JP2002052596A - Method for preventing mixture of colored foreign matter with molding by extrusion molding - Google Patents

Method for preventing mixture of colored foreign matter with molding by extrusion molding

Info

Publication number
JP2002052596A
JP2002052596A JP2000238849A JP2000238849A JP2002052596A JP 2002052596 A JP2002052596 A JP 2002052596A JP 2000238849 A JP2000238849 A JP 2000238849A JP 2000238849 A JP2000238849 A JP 2000238849A JP 2002052596 A JP2002052596 A JP 2002052596A
Authority
JP
Japan
Prior art keywords
resin composition
cylinder
resin
temperature
foreign matter
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
JP2000238849A
Other languages
Japanese (ja)
Inventor
Takeshi Yasuda
剛 安田
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co Ltd
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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP2000238849A priority Critical patent/JP2002052596A/en
Publication of JP2002052596A publication Critical patent/JP2002052596A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/365Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using pumps, e.g. piston pumps
    • B29C48/37Gear pumps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/387Plasticisers, homogenisers or feeders comprising two or more stages using a screw extruder and a gear pump
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92895Barrel or housing

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for preventing a mixture of a colored foreign matter of a resin carbide or the like in a molding when interrupted extrusion molding is restarted. SOLUTION: The method for preventing the mixture of the colored foreign matter with the molding by extrusion molding comprises the steps of storing a resin composition in a cylinder 11 of an extruder 10 during a period until the interrupted extrusion molding is restarted, and maintaining a temperature of the composition at a temperature higher by 30 to 100 deg.C than a glass transition temperature of the resin. The method also comprises the step of sealing a lip 19 of a die 18 during a period while the extrusion molding is interrupted.

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、押出成形による樹
脂の加工方法に関し、より詳しくは、中断した押出成形
を再開したとき、押出成形による加工品中に有色異物が
混入するのを防止する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for processing a resin by extrusion molding, and more particularly, to a method for preventing colored foreign matter from being mixed into a processed product by extrusion molding when restarting interrupted extrusion molding. About.

【0002】[0002]

【従来の技術】ポリメチルメタクリレート(PMMA)
等のアクリル系樹脂、ポリ塩化ビニル(PVC)系樹
脂、ポリスチレン(PS)系樹脂、ポリカーボネート
(PC)系樹脂といった熱可塑性樹脂の成形加工には、
当該樹脂の組成物を押出機(押出成形機)10のシリン
ダ11内で溶融させ、次いでダイ18から強制的に押し
出して連続的に加工品を得る、いわゆる押出成形法が広
く用いられている(図1参照)。
2. Description of the Related Art Polymethyl methacrylate (PMMA)
Molding of thermoplastic resin such as acrylic resin, polyvinyl chloride (PVC) resin, polystyrene (PS) resin, polycarbonate (PC) resin, etc.
A so-called extrusion molding method is widely used in which the resin composition is melted in a cylinder 11 of an extruder (extrusion molding machine) 10 and then forcedly extruded from a die 18 to continuously obtain a processed product ( (See FIG. 1).

【0003】押出機10の稼働は、一般に、押出機10
の整備点検やシリンダ11内の洗浄を行う場合あるいは
加工品の需要が少ない場合を除いて連続して行われる。
ここで、前者の理由により押出機10の稼働を停止する
場合にはシリンダ11内に残留する樹脂組成物が除去さ
れるが、後者の理由により稼働を一時停止する場合に
は、樹脂組成物を除去する手間や稼働再開時の作業効率
の観点から、シリンダ11内の樹脂組成物を取り除かず
に留置させるのが一般的である。また、後者の場合、コ
スト削減の観点からシリンダ11への加熱は停止され、
放冷される。
The operation of the extruder 10 is generally performed by the extruder 10
It is performed continuously except when performing maintenance inspection and cleaning of the inside of the cylinder 11 or when there is little demand for processed products.
Here, when the operation of the extruder 10 is stopped for the former reason, the resin composition remaining in the cylinder 11 is removed. However, when the operation is temporarily stopped for the latter reason, the resin composition is removed. It is general that the resin composition in the cylinder 11 is left in place without being removed from the viewpoint of the trouble of removing and the work efficiency at the time of restarting operation. In the latter case, the heating of the cylinder 11 is stopped from the viewpoint of cost reduction,
Allowed to cool.

【0004】[0004]

【発明が解決しようとする課題】しかし、押出機の稼働
を一時停止してシリンダ11を放冷した場合には、その
後、押出機の稼働を再開したときに、加工品中に黒点異
物が発生するという問題があった。特に、PMMA等の
加工品については、黒点異物の発生によって樹脂本来の
優れた透明性や装飾性が損なわれてしまうこととなり、
加工品の商品価値が著しく低下する原因となる。
However, if the operation of the extruder is temporarily stopped and the cylinder 11 is allowed to cool, then when the operation of the extruder is restarted, black spot foreign matter is generated in the processed product. There was a problem of doing. In particular, with regard to processed products such as PMMA, the generation of black spot foreign matter will impair the excellent transparency and decorativeness inherent in the resin,
This causes the commercial value of the processed product to be significantly reduced.

