Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0627234B2 - Extruded product - Google Patents
[go: Go Back, main page]

JPH0627234B2 - Extruded product - Google Patents

Extruded product

Info

Publication number
JPH0627234B2
JPH0627234B2 JP61034452A JP3445286A JPH0627234B2 JP H0627234 B2 JPH0627234 B2 JP H0627234B2 JP 61034452 A JP61034452 A JP 61034452A JP 3445286 A JP3445286 A JP 3445286A JP H0627234 B2 JPH0627234 B2 JP H0627234B2
Authority
JP
Japan
Prior art keywords
crosslinking
acid ester
tetrafluoroethylene
mixture
propylene
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
JP61034452A
Other languages
Japanese (ja)
Other versions
JPS62192437A (en
Inventor
典男 池ケ谷
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.)
KURABE KK
Original Assignee
KURABE 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 KURABE KK filed Critical KURABE KK
Priority to JP61034452A priority Critical patent/JPH0627234B2/en
Publication of JPS62192437A publication Critical patent/JPS62192437A/en
Priority to US07/220,351 priority patent/US4904529A/en
Publication of JPH0627234B2 publication Critical patent/JPH0627234B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Processes Of Treating Macromolecular Substances (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、耐熱性,耐油性に優れた押出成形品に関する
ものである。
TECHNICAL FIELD The present invention relates to an extruded product having excellent heat resistance and oil resistance.

(従来の技術と問題点) 4フッ化エチレン−プロピレン系共重合体は、優れた耐
熱性,耐油性をもつことから、耐熱,耐油性が要求され
るチューブ,パッキン等の押出成形品に利用され始めて
いる。従来より4フッ化エチレン−プロピレン系共重合
体を主成分とする組成物から成る押出成形品は、その組
成物中に架橋助剤としてアリル化合物,架橋剤として有
機過酸化物を含み、前記組成物を押出成形したのち、製
品中にボイドが発生しないように加圧水蒸気により加圧
加熱架橋をするか、あるいはベント型押出機を使い、組
成物中に少量含まれる水分,ガスを真空吸引したのち、
押出成形し、常圧にて加熱架橋する方法がとられてい
る。
(Prior art and problems) Since tetrafluoroethylene-propylene-based copolymers have excellent heat resistance and oil resistance, they are used for extruded products such as tubes and packing that require heat resistance and oil resistance. Is being started. Conventionally, an extrusion-molded article made of a composition containing a tetrafluoroethylene-propylene-based copolymer as a main component contains an allyl compound as a cross-linking aid and an organic peroxide as a cross-linking agent in the composition. After extruding the product, press-heat crosslinking with pressurized steam so that voids do not occur in the product, or use a vent type extruder to suck in a small amount of water and gas contained in the composition under vacuum. ,
A method is employed in which extrusion molding is carried out and heat crosslinking is carried out under normal pressure.

しかし加圧加熱架橋する場合には、電線のように張力に
耐える芯線がないため連続で押出成形−架橋−引取りを
一工程で行うことができず短くカットした後、バッチ式
に架橋しなければならなく工程が増えて生産能力が低く
なる上、加圧蒸気を発生させるボイラーが必要となり、
一方常圧下で加熱架橋可能なベント型押出機を用いる場
合には、通常使用する押出機と異なり段取りにかなりの
時間を要しかつ真空ポンプの真空度が下がらないように
常時注意していなければならなく、更にベント型押出機
は複数のシリンダーかそれに相当する大きなシリンダー
と真空ポンプを必要とする特殊構造の大きな装置である
ため、高価なものになるばかりではなく、広い設置空間
も必要となり、その上前記シリンダー内には多くのコン
パウンドが残るなど通常使用する押出機に比べ工程上の
経費が高く、経済的に不利である。
However, in the case of pressure heating crosslinking, since there is no core wire that can withstand tension like electric wires, continuous extrusion molding-crosslinking-takeover cannot be performed in one step, and after short cutting, crosslinking must be done in batch mode. In addition to increasing the number of processes, the production capacity will decrease, and a boiler that generates pressurized steam will be required.
On the other hand, when using a vent-type extruder capable of heat-crosslinking under normal pressure, it takes a considerable time for setup unlike an extruder normally used, and care must always be taken so that the vacuum degree of the vacuum pump does not drop. Moreover, since the vent type extruder is a large device with a special structure that requires multiple cylinders or large cylinders equivalent to it and a vacuum pump, not only is it expensive, but it also requires a large installation space, In addition, a large amount of compound remains in the cylinder, resulting in a higher process cost than an extruder that is normally used, which is economically disadvantageous.

