JP2003001631A - Method for treating foamed resin molding - Google Patents

Method for treating foamed resin molding

Info

Publication number
JP2003001631A
JP2003001631A JP2001193133A JP2001193133A JP2003001631A JP 2003001631 A JP2003001631 A JP 2003001631A JP 2001193133 A JP2001193133 A JP 2001193133A JP 2001193133 A JP2001193133 A JP 2001193133A JP 2003001631 A JP2003001631 A JP 2003001631A
Authority
JP
Japan
Prior art keywords
volume
molding
foamed resin
crushed
steam
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.)
Pending
Application number
JP2001193133A
Other languages
Japanese (ja)
Inventor
Masao Seki
雅夫 関
Yutaka Tsuda
裕 都田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SEKI SEISAKUSHO KK
Original Assignee
SEKI SEISAKUSHO KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SEKI SEISAKUSHO KK filed Critical SEKI SEISAKUSHO KK
Priority to JP2001193133A priority Critical patent/JP2003001631A/en
Publication of JP2003001631A publication Critical patent/JP2003001631A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a process in which when a foamed resin molding is regenerated, heating volume reduction treatment is made uniform, the volume reduction in a high quality state is done efficiently in a short time, the bulk density of the volume-reduced molding can be controlled widely, the reduction of the bulk density can be improved, the volume of the crushed molding can be reduced efficiently even when it is wet, and the burning of the treated molding and a phenomenon of the growth of a cake of the treated molding during the treatment can be prevented since there is no fear of fire by generated gas, enabling the safe operation of the treatment. SOLUTION: In a volume reduction process, the used foamed resin molding is crushed primarily and secondarily by crushing means into particles of 3-10 mm particle size, the crushed molding is packed in the volume reduction part of a mold having a steam hole, steam of 116-126 deg.C is supplied into the mold of the volume reduction part for a heating time of 30-60 s to reduce the volume of the crushed molding by heating. The volume-reduced crushed molding is taken out from the mold and crushed tertiarily into granules, and the granules wetted by the steam are dried in a drying process.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、梱包材や包装材と
して用いられる発泡スチロールなどの熱可塑性合成樹脂
ブロック、若しくはプレートなどの成形品を回収して再
生するために用いられる発泡樹脂成形物処理方法、特に
溶融分解を起こさずに素材として容積の縮減減容化を効
率よく行なう発泡スチロール製品の処理方法に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating a foamed resin molded article used for collecting and reclaiming a molded article such as a thermoplastic synthetic resin block such as expanded polystyrene used as a packaging material or a packaging material, or a plate. In particular, the present invention relates to a method for treating a Styrofoam product that efficiently reduces and reduces the volume as a raw material without causing melt decomposition.

【0002】[0002]

【従来の技術】一般に、発泡スチロールは、緩衝性、断
熱性、保温性の各点で優れているため各種製品の梱包材
や包装材として多用されているが、これら梱包などに用
いられた或る形に成形されてなる梱包材や包装材は、こ
れまで使用済後は単に使い捨てとなって廃棄され、また
は焼却処分されてきたため、ごみ処理に伴う弊害、例え
ば捨て場の確保の問題や、焼却時に発生する悪臭発生や
排煙による大気汚染など環境破壊の公害問題の上から、
その処分が苦慮されている。そこで従来では、これら発
泡スチロール成形品を再生するために小さく破砕して、
これをコンベアで搬送中に遠赤外線照射の熱源によって
その容積を縮減させることが提案されている。(実開平
1−89110号公報、特開平6−166034号公
報)。
2. Description of the Related Art Generally, Styrofoam is widely used as a packing material or packing material for various products because it is excellent in cushioning property, heat insulating property, and heat retaining property. Since the packaging materials and packaging materials that have been molded into shapes have been used up until now, they have been simply thrown away and discarded or incinerated. From the pollution problem of environmental destruction such as air pollution due to foul odor generation and smoke emission,
Its disposal is difficult. Therefore, in the past, in order to regenerate these Styrofoam molded products, they were crushed into small pieces,
It has been proposed to reduce the volume of this by a heat source of far-infrared radiation during transportation on a conveyor. (Japanese Utility Model Laid-Open No. 1-89110, Japanese Patent Laid-Open No. 6-166034).