【0005】そこで、本発明の目的は、中断した押出成
形を再開する場合に、黒点異物が加工品中に発生するの
を防止する方法を提供することである。
Accordingly, an object of the present invention is to provide a method for preventing black spot foreign matter from being generated in a processed product when the interrupted extrusion is restarted.

【0006】[0006]

【課題を解決するための手段および発明の効果】本発明
者らは、上記課題を解決するための検討において、押出
機の稼働を一時中断した後で加工品中に黒点異物が発生
するのは、以下の理由によるものであると推測するに至
った。すなわち、押出機のシリンダから樹脂組成物を除
去せずに放冷すると、シリンダと樹脂組成物との熱収縮
率の相違に起因して両者の間に空隙部が生じ、その空隙
部に空気が入り込む。これにより樹脂組成物が酸化、分
解され、さらにシリンダの余熱等によって酸化、分解さ
れた樹脂組成物が炭化するに至り、最終的に樹脂の炭化
物がシリンダ内壁部に付着する。このように樹脂炭化物
がシリンダ内壁部に付着した状態で押出機の稼働を再開
すると、前記炭化物は内壁部から剥離して溶融した樹脂
組成物中に混ざり込む。通常、シリンダ11の吐出口1
5にはスクリーン16が連結されているが(図1参
照)、シリンダ11内での混練等によって微細化された
炭化物はスクリーン16をすり抜けることがあり、最終
的に加工品中に混入して小さな黒点異物となる。
Means for Solving the Problems and Effects of the Invention In the study for solving the above problems, the present inventors have found that black spot foreign matter is generated in the processed product after the operation of the extruder is temporarily suspended. , For the following reasons. That is, when the resin composition is allowed to cool without being removed from the cylinder of the extruder, a gap is generated between the cylinder and the resin composition due to a difference in the thermal shrinkage rate between the cylinder and the resin composition, and air is generated in the gap. Get in. As a result, the resin composition is oxidized and decomposed, and furthermore, the oxidized and decomposed resin composition is carbonized by the residual heat of the cylinder and the like, and finally, the carbide of the resin adheres to the inner wall of the cylinder. When the operation of the extruder is resumed with the resin carbide adhered to the inner wall of the cylinder, the carbide is separated from the inner wall and mixed into the molten resin composition. Usually, the discharge port 1 of the cylinder 11
5 is connected to a screen 16 (see FIG. 1), but carbides fined by kneading in the cylinder 11 may pass through the screen 16 and eventually enter the processed product and become small. It becomes black spot foreign matter.

【0007】そこで本発明者らは、樹脂炭化物の発生を
防止すべく検討を重ねていく中で、押出機の稼働を停止
している間にもシリンダの加熱を継続して行い、シリン
ダ内に貯留されている樹脂組成物が所定の温度となるよ
うに保温すれば、稼働停止中に樹脂組成物が熱収縮する
のを抑制することができ、それゆえシリンダと樹脂組成
物との間に空隙部が生じるのを抑制し、ひいては樹脂炭
化物の発生および加工品中への有色異物の混入を防止で
きるのではないかとの着想を得、さらに検討を重ねた。
その結果、押出成形の対象となる樹脂のガラス転移温度
よりも30〜100℃高い温度でシリンダ内の樹脂組成
物を保温したときは、意外にも、加熱に要するコストを
抑えつつ炭化物の発生および混入を効果的に防止するこ
とができ、しかも継続して樹脂組成物を加熱することに
伴う樹脂の劣化をも防止することができるという新たな
事実を見出し、本発明を完成するに至った。
[0007] The inventors of the present invention have continued to study to prevent the generation of resin carbide, and while the operation of the extruder has been stopped, the heating of the cylinder has been continued, and the inside of the cylinder has been heated. If the stored resin composition is kept at a predetermined temperature, the resin composition can be prevented from being thermally contracted during the stoppage of operation, and therefore, the gap between the cylinder and the resin composition can be suppressed. The generation of parts was suppressed, and the idea of preventing the occurrence of resin carbide and the incorporation of colored foreign matter into processed products was obtained, and further studies were repeated.
As a result, when the resin composition in the cylinder is kept at a temperature 30 to 100 ° C. higher than the glass transition temperature of the resin to be extruded, unexpectedly, the generation of carbides and The present inventors have found a new fact that mixing can be effectively prevented, and furthermore, deterioration of the resin due to continuous heating of the resin composition can be prevented, and the present invention has been completed.

