0017】(4) 上記(3)ののち、スクリュ式押
出機9内へ供給された体積が収縮した収縮済破砕片19
はシリンダ10内において回転するスクリュ11によっ
て下流側へ移送される間に、シリンダ10の外壁に配設
された加熱手段(不図示)による加熱とスクリュ11に
よるせん断発熱とにより混練・溶融されたのちダイス1
2よりストランド13として押し出される。(4) After the above (3), the contracted crushed pieces 19 whose volume supplied into the screw type extruder 9 has contracted.
Is kneaded and melted by heating by a heating means (not shown) provided on the outer wall of the cylinder 10 and shearing heat generated by the screw 11 while being transferred to the downstream side by the screw 11 rotating in the cylinder 10. Dice 1
It is extruded as a strand 13 from 2.
【0018】一方、収縮済破砕片に含まれる発泡剤はガ
ス状で、ベント口20より真空ポンプ22を介して真空
吸引する等の方法により機外へ除去される。On the other hand, the foaming agent contained in the shrunk crushed pieces is removed from the machine in a gaseous state by a method such as vacuum suction through a vent port 20 through a vacuum pump 22.
【0019】(5) 上記(4)ののち、押し出された
ストランド13はストランドバス14中において冷却液
15によって冷却されたのち、切断手段16により所定
の長さに逐次切断されてペレット17になる。(5) After the above (4), the extruded strand 13 is cooled by a cooling liquid 15 in a strand bath 14 and then sequentially cut into a predetermined length by a cutting means 16 to form a pellet 17. .
【0020】なお、スクリュ式押出機を備えたペレタイ
ザーとしては、上述したスクリュ式押出機9のダイス1
2により押し出されたストランド13をストランドバス
14にて冷却したのち切断手段16により逐次所定の長
さに切断してペレット17にするものに限らず、ダイス
の吐出側に近接して配設された回転刃等を備えたもの等
他の公知のスクリュ式押出機を備えたペレタイザーを用
いることができる。The pelletizer provided with the screw type extruder includes the die 1 of the screw type extruder 9 described above.
The strand 13 extruded by 2 is cooled by a strand bath 14 and then sequentially cut to a predetermined length by a cutting means 16 into pellets 17. The pellets 17 are arranged close to the die discharge side. A pelletizer equipped with another known screw type extruder such as one equipped with a rotary blade or the like can be used.
【0021】[0021]
【発明の効果】本発明は上述のとおり構成されているの
で、次に記載するような効果を奏する。Since the present invention is configured as described above, the following effects can be obtained.
【0022】発泡ポリスチレン成形体の破砕片は、気流
により気力輸送する配管の一端側より他端側へ移送され
る間に、前記配管の外壁に配設された加熱手段によって
所定の温度に加熱されてその体積が収縮し、この体積が
収縮した収縮済破砕片が引き続きスクリュ式押出機に供
給されるため、スクリュ式押出機での発泡ポリスチレン
成形体の処理量を増加させることができる。また、スク
リュ式押出機において混練・溶融させる際に必要な熱量
が低減される。その結果、スクリュ式押出機のシリンダ
の長さが短くて済み、回収コストが低減される。また、
発泡ポリスチレンの破砕片が不必要に加熱されないた
め、熱分解による悪臭が発生したり分子量が低下するこ
ともなく良質のペレットを得ることができる。[0022] The crushed pieces of expanded polystyrene moldings, air flow
Is transferred from one end to the other end of the pipe for pneumatic transport
In the meantime, the volume is shrunk by being heated to a predetermined temperature by a heating means disposed on the outer wall of the pipe, and the shrunk crushed pieces having the shrunk volume are continuously supplied to the screw type extruder. Therefore, the throughput of the expanded polystyrene molded article in the screw extruder can be increased. Further, the amount of heat required for kneading and melting in the screw type extruder is reduced. As a result, the length of the cylinder of the screw-type extruder can be shortened, and the recovery cost is reduced. Also,
Since the crushed pieces of the expanded polystyrene are not unnecessarily heated, good-quality pellets can be obtained without generating a bad odor or reducing the molecular weight due to thermal decomposition.
【図1】一実施の形態による発泡ポリスチレンの回収方
法を示す説明図である。FIG. 1 is an explanatory diagram showing a method for collecting expanded polystyrene according to an embodiment.