【0003】[0003]

【発明が解決しようとする課題】ところが、細かく粉砕
された発泡スチロールで遠赤外線による容積縮減化の処
理では収縮に時間がかかり効率が悪く大量処理には不向
きであり、減容工程ではガスの発散を良くするために大
気開放型であるため周辺温度に大きく左右されやすく温
度コントロールも難しく、特に粉砕された被処理物が水
濡れしたものは、熱の掛かり方が不安定のため一定品質
減容が不可能になったり、被処理物の量の変化によって
減容率が変わり一定にすることが難しく不均質となり、
また減容嵩比重が、0.2〜0.3となるようにコント
ロールするのが限度であり、減容化に限界があって問題
であった。しかも加熱により粉砕された発泡樹脂の減容
工程では内部に残っていたガスが出るためヒータの熱に
より引火されやすく火災発生のおそれがあり、また、万
一処理中に停電等不測の事態でコンベアが停止した場合
にも、被処理物がオーバーヒートで出火する危険がある
ほか、ガスをブロアなどで吸引して機外に排出しなけれ
ばなならない設備が必要となるし、収集ボックスに落下
する処理物が団子状の塊りとなる不具合があって、運転
操業の安全性や保守点検など取扱上煩雑であるなどの問
題があった。
However, in the process of volume reduction by far infrared rays with finely pulverized styrofoam, the shrinkage is time-consuming and inefficient, and is not suitable for large-scale processing. Because it is open to the atmosphere for improvement, it is easily affected by the ambient temperature and temperature control is difficult.In particular, crushed objects to be wetted with water have a certain volume loss due to unstable heat application. It becomes impossible or the volume reduction rate changes due to changes in the amount of processed material, making it difficult to keep constant and becoming inhomogeneous.
Further, there is a limit in controlling the volume specific gravity to be 0.2 to 0.3, which is a problem because the volume reduction is limited. Moreover, in the volume reduction process of the foamed resin crushed by heating, the gas remaining inside will come out and the heat of the heater will easily ignite the fire, which may cause a fire. Even if the machine stops, there is a risk that the object to be processed will overheat and the gas will need to be sucked out with a blower or the like and discharged to the outside of the machine. There was a problem that the objects became dumpling-like lumps, and it was troublesome in handling such as safety of operation and maintenance and maintenance inspection.

【0004】本発明は、これら従来の諸欠点を排除しよ
うとするもので、発泡樹脂成形物の再生処理の際に破砕
された被処理物の変動によっても減容率を均一化し、高
品質状態の容積縮減が短時間で効率よくでき、減容処理
に蒸気圧をコントロールすることにより減容温度を容易
に選定することができるので、減容嵩比重を幅広くコン
トロールすることができ作業性を著しく向上することが
できると共に、蒸気の熱容量が比較的に大きいので、減
容設備の周辺の温度に左右されず作業でき一定品質の減
容化が可能であり、粉砕されたものが水濡れしていても
効率よく減容化でき、しかも発生ガスによる火災の心配
がないので、処理中に被処理物が燃え出す危険や処理物
の塊状肥大化現象を未然に防止し、安全に運転操業でき
保守保安も楽な発泡樹脂成形物処理方法を提供すること
を目的としたものである。
The present invention is intended to eliminate these conventional drawbacks, and the volume reduction rate is made uniform by the fluctuation of the object to be crushed during the reprocessing of the foamed resin molded product, resulting in a high quality condition. The volume can be reduced efficiently in a short time, and the volume reduction temperature can be easily selected by controlling the vapor pressure for volume reduction treatment, so the volume reduction bulk density can be widely controlled and workability is remarkably improved. In addition to being able to improve, the heat capacity of the steam is relatively large, so that it is possible to work without being influenced by the temperature around the volume reduction equipment, it is possible to reduce the volume of a certain quality, and the crushed material is wet with water. However, since the volume can be reduced efficiently and there is no risk of fire due to the generated gas, the danger of burning of the object to be processed during processing and the bloat of the processed material can be prevented, and safe operation can be maintained. Easy departure from security It is intended to provide a resin molded product processing method.

