JPS6111223A - Manufacture of silane-bridged organic polymer film - Google Patents

Manufacture of silane-bridged organic polymer film

Info

Publication number
JPS6111223A
JPS6111223A JP59132717A JP13271784A JPS6111223A JP S6111223 A JPS6111223 A JP S6111223A JP 59132717 A JP59132717 A JP 59132717A JP 13271784 A JP13271784 A JP 13271784A JP S6111223 A JPS6111223 A JP S6111223A
Authority
JP
Japan
Prior art keywords
organic polymer
film
tube
condensation catalyst
silanol condensation
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
JP59132717A
Other languages
Japanese (ja)
Inventor
Shiro Kodama
児玉 四郎
Shigeki Sano
茂樹 佐野
Ichiro Nishikawa
一郎 西川
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.)
SWCC Corp
Original Assignee
Showa Electric Wire and Cable Co
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 Showa Electric Wire and Cable Co filed Critical Showa Electric Wire and Cable Co
Priority to JP59132717A priority Critical patent/JPS6111223A/en
Publication of JPS6111223A publication Critical patent/JPS6111223A/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
    • B29C48/03Extrusion 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
    • 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
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0018Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
    • 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
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0019Combinations of extrusion moulding with other shaping operations combined with shaping by flattening, folding or bending
    • 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
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To prevent the occurrence of blisters and burned spots on the surface of a film by sending an atomized silanol condensation catalyst with an expanding air into a tube. CONSTITUTION:An organic polymer after the ending of grafting reactions is extruded through a die 4 attached to the head 3 of an extruder 1 into a thin tubular form. During the period, expanding air containing atomized liquid with dispersed or dissolved a silanol condensation catalyst is sent into the tube 6 and the tube 6 is continuously wound around a roll through a pinch roller 5 while being expanded into a given size. The film 8 so obtained is allowed to stand in the air and becomes a sufficiently bridged state. As the silanol catalyst, carboxylic acid salts such as dibutyl-tin di-laurate, cobalt naphthalate, etc., organic bases such as ethylamine, hexylamine, etc., and acids such as inorganic acids, and fatty acids, etc., may be cited. About 0.01-0.5pts.wt. silanol condensation catalyst is preferably used on the basis of 100pts.wt. organic polymer.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はシラン架橋有機重合体フィルムの製造方法に関
する (従来の技術) 従来、シラン架橋有機重合体フィルムは、例えば有機過
酸化物架橋剤により架橋したフィルムのように架橋剤に
よるフィルムの特性低下が少ないこと、又架橋コントロ
ール上の困難性が少ないこと、更に他の電子線照射のよ
うな高価な設備が不要であるなどめ理由により特に近年
注目されているものである。かかるシラン架橋有機重合
体フィルムの製造方法としては、加水分解し得る有機基
をもつ不飽和シランと遊離ラジカル発生剤および有機重
合体ベースの混合物を押出成型し、ペレット化したもの
をグラフトポリマーとし、更に有機重合体に高濃度にシ
ラノール縮合触媒を混合したものを押出成型し、ペレッ
ト化したものを触媒マスターバッチとしてこれをはぼ9
:1の割合に混合したものをインフレーション法により
押出機で押出成型するが、この際ベレットやエアー中の
微量の水分のために押出機中で若干の架橋が促進されフ
ィルムの外観に焼け、プツ等を生じ問題となっていた。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for producing a silane-crosslinked organic polymer film (Prior Art) Conventionally, a silane-crosslinked organic polymer film has been manufactured by using, for example, an organic peroxide crosslinking agent. It has become particularly popular in recent years due to the fact that unlike crosslinked films, there is less deterioration in film properties due to crosslinking agents, there are fewer difficulties in controlling crosslinking, and there is no need for other expensive equipment such as electron beam irradiation. This is something that is attracting attention. A method for producing such a silane-crosslinked organic polymer film includes extrusion molding a mixture of an unsaturated silane having a hydrolyzable organic group, a free radical generator, and an organic polymer base, and forming pellets into graft polymers. Furthermore, a mixture of an organic polymer and a silanol condensation catalyst at a high concentration is extruded and pelletized, which is then used as a catalyst masterbatch.
A mixture of 1:1 and 1:1 is extruded using an extruder using the inflation method, but at this time, slight crosslinking is promoted in the extruder due to a small amount of moisture in the pellets and air, causing the film to burn and become sticky. etc., which caused problems.

