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JP2002120224A - Recycling method of glass fiber reinforced thermoplastic resin - Google Patents

Recycling method of glass fiber reinforced thermoplastic resin

Info

Publication number
JP2002120224A
JP2002120224A JP2000315019A JP2000315019A JP2002120224A JP 2002120224 A JP2002120224 A JP 2002120224A JP 2000315019 A JP2000315019 A JP 2000315019A JP 2000315019 A JP2000315019 A JP 2000315019A JP 2002120224 A JP2002120224 A JP 2002120224A
Authority
JP
Japan
Prior art keywords
thermoplastic resin
glass fiber
fiber reinforced
reinforced thermoplastic
regenerated
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
JP2000315019A
Other languages
Japanese (ja)
Inventor
Osamu Fujii
修 藤井
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.)
Asahi Kasei Corp
Original Assignee
Asahi Kasei Corp
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 Asahi Kasei Corp filed Critical Asahi Kasei Corp
Priority to JP2000315019A priority Critical patent/JP2002120224A/en
Publication of JP2002120224A publication Critical patent/JP2002120224A/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

  • Processes Of Treating Macromolecular Substances (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

(57)【要約】 【課題】 ガラス繊維強化熱可塑性樹脂を再溶融混練
し、再利用するいわゆる、マテリアルリサイクルの方法
において、ガラス繊維の折損に伴う機械的特性の劣化を
極力抑制し、再生材を非再生材に高濃度に配合し、再生
率を向上させ、効率的かつ、経済的にリサイクル出来る
方法を提供すること。 【解決手段】 ガラス繊維強化熱可塑性樹脂を再溶融混
練して、再生する方法において、(A)再生用ガラス繊
維強化熱可塑性樹脂、(B)非再生熱可塑性樹脂、およ
び(C)非再生ガラス繊維の配合量をそれぞれa、b、
c重量部としたとき、a+b+c=100、a>0、b
>0、c≧0、a/(b+c)<0.8を満足し、か
つ、(A)再生用ガラス繊維強化熱可塑性樹脂を(B)
非再生熱可塑性樹脂が溶融状態である工程に供給するこ
とを特徴とするガラス繊維強化熱可塑性樹脂のリサイク
ル方法。
(57) [Summary] [PROBLEMS] In a so-called material recycling method in which glass fiber reinforced thermoplastic resin is re-melted and kneaded and reused, deterioration of mechanical properties due to breakage of glass fiber is suppressed as much as possible, and recycled material is used. A high-concentration of non-recycled material to improve the regeneration rate, and provide a method that can be recycled efficiently and economically. SOLUTION: In the method of remelting and kneading a glass fiber reinforced thermoplastic resin to regenerate, a (A) glass fiber reinforced thermoplastic resin for reproduction, (B) a non-regenerated thermoplastic resin, and (C) a non-regenerated glass. The compounding amounts of the fibers are respectively a, b,
a + b + c = 100, a> 0, b
> 0, c ≧ 0, a / (b + c) <0.8, and (A) a glass fiber reinforced thermoplastic resin for regeneration
A method for recycling a glass fiber reinforced thermoplastic resin, comprising supplying the non-regenerated thermoplastic resin to a process in a molten state.

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、ガラス繊維強化熱
可塑性樹脂を再溶融混練し、再利用するいわゆる、マテ
リアルリサイクルの方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a so-called material recycling method in which a glass fiber reinforced thermoplastic resin is re-melted and kneaded and reused.

【0002】[0002]

【従来の技術】ガラス繊維強化熱可塑性樹脂は、その優
れた機械的特性から、多くの構造部品や、機能部品に利
用されている。最近では、資源の有効利用、地球環境負
荷低減の動きから、リサイクルを推進する必要に迫られ
てきた。多くのガラス繊維強化熱可塑性樹脂は、成形時
のスプルーやランナーなどの不要部や、製品寿命を全う
した物は、廃棄され、埋め立てや、焼却処理されてい
た。再利用する場合、最も簡便な方法としては、スプル
ーや、ランナー、回収製品等を粉砕する、などして、非
再生材と一定割合配合して、成形する方法がある。しか
し、この方法は、再生材が粉砕品であるため、成形機へ
の供給性、可塑化性が不安定で、製品品質に影響を与え
る場合がある。また、スプルー、ランナー等の不要部
や、回収製品を、再溶融混練して粒状にして、非再生材
に一定の割合で配合して成形する方法も一般的に行われ
ている。しかし、この方法も、ガラス繊維強化熱可塑性
樹脂の場合、再溶融混練の際、ガラス繊維の折損が大き
いため、非再生材と同等の機械的特性が発現され難く、
非再生材料への混合比を極力少なくして、品質に影響を
及ぼさない様にする必要があった。
2. Description of the Related Art Glass fiber reinforced thermoplastic resins are used for many structural parts and functional parts because of their excellent mechanical properties. Recently, there has been a pressing need to promote recycling due to the effective use of resources and the reduction of the burden on the global environment. In many glass fiber reinforced thermoplastic resins, unnecessary parts such as sprues and runners at the time of molding, and those that have completed their product life have been discarded, landfilled, or incinerated. In the case of re-use, the simplest method is a method in which a sprue, a runner, a recovered product, or the like is pulverized, mixed with a non-recycled material at a fixed ratio, and molded. However, in this method, since the recycled material is a crushed product, the supply property to the molding machine and the plasticization property are unstable, which may affect the product quality. In addition, a method of re-melting and kneading unnecessary portions such as sprues and runners and the like to obtain granules, blending them with a non-recycled material at a fixed ratio, and forming the same is also generally performed. However, also in this method, in the case of the glass fiber reinforced thermoplastic resin, during re-melting and kneading, since the glass fiber breakage is large, it is difficult to exhibit the same mechanical properties as the non-recycled material,
It was necessary to minimize the mixing ratio to the non-recycled material so as not to affect the quality.