【0008】すなわち、上記課題を解決するための、本
発明に係る押出成形による加工品への有色異物の混入防
止方法は、中断された押出成形を再開するまでの間、押
出機のシリンダ内に樹脂組成物を貯留し、かつ、シリン
ダの少なくとも溶融部における樹脂組成物の温度を前記
樹脂のガラス転移温度より30〜100℃高い温度で維
持することを特徴とする。一般に、押出成形時における
樹脂組成物の温度は、成形の対象となる樹脂の種類によ
って異なるものの、当該樹脂のガラス転移温度よりも1
30〜200℃程度高い温度に、より一般的には150
〜180℃程度高い温度に設定される。従って、シリン
ダ内に貯留される樹脂組成物を上記の温度となるように
して保温すれば、シリンダと樹脂組成物との間に空隙部
が生じることはなく、それゆえ樹脂炭化物の発生やそれ
に伴う加工品への有色異物の混入が生じることはない。
しかしながら、樹脂のガラス転移温度より130〜20
0℃も高い温度にて樹脂組成物をシリンダ内に長時間保
留した場合には、熱劣化が生じて樹脂の黄変等を招くお
それがある。一方、樹脂のガラス転移温度程度(より詳
しくは、ガラス転移温度より10〜20℃程度高い温
度)よりも低い温度にて樹脂組成物をシリンダ内に貯留
した場合には、樹脂組成物の収縮が顕著に生じるため、
シリンダと樹脂組成物との間に空隙部が形成されるのを
避けることができない。
That is, in order to solve the above-mentioned problems, the method for preventing colored foreign matter from being mixed into a processed product by extrusion according to the present invention is provided in a cylinder of an extruder until the interrupted extrusion is restarted. The resin composition is stored, and the temperature of the resin composition in at least the molten portion of the cylinder is maintained at a temperature higher by 30 to 100 ° C. than the glass transition temperature of the resin. Generally, the temperature of the resin composition at the time of extrusion molding varies depending on the type of the resin to be molded, but is one point lower than the glass transition temperature of the resin.
Temperatures as high as 30-200 ° C., more typically 150
The temperature is set to about 180 ° C. higher. Therefore, if the resin composition stored in the cylinder is kept at the above-mentioned temperature and kept warm, there is no gap between the cylinder and the resin composition, and therefore the generation of resin carbide and the accompanying No colored foreign matter is mixed into the processed product.
However, the glass transition temperature of the resin is 130 to 20
If the resin composition is kept in the cylinder at a temperature as high as 0 ° C. for a long time, thermal deterioration may occur and yellowing of the resin may be caused. On the other hand, when the resin composition is stored in the cylinder at a temperature lower than about the glass transition temperature of the resin (more specifically, a temperature about 10 to 20 ° C. higher than the glass transition temperature), the shrinkage of the resin composition is reduced. Because it occurs remarkably,
It is unavoidable that a void is formed between the cylinder and the resin composition.

【0009】これに対し、上記本発明の方法によれば、
シリンダ内に貯留される樹脂組成物の保温温度を樹脂の
ガラス転移温度よりも30〜100℃高い温度で実施し
ている。これは、樹脂組成物の保温を上記温度範囲にて
行うときは、実際に押出成形を行う際と、シリンダ内に
て樹脂組成物を保温する際とにおける樹脂組成物の体積
に顕著な差異が生じることがないからである。しかも、
実際に押出成形を行う程度にまでシリンダを昇温させる
必要がないことから、シリンダの加熱に要するコストを
抑制できるだけでなく、加熱に伴う樹脂の劣化を最小限
に抑制することができる。
On the other hand, according to the method of the present invention,
The temperature of the resin composition stored in the cylinder is maintained at a temperature 30 to 100 ° C. higher than the glass transition temperature of the resin. This is because when the temperature of the resin composition is kept in the above temperature range, there is a remarkable difference in the volume of the resin composition between the time of actually performing the extrusion molding and the time of keeping the resin composition in the cylinder. This is because it does not occur. Moreover,
Since it is not necessary to raise the temperature of the cylinder to such an extent that the extrusion is actually performed, not only the cost required for heating the cylinder but also the deterioration of the resin due to the heating can be minimized.

【0010】上記本発明の方法において、押出成形の対
象となる樹脂にはポリメチルメタクリレートが挙げられ
る。このポリメチルメタクリレートは本来、透明性が極
めて高い樹脂であるため、本発明の方法で有色異物の混
入を防止することにより得られる効果は極めて大きい。
また、上記本発明の方法において、押出成形を中断して
いる間には、押出機のダイリップ部を封止するのが好ま
しい。ダイリップ部を封止することによって、ダイ内部
の樹脂溶融物が空気と接触するのを防止することができ
る。それゆえ、たとえ押出機の稼働停止時にダイを押出
機に装着し続けたとしても、ダイ内に残存する樹脂組成
物の酸化劣化および樹脂炭化物の発生を抑制することが
できる。なお、ダイの内壁にて樹脂の炭化物が発生した
場合には、鱗片状または塊状の鮮明な茶褐色から黒色の
異物が加工品中に混入するおそれがある。
In the method of the present invention, the resin to be subjected to extrusion molding includes polymethyl methacrylate. Since polymethyl methacrylate is originally a resin having extremely high transparency, the effect obtained by preventing the contamination of colored foreign matter by the method of the present invention is extremely large.
In the method of the present invention, the die lip of the extruder is preferably sealed while the extrusion is interrupted. By sealing the die lip, it is possible to prevent the resin melt inside the die from coming into contact with air. Therefore, even if the die is continuously mounted on the extruder when the operation of the extruder is stopped, it is possible to suppress the oxidative deterioration of the resin composition remaining in the die and the generation of resin carbide. When a resin carbide is generated on the inner wall of the die, a scaly or massive clear brown to black foreign substance may be mixed into the processed product.