【0005】[0005]

【課題を解決するための手段】本発明は、使用済みの発
泡樹脂成形物を粉砕手段によって一次粉砕、二次粉砕し
て、粒径3〜10mmφとし、該粉砕物を蒸気孔のある
金型の減容部内に充填し、この減容部の金型内に温度1
16〜126℃の蒸気を加熱時間30〜60秒間給入し
て加熱縮減減容化する減容工程を経たのち、該金型より
減容体を取り出してこれを破砕手段により顆粒状に三次
粉砕すると共に、前記蒸気で濡れた顆粒体を乾燥工程に
より乾燥して発泡樹脂成形物を処理するもので、発泡樹
脂成形物の減容率を均一化し、高品質状態の容積縮減が
短時間で効率よくできる。さらに、この発明では、加熱
減容工程において、供給される蒸気の蒸気圧力を0.0
78〜0.147MpaG(0.8〜1.5kg/cm
)に制御して減容化すること、また減容嵩比重
が、0.1〜0.3となるようにコントロールすること
を特徴としており、蒸気圧力をコントロールすることに
より減容温度を容易に選定することができるので、減容
嵩比重を大巾に改善できるし、幅広くコントロールする
ことができ作業性を著しく向上することができる。
According to the present invention, a used foamed resin molded product is subjected to primary crushing and secondary crushing by a crushing means to obtain a particle size of 3 to 10 mmφ, and the crushed product is a mold having a steam hole. Fill the inside of the volume reducing part of the
After a volume reduction process of supplying steam at 16 to 126 ° C. for a heating time of 30 to 60 seconds to reduce the volume by heating, the volume reducing body is taken out of the mold and is pulverized into third particles by crushing means. Along with the above, the steam-wet granules are dried in a drying step to process the foamed resin molded product, and the volumetric reduction rate of the foamed resin molded product is made uniform, resulting in efficient volume reduction in a high quality state in a short time. it can. Further, in the present invention, the steam pressure of the steam supplied is 0.0
78 to 0.147 MpaG (0.8 to 1.5 kg / cm
2 G ) To reduce the volume and to control the volume specific gravity so that the volume specific gravity is 0.1 to 0.3. The volume reduction temperature can be easily controlled by controlling the vapor pressure. Since it can be selected, the volume specific gravity can be greatly improved, and it can be widely controlled, and the workability can be remarkably improved.

【0006】[0006]