【0003】一方、特開平12−80199号公報に
は、ガラス繊維強化ポリアミドのケミカルリサイクルの
方法が開示されている。しかし、成形品等を解重合し
て、モノマーにする方法は、解重合設備やガラス繊維を
分離する設備も必要な上、多くの工程が必要なため不経
済であった。
On the other hand, Japanese Patent Application Laid-Open No. 12-80199 discloses a method of chemically recycling glass fiber reinforced polyamide. However, the method of depolymerizing a molded article or the like to produce a monomer is uneconomical because it requires depolymerization equipment and equipment for separating glass fibers, and requires many steps.

【0004】[0004]

【発明が解決しようとする課題】本発明は、ガラス繊維
強化熱可塑性樹脂を再溶融混練し、再利用するいわゆ
る、マテリアルリサイクルの方法において、ガラス繊維
の折損に伴う機械的特性の劣化を極力抑制し、再生材で
あるガラス繊維強化熱可塑性樹脂を非再生材に高濃度に
配合し、再生率を向上させ、効率的かつ、経済的にリサ
イクル出来る方法を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention relates to a so-called material recycling method in which a glass fiber reinforced thermoplastic resin is re-melted, kneaded, and reused, so that deterioration of mechanical properties due to breakage of glass fiber is suppressed as much as possible. In addition, it is an object of the present invention to provide a method in which a glass fiber reinforced thermoplastic resin, which is a recycled material, is blended in a high concentration in a non-recycled material, thereby improving a recycling rate and enabling efficient and economical recycling.

【0005】[0005]

【課題を解決するための手段】本発明者は、前記課題を
解決するため、鋭意検討した結果、ガラス繊維強化熱可
塑性樹脂を再溶融混練して、再生する方法において、再
生材と、非再生材を特定の比率で配合し、かつ再生材で
あるガラス繊維強化熱可塑性樹脂を非再生熱可塑樹脂が
溶融状態である工程に供給することで、ガラス繊維の折
損を抑制でき、機械的特性の劣化が少ない再生材含有ガ
ラス繊維強化熱可塑性樹脂が得られることを見出し、本
発明をなすに至った。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, in a method of re-melting and kneading a glass fiber reinforced thermoplastic resin to regenerate, a regenerated material and a non-regenerated material are used. By blending the materials in a specific ratio, and supplying the recycled glass fiber reinforced thermoplastic resin to the process in which the non-regenerated thermoplastic resin is in a molten state, the breakage of the glass fibers can be suppressed, and the mechanical properties The present inventors have found that a recycled material-containing glass fiber reinforced thermoplastic resin with little deterioration can be obtained, and have accomplished the present invention.

【0006】すなわち、本発明は、1.ガラス繊維強化
熱可塑性樹脂を再溶融混練して、再生する方法におい
て、(A)再生用ガラス繊維強化熱可塑性樹脂、(B)
非再生熱可塑性樹脂、および(C)非再生ガラス繊維の
配合量をそれぞれa、b、c重量部としたとき、 a+b+c=100 a>0、b>0、c≧0 a/(b+c)<0.8 を満足し、かつ、(A)再生用ガラス繊維強化熱可塑性
樹脂を(B)非再生熱可塑性樹脂が溶融状態である工程
に供給することを特徴とするガラス繊維強化熱可塑性樹
脂のリサイクル方法、
That is, the present invention provides: In the method of re-melting and kneading a glass fiber reinforced thermoplastic resin and regenerating, (A) a glass fiber reinforced thermoplastic resin for reproduction, (B)
When the blending amounts of the non-regenerated thermoplastic resin and the (C) non-regenerated glass fiber are respectively a, b, and c parts by weight, a + b + c = 100 a> 0, b> 0, c ≧ 0 a / (b + c) < 0.8, and (A) supplying the recycled glass fiber reinforced thermoplastic resin to the step (B) in which the non-regenerated thermoplastic resin is in a molten state. Recycling method,

【0007】2.熱可塑性樹脂がポリアミドであること
を特徴とする上記1に記載のガラス繊維強化熱可塑性樹
脂のリサイクル方法、 3.熱可塑性樹脂が芳香族ポリエステルであることを特
徴とする上記1に記載のガラス繊維強化熱可塑性樹脂の
リサイクル方法、 4.上記1に記載の方法で得られた再生材を含むガラス
繊維強化熱可塑性樹脂組成物、である。
[0007] 2. 2. The method for recycling a glass fiber reinforced thermoplastic resin according to the above item 1, wherein the thermoplastic resin is a polyamide. 3. The method for recycling a glass fiber-reinforced thermoplastic resin according to the above item 1, wherein the thermoplastic resin is an aromatic polyester. 2. A glass fiber reinforced thermoplastic resin composition containing a recycled material obtained by the method described in 1 above.