(発明の目的) 本発明の目的は前記の問題を解決し、耐熱性,耐油性に
優れた押出成形品を提供するものである。更に本発明の
目的はかヽる押出成形品をベント型押出機を用いること
なく、押出成形後同一工程で常圧にて連続加熱架橋する
方法により安価に製造することである。
(Object of the Invention) An object of the present invention is to solve the above problems and to provide an extrusion-molded article having excellent heat resistance and oil resistance. Further, an object of the present invention is to inexpensively produce such an extrusion-molded product by a method of continuously heating and crosslinking at normal pressure in the same step after extrusion molding without using a vent type extruder.

(発明の構成と作用) 即ち、本発明の押出成形品は4フッ化エチレン−プロピ
レン系共重合体を主成分とする組成物に架橋助剤である
メタクリル酸エステル又はアクリル酸エステルと、架橋
剤である有機過酸化物を加えた混合物を、常圧加熱して
架橋した押出成形品、あるいは4フッ化エチレン−プロ
ピレン系共重合体を主成分とする組成物に、架橋助剤で
あるメタクリル酸エステル又はアクリル酸エステルと、
架橋剤である有機過酸化物とを混合し、これにシリコー
ンゴムを4フッ化エチレン−プロピレン系共重合体10
0重量部に対して200重量部以下加えた混合物を、常
圧加熱して架橋した押出成形品である。
(Structure and Action of the Invention) That is, the extrusion-molded product of the present invention comprises a composition containing a tetrafluoroethylene-propylene-based copolymer as a main component, a methacrylic acid ester or an acrylic acid ester as a crosslinking aid, and a crosslinking agent. The mixture obtained by adding the organic peroxide is an extruded product obtained by heating at atmospheric pressure for crosslinking, or a composition containing a tetrafluoroethylene-propylene copolymer as a main component, and methacrylic acid as a crosslinking aid. An ester or an acrylic ester,
An organic peroxide, which is a cross-linking agent, is mixed, and silicone rubber is mixed therein with a tetrafluoroethylene-propylene copolymer 10.
It is an extrusion-molded product obtained by heating a mixture obtained by adding 200 parts by weight or less to 0 parts by weight and heating the mixture under normal pressure to crosslink.

4フッ化エチレン−プロピレン系共重合体は架橋助剤と
してアリル化合物,架橋剤として有機過酸化物を併用し
て架橋するのが通常であるが、本発明においては架橋助
剤としてメタクリル酸エステル又はアクリル酸エステル
と架橋剤として有機過酸化物を併用して架橋することが
特徴である。
The tetrafluoroethylene-propylene copolymer is usually crosslinked by using an allyl compound as a cross-linking aid and an organic peroxide together as a cross-linking agent, but in the present invention, a methacrylic acid ester or a cross-linking aid is used. The feature is that the acrylic ester is used in combination with an organic peroxide as a crosslinking agent for crosslinking.

本発明による混合物は80〜100℃という低温でも架
橋させることが可能であり、ベント型押出機を用いるこ
となく常圧で加熱架橋しても製品中にボイドが発生する
ことがない。架橋助剤としてメタクリル酸エステル又は
アクリル酸エステルに代えてアリル化合物,オキシム化
合物,イオウ,マレイミド化合物等の架橋助剤を使用す
る場合、あるいはメタクリル酸エステル又はアクリル酸
エステルを有機過酸化物と併用しないで単独に使用した
場合、更には架橋剤単独で使用した場合には80〜10
0℃という低温では数10分という単位では殆ど架橋せ
ず、温度を150〜200℃に上げても常圧では製品中
にボイドが発生してしまう。本発明においてメタクリル
酸エステル又はアクリル酸エステルとしてはトリメチロ
ールプロパントリメタクリレート,エチレンジメタクリ
レート,ポリエチレングリコールジメタクリレート,シ
クロヘキシルメタクリレート,ジアルキルアミノアルキ
ルメタクリレート,アルミニウムメタクリレート,アル
ミニウムアクリレート,ジンクメタクリレート,ジンク
アクリレートなどが挙げられる。これらは単独あるいは
二種類以上混合して使用される。また有機過酸化物とし
ては一般的に使用される種々のパーオキサイド化合物が
使用可能である。これ以外に必要に応じ、充填剤,補強
剤,安定剤,軟化剤,顔料等一般的に使用されるゴム配
合薬品を加えても差支えない。
The mixture according to the present invention can be crosslinked even at a low temperature of 80 to 100 ° C., and voids do not occur in the product even if it is heated and crosslinked at normal pressure without using a vent type extruder. When a crosslinking aid such as an allyl compound, oxime compound, sulfur, maleimide compound, etc. is used as the crosslinking aid instead of the methacrylic acid ester or acrylic acid ester, or the methacrylic acid ester or acrylic acid ester is not used in combination with the organic peroxide. 80 to 10 when used alone in the above, or when used alone as a crosslinking agent.
At a low temperature of 0 ° C., almost no crosslinking occurs in a unit of several tens of minutes, and even if the temperature is raised to 150 to 200 ° C., voids are generated in the product at normal pressure. Examples of the methacrylic acid ester or acrylic acid ester in the present invention include trimethylolpropane trimethacrylate, ethylene dimethacrylate, polyethylene glycol dimethacrylate, cyclohexyl methacrylate, dialkylaminoalkyl methacrylate, aluminum methacrylate, aluminum acrylate, zinc methacrylate, zinc acrylate and the like. . These may be used alone or in combination of two or more. As the organic peroxide, various peroxide compounds which are generally used can be used. In addition to the above, generally used rubber compounding chemicals such as a filler, a reinforcing agent, a stabilizer, a softening agent, and a pigment may be added if necessary.

更に本発明の4フッ化エチレン−プロピレン系共重合体
を主成分とし、架橋助剤であるメタクリル酸エステル又
はアクリル酸エステルと、架橋剤である有機過酸化物を
加えた混合物に80〜100℃という低温で架橋させる
ことが可能でかつベント型押出機を用いることなく常圧
で加熱架橋させても製品中にボイドを発生することのな
いシリコーンゴムを、任意の割合で混合しても前記特徴
を失うことなく80〜100℃という低温で架橋させる
ことが可能であり、ベント型押出機を用いることなく常
圧で加熱架橋させても製品中にボイドが発生しない利点
がある。しかしながらシリコーンゴムはある種の油類,
溶剤類に対する抵抗性が不十分であり、4フッ化エチレ
ン−プロピレン系共重合体100重量部に対する混合比
が200重量部を越える場合には耐油性,耐溶剤性の低
下が大きく耐熱耐油を特徴とする押出成形品として実用
的でない。
Further, a mixture containing, as a main component, the tetrafluoroethylene-propylene copolymer of the present invention, a methacrylic acid ester or an acrylic acid ester which is a crosslinking agent, and an organic peroxide which is a crosslinking agent is added at 80 to 100 ° C. The silicone rubber that can be crosslinked at a low temperature and that does not generate voids in the product even if it is heated and crosslinked at normal pressure without using a vent type extruder is mixed at any ratio It is possible to carry out crosslinking at a low temperature of 80 to 100 ° C. without loss of temperature, and there is an advantage that voids do not occur in the product even if it is heated and crosslinked at normal pressure without using a vent type extruder. However, silicone rubber is a type of oil,
Insufficient resistance to solvents, and when the mixing ratio with respect to 100 parts by weight of tetrafluoroethylene-propylene copolymer exceeds 200 parts by weight, oil resistance and solvent resistance are greatly reduced, and heat and oil resistance are characteristic. Is not practical as an extrusion molded product.

シリコーンゴムは通常充填剤等をシリコーンゴム100
重量部に対して30〜100重量部程度を含んだシリコ
ーンゴムコンパウンドとして市販されており、本発明の
混合物はシリコーンゴムコンパウンドを用いて混和した
ものであっても良い。
Silicone rubber is usually filled with a filler such as silicone rubber 100
It is commercially available as a silicone rubber compound containing about 30 to 100 parts by weight with respect to parts by weight, and the mixture of the present invention may be a mixture obtained by using the silicone rubber compound.

