JPS5941240A - Method of extrusion - Google Patents

Method of extrusion

Info

Publication number
JPS5941240A
JPS5941240A JP57152457A JP15245782A JPS5941240A JP S5941240 A JPS5941240 A JP S5941240A JP 57152457 A JP57152457 A JP 57152457A JP 15245782 A JP15245782 A JP 15245782A JP S5941240 A JPS5941240 A JP S5941240A
Authority
JP
Japan
Prior art keywords
die
refuse
lubricant
amount
extrusion
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.)
Granted
Application number
JP57152457A
Other languages
Japanese (ja)
Other versions
JPH0331572B2 (en
Inventor
Makoto Hashimoto
誠 橋本
Yoshiyuki Nishikawa
西川 善之
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.)
Dainichi Nippon Cables Ltd
Original Assignee
Dainichi Nippon Cables 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 Dainichi Nippon Cables Ltd filed Critical Dainichi Nippon Cables Ltd
Priority to JP57152457A priority Critical patent/JPS5941240A/en
Publication of JPS5941240A publication Critical patent/JPS5941240A/en
Publication of JPH0331572B2 publication Critical patent/JPH0331572B2/ja
Granted 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
    • B29C48/94Lubricating
    • 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
    • B29C48/27Cleaning; Purging; Avoiding contamination
    • B29C48/272Cleaning; Purging; Avoiding contamination of dies
    • 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
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion

Landscapes

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

Abstract

PURPOSE:To reduce the amount of die refuse resulting from the extrusion of rubber or plastic compositions, and to continuously removing such die refuse thereby preventing the appearance of an extrudate from becoming defective, by supplying a lubricant to the inner surface of an extruding die. CONSTITUTION:When a rubber or plastic composition (in particular, a composition containing a compound having high adhesion to metals such as Si-O compounds or a composition containing a higher amount of an inorganic filler) is continuously extruded for a longer period, it is liable to allow solids (die refuse) to accumulate at the outlet section of the die. This can be prevented by supplying a lubricant (e.g. mineral oils, polybutenes, silicone oils, etc.) to the die inner wall. It is suitable that the amount of the application is on the order of 10- 100mumin terms of the thickness of the lubricant applied on the die inner wall.

Description

【発明の詳細な説明】 ゴム、プラスチック組成物のある種のもの。[Detailed description of the invention] Certain types of rubber and plastic compositions.

たとえば5i−0化合物のように金属との付着性のよい
化合物を含む組成物や多量の無機質充填剤を含むものは
、長時間の連続押出の間にダイ出口部に”ダイ粕”と通
称されている固形分が溜る問題がある。このダイ粕は、
押出物の表面に掻きずを生ぜしめる、あるいは不定期的
にダイから剥離して押出物の表面に固着するなどして押
出物の外観不良の原因となる。
For example, compositions containing compounds with good adhesion to metals, such as 5i-0 compounds, and those containing large amounts of inorganic fillers are commonly known as "die sludge" at the die exit during long-term continuous extrusion. There is a problem with solids buildup. This die lees is
It causes scratches on the surface of the extrudate, or it irregularly peels off from the die and sticks to the surface of the extrudate, causing poor appearance of the extrudate.

本発明者らの研究によれば、このダイ粕は。According to the research of the present inventors, this die lees.

ゴム、プラスチック組成物がダイ内を通過する際5該組
成物とダイ内壁との間の摩擦によって該組成物表面層近
傍に大きな剪断力が生じ、この剪断力によってゴト、プ
ラスチック組成物の一部が粒状となって離脱する。ある
いは組成物中の充填剤が離脱する、ことにより発生する
ものである。更に本発明者らの研究によれば、ダイ内壁
に潤滑油を供給することにより上記した摩擦力が軽減し
、而してグイ粕の発生量自体が減少するとともに、たと
え微量の固形分の離脱があっても、ダイ出口の表面を覆
う潤滑油の付着防止作用により、それら微量の固形分は
押出物の表面に付着してダイの外部に出て行くのでダイ
粕として溜ることはない。また、押出物の表面に付着し
た個々の固形分は微量であるので、。
When a rubber or plastic composition passes through the die, a large shearing force is generated near the surface layer of the composition due to friction between the composition and the inner wall of the die, and this shearing force causes a part of the plastic composition to break down. becomes granular and separates. Alternatively, it may occur due to detachment of the filler in the composition. Furthermore, according to the research conducted by the present inventors, supplying lubricating oil to the inner wall of the die reduces the above-mentioned frictional force, thereby reducing the amount of lees generated and preventing the separation of even a small amount of solid matter. However, due to the adhesion prevention effect of the lubricating oil that covers the surface of the die outlet, these minute amounts of solid matter adhere to the surface of the extrudate and exit the die, so they do not accumulate as die sludge. In addition, since the amount of individual solids adhering to the surface of the extrudate is very small.

押出物の外観を実質的に損うことはない。The appearance of the extrudate is not substantially impaired.

本発明は、上記の新知見に基づいて完成した特許請求の
範囲に記載の押出成形法を提案するものである。
The present invention proposes an extrusion molding method as described in the claims, which was completed based on the above new findings.

自滑油としては、押出成形の対象とするゴム。As a self-lubricating oil, rubber is used for extrusion molding.

プラスチ・νり組成物に対して実際上の見地から悪影響
を及ぼすものでない限り、化学種を問わず種々のものが
用いられる。たとえば鉱油、不乾性の動植物油などの天
然油類、ポリブテン、エチレンオキサイドーグロビレノ
オキサイド共重合体油、シリコン油、重質アルキルベン
ゼン油、などの合成油類である。
A variety of chemical substances may be used, as long as they do not have an adverse effect on the plastic composition from a practical standpoint. Examples include natural oils such as mineral oil and non-drying animal and vegetable oils, and synthetic oils such as polybutene, ethylene oxide-globylen oxide copolymer oil, silicone oil, and heavy alkylbenzene oil.

ダイ内壁への潤滑油の供給方法については。Regarding the method of supplying lubricating oil to the inner wall of the die.

特に−制限がなく、たとえば、ダイそのものを焼結金属
にて形成し、外部より供給する潤滑油をダイ内壁全面か
らにじみ出させる方法、ダイのランド部及び/又はテー
バ部に円周状の潤滑油放出スリットを設けておき外部よ
り供給する潤滑油を該スリットよりダイ内壁に供給する
方法などである。
There are no particular restrictions, such as a method in which the die itself is made of sintered metal and lubricating oil supplied from the outside oozes out from the entire inner wall of the die, or a method in which lubricating oil is applied in a circumferential manner to the land and/or taper portion of the die. This method includes providing a discharge slit and supplying lubricating oil from the outside to the inner wall of the die through the slit.

潤滑油の供給量は、ダイ粕の発生の有無により試行錯誤
的に決定することができるが、一般的にはダイ内壁上の
油膜厚さにしてlOμm〜100μm程度が適当である
。上記したスリットから潤滑油をダイ内に供給する場合
、該スリットは、ダイの出口近傍に設けても充分グイ粕
発生防止効果はあるが、ダイのテーバ部乃至ダイのラン
ド入口部あたりに設けるのが好ましい。
The amount of lubricating oil to be supplied can be determined by trial and error depending on the presence or absence of die sludge, but generally the thickness of the oil film on the inner wall of the die is approximately 10 μm to 100 μm. When lubricating oil is supplied into the die from the above-mentioned slit, the slit can be provided near the exit of the die to sufficiently prevent the generation of scum, but it is not recommended to provide the slit near the taper part of the die or the land entrance of the die. is preferred.

以下に示す実施例、比較例から本発明の顕著な効果が理
解されよう。
The remarkable effects of the present invention will be understood from the Examples and Comparative Examples shown below.

実施例1、比較例1 ポリエチレン100部(重量部、以下同様)、ビニルト
リメトキシシラン2部、ジクミルパーオキシド02部、
及びジブチル−錫−ジラウレ−ト0.05部からなる水
架橋性ポリエチレン組成物をクロスヘッド温度160℃
、シリンダ−11!度120〜150°Cに設定したL
/D 28のスクリl−を有する押出機にて断面積20
0闇でかつ導体遮蔽層を有する撚線銅導体上に6.5闇
厚で押出しだ。押出開始10分層上りからダ1粕の発生
がみられ、更に60分右心たりから直径2〜5咽のグイ
粕が約05ケ/分の割合でダイから離脱してポリエチレ
ン層表面に付着した。押出開始80分右上りダイのう/
ド入口に設けた円周状スリットから1.2cc/分の流
量にてユニループ50MB−26X(日本油脂社製のエ
チレンオキサイド−プロピレンオキサイドブロック共重
合体、230℃の粘度:5.73c、s、t、)を連・
続供給したところ、上記潤滑油供給開始約1右心、それ
まで存在していたグイ粕がはソ全部グイより離脱し、以
后ダイ粕の新たな発生はみられなかった。
Example 1, Comparative Example 1 100 parts of polyethylene (parts by weight, same hereinafter), 2 parts of vinyltrimethoxysilane, 02 parts of dicumyl peroxide,
and 0.05 part of dibutyl-tin-dilaurate at a crosshead temperature of 160°C.
, cylinder-11! L set at 120-150°C
/D 28 cross-sectional area 20 in an extruder with a screen l-
It was extruded at a thickness of 0 and 6.5 mm onto a stranded copper conductor with a conductor shielding layer. 10 minutes after the start of extrusion, the generation of 1 dregs was observed, and after 60 minutes from the right center, 2 to 5 sq. diameter dregs were detached from the die at a rate of approximately 0.05 sq./min and adhered to the surface of the polyethylene layer. did. Extrusion starts 80 minutes right-up die/
Uniloop 50MB-26X (ethylene oxide-propylene oxide block copolymer manufactured by NOF Corporation, viscosity at 230°C: 5.73 c, s, t,)
When the lubricating oil was continued to be supplied, about 1 hour after the start of the supply of the lubricating oil, all of the guinea sludge that had existed up to that time was separated from the guinea fluid, and no new guinea sludge was observed to occur after that.