【0008】[0008]

【発明の実施の形態】本発明について、以下具体的に説
明する。本発明における、再生用ガラス繊維強化熱可塑
性樹脂とは、リサイクル対象材であり、特に制限はない
が、本発明の目的を損なわない範囲で、回収製品であっ
ても良いし、成形加工時に発生するスプルー、ランナー
等の不要部分の樹脂であっても良い。但し、使用環境、
保管環境、等の影響で、分子量の低下や変色、等の著し
い劣化を受けているものは、好ましくない。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described below. In the present invention, the glass fiber reinforced thermoplastic resin for recycling is a material to be recycled, and is not particularly limited. However, as long as the object of the present invention is not impaired, it may be a recovered product or may be generated during molding. Unnecessary resin such as a sprue and a runner may be used. However, use environment,
Those that have undergone significant deterioration such as a decrease in molecular weight or discoloration due to the influence of the storage environment and the like are not preferred.

【0009】本発明における、非再生熱可塑性樹脂と
は、再生用ガラス繊維強化熱可塑性樹脂を一定割合で配
合して、再溶融混練する際に用いる熱可塑性樹脂であっ
て、実質的に再生材等を含まないことが望ましいが、本
発明の目的を損なわない範囲で、一部マテリアルリサイ
クルによって得られた熱可塑性樹脂、ケミカルリサイク
ルによって得られた熱可塑性樹脂を含有していてもかま
わない。
In the present invention, the non-regenerated thermoplastic resin is a thermoplastic resin to be used for mixing and remelting and kneading a recycled glass fiber reinforced thermoplastic resin at a certain ratio, and is substantially a recycled material. It is desirable not to include the same, but as long as the object of the present invention is not impaired, a thermoplastic resin partially obtained by material recycling or a thermoplastic resin obtained by chemical recycling may be contained.

【0010】本発明における、再生用ガラス繊維強化熱
可塑性樹脂と、非再生熱可塑性樹脂の熱可塑性樹脂に特
に制限はなく、例えばポリエチレン樹脂、ポリスチレン
樹脂、ポリプロピレン樹脂、ポリアミド樹脂、ポリエス
テル樹脂、ポリカーボネート樹脂、ポリオキシメチレン
樹脂、ポリフェニレンエーテル樹脂等が挙げられる。好
ましい樹脂は、ポリアミドおよび芳香族ポリエステルで
ある。ポリアミドおよび芳香族ポリエステルは、ガラス
繊維による補強効果が高く、一般に、ガラス繊維を10
〜60wt%程度配合して用いられるが、特に、ガラス
繊維濃度が高いガラス繊維強化樹脂ほど、再溶融混練時
のガラス繊維の折損が大きいため、本発明のリサイクル
方法により、ガラス繊維の折損が抑制される効果は大き
い。ポリアミド樹脂の例としては、ポリアミド6、ポリ
アミド11、ポリアミド12、ポリアミド66、ポリア
ミド610、ポリアミド612、ポリアミド46等の脂
肪族ポリアミド、およびこれらのポリアミドとテレフタ
ル酸成分、イソフタル酸成分、メタキシレイレンジアミ
ンとより得られるポリアミド6T、ポリアミド6I、ポ
リアミドMXD6、等の芳香族ポリアミドが挙げられ
る。これらポリアミドは、ホモポリマーとして用いても
良いし、上記ポリアミドをブレンドして用いても、上記
ポリアミド成分を共重合したコポリアミドであっても良
い。芳香族ポリエステルの例としては、ポリエチレンテ
レフタレート、ポリブチレンテレフタレート、ポリトリ
メチレンテレフタレート(以下「PTT」と略す)、等
が挙げられる。これら芳香族ポリエステルは、ホモポリ
マーで用いても、ブレンドあるいは共重合体であっても
良い。
In the present invention, there is no particular limitation on the recycled glass fiber reinforced thermoplastic resin and the non-regenerated thermoplastic resin, and examples thereof include polyethylene resin, polystyrene resin, polypropylene resin, polyamide resin, polyester resin, and polycarbonate resin. , Polyoxymethylene resin, polyphenylene ether resin and the like. Preferred resins are polyamides and aromatic polyesters. Polyamides and aromatic polyesters have a high reinforcing effect by glass fibers.
The glass fiber reinforced resin having a higher glass fiber concentration has a higher breakage of the glass fiber during remelting and kneading. Therefore, the breakage of the glass fiber is suppressed by the recycling method of the present invention. The effect is great. Examples of the polyamide resin include aliphatic polyamides such as polyamide 6, polyamide 11, polyamide 12, polyamide 66, polyamide 610, polyamide 612, and polyamide 46, and these polyamides and terephthalic acid components, isophthalic acid components, and metaxylene range. Aromatic polyamides such as polyamide 6T, polyamide 6I, polyamide MXD6, etc. obtained from amines are exemplified. These polyamides may be used as a homopolymer, may be used by blending the above polyamide, or may be a copolyamide obtained by copolymerizing the above polyamide component. Examples of the aromatic polyester include polyethylene terephthalate, polybutylene terephthalate, polytrimethylene terephthalate (hereinafter abbreviated as “PTT”), and the like. These aromatic polyesters may be used as a homopolymer, a blend or a copolymer.