本発明の製造方法はシリコーンゴム押出成形品の工程上
の経費が安価な常圧加熱架橋方法と全く同じで本発明の
混合物を押出成形したのち約200℃の加熱炉中にて5
分間程度常圧加熱架橋するものである。押出機のシリン
ダー及びヘッドの温度は絶縁体混合物が80℃で架橋す
ることを考慮し50℃以下にする。
The production method of the present invention is exactly the same as the atmospheric pressure heating crosslinking method, which is inexpensive in terms of the process cost of the silicone rubber extruded product, and the mixture of the present invention is extruded and then heated at about 200 ° C. in a heating furnace.
Crosslinking is carried out by heating under atmospheric pressure for about a minute. The temperature of the cylinder and head of the extruder is set to 50 ° C or lower in consideration of the fact that the insulator mixture is crosslinked at 80 ° C.

(実施例及び比較例) 表−1に示す混合物をチューブ状に0.8mm厚さで内径
2mmに押出成形したのち、200℃の加熱炉中で常圧で
5分間加熱して架橋せしめた。この時、押出機のシリン
ダー及びヘッドは50℃とした。尚、表−1の組成中、
充填剤はケイ酸質充填剤を使用し、軟化剤としてはシリ
コーンオイルを用いた。又ステアリン酸ソーダは滑剤と
して用いた。実施例3,4及び比較例4の4フッ化エチレ
ン−プロピレン系共重合体とシリコーンゴムの混合系で
はシリコーンゴムの架橋剤を混合割合に比例させて添加
した。
(Examples and Comparative Examples) The mixture shown in Table 1 was extruded into a tube shape having a thickness of 0.8 mm and an inner diameter of 2 mm, and then heated in a heating furnace at 200 ° C for 5 minutes at normal pressure to crosslink. At this time, the cylinder and head of the extruder were set at 50 ° C. Incidentally, in the composition of Table-1,
A siliceous filler was used as the filler, and silicone oil was used as the softening agent. Sodium stearate was used as a lubricant. In the mixed system of the tetrafluoroethylene-propylene copolymers of Examples 3 and 4 and Comparative Example 4 and the silicone rubber, the crosslinking agent of the silicone rubber was added in proportion to the mixing ratio.

実施例1〜4及び比較例1〜4の試験結果を表−2に示
す。
Table 2 shows the test results of Examples 1 to 4 and Comparative Examples 1 to 4.

(発明の効果) これらの試験結果に示すように実施例1〜4は、工程上
の経費が安価な常圧加熱架橋をしても試験品中にボイド
が発生しない。これに対し比較例1〜3のようにメタク
リル酸エステル又はアクリル酸エステルの代りに他の架
橋助剤を使用した場合は、常圧加熱架橋では試験品中に
無数のボイドが発生して製品として使用できない。更に
実施例3及び4のように常圧加熱架橋可能なシリコーン
ゴムとの混合も4フッ化エチレン−プロピレン系共重合
体100重量部に対し200重量部までは耐油性の大き
な低下はなく実用上問題はない。これに対し、比較例4
のようにシリコーンゴムが多すぎる場合は4フッ化エチ
レン−プロピレン系共重合体の特徴である耐油性が失わ
れてしまう。
(Effects of the Invention) As shown in these test results, in Examples 1 to 4, voids do not occur in the test product even when the crosslinking under atmospheric pressure is carried out at low process cost. On the other hand, when other cross-linking aids were used instead of the methacrylic acid ester or the acrylic acid ester as in Comparative Examples 1 to 3, in the atmospheric pressure heating cross-linking, innumerable voids were generated in the test product to give a product. I can not use it. Further, as in Examples 3 and 4, mixing with a silicone rubber that can be crosslinked by heating under normal pressure does not cause a significant decrease in oil resistance up to 200 parts by weight with respect to 100 parts by weight of the tetrafluoroethylene-propylene copolymer, and is practically used. No problem. On the other hand, Comparative Example 4
When the amount of silicone rubber is too large as described above, the oil resistance, which is a characteristic of the tetrafluoroethylene-propylene copolymer, is lost.