さらにフィルムの架橋はインフレーション法による押出
成型徒刑行程で行なわれるが、大気に放置した場合は、
ロールの内側の層が未架橋状態、になりやすく、又加湿
状態にした場合には、一工程増え煩雑になるという欠点
を有していた。
Furthermore, crosslinking of the film is carried out through an extrusion molding process using the inflation method, but when left in the atmosphere,
The inner layer of the roll tends to be in an uncrosslinked state, and when it is kept in a humidified state, it has the drawback that one step is added and the process becomes complicated.

(問題点を解決するための手段) 本発明の架橋ポリオレ・フィンの製造方法は加水分解し
得る有機基をもつ不飽和シラン、遊離ラジカル発生剤お
よび有機重合体ベースの混合物を、・押出機に供給し、
前記押出機内で前記不飽和シランを有機重合体へグラフ
ト化させた後、これを薄肉チューブ状に押し出しながら
、前記チューブ内にシラノール縮合触媒を含む空気を送
り込み所定サイズまで、ふくらませつつ連続的にフィル
ムを巻き取ることを特徴としている。
(Means for Solving the Problems) The method for producing crosslinked polyolefins of the present invention involves introducing a mixture based on an unsaturated silane having a hydrolyzable organic group, a free radical generator, and an organic polymer into an extruder. supply,
After grafting the unsaturated silane to the organic polymer in the extruder, while extruding this into a thin tube, air containing a silanol condensation catalyst is fed into the tube to continuously inflate and form a film to a predetermined size. It is characterized by winding up.

本発明に使用される有機重合体としては、ポリエチレン
、ポリプロピレン、エチレン−アクリル酸エチル共重合
体エチレン酢酸ビニル共重合体、エチレン−プルピレン
共重合体、ポリ塩化ビニル、ポリスチレンポリメタクリ
レート、ポリアミド等がある。
Organic polymers used in the present invention include polyethylene, polypropylene, ethylene-ethyl acrylate copolymer, ethylene-vinyl acetate copolymer, ethylene-propylene copolymer, polyvinyl chloride, polystyrene polymethacrylate, polyamide, etc. .

また、本発明に使用する不飽和シランとしては、ビニル
トリメトキシシラン(VTMO8)、ビニルトリエトキ
シシラン等のアルコキシル基を有するものの他、”アセ
トキシ基、プpビオノキシ基等を含むシリル構造の化合
物等があげられる。
In addition, the unsaturated silanes used in the present invention include those having an alkoxyl group such as vinyltrimethoxysilane (VTMO8) and vinyltriethoxysilane, as well as compounds with a silyl structure containing an acetoxy group, a p-bionoxy group, etc. can be given.

更に、遊離ラジカル発生剤としては、ジクミルパーオキ
サイド(DOP)、ベンゾイルパーオキサイド等の有機
過酸化物、アゾビスイソブチo=トリル、メチルアゾジ
イソ、ブチレート等のアゾ化合物等があげられる。
Furthermore, examples of the free radical generator include organic peroxides such as dicumyl peroxide (DOP) and benzoyl peroxide, and azo compounds such as azobisisobutio=tolyl, methyl azodiiso and butyrate.

更にまた、本発明に使用されるシラノール縮合触媒とし
ては、ジプチル錫ジラウレート(DBTDL)、オクタ
ン酸第−錫、ナフテン酸コバルト等のカルボン醗塩、エ
チルアミン、ジブチルアミン、ヘキシルアミン等の有機
塩基、無機酸および脂肪醸等の酸があげられる。
Further, as the silanol condensation catalyst used in the present invention, carbon salts such as diptyltin dilaurate (DBTDL), stannous octoate, and cobalt naphthenate, organic bases such as ethylamine, dibutylamine, and hexylamine, and inorganic Examples include acids and fatty acids.