【0011】本発明のガラス繊維強化熱可塑性樹脂の熱
可塑性樹脂と、非再生熱可塑性樹脂は、一般的には同種
のものを用いるが、目的によっては、必ずしも同一の熱
可塑性樹脂で無くても良い。また、本発明の再生用ガラ
ス繊維強化熱可塑性樹脂の熱可塑性樹脂中および、非再
生熱可塑性樹脂中には、本発明の目的を損なわない範囲
で、一般的に用いられる熱安定剤、酸化防止剤、光安定
剤、ラジカル禁止剤、紫外線吸収剤、核剤、滑剤、離型
剤、着色顔料、染料、ガラス繊維以外の強化剤等の添加
剤を含むことができる。
The thermoplastic resin of the glass fiber reinforced thermoplastic resin of the present invention and the non-regenerated thermoplastic resin are generally of the same kind, but depending on the purpose, it is not always necessary to use the same thermoplastic resin. good. Further, in the thermoplastic resin of the recycled glass fiber reinforced thermoplastic resin of the present invention, and in the non-regenerated thermoplastic resin, generally used heat stabilizers and antioxidants are used as long as the object of the present invention is not impaired. Additives such as agents, light stabilizers, radical inhibitors, ultraviolet absorbers, nucleating agents, lubricants, release agents, coloring pigments, dyes, and reinforcing agents other than glass fibers.

【0012】本発明で用いる、再生用ガラス繊維強化熱
可塑性樹脂中のガラス繊維および、非再生ガラス繊維に
特に制限はなく、通常熱可塑性樹脂に使用されているも
のを使うことができ、原料としてのガラス繊維径やガラ
ス繊維のチョップ長に特に制限はなく、例えば直径が5
〜25μのチョップドストランド、ロービング、ミルド
ファイバーのいずれを使用しても良い。チョップドスト
ランドを用いる場合には、その長さが0.1から12m
mの範囲で適宜選択して用いることができる。
The glass fibers in the glass fiber reinforced thermoplastic resin for regeneration and the non-recycled glass fibers used in the present invention are not particularly limited, and those usually used for thermoplastic resins can be used. The glass fiber diameter and the chop length of the glass fiber are not particularly limited.
Any of chopped strands, rovings, and milled fibers of 2525 μm may be used. When using chopped strands, the length is 0.1 to 12m
It can be appropriately selected and used in the range of m.

【0013】また、ガラス繊維の表面に通常公知のシラ
ン系カップリング剤を付着させたものを用いても良い。
例えばγ−アミノプロピルトリメトキシシラン、γ−ア
ミノプロピルトリエトキシシラン、N−β(アミノエチ
ル)−γ−アミノプロピルトリメトキシシラン、ビニル
トリエトキシシラン、γ−グリシドキシプロピルトリメ
トキシシランなどが利用できる。さらに、集束剤とし
て、ウレタン系樹脂、無水マレイン酸変性ブタジエン系
樹脂、無水マレイン酸スチレン系、アクリル酸等の公知
の集束剤で処理されたガラス繊維を用いることができ
る。再生用ガラス繊維強化熱可塑性樹脂中のガラス繊維
および、非再生ガラス繊維の種類および、配合量は、一
般的には、同一の物が用いられるが、目的に応じて、種
類、および配合量が異なっていても良い。
Further, a material obtained by attaching a generally known silane coupling agent to the surface of glass fiber may be used.
For example, γ-aminopropyltrimethoxysilane, γ-aminopropyltriethoxysilane, N-β (aminoethyl) -γ-aminopropyltrimethoxysilane, vinyltriethoxysilane, γ-glycidoxypropyltrimethoxysilane and the like are used. it can. Further, as the sizing agent, a glass fiber treated with a known sizing agent such as a urethane resin, a maleic anhydride-modified butadiene resin, a styrene maleic anhydride, or acrylic acid can be used. In general, the same type and amount of glass fiber and non-regenerated glass fiber in the glass fiber reinforced thermoplastic resin for regeneration are used, but depending on the purpose, the type and the amount of blending are different. It may be different.

【0014】本発明において、再生用ガラス繊維強化熱
可塑性樹脂の配合量をa重量部、非再生熱可塑性樹脂の
配合量をb重量部、非再生ガラス繊維の配合量をc重量
部とした時、a+b+c=100、a>0、b>0、c
≧0,a/(b+c)<0.8を満足する必要がある。
a/(b+c)が0.8より大きいと、ガラス繊維の折
損が抑制し難くなり、機械的特性の劣化が顕著となる。
好ましくは、a/(b+c)<0.5である。
In the present invention, when the amount of the recycled glass fiber reinforced thermoplastic resin is a part by weight, the amount of the non-regenerated thermoplastic resin is b part by weight, and the amount of the non-regenerated glass fiber is c part by weight. , A + b + c = 100, a> 0, b> 0, c
≧ 0, a / (b + c) <0.8 must be satisfied.
When a / (b + c) is larger than 0.8, it is difficult to suppress breakage of the glass fiber, and deterioration of mechanical properties becomes remarkable.
Preferably, a / (b + c) <0.5.