【発明の実施の形態】本発明の実施形態では、使用済み
の発泡樹脂成形物をコンベアで移送して異物除去を行な
って破砕機に投入し、破砕機の粉砕手段によって破砕機
に投入された発泡樹脂成形物は一次粉砕、二次粉砕し
て、短時間で粒径3〜10mmφの細片に粉砕されてサ
イロに一旦供給され、該粉砕物を成形機ホッパーを経て
蒸気孔のある金型の減容部内に投入器により充填し、こ
の減容部の金型内に温度110〜130℃好ましくは1
16〜126℃の蒸気の蒸気圧力を0.078〜0.1
47MpaG(0.8〜1.5kg/cm )に制
御して加熱時間30〜60秒間給入して、金型内の粉砕
物を加熱縮減減容化し、減容率の均一化が計られる。こ
の減容化工程を経たのち、前記金型より減容体を取り出
して、これをコンベア上に落下させ搬送して破砕手段に
より顆粒状に三次粉砕すると共に、前記蒸気で濡れた顆
粒体を真空などの乾燥工程により乾燥して発泡樹脂成形
物を処理するもので、蒸気の熱容量が比較的に大きいの
で、減容設備の周辺の温度に左右されず作業でき一定品
質の減容化が可能であり、粉砕されたものが水濡れして
いても効率よく減容化でき、しかも発生ガスによる火災
の心配がないので、処理中に被処理物が燃え出す危険や
処理物の塊状肥大化現象を未然に防止し、安全に運転操
業でき保守保安も楽な処理ができるものである。
BEST MODE FOR CARRYING OUT THE INVENTION In the embodiment of the present invention, a used foamed resin molded product is transferred by a conveyor to remove foreign matters and put into a crusher, and then put into a crusher by a crushing means of the crusher. The foamed resin molded product is subjected to primary crushing and secondary crushing, crushed into small pieces having a particle size of 3 to 10 mmφ in a short time and once supplied to a silo, and the crushed product passes through a molding machine hopper and is a mold having steam holes. The volume-reducing part of No. 1 is filled with an injector, and the temperature of the volume-reducing part is 110 to 130 ° C, preferably 1
The steam pressure of 16 to 126 ° C is 0.078 to 0.1.
47 MpaG (0.8-1.5 kg / cm 2 G ), And the heating time is fed for 30 to 60 seconds to reduce the volume of the pulverized material in the mold by heating, reducing the volume, and making the volume reduction rate uniform. After this volume reduction process, the volume reducing body is taken out from the mold, and is dropped on a conveyor to be conveyed and pulverized by a crushing means to be tertiary pulverized. The foaming resin molded product is processed by drying in the drying process described above.Since the heat capacity of steam is relatively large, it is possible to work regardless of the temperature around the volume reduction equipment, and it is possible to reduce the volume of a certain quality. Even if the crushed product is wet with water, the volume can be efficiently reduced, and there is no risk of fire due to the generated gas, so there is a risk that the object to be processed will burn during processing and the lumpy expansion phenomenon of the object to be processed. In addition, it can be operated safely, and maintenance and security can be done easily.

【0007】[0007]

【実施例】本発明の実施例を図1の系統図の例で説明す
ると、使用済みの発泡樹脂成形物aをコンベア1で移送
して異物除去を行なって破砕機2に投入し、発泡樹脂成
形物を粉砕する第1粉砕ロール3が複数対向配備され、
その下方に第2粉砕ロール4を複数対向配備された破砕
機2の粉砕手段によって投入された発泡樹脂成形物aは
一次粉砕、二次粉砕されて短時間で粒径3〜10mmφ
の細片に粉砕されてサイロ5に一旦供給貯溜される。そ
して、破砕機2で粉砕した樹脂素材を前記サイロ5から
成形機ホッパーを経て蒸気孔のある金型6の減容部内に
投入器7により充填し、この減容部の金型6内に温度1
10℃〜130℃好ましくは116〜126℃の蒸気を
蒸気源8より蒸気圧力を0.078〜0.147Mpa
G(0.8〜1.5kg/cm )に制御して加熱時
間30〜60秒間給入して、金型6内の粉砕物を加熱縮
減減容化し、減容率の均一化が計られた減容体bを成形
する。次いで、減容部の金型6を開いて減容体bを取り
出して、粉砕ロールを備えた破砕機9にて顆粒状に粉砕
する第3次粉砕工程を経て顆粒体cとしてベルトコンベ
ア10上に落下供給し、該ベルトコンベア10で移送し
て前記蒸気で濡れた顆粒体cを真空装置12、送風源な
どに連なる乾燥装置11による乾燥工程により乾燥して
発泡樹脂成形物を処理するものである。
EXAMPLE An example of the present invention will be described with reference to the example of the system diagram of FIG.
Then, the used foamed resin molding a is transferred by the conveyor 1.
Then remove foreign matter and put it into the crusher 2 to form the foamed resin.
A plurality of first crushing rolls 3 for crushing the shaped object are arranged opposite to each other,
Crushing in which a plurality of second crushing rolls 4 are arranged facing each other below
The foamed resin molding a introduced by the crushing means of the machine 2 is
Primary pulverization, secondary pulverization, particle size 3-10 mmφ in a short time
Is crushed into small pieces and once supplied and stored in the silo 5. So
Then, the resin material crushed by the crusher 2 is removed from the silo 5
After passing through the molding machine hopper, inside the volume reduction part of the die 6 with steam holes
It is filled with a throwing device 7, and the temperature of 1
Steam at 10 ° C to 130 ° C, preferably 116 to 126 ° C
The steam pressure from the steam source 8 is 0.078 to 0.147 MPa.
G (0.8-1.5 kg / cmTwoG ) Control and heating
For 30 to 60 seconds while heating and shrinking the crushed material in the mold 6.
Mold volume-reduced body b with reduced volume and uniform volume reduction rate
To do. Next, the mold 6 of the volume reducing part is opened to remove the volume reducing body b.
Take out and crush into granules with a crusher 9 equipped with a crushing roll
After the third crushing step,
A) Drop supply on 10 and transfer on the belt conveyor 10.
The granules c that have been wetted with the steam are not supplied to the vacuum device 12 and the air source.
Dry in the drying process by the drying device 11 connected to
This is to treat a foamed resin molded product.