1 発泡ポリスチレン成形体 2 破砕機供給口 3 破砕機 4 配管供給口 5 送風機 6 配管 7 加熱手段 8 押出機供給口 9 スクリュ式押出機 10 シリンダ 11 スクリュ 12 ダイス 13 ストランド 14 ストランドバス 15 冷却液 16 切断手段 17 ペレット 18 破砕片 19 収縮済破砕片 20 ベント口 21 気固分離器 22 真空ポンプ DESCRIPTION OF SYMBOLS 1 Expanded polystyrene molded body 2 Crusher supply port 3 Crusher 4 Pipe supply port 5 Blower 6 Pipe 7 Heating means 8 Extruder supply port 9 Screw type extruder 10 Cylinder 11 Screw 12 Die 13 Strand 14 Strand bath 15 Coolant 16 Cutting Means 17 Pellets 18 Crushed pieces 19 Shrinked crushed pieces 20 Vent port 21 Gas-solid separator 22 Vacuum pump
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平5−92429(JP,A) 特開 平5−92428(JP,A) 特開 平5−162136(JP,A) 特開 昭62−121018(JP,A) 実開 平3−103709(JP,U) 実開 平3−39512(JP,U) 実開 平5−53909(JP,U) 実開 昭51−156066(JP,U) (58)調査した分野(Int.Cl.7,DB名) B29B 17/00 - 17/02 C08J 11/00 - 11/28 B09B 3/00 - 5/00 ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-5-92429 (JP, A) JP-A-5-92428 (JP, A) JP-A-5-162136 (JP, A) JP-A Sho 62- 121018 (JP, A) Japanese Utility Model 3-103709 (JP, U) Japanese Utility Model 3-39512 (JP, U) Japanese Utility Model 5-53909 (JP, U) Japanese Utility Model 51-156066 (JP, U) (58) Field surveyed (Int.Cl. 7 , DB name) B29B 17/00-17/02 C08J 11/00-11/28 B09B 3/00-5/00
Claims (1)
所定の大きさの破砕片に破砕したのち、前記破砕片を気
流により気力輸送する配管の一端側より他端側へ移送す
る間に、前記配管の外壁に配設された加熱手段によって
所定の温度に加熱して前記破砕片の体積を収縮させ、体
積が収縮した収縮済破砕片を引き続いてスクリュ式押出
機を備えたペレタイザーによりペレットに加工すること
を特徴とする発泡ポリスチレンの回収方法。1. A foamed polystyrene molded body is crushed by a crusher into crushed pieces of a predetermined size, and then the crushed pieces are air- crushed.
Transfer from one end to the other end of pipes that pneumatically transport by flow
In the meantime, the volume of the shredded pieces is shrunk by heating to a predetermined temperature by a heating means disposed on the outer wall of the pipe, and the shrunk pieces of shrunk volume are continuously extruded by screw-type extrusion. A method for recovering expanded polystyrene, comprising processing into pellets by a pelletizer equipped with a machine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33357297A JP3300652B2 (en) | 1997-11-18 | 1997-11-18 | Method for recovering expanded polystyrene |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33357297A JP3300652B2 (en) | 1997-11-18 | 1997-11-18 | Method for recovering expanded polystyrene |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH11147224A JPH11147224A (en) | 1999-06-02 |
JP3300652B2 true JP3300652B2 (en) | 2002-07-08 |
Family
ID=18267550
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33357297A Expired - Fee Related JP3300652B2 (en) | 1997-11-18 | 1997-11-18 | Method for recovering expanded polystyrene |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3300652B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110918603A (en) * | 2019-12-02 | 2020-03-27 | 江苏泓润生物质能科技有限公司 | Conveying method used in kitchen waste pretreatment process |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100756060B1 (en) | 2007-04-30 | 2007-09-07 | 한국이엠 주식회사 | 2-axis extrusion machine with forced feeder |
CN101693397B (en) | 2009-09-28 | 2012-02-22 | 江苏联冠科技发展有限公司 | Double-shaft crushing knife for hot melt recycling machine of expanded polystyrene |
CN110871562B (en) * | 2019-11-24 | 2020-12-08 | 浙江科瑞达塑胶有限公司 | Multi-channel confluence mixed plastic grain cutting process |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3103709U (en) | 2004-02-02 | 2004-08-19 | 維熹科技股▲ふん▼有限公司 | Power adapter |
-
1997
- 1997-11-18 JP JP33357297A patent/JP3300652B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3103709U (en) | 2004-02-02 | 2004-08-19 | 維熹科技股▲ふん▼有限公司 | Power adapter |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110918603A (en) * | 2019-12-02 | 2020-03-27 | 江苏泓润生物质能科技有限公司 | Conveying method used in kitchen waste pretreatment process |
Also Published As
Publication number | Publication date |
---|---|
JPH11147224A (en) | 1999-06-02 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5463411B2 (en) | How to recycle plastic materials | |
JPH0628244Y2 (en) | Foam plastic volume reduction machine | |
JP3300652B2 (en) | Method for recovering expanded polystyrene | |
KR101981193B1 (en) | Waste carpet reproduction device | |
JPH11226955A (en) | Method and apparatus for treating used expanded polystyrene | |
JPH01146708A (en) | Compression molding method for waste plastic and device thereof | |
EP1550536B1 (en) | Method for recycling foamed polystyrol resin | |
JP3607051B2 (en) | Waste plastics into solid fuel | |
JPH05147036A (en) | Method and apparatus for reclaiming waste plastic | |
KR0175915B1 (en) | Waste styrofoam recycling apparatus | |
JPH065853Y2 (en) | Foam plastic volume reduction machine | |
JP3578792B2 (en) | Equipment for manufacturing recycled synthetic resin pellets | |
JP3145683B2 (en) | How to increase the bulk density of waste plastic | |
KR200304705Y1 (en) | A reclaiming pellet making device | |
JPH0699430A (en) | Pelletizer for resin | |
JP4653699B2 (en) | Exhaust method of waste plastic high density volume reduction molding machine and waste plastic high density volume reduction molding machine | |
JP2004188695A (en) | Method for recycling waste polyolefins and system therefor | |
JPH0375234B2 (en) | ||
CN110900890B (en) | High-speed film recycling granulation device | |
CN212888453U (en) | Full biodegradable inflation film manufacturing machine rim charge recovery unit for express delivery bag | |
JPH1158381A (en) | Plastic scrap reprocessing method and reprocessing device | |
JP7621592B2 (en) | Manufacturing method of molded body | |
JPS61116507A (en) | Reclaiming equipment for formed plastics | |
JP2000169859A (en) | Recycled pellet production equipment | |
JPH01262958A (en) | Waste punching piece recycling device using a cyclone separator |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |