JP2637664B2 - Method for producing recycled expanded polystyrene resin molded article - Google Patents

Method for producing recycled expanded polystyrene resin molded article

Info

Publication number
JP2637664B2
JP2637664B2 JP6695092A JP6695092A JP2637664B2 JP 2637664 B2 JP2637664 B2 JP 2637664B2 JP 6695092 A JP6695092 A JP 6695092A JP 6695092 A JP6695092 A JP 6695092A JP 2637664 B2 JP2637664 B2 JP 2637664B2
Authority
JP
Japan
Prior art keywords
foamed
molded article
particles
resin particles
resin
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 - Lifetime
Application number
JP6695092A
Other languages
Japanese (ja)
Other versions
JPH05271459A (en
Inventor
敏喜 池田
新平 中山
靖博 上田
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.)
Sekisui Kaseihin Kogyo KK
Original Assignee
Sekisui Kaseihin Kogyo 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 Sekisui Kaseihin Kogyo KK filed Critical Sekisui Kaseihin Kogyo KK
Priority to JP6695092A priority Critical patent/JP2637664B2/en
Publication of JPH05271459A publication Critical patent/JPH05271459A/en
Application granted granted Critical
Publication of JP2637664B2 publication Critical patent/JP2637664B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics
    • 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

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は使用済の発泡ポリスチレ
ン系樹脂成形体、あるいは成形時に副生する不良品等の
廃発泡成形体を再生して、再生発泡成形体を製造する方
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 producing a recycled foamed molded article by regenerating a used foamed polystyrene resin molded article or a waste foamed molded article such as a defective product by-produced during molding. is there.

【0002】[0002]

【従来の技術】発泡ポリスチレン系樹脂成形体は、家電
製品の緩衝包装材、あるいは魚介類や生鮮食品の運搬用
容器等として大量に使用されているが、その一方で、使
用済の発泡成形体の廃棄処理対策は、社会的に大きな問
題となっている。そこで、近年では、使用済の発泡ポリ
スチレン系樹脂成形体を再生して、良好な発泡成形体を
製造することのできる発泡性ポリスチレン系の再生樹脂
粒子を得るために、種々の研究がなされている。
2. Description of the Related Art Foamed polystyrene resin moldings are used in large quantities as buffer packaging materials for home appliances or as containers for transport of seafood and fresh foods. Has become a major social issue. Therefore, in recent years, various studies have been made in order to regenerate a used foamed polystyrene-based resin molded article and obtain foamed polystyrene-based regenerated resin particles capable of producing a good foamed molded article. .

【0003】従来、使用済の発泡ポリスチレン系樹脂成
形体を破砕して、押出機により加熱溶融して、ダイスよ
り押し出して冷却した後、切断してペレットを得て、こ
のペレットに水分散状態で、ブタン、ペンタン等の発泡
剤を含浸することにより再生発泡性樹脂粒子を製造する
方法が知られている。また、押出機内の溶融樹脂中に発
泡剤を圧入して混練し、ダイスより押し出して冷却、切
断することにより、再生発泡性樹脂粒子を製造する方法
も公知である。
Conventionally, a used foamed polystyrene resin molded product is crushed, heated and melted by an extruder, extruded from a die, cooled, and then cut to obtain a pellet. A method for producing regenerated foamable resin particles by impregnating a foaming agent such as butane, pentane or the like is known. There is also known a method for producing regenerated foamable resin particles by press-fitting and kneading a foaming agent into a molten resin in an extruder, extruding from a die, cooling and cutting.

【0004】[0004]

【発明が解決しようとする課題】ところが、上記の従来
の方法で製造された発泡性ポリスチレン系樹脂粒子を、
水蒸気により加熱発泡成形した再生発泡成形体では、気
泡が極端に細かくなり、耐熱性が低下するばかりでな
く、予備発泡粒子同士の密着性が悪いために、満足な成
形外観を有するものを得ることができない。また、この
発泡成形体は、機械的強度が低い等の欠点がある。
However, the expandable polystyrene resin particles produced by the above-mentioned conventional method are
In the case of a regenerated foam molded article that is foamed by heating with water vapor, not only the cells become extremely fine and the heat resistance is reduced, but also the adhesiveness between the pre-expanded particles is poor, so that a molded article having a satisfactory molded appearance is obtained. Can not. Further, this foamed molded article has disadvantages such as low mechanical strength.

【0005】そこで特公昭58−24449号公報に
は、既に発泡したポリスチレン系樹脂粒子を原料とし
て、これに水分散状態で有機溶剤を加え、樹脂の軟化点
以上で攪拌した後、ブタン、ペンタン等の発泡剤を含浸
する方法が提案されている。また、特公昭58−244
50号公報には、同様の樹脂粒子を原料として、これに
水分散系でスチレン単量体を徐々に加えて発泡樹脂粒子
に吸収させ、加温して重合を行い、重合過程叉は重合後
に、ブタン、ペンタン等の発泡剤を含浸する方法が提案
されている。しかし、これらの方法で得られた発泡性ポ
リスチレン樹脂粒子は、元の発泡体を構成する多数の気
泡は消失して、全く気泡のない樹脂粒子となっており、
これを発泡成形して得られる発泡成形体の気泡状態、機
械的強度等は、ある程度改善されるものの、必ずしも十
分なものではない。しかも、これらの方法では、発泡し
たポリスチレン系樹脂成形体を、一旦もとの非発泡の樹
脂粒子の状態に戻してから発泡性樹脂粒子として再生す
るものであるため、工数がかかり、しかも多くの熱エネ
ルギーを必要とすることから、製造コスト的にも不利で
ある。
Japanese Patent Publication No. 58-24449 discloses that polystyrene resin particles which have already been foamed are used as a raw material, an organic solvent is added thereto in a water-dispersed state, and the mixture is stirred at a temperature higher than the softening point of the resin. Has been proposed. In addition, Japanese Patent Publication No. 58-244
No. 50 discloses that the same resin particles are used as a raw material, a styrene monomer is gradually added thereto in an aqueous dispersion to be absorbed by foamed resin particles, and heated to carry out polymerization. A method of impregnating a blowing agent such as butane and pentane has been proposed. However, in the expandable polystyrene resin particles obtained by these methods, a large number of bubbles constituting the original foam disappear, and the resin particles have no bubbles at all.
Although the foam state, mechanical strength, and the like of a foam molded article obtained by foam molding the foam are improved to some extent, they are not always sufficient. Moreover, in these methods, the expanded polystyrene-based resin molded body is returned to the original state of the non-expanded resin particles and then regenerated as the expandable resin particles. Since heat energy is required, it is disadvantageous in terms of manufacturing cost.

【0006】このように従来の方法では、発泡体を構成
する気泡を一旦消失させて、気泡を含まない樹脂粒子を
製造するという工程を経るために、工程が複雑になるば
かりでなく、加熱のために多くのエネルギーを消費する
とともに、加熱による樹脂の劣化によって、得られる再
生発泡体の品質が低下するという問題があった。
As described above, in the conventional method, since the bubbles constituting the foam are once eliminated to produce resin particles containing no bubbles, the process is not only complicated, but also involves heating. For this reason, there is a problem that a large amount of energy is consumed, and the quality of the obtained recycled foam is deteriorated due to deterioration of the resin due to heating.

【0007】[0007]

【課題を解決するための手段】本発明者等は、上記の課
題を解決するために、鋭意研究を重ねた結果、使用済の
発泡成形体を破砕した発泡樹脂粒子に、無機ガスを加圧
下において気相含浸するとともに、発泡粒子を圧縮した
状態で成形型内に充填し、発泡成形することにより、発
泡粒子の正常な気泡をそのまま利用して、成形体の煩雑
な工程を経ることなしに、しかも多くの熱エネルギーを
消費することなしに、容易に高品質の再生発泡成形体が
得られることを見いだし、本発明を完成するに至ったも
のである。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies in order to solve the above-mentioned problems, and as a result, an inorganic gas was applied to foamed resin particles obtained by crushing a used foamed molded product under pressure. In the gas phase impregnation, the foamed particles are filled into a mold in a compressed state, and foamed, so that the normal cells of the foamed particles can be used as they are, without going through complicated steps of the molded body. Further, they have found that a high-quality regenerated foam molded article can be easily obtained without consuming a large amount of heat energy, and have completed the present invention.

【0008】かくして本発明によれば、廃発泡ポリスチ
レン系樹脂成形体を破砕した発泡樹脂粒子に、その粒子
が合着しない緩和な温度下で、かつ加圧下において無機
ガスを気相含浸して、発泡樹脂粒子中に無機ガスを0.
5モル/kg(樹脂)以上含有させ、該無機ガス含有発泡
樹脂粒子を、成形型内充填後の発泡樹脂粒子のカサ容積
が元のカサ容積の70%以下になるように加圧ガスを用
いて圧縮しながら型内に供給し、基材樹脂のビカット軟
化点より10〜30℃高い温度域の水蒸気を導入して加
熱融着させて発泡成形体を得ることを特徴とする再生発
泡ポリスチレン系樹脂成形体の製造方法が提供される。
Thus, according to the present invention, the foamed resin particles obtained by crushing the waste foamed polystyrene resin molded article are gas-phase impregnated with an inorganic gas at a moderate temperature at which the particles do not coalesce and under pressure. Inorganic gas is added to the foamed resin particles in an amount of 0.
5 mol / kg (resin) or more, and pressurized gas is used so that the foam volume of the inorganic gas-containing foam resin particles after filling in the mold is 70% or less of the original foam volume. Recycled foamed polystyrene, characterized in that a foamed molded product is obtained by introducing into a mold while compressing the mixture, introducing steam in a temperature range higher by 10 to 30 ° C. than the Vicat softening point of the base resin, and heating and fusing the steam. A method for manufacturing a resin molded article is provided.

【0009】この発明おいて、その出発原料として用い
られる廃発泡ポリスチレン系樹脂成形体を構成する樹脂
としては、スチレン重合体、少なくとも50重量%以上
のスチレン成分と他の重合可能な不飽和化合物との共重
合体、これらの混合樹脂、スチレンとポリエチレンある
いはポリプロピレンとの架橋重合体、並びにこれらの樹
脂に適量のゴム状物質を添加した強化樹脂等があげられ
る。上記共重合可能な不飽和化合物としては、α−メチ
ルスチレン、アクリロニトリル、アクリル酸もしくはメ
タクリル酸と1〜8個の炭素原子を有するアルコールと
のエステル、マレイン酸、フマル酸と1〜8個の炭素原
子を有するアルコールとのエステル、無水マレイン酸等
や、更に少量の架橋剤として、ジビニルベンゼン、ブタ
ジエン、ポリエチレングリコールジメタクリレート等も
挙げることができる。廃発泡ポリスチレン系樹脂成形体
は、上記のポリスチレン系樹脂の粒子に発泡剤を含浸さ
せた発泡性樹脂粒子を、予備発泡した後、所定の成形型
内で発泡成形して得られる発泡成形体であって、各種容
器、緩衝包装材、その他一定の用途に供された後の、使
用済みの廃棄されるべき発泡成形体、及びこれらの成形
体を製造するときに副生する成形不良品等が含まれる。
なお、廃発泡ポリスチレン系樹脂成形体としては、上記
の樹脂を押出発泡して得られた発泡成形体の使用済み成
形体、成形不良品、トリミング時の裁断屑等を原料とす
ることも可能である。
In the present invention, the resin constituting the waste foamed polystyrene resin molded article used as a starting material is a styrene polymer, at least 50% by weight or more of a styrene component and another polymerizable unsaturated compound. And mixed resins thereof, crosslinked polymers of styrene and polyethylene or polypropylene, and reinforced resins obtained by adding an appropriate amount of a rubbery substance to these resins. Examples of the copolymerizable unsaturated compound include α-methylstyrene, acrylonitrile, an ester of acrylic acid or methacrylic acid with an alcohol having 1 to 8 carbon atoms, maleic acid, fumaric acid and 1 to 8 carbon atoms. Esters with an alcohol having an atom, maleic anhydride and the like, and as a small amount of a crosslinking agent, divinylbenzene, butadiene, polyethylene glycol dimethacrylate and the like can also be mentioned. A waste foamed polystyrene resin molded product is a foam molded product obtained by pre-foaming foamable resin particles obtained by impregnating the above polystyrene resin particles with a foaming agent, and then performing foam molding in a predetermined mold. In addition, after being used for various containers, cushioning packaging materials, and other certain uses, used foamed molded products to be discarded, and defective molded products produced as by-products when manufacturing these molded products. included.
In addition, as the waste expanded polystyrene resin molded article, it is also possible to use as a raw material a used molded article of a foamed molded article obtained by extrusion foaming the above resin, a defective molded article, cutting waste during trimming, and the like. is there.

【0010】なお、発泡成形体を構成する樹脂中には、
充填剤、可塑剤、難燃剤、滑剤、着色剤、紫外線吸収
剤、酸化防止剤等、種々の添加剤が含有されていてもよ
い。本発明において、出発原料として用いる廃発泡ポリ
スチレン系樹脂成形体の基材樹脂は、単一の樹脂種を使
用することが望ましいが、発泡体の熱的性質(発泡成形
性)、気泡サイズ(成形品外観)がほぼ同等であれば、
2種以上の基材樹脂を混合して使用することもできる。
[0010] In the resin constituting the foam molded article,
Various additives such as a filler, a plasticizer, a flame retardant, a lubricant, a coloring agent, an ultraviolet absorber, and an antioxidant may be contained. In the present invention, it is desirable to use a single resin type as the base resin of the waste expanded polystyrene resin molded article used as a starting material, but the thermal properties of the foam (foaming moldability) and the cell size (molding) Product appearance) are almost the same,
Two or more base resins may be used in combination.

【0011】また、廃発泡ポリスチレン系樹脂成形体
は、その用途に応じて発泡倍数が異なるが、本発明方法
によって均質な再生発泡成形体を得るためには、ほぼ同
じ発泡倍数の成形体を分別して原料として使用すること
が望ましい。廃発泡成形体の大半を占める家電製品の緩
衝包装材、魚介類用容器、リンゴ箱等は、およそ50〜
60倍の発泡成形体である。しかし、この程度のばらつ
き範囲内であれば、本願の原料として特に支障なく使用
することができる。
Although the waste expanded polystyrene resin molded article has a different expansion factor depending on its use, in order to obtain a homogeneous regenerated expanded molded article by the method of the present invention, a molded article having substantially the same expansion factor is divided. It is desirable to use it separately as a raw material. Buffer packaging materials for home appliances, fish and shellfish containers, apple boxes, etc., which occupy the majority of waste foam molded products, are approximately 50-
It is a 60 times expanded molded article. However, as long as it is within such a range of variation, it can be used as a raw material of the present invention without any particular problem.

【0012】廃発泡ポリスチレン系樹脂成形体は、破砕
機あるいは裁断機、その他任意の方法により、ほぼ球
状、立方体状等の形状を有する発泡樹脂粒子に破砕され
る。発泡樹脂粒子の平均粒子径は、再生発泡成形する成
形体の大きさにより適宜決められるが、一般的には、5
〜50mmであり、好ましくは10〜30mm程度である。
平均粒子径が50mmより大きい場合には、空気輸送時に
配管が詰まったり、成形型への充填性が悪くなる。一方
平均粒子径が5mmよりも小さい場合には、発泡成形体の
破砕時に発泡体の気泡が破壊されて、独立気泡率が低下
し、発泡成形時に十分な発泡性が得られず正常な発泡成
形体が得られない。
The waste foamed polystyrene resin molded product is crushed into foamed resin particles having a substantially spherical or cubic shape by a crusher or a cutter, or any other method. The average particle diameter of the foamed resin particles is appropriately determined depending on the size of the molded article to be regenerated and foamed.
5050 mm, preferably about 10-30 mm.
If the average particle diameter is larger than 50 mm, the pipes will be clogged during pneumatic transportation, or the filling property of the mold will be poor. On the other hand, if the average particle size is smaller than 5 mm, the foam cells are destroyed when the foam molding is crushed, the closed cell ratio is reduced, and sufficient foaming property cannot be obtained at the time of foam molding. I can't get my body.

【0013】本発明で使用する発泡樹脂粒子の独立気泡
率は、65%以上、好ましくは80%以上であることが
必要である。発泡成形体を破砕するときに発生する不適
当な微粒子が多量に含まれる場合は、ふるい分けして微
粒子を除去することが望ましい。また破砕機あるいは裁
断機としては、発泡成形体の気泡をできるだけ破壊しな
いで、しかも微細粒子の発生を抑え、粒子径が揃い、球
状、立方体に近い形状の所望の発泡粒子が得られるもの
が好適に使用される。
The closed cell ratio of the expanded resin particles used in the present invention must be 65% or more, preferably 80% or more. When a large amount of inappropriate fine particles generated when crushing the foam molded article is contained, it is desirable to remove the fine particles by sieving. Further, as the crushing machine or the cutting machine, the one which can obtain the desired foamed particles having a shape similar to a sphere or a cubic shape without breaking the bubbles of the foamed product as much as possible, suppressing the generation of fine particles, having a uniform particle diameter, and preferably a cubic shape is preferable. Used for

【0014】本発明においては、まず上記発泡樹脂粒子
に、この粒子が合着しない緩和な温度下で、かつ加圧下
において、無機ガスを気相含浸する。本発明における無
機ガスとしては、炭酸ガス、窒素、空気等が用いられ、
これらは単独であるいは混合して使用される。無機ガス
の含浸処理は、耐圧密閉容器内で、発泡樹脂粒子が合着
しない緩和な温度下で行われる。ここで緩和な温度と
は、含浸処理中に発泡粒子間で合着が生起せず、かつ発
泡粒子が収縮しない温度を意味し、具体的には基材樹脂
のビカット軟化点より少なくとも20℃以上低い温度域
をいう。好ましい温度域は、使用する発泡樹脂粒子の基
材樹脂によって変化し、また無機ガスによっても変化す
るが、通常無機ガスの実質的含浸量を多くできること、
及び耐圧容器の内圧を低めに設定できること等から、含
浸処理温度は、より低温が望ましく、40℃以下が好ま
しい。しかし0℃以下の場合には、通常冷却のために工
業的にエネルギー消費量が大きくなり、好ましくない。
無機ガスの含浸速度の面からは、高い温度が望ましい
が、ガス含浸量が減少するために、炭酸ガスの場合、好
ましくは5〜40℃であり、窒素、空気の場合5〜30
℃である。なお基材樹脂のビカット軟化点−20℃以上
の温度で含浸を行うときには、発泡成形するまでに多量
のガスが逸散してしまい、発泡性が低下して、良好な発
泡成形体が得られない。
In the present invention, first, the foamed resin particles are gas-phase impregnated with an inorganic gas at a moderate temperature at which the particles do not coalesce and under pressure. As the inorganic gas in the present invention, carbon dioxide, nitrogen, air and the like are used,
These may be used alone or as a mixture. The impregnation treatment with an inorganic gas is performed in a pressure-tight container at a moderate temperature at which the foamed resin particles do not coalesce. Here, the mild temperature means a temperature at which coalescence does not occur between the foamed particles during the impregnation process and the foamed particles do not shrink, and specifically, at least 20 ° C. or more from the Vicat softening point of the base resin. Refers to the low temperature range. The preferred temperature range varies depending on the base resin of the foamed resin particles to be used, and also varies depending on the inorganic gas.However, it is usually possible to increase the substantial impregnation amount of the inorganic gas.
In view of the fact that the internal pressure of the pressure vessel can be set lower, the impregnation temperature is desirably lower, and is preferably 40 ° C. or lower. However, when the temperature is 0 ° C. or lower, energy consumption is industrially large for cooling usually, which is not preferable.
From the viewpoint of the impregnation rate of the inorganic gas, a high temperature is desirable, but in order to reduce the gas impregnation amount, it is preferably 5 to 40 ° C. in the case of carbon dioxide gas, and 5 to 30 ° C. in the case of nitrogen and air.
° C. When the impregnation is performed at a temperature higher than the Vicat softening point of the base resin −20 ° C., a large amount of gas is dissipated until foaming is performed, the foaming property is reduced, and a good foamed molded article is obtained. Absent.

【0015】かかる緩和な温度条件下においては、無機
ガスは樹脂に対して溶媒として作用することがないた
め、発泡樹脂粒子同士が合着する恐れはない。したがっ
て、発泡樹脂粒子を静置した状態で、無機ガスのガス含
浸を行うことができる。また静置して無機ガスを含浸す
るに際して、加圧下の無機ガスを、ポンプ等により吸引
して調温室を通した後、容器下部に戻す等して循環させ
てもよい。
Under such a mild temperature condition, the inorganic gas does not act as a solvent for the resin, so that there is no possibility that the foamed resin particles coalesce. Therefore, the gas impregnation with the inorganic gas can be performed while the foamed resin particles are left still. In addition, when the inorganic gas is impregnated by standing, the inorganic gas under pressure may be sucked by a pump or the like and passed through a temperature control chamber, and then returned to the lower part of the container and circulated.

【0016】発泡樹脂粒子に無機ガスを含浸させる適当
な圧力は、1kg/cm2G以上、好ましくは2〜10kg/cm2
Gである。無機ガスの含浸は、無機ガスの種類、含浸圧
力、基材樹脂の種類、及び発泡樹脂粒子の粒子径等によ
って異なるが、少なくとも無機ガスが0.5モル/kg
(樹脂)以上含浸するまで行われ、通常1時間以内に達
成される。なお、発泡樹脂粒子内の無機ガス含有量は、
容器内で加圧下にある発泡樹脂粒子を容器から取り出
し、発泡樹脂粒子から逸散する無機ガスの容量または重
量を測定することにより求めることができる。
An appropriate pressure for impregnating the foamed resin particles with the inorganic gas is 1 kg / cm 2 G or more, preferably 2 to 10 kg / cm 2.
G. The impregnation of the inorganic gas depends on the type of the inorganic gas, the impregnation pressure, the type of the base resin, the particle size of the foamed resin particles, etc., but at least the inorganic gas is 0.5 mol / kg.
(Resin) This is carried out until the above impregnation, and is usually achieved within one hour. In addition, the inorganic gas content in the expanded resin particles,
It can be determined by taking out the foamed resin particles under pressure in the container from the container and measuring the volume or weight of the inorganic gas that escapes from the foamed resin particles.

【0017】発泡樹脂粒子からの無機ガス逸散は比較的
速いことから、無機ガスが含浸された発泡樹脂粒子は、
成形型内に充填された時点で無機ガスを少なくとも0.
5モル/kg(樹脂)以上含有していることが必要であ
る。発泡樹脂粒子中の無機ガス含有量が、0.5モル/
kg(樹脂)未満なると発泡力が不足して、良好な発泡成
形体を得ることが難しい。
Since the escape of the inorganic gas from the foamed resin particles is relatively fast, the foamed resin particles impregnated with the inorganic gas are:
At the time of filling the mold, the inorganic gas is filled with at least 0.1%.
It is necessary to contain 5 mol / kg (resin) or more. When the inorganic gas content in the expanded resin particles is 0.5 mol /
If the weight is less than kg (resin), the foaming power is insufficient, and it is difficult to obtain a good foam molded article.

【0018】なお本発明では、無機ガスを使用するもの
であるが、本発明の効果が阻害されない限り、若干の揮
発性有機発泡剤を併用することも可能である。例えばプ
ロパン、ブタン等を、無機ガス1に対して、少量例えば
0.2以下のモル比で併用しても同様の効果を得ること
ができる。次いでこのようにして無機ガスを含浸した発
泡樹脂粒子を、加圧ガスを用いて圧縮しながら成形型内
に充填する。通常の予備発泡粒子の空間率は、約35〜
40%である。これに対して、本発明で使用される廃発
泡ポリスチレン系樹脂成形体を破砕した発泡樹脂粒子
は、カサ容積が大きく、空間率は約50〜60%とな
る。したがって、発泡成形時に十分な発泡性を得るため
には、発泡樹脂粒子を成形内に充填するに際して、発泡
粒子間の空間を小さくしておくことが必要となる。そこ
で、本願発明においては、成形型内に充填された発泡樹
脂粒子のカサ容積が、元のカサ容積の70%以下、より
好ましくは65%以下、40%以上になるよう圧縮しな
がら成形型内に供給する。発泡樹脂粒子の圧縮が70%
に満たないとには、発泡成形時に発泡力が不足して、発
泡樹脂粒子間の空間を十分に埋めることができず、隙間
ができて発泡成形体の外観が悪くなる。一方圧縮が40
%を越えると、過大な耐圧容器が必要となる割に、その
改善効果はあまり認められない。また過剰充填の兆候を
示し、成形時の水蒸気の通過が抑制され、発泡粒子間の
融着を阻害原因となる。
In the present invention, an inorganic gas is used. However, as long as the effects of the present invention are not impaired, a small amount of a volatile organic foaming agent can be used in combination. For example, the same effect can be obtained by using propane, butane, or the like in a small amount, for example, 0.2 or less with respect to 1 of the inorganic gas. Next, the foamed resin particles impregnated with the inorganic gas in this manner are filled in a molding die while being compressed using a pressurized gas. The porosity of normal pre-expanded particles is about 35-
40%. On the other hand, the foamed resin particles obtained by crushing the waste foamed polystyrene resin molded article used in the present invention have a large bulk and a porosity of about 50 to 60%. Therefore, in order to obtain sufficient foaming property during foam molding, it is necessary to reduce the space between foamed particles when filling the foamed resin particles into the molding. Therefore, in the present invention, the foamed resin particles filled in the mold are compressed so that the bulk of the foamed resin particles becomes 70% or less, more preferably 65% or less, and 40% or more of the original bulk. To supply. 70% compression of expanded resin particles
If it is less than the above range, the foaming power will be insufficient at the time of foam molding, the space between the foamed resin particles cannot be sufficiently filled, a gap will be formed, and the appearance of the foamed molded article will be deteriorated. On the other hand, compression is 40
%, The improvement effect is not so much recognized, although an excessive pressure vessel is required. Further, it shows a sign of overfilling, suppresses passage of water vapor during molding, and inhibits fusion between the foamed particles.

【0019】また本発明では、発泡樹脂粒子の圧縮状態
を維持するために、発泡樹脂粒子の充填前、及び充填中
の成形型内を、加圧状態に維持しておくことが望まし
い。発泡樹脂粒子を加熱成形して得られる再生発泡成形
体の発泡倍数は、元の廃発泡樹脂成形体の発泡倍数と、
加圧下の発泡樹脂粒子の圧縮率で決まり、成形型内での
発泡粒子のカサ倍数が、再生発泡成形体の発泡倍数とな
る。したがって、成形型内の内圧を、予め所定の加圧状
態に設定しておいて、発泡樹脂粒子を加圧充填する必要
がある。
In the present invention, in order to maintain the compressed state of the foamed resin particles, it is desirable to maintain the inside of the mold before and during filling with the foamed resin particles in a pressurized state. The foaming multiple of the recycled foamed molded article obtained by heat molding the foamed resin particles is the foaming multiple of the original waste foamed resin molded article,
It is determined by the compression ratio of the expanded resin particles under pressure, and the multiple of the expanded particles in the mold becomes the expanded multiple of the regenerated expanded molded article. Therefore, it is necessary to previously set the internal pressure in the mold to a predetermined pressurized state, and then pressurize and fill the foamed resin particles.

【0020】本発明において、発泡樹脂粒子の加圧充
填、型内加圧に用いるガスとしては、気相含浸時に用い
る無機ガスを使用できるが、通常は圧縮空気が好適に使
用される。本発明においては、成形型の加圧状態を解放
して圧抜きをして成形型の内圧を大気圧に戻し、発泡粒
子間のガスを排出すると共に、圧縮された発泡粒子を膨
張復元した後、成形型に水蒸気を導入して発泡粒子を加
熱融着させて、発泡成形体を成形する。なお、発泡粒子
間のガスの排出は、型を加圧状態に維持したままで、水
蒸気を導入することにより、水蒸気を流通させて行って
もよい。加熱成形して得られた発泡成形体は、冷却水に
より冷却した後、成形型から取り出される。
In the present invention, as a gas used for filling the foamed resin particles under pressure and pressurizing the inside of the mold, an inorganic gas used at the time of gas phase impregnation can be used, but usually compressed air is preferably used. In the present invention, after the pressurized state of the mold is released and depressurized to return the internal pressure of the mold to atmospheric pressure, the gas between the foamed particles is exhausted, and the compressed foamed particles are expanded and restored. Then, steam is introduced into the mold and the foamed particles are heated and fused to form a foamed molded article. The gas between the foamed particles may be discharged by introducing steam while keeping the mold in a pressurized state so that the steam is allowed to flow. The foam molded body obtained by the heat molding is taken out of the mold after cooling with cooling water.

【0021】発泡樹脂粒子の加熱成形に用いられる水蒸
気は、基材樹脂のビカット軟化点より10〜30℃高い
温度域になるように制御され、より好ましくは10〜2
0℃高い温度域に制御される。成形時の水蒸気温度がビ
カット軟化点+10℃より低い温度では、発泡速度が遅
く、無機ガスの外部への逸散が優位となって十分な発泡
効果が得られず、その結果、高品質の発泡成形体が得ら
れない。またビカット軟化点+30℃以上の温度域の場
合には、発泡適正幅が極度に狭くなり、工業的に正常な
発泡成形体を得ることが極めて困難である。なお、成形
加熱時間は、発泡成形体の大きさや発泡倍数等によって
変化するが、一般に10〜180秒程度であり、好まし
くは約15〜90秒である。なお、水蒸気としては、水
蒸気−空気混合媒体を用いることも可能である。
The water vapor used for heat molding the foamed resin particles is controlled so as to be in a temperature range higher by 10 to 30 ° C. than the Vicat softening point of the base resin, and more preferably by 10 to 2 ° C.
The temperature is controlled to be higher by 0 ° C. If the water vapor temperature at the time of molding is lower than the Vicat softening point + 10 ° C., the foaming rate is slow, and the escape of the inorganic gas to the outside becomes dominant, and a sufficient foaming effect cannot be obtained. As a result, high quality foaming A molded product cannot be obtained. In the case of a temperature range of not less than the Vicat softening point + 30 ° C., the appropriate foaming width becomes extremely narrow, and it is extremely difficult to obtain an industrially normal foamed molded product. In addition, the molding heating time varies depending on the size of the foam molded article, the number of times of foaming, and the like, but is generally about 10 to 180 seconds, and preferably about 15 to 90 seconds. In addition, as the steam, a steam-air mixed medium can be used.

【0022】以上のようにして、発泡樹脂粒子に無機ガ
スを含浸し、成形型に加圧充填した後、加熱成形して得
られた本願の再生発泡成形体は、建築用途の断熱壁材や
床下地材、及び土木用途の軟弱地盤改良用EPS土木工
法の埋設材等として好適に使用される。これらの用途に
おいては、本願の再生発泡成形体は、比較的に肉厚なブ
ロック形状、あるいは板状の形状とされ、特に複雑な形
状に成形する必要のないことから、何等支障なく使用す
ることができる。これら用途については、望まれる発泡
成形体の発泡倍数は、40〜50程度であって、使用済
みの家電製品の緩衝包装材、あるいは魚介類や生鮮食品
の運搬容器等を、本願発明の原料として好適に使用され
る。
As described above, the regenerated foam molded article of the present invention obtained by impregnating the foamed resin particles with the inorganic gas, filling the mold with pressure, and then subjecting the molded article to heat molding is a heat-insulating wall material for architectural use. It is suitably used as a flooring material, as a buried material in an EPS civil engineering method for improving soft ground for civil engineering, and the like. In these applications, the reclaimed foam molded article of the present application is formed into a relatively thick block shape or plate shape, and it is not necessary to mold it into a complicated shape. Can be. For these applications, the desired foaming multiple of the foamed molded product is about 40 to 50, and a buffer packaging material for used home electric appliances, or a transport container for fish and shellfish or fresh food, etc., is used as a raw material of the present invention. It is preferably used.

【0023】なお、本発明により得られた再生発泡体
を、上記の建築用途あるいは土木用途に使用する場合に
は、発泡成形体に自消性、難燃性を付与することが必要
となる。再生発泡成形体に自消性、難燃性を付与するに
は、発泡樹脂粒子の表面に、難燃剤、必要に応じて難燃
助剤加えて、被覆処理したものを、発泡成形すればよ
い。難燃剤としては、臭素化脂環族化合物、臭素化芳香
族化合物、臭素化芳香族ポリマー、臭素化フェニル(メ
タ)アクリル酸エステル等が好適に使用される。難燃剤
が粉末状の場合、JIS標準ふるい149μ通過の微粉
末を使用することが、粒子表面への付着性の面から望ま
しい。また、粒子に対する付着を確実にするために、適
度な粘性を有する液状難燃剤を一部被覆した後に、粉末
状難燃剤を被覆展着処理してもよい。更に比較的低融点
を有する粉末状難燃剤を、加温して溶融させて被覆処理
してもよい。かかる難燃剤としては、比較的少量の使用
で自消性をもたらし、発泡樹脂粒子表面への付着性がよ
く、成形時に発泡粒子間の融着を阻害せず、耐候性がよ
く、しかも樹脂基材を劣化させないものとして、ヘキサ
ブロモシクロドデカン、テトラブロモシクロオクタン、
トリブロモフェニルアリルエーテル、ペンタブロモフェ
ニルアリルエーアル、テトラブロモビスフェールのビス
アリールエーテル、テトラブロモビスフェノールのビス
ジブロモプロピルエーテル等が、特に好適に使用され
る。これらの難燃剤は、発泡樹脂粒子に対して、0.5
〜2.0重量%、より好ましくは0.8〜1.5重量%
の範囲で使用される。また、有機過酸化物等の、例えば
O−O、C−C、N=N結合を有する化合物を難燃助剤
として、0.1〜0.5重量%、難燃剤と併用して使用
してもよい。好ましい難燃助剤の例としては、ジクミル
パーオキサイド、1、1−ジフェニルビシクロヘキシ
ル、アゾジイソブチロニトリル等が挙げられる。
When the reclaimed foam obtained by the present invention is used for the above-mentioned architectural or civil engineering applications, it is necessary to impart self-extinguishing properties and flame retardancy to the foamed molded article. In order to impart self-extinguishing properties and flame retardancy to the regenerated foam molded article, a flame-retardant and, if necessary, a flame-retardant auxiliary agent may be added to the surface of the foamed resin particles, and the coated article may be subjected to foam molding. . As the flame retardant, a brominated alicyclic compound, a brominated aromatic compound, a brominated aromatic polymer, a brominated phenyl (meth) acrylate, and the like are suitably used. When the flame retardant is in a powder form, it is desirable to use a fine powder that passes 149 μm according to a JIS standard sieve from the viewpoint of adhesion to the particle surface. Further, in order to ensure the adhesion to the particles, the powdered flame retardant may be coated and spread after partially coating the liquid flame retardant having an appropriate viscosity. Further, a powdery flame retardant having a relatively low melting point may be heated and melted for coating. Such a flame retardant provides self-extinguishing properties when used in a relatively small amount, has good adhesion to foamed resin particle surfaces, does not inhibit fusion between foamed particles during molding, has good weather resistance, and has a resin base. Hexabromocyclododecane, tetrabromocyclooctane,
Tribromophenyl allyl ether, pentabromophenyl allyl ether, bisaryl ether of tetrabromobisphenol, bisdibromopropyl ether of tetrabromobisphenol, and the like are particularly preferably used. These flame retardants are used in an amount of 0.5 to the foamed resin particles.
To 2.0% by weight, more preferably 0.8 to 1.5% by weight
Used in the range. Further, a compound having, for example, an O—O, C—C, N = N bond such as an organic peroxide is used as a flame retardant auxiliary in an amount of 0.1 to 0.5% by weight in combination with the flame retardant. You may. Preferred examples of the flame retardant aid include dicumyl peroxide, 1,1-diphenylbicyclohexyl, azodiisobutyronitrile, and the like.

【0024】また本発明の発泡樹脂粒子には、成形型へ
の充填性を改善する滑剤、成形時の融着促進剤、成形冷
却時間短縮剤、帯電防止剤、着色剤等の表面処理剤を被
覆してもよい。具体的には、エチレンビスステアロアミ
ド、高級脂肪酸、高級脂肪酸アミド、食用油、高級脂肪
酸トリグリセライド、高級脂肪酸モノグリセライド、パ
ラフィンワックス、ポリエチレンワックス、ジンクステ
アレート等を挙げることができる。
Further, the foamed resin particles of the present invention are provided with a surface treatment agent such as a lubricant for improving the filling property into a molding die, a fusion promoter during molding, a molding cooling time shortening agent, an antistatic agent and a coloring agent. It may be coated. Specific examples include ethylene bis stearamide, higher fatty acid, higher fatty acid amide, edible oil, higher fatty acid triglyceride, higher fatty acid monoglyceride, paraffin wax, polyethylene wax, zinc stearate and the like.

【0025】なお、かかる表面被覆処理は、無機ガスの
含浸に先だって、リボンブレンダー、タンブラー、レー
ディゲミキサー、ナウターミキサー、スーパーミキサー
等を利用して行われる。または無機ガスの含浸容器が回
転もしくは攪拌機能を有するものであれば、ガス含浸時
に同時に被覆処理を行ってもよい。
The surface coating treatment is performed by using a ribbon blender, a tumbler, a Lodige mixer, a Nauter mixer, a super mixer or the like before the impregnation with the inorganic gas. Alternatively, if the container impregnated with the inorganic gas has a rotating or stirring function, the coating treatment may be performed simultaneously with the gas impregnation.

【0026】[0026]

【実施例】以下、本発明を実施例を用いて説明するが、
これにより本発明は限定されるものではなく、本発明の
範囲内で種々の変更が可能である。家電製品の緩衝包装
材として使用された発泡性ポリスチレン樹脂粒子の発泡
成形品を、破砕機で粒子径約10〜20mmに破砕し、こ
れを再生発泡体成形の出発原料として用いた。この破砕
した発泡樹脂粒子に難燃剤として、テトラブロモビスフ
ェノールのビスアリルエーテルを1.2重量%、スーパ
ミキサーを用いて表面被覆処理した。この難燃剤を被覆
した発泡粒子を、容積1000mlの耐圧容器に入れ、密
閉し、無機ガスを所定圧力で、全体を調温しながら1時
間保持して発泡樹脂粒子に無機ガスを含浸した。次い
で、加圧状態に維持した、内寸が30×7.5×2.5
cmの型窩有した成形型内に、上記の無機ガスを含浸した
発泡粒子を充填した。樹脂粒子の充填後、成形型の加圧
状態を解除して、成形型内の無機ガスを排出し、所定温
度の水蒸気を導入して加熱発泡することにより、再生発
泡成形体を製造した。
Hereinafter, the present invention will be described with reference to examples.
Accordingly, the present invention is not limited, and various changes can be made within the scope of the present invention. An expanded molded article of expandable polystyrene resin particles used as a buffer packaging material for home appliances was crushed by a crusher to a particle diameter of about 10 to 20 mm, and this was used as a starting material for forming a recycled foam. The crushed foamed resin particles were subjected to a surface coating treatment using 1.2% by weight of bisallyl ether of tetrabromobisphenol as a flame retardant using a super mixer. The foamed particles coated with the flame retardant were placed in a pressure-resistant container having a capacity of 1000 ml, sealed, and kept at a predetermined pressure for 1 hour while controlling the temperature of the inorganic gas to impregnate the foamed resin particles with the inorganic gas. Next, the inner dimensions were 30 × 7.5 × 2.5, maintained in a pressurized state.
The foamed particles impregnated with the above-mentioned inorganic gas were filled in a mold having a cm cavity. After the resin particles were filled, the pressurized state of the mold was released, the inorganic gas in the mold was discharged, steam at a predetermined temperature was introduced, and the foam was heated and foamed to produce a regenerated foamed article.

【0027】無機ガスの含浸条件、型内成形条件、及び
得られた再生発泡成形体について表1に示す。なお出発
原料として用いた廃発泡成形体は、一度使用した家電製
品の緩衝包装材であって、実施例1、比較例1、2、
4、5、および6は55倍発泡品、実施例2、比較例3
は40倍発泡品、実施例3は60倍発泡品である。これ
らの基材樹脂は、ポリスチレンである。
Table 1 shows the impregnation conditions of the inorganic gas, the molding conditions in the mold, and the obtained regenerated foamed molded product. The waste foam molded article used as a starting material was a buffer packaging material for home appliances used once, and was used in Example 1, Comparative Examples 1, 2,
4, 5, and 6 are 55 times expanded products, Example 2, Comparative Example 3
Is a 40-fold expanded product, and Example 3 is a 60-fold expanded product. These base resins are polystyrene.

【0028】実施例4は、スチレン92%、無水マレイ
ン酸8%の共重合体の40倍発泡成形品である。実施例
1〜4は何れも製造上支障はなく、得られた再生発泡成
形体は、均質で融着良好な高品質のものであった。得ら
れた再生発泡成形体について、JISK−7201の酸
素指数法による燃焼試験方法に準拠して自消性を評価し
た結果、酸素指数26以上であり、良好な難燃性を有し
ていた。これに対し比較例1は、無機ガス含浸温度が高
過ぎて、発泡樹脂粒子が収縮する兆候があった。比較例
2は成形型充填時に、発泡樹脂粒子の圧縮が不足して、
高倍となり正常な成形ができなかった。比較例3は、無
機ガスの含浸圧力が不足して正常な成形ができなかっ
た。比較例4は、成形時の水蒸気温度が低く、発泡粒子
間の融着が不良であった。比較例5は、成形時の水蒸気
温度が高く、発泡成形体が収縮した。比較例6は、発泡
粒子が過剰に充填され、発泡粒子間の融着が不良であっ
た。
Example 4 is a 40-fold foam molded article of a copolymer of 92% styrene and 8% maleic anhydride. In all of Examples 1 to 4, there was no problem in production, and the obtained regenerated foamed molded product was of high quality with uniform and good fusion. The self-extinguishing property of the obtained regenerated foam molded article was evaluated in accordance with the combustion test method based on the oxygen index method of JIS K-7201, and as a result, the oxygen index was 26 or more, indicating that the article had good flame retardancy. On the other hand, in Comparative Example 1, the inorganic resin impregnation temperature was too high, and there was a sign that the foamed resin particles contracted. In Comparative Example 2, the compression of the foamed resin particles was insufficient at the time of filling the mold,
It was high magnification, and normal molding could not be performed. In Comparative Example 3, normal molding was not possible due to insufficient impregnation pressure of the inorganic gas. In Comparative Example 4, the steam temperature during molding was low, and the fusion between the foamed particles was poor. In Comparative Example 5, the steam temperature during molding was high, and the foamed molded product shrank. In Comparative Example 6, the expanded particles were excessively filled, and the fusion between the expanded particles was poor.

【0029】[0029]

【表1】 [Table 1]

【0030】[0030]

【発明の効果】本発明によれば、使用済みの発泡ポリス
チレン系樹脂成形体を破砕した発泡樹脂粒子に、無機ガ
スを加圧下において気相含浸するとともに、発泡粒子を
圧縮した状態で成形型内に充填し、発泡成形することに
より、発泡粒子の正常な気泡をそのまま利用して、廃発
泡体の減容化、リペレット、発泡剤含浸、予備発泡、加
熱成形という従来の煩雑な工程を経ることなしに、しか
も多くの熱エネルギーを消費することなしに、高品質の
再生発泡成形体を製造することができる。そして、本発
明により得られた再生発泡成形体は、建築用途、土木用
途をはじめ、多くの分野に利用可能である。
According to the present invention, a foamed resin particle obtained by crushing a used foamed polystyrene resin molded body is impregnated with an inorganic gas under pressure in a gas phase, and the foamed particles are compressed and placed in a molding die. By using the normal cells of the foamed particles as they are, and performing the conventional complicated steps of volume reduction of waste foam, repellet, impregnation of foaming agent, prefoaming, and heat molding. A high-quality regenerated foamed molded article can be produced without using any heat energy. The recycled foam molded article obtained according to the present invention can be used in many fields including architectural applications and civil engineering applications.

【0031】本発明の再生発泡成形体の製造方法は、大
量に発生する使用済み発泡成形体を有効に再生すること
ができ、廃棄処理対策あるいは資源の有効利用法として
多大な効果が得られる。
The method for producing a regenerated foam molded article of the present invention can effectively recycle a large amount of used foam molded articles, and has a great effect as a disposal treatment measure or a method for effectively utilizing resources.

フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B29K 105:26 C08L 25:00 Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI Technical display location B29K 105: 26 C08L 25:00

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 廃発泡ポリスチレン系樹脂成形体を破砕
した発泡樹脂粒子に、その粒子が合着しない緩和な温度
下で、かつ加圧下において無機ガスを気相含浸して、発
泡樹脂粒子中に無機ガスを0.5モル/kg(樹脂)以上
含有させ、該無機ガス含有発泡樹脂粒子を、成形型内充
填後の発泡樹脂粒子のカサ容積が元のカサ容積の70%
以下になるように加圧ガスを用いて圧縮しながら型内に
供給し、基材樹脂のビカット軟化点より10〜30℃高
い温度域の水蒸気を導入して加熱融着させて発泡成形体
を得ることを特徴とする再生発泡ポリスチレン系樹脂成
形体の製造方法。
1. A foamed resin particle obtained by crushing a waste foamed polystyrene-based resin molded article is impregnated with an inorganic gas in a gaseous phase under a moderate temperature and under a pressure at which the particles are not coalesced, so that the foamed resin particles are At least 0.5 mol / kg (resin) of an inorganic gas is contained, and the foam volume of the foamed resin particles after filling in the mold is 70% of the original foam volume.
It is supplied into the mold while compressing using a pressurized gas so that the foamed molded body is heated and fused by introducing steam in a temperature range higher than the Vicat softening point of the base resin by 10 to 30 ° C. A method for producing a recycled foamed polystyrene resin molded article, characterized by being obtained.
JP6695092A 1992-03-25 1992-03-25 Method for producing recycled expanded polystyrene resin molded article Expired - Lifetime JP2637664B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6695092A JP2637664B2 (en) 1992-03-25 1992-03-25 Method for producing recycled expanded polystyrene resin molded article

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6695092A JP2637664B2 (en) 1992-03-25 1992-03-25 Method for producing recycled expanded polystyrene resin molded article

Publications (2)

Publication Number Publication Date
JPH05271459A JPH05271459A (en) 1993-10-19
JP2637664B2 true JP2637664B2 (en) 1997-08-06

Family

ID=13330807

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6695092A Expired - Lifetime JP2637664B2 (en) 1992-03-25 1992-03-25 Method for producing recycled expanded polystyrene resin molded article

Country Status (1)

Country Link
JP (1) JP2637664B2 (en)

Also Published As

Publication number Publication date
JPH05271459A (en) 1993-10-19

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