【0008】この場合、蒸気温度としては、110℃〜
130℃好ましくは116〜126℃とするのは発泡性
ポリスチロールの熱変形温度が95℃位から始まり、発
泡スチロールの成形温度が110℃〜120℃であるこ
とを考慮する。即ち110℃以下の温度では収縮が始ま
らず、また130℃以上になると収縮が熱湯に始まり、
一定しなく、融解固化してしまうためである。さらに、
使用される前記蒸気の圧力は温度と正比例するので、
0.078〜0.147MpaG(0.8〜1.5kg
/cm )とするのがよい。さらに加熱時間は、3
0〜60秒間蒸気を給入して加熱縮減減容化する減容工
程としてあるが、一次、二次破砕されたスチロールの箱
の成形倍率が異なるため、又、水ぬれ等あり30秒以下
であると収縮しないし、また60秒以上であると収縮せ
ずに融解固化するので避けるべきである。温度=圧力と
加熱時間は必要とする嵩比重によりコントロールする。
また、加熱減容工程においては、供給減容嵩比重が、
0.1〜0.3となるようにコントロールするのがよ
く、蒸気圧力をコントロールすることにより減容温度も
容易に選定することができる。
In this case, the steam temperature is 110 ° C.
It is considered that the temperature is 130 ° C., preferably 116 to 126 ° C., considering that the heat distortion temperature of the expandable polystyrene starts at about 95 ° C. and the molding temperature of the expanded polystyrene is 110 ° C. to 120 ° C. That is, the shrinkage does not start at a temperature of 110 ° C or lower, and the shrinkage starts in hot water at a temperature of 130 ° C or higher,
This is because they are not constant and melt and solidify. further,
Since the pressure of the steam used is directly proportional to the temperature,
0.078-0.147MpaG (0.8-1.5kg
/ Cm 2 G ) Is recommended. Furthermore, the heating time is 3
This is a volume reduction process in which steam is supplied for 0 to 60 seconds to reduce the volume by heating and shrinking, but because the molding ratio of the primary and secondary crushed styrene boxes is different, there is also water wetting and the like, and it takes less than 30 seconds. If it is present, it will not shrink, and if it is 60 seconds or more, it will melt and solidify without shrinking, so it should be avoided. Temperature = pressure and heating time are controlled by the required bulk specific gravity.
Further, in the heating volume reduction step, the volume specific gravity of supply volume reduction is
The volume reduction temperature can be easily selected by controlling the vapor pressure by controlling the vapor pressure to 0.1 to 0.3.

【0009】前記粉砕ロール3、4は、外周に切刃を有
し、該切刃が互に噛み合うように対設されてモータ(図
示せず)で連動駆動され投入される梱包材を所定の大き
さに粉砕するもので、破砕機2を構成してあって前記コ
ンベア1上に連設配備されている。
The crushing rolls 3 and 4 have cutting blades on their outer circumferences, and the cutting blades are arranged so as to mesh with each other, and a predetermined packing material is loaded by being driven by a motor (not shown). The crusher 2 is crushed into a size and constitutes a crusher 2 which is continuously arranged on the conveyor 1.