【0015】本発明の再生用ガラス繊維強化熱可塑性樹
脂は、非再生熱可塑性樹脂が溶融状態にある工程で供給
する必要がる。再生用ガラス繊維強化熱可塑性樹脂を、
非再生熱可塑性樹脂が非溶融状態の工程に供給すると、
ガラス繊維の折損が抑制し難くなり、機械的特性の劣化
が顕著となる。再生用ガラス繊維強化熱可塑性樹脂を、
非再生熱可塑性樹脂が溶融状態の工程にフィードする方
法に特に制限はないが、例えば、2軸押出機の最上流よ
り非再生熱可塑性樹脂を供給し、該供給口の下流で、非
再生熱可塑性樹脂が溶融可塑化された状態の工程(部
位)に、再生用ガラス繊維強化熱可塑性樹脂を供給する
方法を例示できる。再生用ガラス繊維強化熱可塑性樹脂
と非再生熱可塑性樹脂のみでは、当然、再生された組成
物中のガラス繊維配合量が、再生用ガラス繊維強化熱可
塑性樹脂より少なくなる。目的によっては、この方法で
リサイクルしても良いが、一般的には、再生用ガラス繊
維強化熱可塑性樹脂のガラス繊維配合量と同量以上のガ
ラス繊維配合量を有する再生材を製造する。この場合、
ガラス繊維の折損抑制の観点から、非再生ガラス繊維を
同時に配合することも可能であるが、上記の再生用ガラ
ス繊維強化熱可塑性樹脂の供給位置よりさらに下流で、
非再生ガラス繊維を供給することが望ましい。
The recycled glass fiber reinforced thermoplastic resin of the present invention needs to be supplied in a step where the non-regenerated thermoplastic resin is in a molten state. Glass fiber reinforced thermoplastic resin for recycling
When the non-regenerated thermoplastic resin is supplied to the non-molten process,
It becomes difficult to suppress breakage of the glass fiber, and deterioration of mechanical properties becomes remarkable. Glass fiber reinforced thermoplastic resin for recycling
The method for feeding the non-regenerated thermoplastic resin to the process in the molten state is not particularly limited. For example, the non-regenerated thermoplastic resin is supplied from the uppermost stream of a twin-screw extruder, and the non-regenerated heat is supplied downstream of the supply port. A method of supplying a glass fiber reinforced thermoplastic resin for regeneration to a process (site) where the plastic resin is melt-plasticized can be exemplified. When the recycled glass fiber reinforced thermoplastic resin and the non-regenerated thermoplastic resin alone are used, the blended amount of the glass fiber in the regenerated composition is naturally smaller than that of the recycled glass fiber reinforced thermoplastic resin. Depending on the purpose, it may be recycled by this method, but in general, a recycled material having a glass fiber content equal to or more than the glass fiber content of the glass fiber reinforced thermoplastic resin for reproduction is produced. in this case,
From the viewpoint of glass fiber breakage suppression, it is also possible to simultaneously blend non-regenerated glass fibers, but further downstream from the supply position of the above-mentioned recycled glass fiber reinforced thermoplastic resin,
It is desirable to provide non-recycled glass fibers.

【0016】本発明のリサイクル方法を実施する装置
は、特に制限は無いが、通常用いられる溶融混練装置、
例えば、単軸押出機、2軸押出機、ニーダー、ブラベン
ダー、プラストミル等を用いることができる。しかしい
ずれの装置も非再生熱可塑性樹脂が溶融状態にある部位
に再生用ガラス繊維強化熱可塑性樹脂を供給できる装置
を有している必要がある。本発明のリサイクル方法を実
施する溶融混練条件は、特に制限は無いが、一般に熱可
塑性樹脂の融点より高いバレル温度条件にて、非再生熱
可塑性樹脂を溶融させ、再生用ガラス繊維強化熱可塑性
樹脂が供給される工程(部位)において、再生用ガラス
繊維強化熱可塑性樹脂が速やかに溶融されるように適宜
温度設定することが望ましい。押出量、スクリュー構
成、スクリュー回転数、ダイ構成、ベント真空条件に特
に制限はないが、再生用ガラス繊維強化熱可塑性樹脂中
のガラス繊維および非再生ガラス繊維が、過大に折損し
ない様な条件が望ましい。
The apparatus for carrying out the recycling method of the present invention is not particularly limited.
For example, a single-screw extruder, a twin-screw extruder, a kneader, a Brabender, a plastmill, or the like can be used. However, each apparatus needs to have an apparatus capable of supplying a recycled glass fiber reinforced thermoplastic resin to a portion where the non-regenerated thermoplastic resin is in a molten state. The melt-kneading conditions for carrying out the recycling method of the present invention are not particularly limited, but generally, at a barrel temperature condition higher than the melting point of the thermoplastic resin, the non-regenerated thermoplastic resin is melted, and the glass fiber reinforced thermoplastic resin for regeneration. In the step (site) where is supplied, it is desirable to appropriately set the temperature so that the glass fiber reinforced thermoplastic resin for regeneration is quickly melted. There is no particular limitation on the amount of extrusion, screw configuration, screw rotation speed, die configuration, vent vacuum conditions, but there are conditions such that the glass fibers and non-regenerated glass fibers in the glass fiber reinforced thermoplastic resin for regeneration do not break excessively. desirable.

【0017】また、本発明のリサイクル工程において、
必要に応じ、熱安定剤、酸化防止剤、分子量回復のため
の触媒等を添加しても良い。本発明について、以下実施
例に基づいて説明する。実施例、および比較例中の評価
は、次の方法で行った。 (1)ガラス繊維濃度:組成物のペレットをるつぼ中
で、焼却し、さらに650℃にて樹脂成分を灰化させ、
灰化前後の重量測定結果から、灰化物重量/灰化前ペレ
ット重量X100(wt%)よりガラス繊維濃度を求め
た。 (2)機械的特性:引張強度をASTM D638、曲
げ強度、曲げ弾性率をASTM D790に準じて測定
した。
In the recycling process of the present invention,
If necessary, a heat stabilizer, an antioxidant, a catalyst for recovering the molecular weight, and the like may be added. The present invention will be described below based on examples. The evaluation in Examples and Comparative Examples was performed by the following method. (1) Glass fiber concentration: pellets of the composition are incinerated in a crucible, and the resin component is further ashed at 650 ° C.
From the weight measurement results before and after the incineration, the glass fiber concentration was calculated from the weight of the incinerated material / the weight of the pellet before incineration × 100 (wt%). (2) Mechanical properties: Tensile strength was measured according to ASTM D638, and bending strength and flexural modulus were measured according to ASTM D790.

【0018】実施例、および比較例中では、次の再生用
熱可塑性樹脂、非再生用熱可塑性樹脂、およびガラス繊
維を用いた。 (1)再生用熱可塑性樹脂 (A−1)ガラス繊維強化ポリアミド66樹脂:旭化成
工業(株)社製Leona 1300G ガラス繊維濃
度33wt% (A−2)ガラス繊維強化PTT樹脂:シェル社製 P
TT樹脂 Corterra CP509200、およ
び日本電気硝子社製ガラス繊維T187を用い、東芝機
械(株)製2軸押出機TEM35により、ガラス繊維濃
度30%のガラス繊維強化PTT樹脂を作成した。(A
−1)、(A−2)ともに、東芝機械(株)製 射出成
形機IS−50EPを用い、厚さ3mmのASTM D
638およびD790に準ずる試験片を得、該試験片お
よび、スプルー、ランナー部とともに、粉砕機にて平均
径約3mmに粉砕したものを再生用熱可塑性樹脂とし
た。
In the examples and comparative examples, the following thermoplastic resin for regeneration, thermoplastic resin for non-regeneration, and glass fiber were used. (1) Thermoplastic resin for regeneration (A-1) Glass fiber reinforced polyamide 66 resin: Leona 1300G manufactured by Asahi Kasei Corporation Glass fiber concentration 33 wt% (A-2) Glass fiber reinforced PTT resin: P manufactured by Shell
TT resin A glass fiber reinforced PTT resin having a glass fiber concentration of 30% was produced using a twin screw extruder TEM35 manufactured by Toshiba Machine Co., Ltd. using Cortera CP509200 and glass fiber T187 manufactured by Nippon Electric Glass Co., Ltd. (A
For both -1) and (A-2), ASTM D having a thickness of 3 mm was used using an injection molding machine IS-50EP manufactured by Toshiba Machine Co., Ltd.
A test piece conforming to 638 and D790 was obtained, and the test piece, the sprue, and the runner portion were pulverized to an average diameter of about 3 mm with a pulverizer to obtain a thermoplastic resin for regeneration.

【0019】(2)非再生熱可塑性樹脂 (B−1)ポリアミド66樹脂:旭化成工業(株)社製
Leona 1300 (B−2)PTT樹脂:シェル社製 Corterra
CP509200(3)非再生ガラス繊維: (C−1)日本電気硝子(株)社製 T275 (繊維
径10μ ポリアミド用) (C−2)日本電気硝子(株)社製 T187 (繊維
径13μm ポリエステル用)
(2) Non-regenerated thermoplastic resin (B-1) Polyamide 66 resin: Leona 1300 manufactured by Asahi Kasei Corporation (B-2) PTT resin: Corterra manufactured by Shell Co.
CP509200 (3) Non-recycled glass fiber: (C-1) T275 manufactured by NEC Corporation (for fiber 10 μm polyamide) (C-2) T187 manufactured by NEC Corporation (fiber diameter 13 μm for polyester) )

【0020】[0020]

【実施例1】再生用ガラス繊維強化熱可塑性樹脂として
(A−1)、非再生熱可塑性樹脂として(B−1)、非
再生ガラス繊維として(C−1)を用いた。(B−1)
を東芝機械(株)社製同方向2軸押出機TEM35(L
/D47)の最上流供給口より定重量式フィーダーを用
いて20kg/hrで供給し、押出機下流の(B−1)
が完全に溶融した位置に、(A−1)を定重量式フィー
ダーを用いて30kg/hrでサイドフィードし、更に
下流で、(C−1)を定重量式フィーダーを用いて10
kg/hrでサイドフィードした。尚、押出条件はバレ
ル温度290℃、スクリュー回転数300回転、ベント
真空度60cmHg、吐出量60kg/hrである。ま
た、スクリュー構成は、(B−1)の可塑化のため、
(A−1)供給位置より上流にL/D8.5のニーディ
ングブロックおよびL/D0.4の逆ネジを設け、(A
−1)供給位置の下流にL/D0.4の逆ネジスクリュ
ーを一ヶ所設け、(C−1)供給位置より下流にL/D
0.4の逆ネジスクリューを一ヶ所設けた他は、順ネジ
のみで構成した。ベント口は、(C−1)供給位置の下
流に設けた。ダイは、径3mmのオリフィスが4穴のも
のを用いた。ダイより押し出された溶融樹脂組成物を冷
水バス中で冷却後、連続的にペレット状にカッティング
して、ガラス繊維強化熱可塑性樹脂を得た。得られたガ
ラス繊維強化ポリアミド樹脂組成物の評価結果を表1に
示す。下記の比較例1に比べ、機械的特性に優れ、下記
の参考例1とほぼ同等の性能が得られた。
Example 1 (A-1) was used as a recycled glass fiber reinforced thermoplastic resin, (B-1) was used as a non-regenerated thermoplastic resin, and (C-1) was used as a non-regenerated glass fiber. (B-1)
To the same direction twin screw extruder TEM35 (L manufactured by Toshiba Machine Co., Ltd.)
/ D47) from the uppermost stream supply port using a constant weight feeder at a rate of 20 kg / hr, and (B-1) downstream of the extruder.
Is completely melted, (A-1) is side-fed at 30 kg / hr using a constant weight feeder, and further downstream, (C-1) is fed to a 10 kg using a constant weight feeder.
Side feed was performed at kg / hr. The extrusion conditions were a barrel temperature of 290 ° C., a screw rotation number of 300, a degree of vent vacuum of 60 cmHg, and a discharge rate of 60 kg / hr. In addition, the screw configuration is for plasticization of (B-1),
(A-1) A kneading block of L / D 8.5 and a reverse screw of L / D 0.4 are provided upstream of the supply position.
-1) One L / D 0.4 reverse screw is provided downstream of the supply position, and (C-1) L / D is provided downstream of the supply position.
Except for providing one 0.4 reverse screw, only the forward screw was used. The vent port was provided downstream of the (C-1) supply position. The die used had a diameter of 3 mm and an orifice of 4 holes. The molten resin composition extruded from the die was cooled in a cold water bath, and then continuously cut into pellets to obtain a glass fiber reinforced thermoplastic resin. Table 1 shows the evaluation results of the obtained glass fiber reinforced polyamide resin composition. As compared with Comparative Example 1 below, the mechanical properties were excellent, and performance almost equivalent to that of Reference Example 1 was obtained.

【0021】[0021]

【実施例2】再生用ガラス繊維強化熱可塑性樹脂として
(A−2)、非再生熱可塑性樹脂として(B−2)、非
再生ガラス繊維として(C−2)を用い、(B−2)を
21kg/hrで供給し、(A−2)を30kg/hr
でサイドフィードし、(C−2)を9kg/hrでサイ
ドフィードした他は、実施例1と同様の方法でガラス繊
維強化熱可塑性樹脂を得た。得られたガラス繊維強化ポ
リエステル樹脂組成物の評価結果を表1に示す。下記の
比較例2に比べ、機械的特性に優れ、下記の参考例2と
ほぼ同等の性能が得られた。
Example 2 (A-2) was used as a glass fiber reinforced thermoplastic resin for regeneration, (B-2) was used as a non-regenerated thermoplastic resin, and (C-2) was used as a non-regenerated glass fiber. Is supplied at 21 kg / hr, and (A-2) is supplied at 30 kg / hr.
, And a glass fiber reinforced thermoplastic resin was obtained in the same manner as in Example 1, except that (C-2) was side fed at 9 kg / hr. Table 1 shows the evaluation results of the obtained glass fiber reinforced polyester resin compositions. As compared with Comparative Example 2 below, the mechanical properties were excellent, and performance almost equivalent to that of Reference Example 2 described below was obtained.

【0022】[0022]

【比較例1】(A−1)を(B−1)と一緒に、押出機
最上流より供給した他は、実施例1と同様の方法でガラ
ス繊維強化熱可塑性樹脂を得た。得られたガラス繊維強
化ポリアミド樹脂組成物の評価結果を表1に示す。
Comparative Example 1 A glass fiber reinforced thermoplastic resin was obtained in the same manner as in Example 1 except that (A-1) and (B-1) were supplied from the uppermost stream of an extruder. Table 1 shows the evaluation results of the obtained glass fiber reinforced polyamide resin composition.

【0023】[0023]

【比較例2】(A−2)を(B−2)と一緒に、押出機
最上流より供給した他は、実施例1と同様の方法でガラ
ス繊維強化熱可塑性樹脂を得た。得られたガラス繊維強
化ポリエステル樹脂組成物の評価結果を表1に示す。
Comparative Example 2 A glass fiber reinforced thermoplastic resin was obtained in the same manner as in Example 1 except that (A-2) and (B-2) were supplied from the uppermost stream of an extruder. Table 1 shows the evaluation results of the obtained glass fiber reinforced polyester resin compositions.

【0024】[0024]

【比較例3】(A−1)を54kg/hr、(B−1)
を4.02kg/hr、(C−1)を1.98kg/h
r供給した他は、実施例1と同様の方法でガラス繊維強
化熱可塑性樹脂を得た。得られたガラス繊維強化ポリア
ミド樹脂組成物の評価結果を表1に示す。
Comparative Example 3 54 kg / hr of (A-1), (B-1)
4.02 kg / hr, (C-1) 1.98 kg / hr
A glass fiber reinforced thermoplastic resin was obtained in the same manner as in Example 1 except that r was supplied. Table 1 shows the evaluation results of the obtained glass fiber reinforced polyamide resin composition.

【0025】[0025]

【参考例1および2】参考例1、および2を表1に併記
した。 参考例1、および2は(A−1)、および(A
−2)に相当するものを再生せずに、それぞれ、(B−
1)と(C−1)、および(B−2)と(C−2)とよ
り得たのであり、それらを評価したものである。
Reference Examples 1 and 2 Reference Examples 1 and 2 are also shown in Table 1. Reference Examples 1 and 2 are (A-1) and (A
Without reproducing the equivalent of (-2), (B-
1) and (C-1), and (B-2) and (C-2), which were evaluated.