【0011】さらに、従来は、ダイ内壁面での樹脂組成
物の炭化を防止するため、押出機の稼働を停止する毎に
ダイの取り外しを要求されることがあったのに対し、上
記の本発明の方法によれば、ダイの取り外しによる余分
な手間を省くことができ、ダイリップ部に封止部材を当
接させるという簡易な処置を施すだけで、前述の効果を
得ることができる。加えて、ダイが縦置き型である場合
には、押出機の稼働停止時にダイ内部に樹脂組成物が散
逸するが、ダイの内壁面にわずかに樹脂組成物が付着し
ているとその樹脂が炭化し易くなり、稼働再開時に黒点
異物を顕著に発生させる原因となる。これに対し、ダイ
リップ部を封止することで稼働停止時の樹脂組成物の散
逸を防ぎ、かつ、シリンダの冷却に伴って樹脂組成物の
収縮が生じたとしても、ダイ内壁面と樹脂組成物との間
に空気が入り込むのを抑制でき、黒点異物の発生防止を
より確実なものとすることができる。
Further, conventionally, in order to prevent carbonization of the resin composition on the inner wall surface of the die, it has been required to remove the die every time the operation of the extruder is stopped. According to the method of the invention, it is possible to save extra labor due to the removal of the die, and the above-described effect can be obtained only by performing a simple treatment of bringing the sealing member into contact with the die lip portion. In addition, when the die is of a vertical type, the resin composition dissipates inside the die when the operation of the extruder is stopped, but if the resin composition adheres slightly to the inner wall surface of the die, the resin is It is easy to carbonize and causes black spot foreign matter to be generated remarkably when the operation is resumed. On the other hand, sealing the die lip prevents the resin composition from dissipating when the operation is stopped, and even if the resin composition shrinks due to the cooling of the cylinder, the die inner wall surface and the resin composition Air can be suppressed from entering between them, and the occurrence of black spot foreign matter can be more reliably prevented.

【0012】一方、ダイが横置き型である場合には、ダ
イ内部における樹脂組成物の散逸量は少ないものの、ダ
イリップ部の封止によってダイ内部への空気の侵入を防
止することができ、上記の場合と同様、黒点異物の発生
防止をより確実なものとすることができる。
On the other hand, when the die is of a horizontal type, although the amount of the resin composition dissipated inside the die is small, it is possible to prevent air from entering the inside of the die by sealing the die lip. As in the case (1), the generation of black spot foreign matter can be more reliably prevented.

【0013】[0013]

【発明の実施の形態】以下、本発明に係る、押出成形に
よる加工品への有色異物の混入防止方法について詳細に
説明する。本発明の方法に適用可能な樹脂組成物を構成
する樹脂としては、例えばポリメチルメタクリレート
(PMMA);ゴムを含有する耐衝撃性(メタ)アクリ
ル樹脂;コモノマーとしてメチルアクリレート、エチル
アクリレート、ブチルアクリレート、スチレン等を含有
する(メタ)アクリル樹脂といった(メタ)アクリル系
樹脂が挙げられる。また、かかる(メタ)アクリル系樹
脂のほかにも、例えばポリ塩化ビニル(PVC)系樹
脂、ポリスチレン(PS)系樹脂、ポリカーボネート
(PC)系樹脂等の、従来公知の種々の熱可塑性樹脂が
挙げられる。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, a method of preventing colored foreign matter from mixing into a processed product by extrusion molding according to the present invention will be described in detail. Examples of the resin constituting the resin composition applicable to the method of the present invention include polymethyl methacrylate (PMMA); impact-resistant (meth) acrylic resin containing rubber; methyl acrylate, ethyl acrylate, butyl acrylate as a comonomer; A (meth) acrylic resin such as a (meth) acrylic resin containing styrene or the like can be used. In addition to the (meth) acrylic resin, various conventionally known thermoplastic resins such as a polyvinyl chloride (PVC) resin, a polystyrene (PS) resin, and a polycarbonate (PC) resin are exemplified. Can be

【0014】上記熱可塑性樹脂には、押出シートの用途
や要求される特性等に応じて、架橋剤、補強剤等の、従
来公知の種々の添加剤を配合することができる。添加剤
の種類、配合量等については、常法に従って設定すれば
よい。 〔樹脂組成物の保温温度〕本発明の方法において、押出
成形を一時停止する際の樹脂組成物の温度(以下、「樹
脂組成物の保温温度」という。)は、少なくともシリン
ダの溶融部において、溶融されている樹脂のガラス転移
温度Tgより30〜100℃高くなるように設定され
る。例えば押出成形の対象となる樹脂がPMMAである
場合、PMMAの分子量によって異なるものの、そのガ
ラス転移温度Tgは100℃前後、より詳しくは85〜
105℃程度であることから、このTgを基準として樹
脂組成物の保温温度が決定される。
The thermoplastic resin may contain various conventionally known additives such as a cross-linking agent and a reinforcing agent, depending on the use of the extruded sheet and the required properties. The type and amount of the additive may be set according to a conventional method. [Insulating Temperature of Resin Composition] In the method of the present invention, the temperature of the resin composition at the time of temporarily stopping the extrusion (hereinafter, referred to as “insulating temperature of the resin composition”) is at least in the melting portion of the cylinder. The temperature is set to be 30 to 100 ° C. higher than the glass transition temperature Tg of the molten resin. For example, when the resin to be subjected to extrusion molding is PMMA, the glass transition temperature Tg is around 100 ° C., more specifically 85 to 85 ° C., although it depends on the molecular weight of PMMA.
Since the temperature is about 105 ° C., the temperature for keeping the resin composition is determined based on the Tg.

【0015】図1は、押出成形機の一例を示す模式的断
面図である。一般に押出機10は、内部にスクリュー1
4を有するシリンダ11、樹脂溶融物の吐出量を調整す
るギヤポンプ17、シリンダの吐出口15にギヤポンプ
17を介して接続されるダイ18、シリンダ11内に樹
脂組成物を供給するホッパー20等を備えている。ホッ
パー20から供給された樹脂組成物(通常、ペレット状
のもの)は、スクリュー14による推進力で吐出口15
側に移動するとともに、シリンダ11の外周面に備えら
れたヒーター13によって加熱される。また、シリンダ
のホッパー20側における供給部11bから、シリンダ
11の吐出口15側における溶融部11aへと樹脂組成
物が移動するに連れて、当該樹脂組成物は溶融状態とな
っていく。
FIG. 1 is a schematic sectional view showing an example of an extruder. Generally, the extruder 10 has a screw 1 inside.
4 includes a cylinder 11, a gear pump 17 for adjusting the discharge amount of the resin melt, a die 18 connected to the discharge port 15 of the cylinder via the gear pump 17, a hopper 20 for supplying the resin composition into the cylinder 11, and the like. ing. The resin composition (usually in the form of pellets) supplied from the hopper 20 is supplied to the discharge port 15 by the driving force of the screw 14.
Side, and is heated by a heater 13 provided on the outer peripheral surface of the cylinder 11. Further, as the resin composition moves from the supply section 11b on the hopper 20 side of the cylinder to the melting section 11a on the discharge port 15 side of the cylinder 11, the resin composition becomes in a molten state.

【0016】本発明においては、少なくとも溶融部11
aにおける樹脂組成物の保温温度(いわゆる押出温度ま
たは出口温度)が上記の範囲を満たすことが求められ
る。従って、供給部11b等の、溶融部11a以外の領
域におけるシリンダ温度は特に限定されるものではな
い。かかる領域での樹脂組成物の保温温度は、熱劣化を
起こすことのない温度範囲で適宜設定すればよい。樹脂
組成物の保温温度(℃)が、シリンダ11の溶融部11
aにおいてTg+30(℃)を下回ると、樹脂組成物の
収縮が顕著に生じてシリンダと樹脂組成物との間に空隙
部が形成されることから、樹脂炭化物の発生および成形
品中での有色異物の混入を防止することができなくな
る。逆に、樹脂組成物の保温温度(℃)がTg+100
(℃)を超えると、シリンダと樹脂組成物との間に空隙
部が形成されるおそれは生じにくいものの、押出機の稼
働を停止している間に樹脂組成物に熱劣化が生じ易くな
り、樹脂の黄変等が起こるおそれが高くなる。
In the present invention, at least the molten portion 11
It is required that the temperature for keeping the resin composition (a) (the so-called extrusion temperature or outlet temperature) satisfy the above range. Therefore, the cylinder temperature in a region other than the melting portion 11a, such as the supply portion 11b, is not particularly limited. The heat retaining temperature of the resin composition in such a region may be appropriately set within a temperature range that does not cause thermal deterioration. The temperature at which the resin composition is kept warm (° C.)
If the temperature is lower than Tg + 30 (° C.), the resin composition significantly shrinks and a void is formed between the cylinder and the resin composition. Cannot be prevented from being mixed. Conversely, the temperature at which the resin composition is kept warm (° C.) is Tg + 100.
When the temperature exceeds (° C.), although there is little possibility that a void is formed between the cylinder and the resin composition, the resin composition tends to undergo thermal deterioration while the operation of the extruder is stopped, The risk of yellowing of the resin and the like increases.

【0017】樹脂組成物の保温温度(℃)は、上記範囲
の中でも特に、Tg+30〜Tg+80(℃)であるの
が好ましく、Tg+40〜Tg+60(℃)であるのが
より好ましい。なお、特に限定されるものではないが、
保温温度は、上記範囲内においてより低い温度であるの
が、シリンダの加熱に要するコストを低減する観点から
より好ましい。 〔本発明の他の適用例〕上記本発明の方法は、例えば2
つのシリンダから別々の樹脂組成物を押し出して樹脂積
層体を製造する場合であって、一方のシリンダからの押
出を一時中断して単層体を成形し、必要に応じて、再度
2つのシリンダ樹脂積層体を形成するような場合におい
ても適用可能である。すなわち、押出を一時中断する側
のシリンダについて、押出成形を再開するまでの間、そ
のシリンダ内に貯留された樹脂組成物の温度を上記の範
囲で設定することによって、稼働再開後の積層体に有色
異物が混入するのを十分に抑制することができる。
The temperature for keeping the resin composition (° C.) is preferably Tg + 30 to Tg + 80 (° C.), and more preferably Tg + 40 to Tg + 60 (° C.). Although not particularly limited,
It is more preferable that the heat retaining temperature be lower within the above range from the viewpoint of reducing the cost required for heating the cylinder. [Other application examples of the present invention] The method of the present invention is, for example, as follows.
In the case where a resin laminate is manufactured by extruding separate resin compositions from one cylinder, extrusion from one cylinder is temporarily interrupted to form a single-layer body, and if necessary, two cylinder resins are formed again. The present invention is also applicable to a case where a laminate is formed. That is, for the cylinder on which the extrusion is temporarily suspended, by setting the temperature of the resin composition stored in the cylinder in the above range until the extrusion is restarted, the laminated body after the restart of the operation The incorporation of colored foreign matter can be sufficiently suppressed.

【0018】〔ダイリップ部の封止〕本発明の方法にお
いて、押出成形を一時停止する際にダイのリップ部を封
止するための部材としては、特に限定されるものではな
く、ダイリップ部の形状等に応じて適宜設計すればよ
い。一般にダイリップ部の封止部材21として好適な形
状は、例えば図2に示すように、ダイ18のリップ部1
9に押し当ててその開口を塞ぐことができ、しかも、ダ
イリップ部19より漏出した樹脂組成物22を貯留する
ことのできる受け部23を備えたものである。
[Sealing of Die Lip] In the method of the present invention, the member for sealing the lip of the die when the extrusion is temporarily stopped is not particularly limited, and the shape of the die lip is not particularly limited. What is necessary is just to design suitably according to the etc. In general, a suitable shape for the sealing member 21 of the die lip portion is, for example, as shown in FIG.
9 is provided with a receiving portion 23 that can close the opening by pressing the resin composition 9 and that can store the resin composition 22 leaked from the die lip portion 19.

【0019】[0019]

〔樹脂組成物の温度制御の効果〕(Effect of temperature control of resin composition)

実施例1 汎用のポリメチルメタクリレート〔PMMA,住友化学
工業(株)製の商品名「スミペックスEX」、ガラス転
移温度Tg102℃〕を市販の押出機におけるシリンダ
内で溶融させ、押出機を稼働してシートの成形を行った
後、シリンダ溶融部における樹脂組成物の温度を150
℃に設定して、24時間保持(保温)した。なお、保温
に際しては、あらかじめダイを取り外した。
Example 1 A general-purpose polymethyl methacrylate (PMMA, trade name “SUMIPEX EX” manufactured by Sumitomo Chemical Co., Ltd., glass transition temperature Tg: 102 ° C.) was melted in a cylinder of a commercially available extruder, and the extruder was operated. After forming the sheet, the temperature of the resin composition in the cylinder fusion zone was raised to 150
C., and kept (warmed) for 24 hours. At the time of keeping the temperature, the die was removed in advance.

【0020】24時間経過後、ダイを取り付け、かつ、
シリンダを250℃程度にまで昇温して、押出成形によ
るシートの製造を連続して行った。こうして得られたシ
ートのうち、押出機の稼働再開後から10分を経過する
毎にサンプルを採取した。このサンプルについては、2
00×200mmの範囲を任意に10点選択して、当該
範囲内での有色異物の発生状況を顕微鏡により観察し
た。こうして、樹脂炭化物の発生が減少して、有色異物
の混入が実用上問題とならない範囲にまで低減される時
間を求めた。
After a lapse of 24 hours, the die is attached, and
The temperature of the cylinder was raised to about 250 ° C., and sheets were continuously manufactured by extrusion. From the sheets thus obtained, samples were taken every 10 minutes after the operation of the extruder was restarted. For this sample,
Ten points in a range of 00 × 200 mm were arbitrarily selected, and the occurrence of colored foreign matters in the range was observed with a microscope. Thus, the time required for reducing the generation of the resin carbide and reducing the mixing of the colored foreign matter to a range that does not pose a practical problem was determined.

【0021】比較例1および2 市販の押出機に代えて試験用の小型押出機を使用し、シ
リンダ溶融部における樹脂組成物の温度を260℃(比
較例1)または50℃(比較例2)としたほかは、実施
例1と同様にしてシートの成形と、稼働の中断およびシ
リンダの保温(24時間)と、稼働再開後のシートの成
形と、を行った。さらに、得られたシートについて有色
異物の発生状況の観察を行った。
Comparative Examples 1 and 2 A small extruder for testing was used in place of a commercially available extruder, and the temperature of the resin composition at the melting portion of the cylinder was 260 ° C. (Comparative Example 1) or 50 ° C. (Comparative Example 2). In the same manner as in Example 1, the sheet was formed, the operation was interrupted and the cylinder was kept warm (24 hours), and the sheet was formed after the operation was restarted. Further, the occurrence of colored foreign matter was observed on the obtained sheet.