【0010】また、前記ベルトコンベア10は、ガラス
繊維等よりなる耐熱ベルトコンベアを用い、粉砕ロール
のある破砕機9で破砕された処理物の量が多いと乾
燥効率が低下するので、ベルトコンベア10の速度を変
化させるようになっている。即ち、乾燥度合い一定にす
るためにベルトコンベア10の駆動部(図示せず)を制
御して該ベルトコンベア10の速度を自動的に変化でき
るようにしてある。
Further, the belt conveyor 10, using a heat resistant belt conveyor made of glass fibers or the like, the amount of has been treated crushed by crusher 9 with grinding rolls 9 1 and often drying efficiency is lowered, the belt The speed of the conveyor 10 is changed. That is, in order to keep the degree of drying constant, the drive unit (not shown) of the belt conveyor 10 is controlled so that the speed of the belt conveyor 10 can be automatically changed.

【0011】この場合、ベルトコンベア10上の処理物
は、収集ボックス13に自重落下するが、ベルトコンベ
ア10の搬出端にベルトコンベア10上の付着物を前記
収集ボックス13に払い落し部材などを備えていて、ベ
ルト上に付着して落ちにくいものを確実に収集ボックス
13に払い落し作業能率を図るようにしてある。なお、
ベルトコンベア10は無端状に架装され、静電気付着防
止のためにベルト表面に導電のためのカーボン入りのテ
フロン(登録商標)加工を施すのも有効である。
In this case, the processed material on the belt conveyor 10 falls to the collection box 13 by its own weight, but the adhering end of the belt conveyor 10 is provided with a member for removing the adhered material on the belt conveyor 10 to the collection box 13. In addition, the thing that adheres to the belt and is hard to fall off is surely blown off to the collection box 13 to improve work efficiency. In addition,
The belt conveyor 10 is mounted endlessly, and it is also effective to apply Teflon (registered trademark) containing carbon for conductivity to the surface of the belt to prevent static electricity adhesion.

【0012】なお、減容化工程においては、温度116
〜126℃の蒸気を蒸気源8より蒸気圧力を0.078
〜0.147MpaG(0.8〜1.5kg/cm
)に制御して加熱時間30〜60秒間給入して処理す
るが、減容する大きさによって蒸気圧力と、加熱時間に
よって自由にコントロールすることができる。例えば使
用する蒸気圧力も発泡スチロール樹脂成形と同様に用い
ることができる。
In the volume reduction process, the temperature 116
Steam pressure of ~ 126 ° C from the steam source 8 to 0.078
~ 0.147 MpaG (0.8-1.5 kg / cm 2 G
The heating time is controlled for 30 to 60 seconds and the treatment is performed, but the steam pressure and the heating time can be freely controlled depending on the volume reduction volume. For example, the steam pressure to be used can be used in the same manner as in the polystyrene foam resin molding.

【0013】また、前記減容部の金型6としては、図2
に示すように開閉自在の一対の金型を用い、この蒸気孔
のある金成形金型6内のキャビティ60に、粉砕された
樹脂素材を成形機ホッパーを経て投入器7により充填
し、この減容部の金型6内に蒸気源8に連なる蒸気管よ
り温度116〜126℃の蒸気を給入するようになって
いて、この加熱工程によって、加熱縮減減容化する装置
としてある。前記加熱減容部6は、処理効率をよくする
ためベルトコンベア10上に配備してあって、第3粉砕
工程での粉砕機9を介在配備するるのがよく、該ベルト
コンベア10上に乾燥装置11を並設して、ベルトコン
ベア10上の処理物を収集ボックス13に回収しやすい
ように配慮するのがよい。この場合、成形金型6を開い
たときに、成形された減容体bを離型しやすくするのに
金型離型用ピン(図示せず)を配備した成形金型を用い
るのがよい。
Further, as the mold 6 of the volume reducing section, as shown in FIG.
As shown in Fig. 5, a pair of molds that can be opened and closed is used, and the crushed resin material is filled in the cavity 60 in the metal mold 6 having the steam holes through the molding machine hopper by the injector 7. The steam at a temperature of 116 to 126 ° C. is fed into the mold 6 of the container from a steam pipe connected to the steam source 8, and this heating process is a device for reducing the heating and reducing the volume. The heating volume reducing unit 6 is arranged on the belt conveyor 10 in order to improve the processing efficiency, and it is preferable to interpose the crusher 9 in the third crushing step, and the heating and reducing unit 6 is dried on the belt conveyor 10. It is preferable to arrange the devices 11 side by side so that the processed products on the belt conveyor 10 can be easily collected in the collection box 13. In this case, when the molding die 6 is opened, it is preferable to use a molding die provided with a mold releasing pin (not shown) to facilitate the mold release of the molded volume reducing body b.