【0026】[0026]

【表1】 [Table 1]

【0027】[0027]

【発明の効果】本発明によって、ガラス繊維強化熱可塑
性樹脂を再溶融混練し、再利用するいわゆる、マテリア
ルリサイクルの方法において、ガラス繊維の折損に伴う
機械的特性の劣化を極力抑制し、非再生材に高濃度に配
合し、再生率を向上させ、効率的かつ、経済的にリサイ
クル出来るようになる。
According to the present invention, in a so-called material recycling method in which a glass fiber reinforced thermoplastic resin is re-melted and kneaded and reused, deterioration of mechanical properties due to breakage of glass fiber is suppressed as much as possible and non-recycling is performed. It can be efficiently and economically recycled by blending it at a high concentration in the material, improving the recycling rate.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) // B29K 105:12 B29K 105:12 105:26 105:26 Fターム(参考) 4F070 AA47 AA54 AB09 AB26 AC28 AD02 AE01 FA03 FB06 FC05 4F301 AA25 AA27 AA30 AB01 AB03 AD09 AD10 BC26 BC36 BC40 BC63 BC71 BC75 BD11 BD31 BD36 BD42 BD44 BF16 BF32 4J002 CF041 CF061 CF071 CL001 CL011 CL021 CL031 DL006 FA046 FD016 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (reference) // B29K 105: 12 B29K 105: 12 105: 26 105: 26 F term (reference) 4F070 AA47 AA54 AB09 AB26 AC28 AD02 AE01 FA03 FB06 FC05 4F301 AA25 AA27 AA30 AB01 AB03 AD09 AD10 BC26 BC36 BC40 BC63 BC71 BC75 BD11 BD31 BD36 BD42 BD44 BF16 BF32 4J002 CF041 CF061 CF071 CL001 CL011 CL021 CL031 DL006 FA046 FD016

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 ガラス繊維強化熱可塑性樹脂を再溶融混
練して、再生する方法において、(A)再生用ガラス繊
維強化熱可塑性樹脂、(B)非再生熱可塑性樹脂、およ
び(C)非再生ガラス繊維の配合量をそれぞれa、b、
c重量部としたとき、 a+b+c=100 a>0、b>0、c≧0 a/(b+c)<0.8 を満足し、かつ、(A)再生用ガラス繊維強化熱可塑性
樹脂を(B)非再生熱可塑性樹脂が溶融状態である工程
に供給することを特徴とするガラス繊維強化熱可塑性樹
脂のリサイクル方法。
1. A method for remelting and kneading a glass fiber reinforced thermoplastic resin to regenerate, wherein (A) a glass fiber reinforced thermoplastic resin for regeneration, (B) a non-regenerated thermoplastic resin, and (C) a non-regenerated thermoplastic resin. The amounts of the glass fibers are respectively a, b,
a + b + c = 100 a> 0, b> 0, c ≧ 0 a / (b + c) <0.8, and (A) the recycled glass fiber reinforced thermoplastic resin is (B) A method for recycling a glass fiber reinforced thermoplastic resin, wherein the method supplies the non-regenerated thermoplastic resin to a step in which the thermoplastic resin is in a molten state.
【請求項2】 熱可塑性樹脂がポリアミドであることを
特徴とする請求項1記載のガラス繊維強化熱可塑性樹脂
のリサイクル方法。
2. The method for recycling a glass fiber reinforced thermoplastic resin according to claim 1, wherein the thermoplastic resin is a polyamide.
【請求項3】 熱可塑性樹脂が芳香族ポリエステルであ
ることを特徴とする請求項1記載のガラス繊維強化熱可
塑性樹脂のリサイクル方法。
3. The method for recycling a glass fiber reinforced thermoplastic resin according to claim 1, wherein the thermoplastic resin is an aromatic polyester.
【請求項4】 請求項1記載のリサイクル方法によって
得られた再生材を含むガラス繊維強化熱可塑性樹脂組成
物。
4. A glass fiber reinforced thermoplastic resin composition containing a recycled material obtained by the recycling method according to claim 1.
JP2000315019A 2000-10-16 2000-10-16 Recycling method of glass fiber reinforced thermoplastic resin Pending JP2002120224A (en)

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Publication Number Publication Date
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Family

ID=18794184

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Country Link
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KR100761944B1 (en) 2006-05-29 2007-10-04 한국환경자원공사 Composite plastic recycled material reinforced with waste glass fiber and its manufacturing method
KR100881646B1 (en) 2007-02-28 2009-02-04 홍익대학교 산학협력단 Fiber reinforcement using waste glass fiber reinforced plastic
EP2433911A1 (en) 2010-09-23 2012-03-28 Johns Manville Methods and apparatus for recycling glass products using submerged combustion
JP2014205833A (en) * 2013-04-10 2014-10-30 ザ・ボーイング・カンパニーTheBoeing Company Recycling of broad goods with thermoplastic stabilizer materials
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JP2019049010A (en) * 2013-04-10 2019-03-28 ザ・ボーイング・カンパニーThe Boeing Company Recycling of broad goods with thermoplastic stabilizer materials
JP2014205833A (en) * 2013-04-10 2014-10-30 ザ・ボーイング・カンパニーTheBoeing Company Recycling of broad goods with thermoplastic stabilizer materials
JP2019049009A (en) * 2013-04-10 2019-03-28 ザ・ボーイング・カンパニーThe Boeing Company Wide-area recycling with thermoplastic stabilization materials
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JP2017105081A (en) * 2015-12-10 2017-06-15 株式会社栗本鐵工所 Kneading method and kneading apparatus
US20210039980A1 (en) * 2018-02-07 2021-02-11 Knauf Insulation Sprl Recycling
CN115216096A (en) * 2022-08-08 2022-10-21 广州市华英防腐设备有限公司 Anticorrosive plate formed by thermoplastic molding of recycled glass fiber and preparation method thereof
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