【0022】〔ダイリップ部のカバー装着効果〕 実施例2 汎用のPMMA(前出の「スミペックスEX」、ガラス
転移温度Tg102℃)を市販の押出機に投入して、シ
ートの成形を行った。この際の、シリンダ溶融部におけ
る樹脂組成物の温度は250℃程度であった。次に、押
出機の稼働を一時停止し、シリンダ溶融部における樹脂
組成物の温度を150℃に設定するとともに、ダイを取
りつけたまま、そのリップ部に封止部材(カバー)を取
付けた。この状態で24時間保持した後、再びシリンダ
を250℃程度にまで昇温して、押出成形によりシート
を成形した。
[Effect of Attaching Cover of Die Lip] Example 2 A general-purpose PMMA (the above-mentioned “SUMIPEX EX”, glass transition temperature Tg: 102 ° C.) was charged into a commercially available extruder to form a sheet. At this time, the temperature of the resin composition in the cylinder melting part was about 250 ° C. Next, the operation of the extruder was temporarily stopped, the temperature of the resin composition in the cylinder melting portion was set to 150 ° C., and a sealing member (cover) was attached to the lip portion of the extruder while the die was attached. After maintaining this state for 24 hours, the temperature of the cylinder was raised again to about 250 ° C., and a sheet was formed by extrusion.

【0023】こうして得られたシートから、200×2
00mmの範囲を任意に10点選択して、顕微鏡により
シート中の有色異物の発生状況を観察した。 比較例3 押出機の稼働を一時停止している間、ダイを取りつけた
状態としつつも、そのリップ部に封止部材を取りつけな
かったほかは、実施例2と同様にしてシートの成形を行
った。
From the sheet thus obtained, 200 × 2
Ten points in a range of 00 mm were arbitrarily selected, and the occurrence of colored foreign matter in the sheet was observed with a microscope. Comparative Example 3 While the operation of the extruder was temporarily stopped, the sheet was formed in the same manner as in Example 2 except that the sealing member was not attached to the lip portion while the die was attached. Was.

【0024】上記実施例1,2および比較例1〜3につ
いて、成形したシート中での有色異物の発生状況を観察
して得られた結果を元にして、押出機の稼働再開後か
ら、異物の混入量が実用上問題とならない程度にまで低
減されるまでに要した時間(混入異物の消失時間)を求
めた。その結果を表1に示す。
In Examples 1 and 2 and Comparative Examples 1 to 3, based on the results obtained by observing the occurrence of colored foreign matter in the formed sheet, the foreign matter was re-started after the extruder was restarted. The amount of time required for the amount of contaminants to be reduced to a level that does not pose a practical problem (the time for disappearance of contaminating foreign substances) was determined. Table 1 shows the results.

【0025】[0025]

【表1】 [Table 1]

【0026】表1より明らかなように、シリンダ溶融部
における樹脂組成物の保温温度を樹脂のガラス転移温度
より30〜100℃の範囲で高く設定した実施例1と、
さらに押出機の稼働中断時にダイリップ部を封止した実
施例2では、茶褐色や黒色の異物の混入量が実用上問題
とならない程度にまで低減されるのに要する時間が極め
て短かった。一方、シリンダ溶融部における樹脂組成物
の保温温度が高過ぎる比較例1では樹脂の黄変が生じて
おり、それに伴い、主に茶褐色の異物混入が顕著に生じ
た。逆に、シリンダ溶融部における樹脂組成物の保温温
度が低すぎる比較例2では、主に黒色の異物混入が顕著
に生じた。押出機の稼働停止時にダイを取りつけたま
ま、そのリップ部を封止しなかった比較例3では、主に
茶褐色の異物混入が顕著に生じた。
As is evident from Table 1, Example 1 in which the temperature for keeping the resin composition in the cylinder melting portion was set higher than the glass transition temperature of the resin in the range of 30 to 100 ° C.,
Further, in Example 2, in which the die lip portion was sealed when the operation of the extruder was interrupted, the time required for reducing the amount of the brown or black foreign matter mixed to such an extent that no practical problem was caused was extremely short. On the other hand, in Comparative Example 1 in which the heat retaining temperature of the resin composition in the cylinder melting portion was too high, yellowing of the resin occurred, and consequently, mainly brownish foreign matter was significantly mixed. Conversely, in Comparative Example 2 in which the temperature of keeping the resin composition in the cylinder fusion zone was too low, the mixing of mainly black foreign substances was remarkable. In Comparative Example 3 in which the lip was not sealed while the die was attached when the operation of the extruder was stopped, mainly brownish foreign matter was conspicuously produced.

【0027】また、上記比較例のいずれにおいても、異
物混入量が実用上問題とならない程度にまで低減される
のには極めて長い時間を要した。
In each of the above comparative examples, it took a very long time for the amount of foreign matter to be reduced to such an extent that no practical problem occurred.

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

【図1】押出機の一例を示す正面図である。FIG. 1 is a front view showing an example of an extruder.

【図2】ダイリップ部の封止部材の一例を示す断面図で
ある。
FIG. 2 is a cross-sectional view illustrating an example of a sealing member of a die lip portion.