実施例2、比較例2 酢酸ビニル含有量20%のエチレン−酸素ビニル共重合
体に5b20810部、炭酸カルシウム60部、及び亜
鉛華15部を配合した難燃性組成物を、実施例1.比較
例1の場合と同じ押出機を用い、同条件で押出したとこ
ろ、押出開始15分右上りダイ粕の発生がみられ、更に
40分右心たりから直径1〜3鯛のグイ粕が約05ケ/
分の割合でダイから離脱してポリマー表面に付着した。
Example 2, Comparative Example 2 A flame retardant composition prepared by blending 20,810 parts of 5b, 60 parts of calcium carbonate, and 15 parts of zinc white into an ethylene-oxygen vinyl copolymer having a vinyl acetate content of 20% was prepared in Example 1. When the same extruder as in Comparative Example 1 was used and extrusion was carried out under the same conditions, 15 minutes after the start of extrusion, formation of die lees rising to the right was observed, and after another 40 minutes, gui lees with a diameter of 1 to 3 sea bream were observed to appear on the right side. 05 pieces/
It detached from the die and adhered to the polymer surface at a rate of 1.5 min.

次いで、潤滑剤として上記押出温度における粘度が10
〜15 c、s、t、のシリコン油を2.UccZ分の
流量でダイ内面に実施例1と同様の方法で供給したとこ
ろ、シリコン油の供給開始から約1右心、それまで存在
していたグイ粕がはy全部ダイより離脱し、以后、ダイ
粕の新たな発生はみられなかった。
Next, a lubricant with a viscosity of 10 at the extrusion temperature was used as a lubricant.
~15 C, S, T, silicone oil 2. When silicone oil was supplied to the inner surface of the die in the same manner as in Example 1 at a flow rate of UccZ, about 1 right from the start of supply of silicone oil, all the scum that had been present until then separated from the die, and after that, No new occurrence of Dairy lees was observed.

特許出願人 大日日本電線株式会社 代表者代表取締役 青山幸雄patent applicant Dainichi Nippon Electric Cable Co., Ltd. Representative Director Yukio Aoyama

Claims (1)

【特許請求の範囲】[Claims] ダイ粕を発生するゴム、プラスチ・ンク組成物の押出成
形において、成形ダイスの内面に潤滑油を供給すること
を特徴とする押出成形法。
An extrusion molding method characterized by supplying lubricating oil to the inner surface of a molding die in extrusion molding of a rubber or plastic composition that generates die residue.
JP57152457A 1982-08-31 1982-08-31 Method of extrusion Granted JPS5941240A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57152457A JPS5941240A (en) 1982-08-31 1982-08-31 Method of extrusion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57152457A JPS5941240A (en) 1982-08-31 1982-08-31 Method of extrusion

Publications (2)

Publication Number Publication Date
JPS5941240A true JPS5941240A (en) 1984-03-07
JPH0331572B2 JPH0331572B2 (en) 1991-05-07

Family

ID=15540931

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57152457A Granted JPS5941240A (en) 1982-08-31 1982-08-31 Method of extrusion

Country Status (1)

Country Link
JP (1) JPS5941240A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5076988A (en) * 1990-03-09 1991-12-31 Union Carbide Chemicals And Plastics Technology Corporation Process for the extrusion of low density polyethylene
JP2007076718A (en) * 2005-09-16 2007-03-29 Dainippon Printing Co Ltd Spout having pull-ring

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4896656A (en) * 1972-02-15 1973-12-10
JPS5094280U (en) * 1973-12-27 1975-08-07

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4896656A (en) * 1972-02-15 1973-12-10
JPS5094280U (en) * 1973-12-27 1975-08-07

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5076988A (en) * 1990-03-09 1991-12-31 Union Carbide Chemicals And Plastics Technology Corporation Process for the extrusion of low density polyethylene
JP2007076718A (en) * 2005-09-16 2007-03-29 Dainippon Printing Co Ltd Spout having pull-ring

Also Published As

Publication number Publication date
JPH0331572B2 (en) 1991-05-07

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