【0014】[0014]

【発明の効果】本発明は、使用済みの発泡樹脂成形物を
破砕手段により一次粉砕、二次粉砕して、粒径3〜10
mmφとし、該粉砕物を蒸気孔のある金型の減容部内に
充填し、この減容部の金型内に温度116〜126℃の
蒸気を加熱時間30〜60秒間給入して加熱縮減減容化
する減容工程を経たのち、該金型より減容体を取り出し
てこれを破砕手段により顆粒状に三次粉砕すると共に、
前記蒸気で濡れた顆粒体を乾燥工程により乾燥すること
ことにより、発泡樹脂成形物の再生処理の際に破砕され
た被処理物の変動によっても減容率を均一化し、高品質
状態の容積縮減が短時間で効率よくでき、さらに減容処
理に蒸気圧をコントロールすることにより減容温度を容
易に選定することができるので、減容嵩比重を幅広くコ
ントロールすることができ作業性を著しく向上すること
ができると共に、蒸気の熱容量が比較的に大きいので、
減容設備の周辺の温度に左右されず作業でき一定品質の
減容化が可能であり、粉砕されたものが水濡れしていて
も効率よく減容化でき、しかも発生ガスによる火災の心
配がないので、処理中に被処理物が燃え出す危険や処理
物の塊状肥大化現象を未然に防止し、安全に運転操業で
き保守保安も楽な取扱いで発泡樹脂成形物の処理を行う
ことができる。
According to the present invention, a used foamed resin molded product is subjected to primary crushing and secondary crushing by a crushing means to obtain a particle size of 3 to 10
mmφ, the crushed product is filled in the volume reducing part of the mold having steam holes, and steam at a temperature of 116 to 126 ° C. is fed into the mold of the volume reducing part for a heating time of 30 to 60 seconds to reduce the heat. After the volume reduction step of reducing the volume, the volume reducing body is taken out from the mold and is pulverized by a crushing means to be thirdly pulverized,
By drying the steam-wet granules in the drying step, the volume reduction rate is made uniform by the fluctuation of the object crushed during the reprocessing of the foamed resin molded product, and the volume reduction in the high quality state is reduced. Can be efficiently performed in a short time, and the volume reduction temperature can be easily selected by controlling the vapor pressure for volume reduction treatment, so that the volumetric volume specific gravity can be widely controlled and the workability is remarkably improved. And the heat capacity of the steam is relatively large,
It is possible to work without being affected by the temperature around the volume reduction equipment, and it is possible to reduce the volume of a certain quality, and even if the crushed material is wet, it is possible to efficiently reduce the volume, and there is a fear of fire due to the generated gas. Since it does not exist, it is possible to prevent the danger of burning of the object to be processed during processing and the bloat phenomenon of the object to be processed, to safely operate and operate the foamed resin molded product with easy maintenance. .

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施例を示す系統説明図である。FIG. 1 is a system explanatory view showing an embodiment of the present invention.

【図2】図1の例で用いられる減容部を示す縦断面図で
ある。
FIG. 2 is a vertical cross-sectional view showing a volume reducing portion used in the example of FIG.