【符号の説明】[Explanation of symbols]

10 押出機 11 シリンダ 11a 溶融部 18 ダイ 19 リップ部 21 封止部材 DESCRIPTION OF SYMBOLS 10 Extruder 11 Cylinder 11a Melting part 18 Die 19 Lip part 21 Sealing member

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】中断された押出成形を再開するまでの間、
押出機のシリンダ内に樹脂組成物を貯留し、かつ、シリ
ンダの少なくとも溶融部における樹脂組成物の温度を前
記樹脂のガラス転移温度より30〜100℃高い温度で
維持することを特徴とする、押出成形による加工品への
有色異物の混入防止方法。
1. Until the interrupted extrusion is restarted,
Extrusion, wherein the resin composition is stored in a cylinder of the extruder, and the temperature of the resin composition in at least a molten portion of the cylinder is maintained at a temperature higher by 30 to 100 ° C. than the glass transition temperature of the resin. A method for preventing colored foreign matter from mixing into processed products by molding.
【請求項2】前記樹脂がポリメチルメタクリレートであ
る請求項1記載の、押出成形による加工品への有色異物
の混入防止方法。
2. The method according to claim 1, wherein said resin is polymethyl methacrylate.
【請求項3】押出成形を中断している間、押出機のダイ
リップ部を封止する請求項1記載の、押出成形による加
工品への有色異物の混入防止方法。
3. The method according to claim 1, wherein the die lip of the extruder is sealed while the extrusion is interrupted.
JP2000238849A 2000-08-07 2000-08-07 Method for preventing mixture of colored foreign matter with molding by extrusion molding Pending JP2002052596A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000238849A JP2002052596A (en) 2000-08-07 2000-08-07 Method for preventing mixture of colored foreign matter with molding by extrusion molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000238849A JP2002052596A (en) 2000-08-07 2000-08-07 Method for preventing mixture of colored foreign matter with molding by extrusion molding

Publications (1)

Publication Number Publication Date
JP2002052596A true JP2002052596A (en) 2002-02-19

Family

ID=18730485

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000238849A Pending JP2002052596A (en) 2000-08-07 2000-08-07 Method for preventing mixture of colored foreign matter with molding by extrusion molding

Country Status (1)

Country Link
JP (1) JP2002052596A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101044765B1 (en) 2009-11-17 2011-06-29 한국타이어 주식회사 Extruder for extruding rubber mix prevention
CN107866956A (en) * 2017-12-11 2018-04-03 黄山永新股份有限公司 The die lip enclosure method of film machine film head closing device and the application device

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5725919A (en) * 1980-07-23 1982-02-10 Mitsubishi Chem Ind Ltd Method and device for extrusion molding of thermoplastic synthetic resin
JPH04276417A (en) * 1991-03-05 1992-10-01 Teijin Chem Ltd Stopping method for molding machine

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5725919A (en) * 1980-07-23 1982-02-10 Mitsubishi Chem Ind Ltd Method and device for extrusion molding of thermoplastic synthetic resin
JPH04276417A (en) * 1991-03-05 1992-10-01 Teijin Chem Ltd Stopping method for molding machine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101044765B1 (en) 2009-11-17 2011-06-29 한국타이어 주식회사 Extruder for extruding rubber mix prevention
CN107866956A (en) * 2017-12-11 2018-04-03 黄山永新股份有限公司 The die lip enclosure method of film machine film head closing device and the application device
CN107866956B (en) * 2017-12-11 2023-09-22 黄山永新股份有限公司 Film spraying head sealing device for film spraying machine and die lip sealing method using same

Similar Documents

Publication Publication Date Title
US20100175720A1 (en) Cleaning agent and process for cleaning resin-molding machine using the same
US6387306B1 (en) Deaeration of feed materials in an extrusion process
WO2015093256A1 (en) Plastic molding method
US5424012A (en) Method for purging thermoplastic extruders
JP5429674B2 (en) Thermoplastic extrusion equipment
JP2007290384A (en) Melt kneading device and production process of thermoplastic resin composition
JP2002052596A (en) Method for preventing mixture of colored foreign matter with molding by extrusion molding
JPH1060487A (en) Substituted pyrrolidone-plasticized thermoplastic resin useful as cleaning agent for plastic treating facility
JPS6289710A (en) Production of methacrylic resin
JP5199215B2 (en) Resin cleaning composition and method for cleaning thermoplastic resin processing apparatus
JP2014214191A (en) Resource recovery method of polycarbonate-based resin waste, production method of regenerated polycarbonate-based resin molded product, and regenerated polycarbonate-based resin molded product
JP5872905B2 (en) Method for producing transparent thermoplastic resin pellets
JP2017128088A (en) Method for producing thermoplastic resin composition
CN212666650U (en) Exhaust stop device
ZA200307599B (en) Method and device for regulating pressure in a single-screw degassing extruder or in a cascade extruder.
JP4350756B2 (en) Processing device for thermoplastic resin composition containing additives
JP4076167B2 (en) Cleaning composition and method for cleaning thermoplastic resin processing apparatus
JP4650963B2 (en) Electric wire coating material recycling method and recycling apparatus
JP6488433B1 (en) Cleaning agent and cleaning method for molding machine cleaning
JP2006123364A (en) Flushing method for sheet extruder
JP2010228408A (en) Extruder for kneading thermoplastic resin and method for manufacturing thermoplastic resin composition
JP3016711B2 (en) Degassing method in extrusion molding and venting device of extruder
JP6951862B2 (en) Manufacturing method of recycled filter, manufacturing method of molded product of recycled filter and thermoplastic resin composition
JPH06226816A (en) Method and apparatus for melting, degassing and extrusion molding
JP2022073727A (en) Plastic granulator and filtration apparatus used therefor

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20070619

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20090825

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090903

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20091029

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20100318