以上のように、本発明は耐熱性,耐油性に優れ、かつ、
安価に製造することができる押出成形品であり、また4
フッ化エチレン−プロピレン系共重合体より安価なシリ
コーンゴムを混合することにより、更に安価で経済的な
押出成形品となる。
As described above, the present invention has excellent heat resistance and oil resistance, and
It is an extruded product that can be manufactured at low cost.
By mixing a silicone rubber, which is cheaper than a fluorinated ethylene-propylene-based copolymer, a cheaper and more economical extruded product can be obtained.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 // B29K 27:12 4F 83:00 4F ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Office reference number FI technical display location // B29K 27:12 4F 83:00 4F

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】4フッ化エチレン−プロピレン系共重合体
を主成分とする組成物に、架橋助剤であるメタクリル酸
エステル又はアクリル酸エステルと、架橋剤である有機
過酸化物を加えた混合物から成り加熱架橋された押出成
形品。
1. A mixture obtained by adding a methacrylic acid ester or acrylic acid ester, which is a crosslinking aid, and an organic peroxide, which is a crosslinking agent, to a composition containing a tetrafluoroethylene-propylene-based copolymer as a main component. An extruded product consisting of a heat-crosslinked product.
【請求項2】4フッ化エチレン−プロピレン系共重合体
を主成分とする組成物に、架橋助剤であるメタクリル酸
エステル又はアクリル酸エステルと、架橋剤である有機
過酸化物とを混合し、これにシリコーンゴムを4フッ化
エチレン−プロピレン系共重合体100重量部に対して
200重量部以下加えた混合物から成り加熱架橋された
押出成形品
2. A composition containing a tetrafluoroethylene-propylene-based copolymer as a main component, and a mixture of a methacrylic acid ester or an acrylic acid ester which is a cross-linking aid and an organic peroxide which is a cross-linking agent. An extruded article obtained by heat-crosslinking, which comprises a mixture of 200 parts by weight or less of silicone rubber added to 100 parts by weight of a tetrafluoroethylene-propylene copolymer.
JP61034452A 1986-02-18 1986-02-18 Extruded product Expired - Lifetime JPH0627234B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP61034452A JPH0627234B2 (en) 1986-02-18 1986-02-18 Extruded product
US07/220,351 US4904529A (en) 1986-02-18 1988-07-15 Heat and oil resistant insulating composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61034452A JPH0627234B2 (en) 1986-02-18 1986-02-18 Extruded product

Publications (2)

Publication Number Publication Date
JPS62192437A JPS62192437A (en) 1987-08-24
JPH0627234B2 true JPH0627234B2 (en) 1994-04-13

Family

ID=12414638

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61034452A Expired - Lifetime JPH0627234B2 (en) 1986-02-18 1986-02-18 Extruded product

Country Status (1)

Country Link
JP (1) JPH0627234B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5342351B2 (en) 2008-07-10 2013-11-13 ザ・スウォッチ・グループ・リサーチ・アンド・ディベロップメント・リミテッド Method for manufacturing micromechanical parts

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5342351B2 (en) 2008-07-10 2013-11-13 ザ・スウォッチ・グループ・リサーチ・アンド・ディベロップメント・リミテッド Method for manufacturing micromechanical parts

Also Published As

Publication number Publication date
JPS62192437A (en) 1987-08-24

Similar Documents

Publication Publication Date Title
US3936572A (en) Electric cable insulated with a corona resistant polyethylene composition containing a silicon additive
JPS6234055B2 (en)
JP2003510394A (en) Extrudable thermoplastic materials and fiber micromodules made from such materials
JPH0627234B2 (en) Extruded product
JP2782880B2 (en) Fluororesin composition
US4904529A (en) Heat and oil resistant insulating composition
JPH0931285A (en) Heat shrinkable tube and composition thereof
JP3175355B2 (en) Heat-shrinkable tube made of resin composition
JP2539737B2 (en) Cord-shaped heater
JP2602722B2 (en) Heat resistant resin composition
JPH08259704A (en) Cross-linked tube and heat shrink tube
JP2852524B2 (en) Fluorine-containing elastomer composition
JPS62193085A (en) Cord heater
JPH09176425A (en) Fluororesin composition
JP2650996B2 (en) Heat shrinkable articles
JP2817320B2 (en) Method for producing crosslinked polyolefin material
JPS58183710A (en) Non-rigid plastic resin for covering electric wire
JPH0627148B2 (en) Crosslinked ethylene copolymer for electrical insulation
JP2555693B2 (en) Method for manufacturing heat-shrinkable tube
JPH07205285A (en) Heat shrinkable tube and manufacturing method thereof
JPH07335027A (en) Fluorine-containing elastomer coated electric wire / cable and manufacturing method thereof
JP2947599B2 (en) Heat shrink tubing
JP3516270B2 (en) Tubed wire and method of manufacturing the same
JP3321990B2 (en) Extruded fluororesin
JPH0627149B2 (en) Crosslinked ethylene copolymer for electrical insulation