【符号の説明】[Explanation of symbols]

1 コンベア 2 破砕機 3,4 粉砕ロール 5 収集ボックス 6 加熱減容部 7 投入器 8 蒸気源 9 破砕機 9 粉砕ロール 10 ベルトコンベア 11 乾燥装置 12 真空装置 13 収集ボックス 60 キャビティ1 Conveyor 2 Crusher 3,4 Grinding Roll 5 Collection Box 6 Heating Volume Reduction Unit 7 Charger 8 Steam Source 9 Crusher 9 1 Grinding Roll 10 Belt Conveyor 11 Dryer 12 Vacuum Device 13 Collection Box 60 Cavity

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】使用済みの発泡樹脂成形物を破砕手段によ
り一次粉砕、二次粉砕して、粒径3〜10mmφとし、
該粉砕物を蒸気孔のある金型の減容部内に充填し、この
減容部の金型内に温度116〜126℃の蒸気を加熱時
間30〜60秒間給入して加熱縮減減容化する減容工程
を経たのち、該金型より減容体を取り出してこれを破砕
手段により顆粒状に三次粉砕すると共に、前記蒸気で濡
れた顆粒体を乾燥工程により乾燥することを特徴とする
発泡樹脂成形物処理方法。
1. A used foamed resin molding is subjected to primary crushing and secondary crushing by a crushing means to obtain a particle size of 3 to 10 mmφ,
The crushed product is filled in the volume reducing part of a die having steam holes, and steam having a temperature of 116 to 126 ° C. is fed into the die of the volume reducing part for a heating time of 30 to 60 seconds to reduce the volume by heating. The foamed resin characterized in that after undergoing the volume reduction step, the volume reduced body is taken out from the mold, the powder is tertiary pulverized by a crushing means, and the steam-wet granules are dried by a drying step. Molded product processing method.
【請求項2】 前記加熱減容工程において、供給される
蒸気の蒸気圧力を0.078〜0.147MpaG
(0.8〜1.5kg/cm )に制御して減容化
することを特徴とした請求項1記載の発泡樹脂成形物処
理方法。
2. The vapor pressure of the vapor supplied in the heating volume reduction step is 0.078 to 0.147 MpaG.
(0.8-1.5 kg / cm 2 G (3) The method for treating a foamed resin molded article according to claim 1, wherein the volume is controlled so that the volume is controlled.
【請求項3】 前記加熱減容工程において減容嵩比重
が、0.1〜0.3となるようにコントロールすること
を特徴とした請求項1または2記載の発泡樹脂成形物処
理方法。
3. The method for treating a foamed resin molded article according to claim 1, wherein the volumetric specific gravity of volume reduction is controlled to be 0.1 to 0.3 in the heating volume reduction step.
【請求項4】 前記減容体の顆粒体の乾燥工程におい
て、前記減容部の金型に用いられる真空手段により顆粒
状物を乾燥することを特徴とする請求項1または2記載
の発泡樹脂成形物処理方法。
4. The foamed resin molding according to claim 1, wherein, in the step of drying the granules of the volume reducing body, the granular material is dried by a vacuum means used for the mold of the volume reducing section. Material processing method.
JP2001193133A 2001-06-26 2001-06-26 Method for treating foamed resin molding Pending JP2003001631A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001193133A JP2003001631A (en) 2001-06-26 2001-06-26 Method for treating foamed resin molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001193133A JP2003001631A (en) 2001-06-26 2001-06-26 Method for treating foamed resin molding

Publications (1)

Publication Number Publication Date
JP2003001631A true JP2003001631A (en) 2003-01-08

Family

ID=19031473

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001193133A Pending JP2003001631A (en) 2001-06-26 2001-06-26 Method for treating foamed resin molding

Country Status (1)

Country Link
JP (1) JP2003001631A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004063369A1 (en) 2003-01-10 2004-07-29 Kagawa University Gene sequence of l-rhamnose isomerase having new catalytic function and use thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004063369A1 (en) 2003-01-10 2004-07-29 Kagawa University Gene sequence of l-rhamnose isomerase having new catalytic function and use thereof

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