以上の添加物の配合量は、有機重合体100重量部あた
り、加水分解し得る不飽和シラン0.1〜5.0重量部
遊離ラジカル発生剤0.01〜1.0重量部、シラノー
ル縮合触媒0.01〜0,5重量部程度が好適している
The amounts of the above additives are 0.1 to 5.0 parts by weight of hydrolyzable unsaturated silane, 0.01 to 1.0 parts by weight of free radical generator, and silanol condensation catalyst per 100 parts by weight of organic polymer. Approximately 0.01 to 0.5 parts by weight is suitable.

本発明方法を実施するにあたっては、図に示すように先
ずシリル変性すべき有機重合体に加水分解し得る不飽和
シラン、遊離ラジカル発生剤ならびに充填剤をその他の
添加物と共に、押出機1のホッパー2に供給して押出機
内を進行せしめることによりグラフト化反応をヘッド3
部までに終了させる。グラフト化反応の終了した有機重
合体は、ヘッド3に装着されたダイス4から薄肉チュー
ブ状に押し出されながら、チューブ6内にシラノール縮
合触媒を分散あるいは溶解させた霧状液体を含む膨張用
エアー1を送りこんで所定の大きさまテチューフヲフく
らませつつピンチローラ5を介して連続的にロールに巻
き取られる。得られたフィルム8は空気中に放置するこ
とにより、充分な架橋状態となる。
In carrying out the method of the present invention, first, an unsaturated silane that can be hydrolyzed into an organic polymer to be silyl-modified, a free radical generator, and a filler are added to the hopper of an extruder 1 along with other additives, as shown in the figure. The grafting reaction is carried out in the extruder by supplying it to head 3 and allowing it to proceed inside the extruder.
Finish by the end of the session. The organic polymer that has undergone the grafting reaction is extruded from a die 4 attached to a head 3 into a thin-walled tube, and is filled with an expanding air 1 containing a mist of liquid in which a silanol condensation catalyst is dispersed or dissolved. The paper is fed into the paper and is continuously wound up into a roll via the pinch roller 5 while being dilated to a predetermined size. The obtained film 8 becomes sufficiently crosslinked by being left in the air.

(実施例) 、次に実施例について記載する。(Example) , Next, examples will be described.

実施例 比重0.92、メルトインデックス3.5のボリエf 
し> 100重量部に、V’l’MO82,5重量部、
DOPo、01重量部〆添加した混合物を押出機に供給
し1厚さ50μmとなるようにイン、フレーク1ン法に
よりチューブ状に押し出しVTMO8に溶解したDB’
FDLを霧状にしたものを膨張用エアーといっしょにチ
ューブ内に送りこん゛で幅2゜備のフィルムをロールに
巻き取った。
Example Bolier f with specific gravity 0.92 and melt index 3.5
> 100 parts by weight, V'l'MO82.5 parts by weight,
The mixture containing 01 parts by weight of DOPo was fed into an extruder and extruded into a tube shape using the in-flake method to a thickness of 50 μm, followed by DB' dissolved in VTMO8.
FDL was atomized and fed into a tube together with inflation air, and a film with a width of 2° was wound onto a roll.

フブルムを巻いたロールを48時間常温に放置してフィ
ルムを架橋させた。
The roll wrapped with Fublum was left at room temperature for 48 hours to crosslink the film.

このようにして得られたフィルムのゲル分率は68%で
かつ、フィルムの表面は平滑であった。
The gel fraction of the film thus obtained was 68%, and the surface of the film was smooth.

一方、前記配合で押出機のホッパ一部でDBTDLを添
加してインフレーション法にてフィルムを製造した場合
には、押出中にフィルムの表面にプツ、焼けが生じ、ま
た押出されたフィルムのゲル分率は68%であった。
On the other hand, when a film is manufactured using the inflation method by adding DBTDL in a part of the hopper of an extruder with the above formulation, the surface of the film will be scorched and burnt during extrusion, and the gel content of the extruded film will be reduced. The rate was 68%.

(発明の効果) この発明は以上の実施例の効果から明らかなように、フ
ィルムを製造する際に、霧状にしたシラノール縮合触媒
をチューブ内に膨張エアーと共に送りこむことにより、
へィルへ表面のプッ、焼けの発生を防止させ得たもので
あり、その工業的価値は非常に大きい。
(Effects of the Invention) As is clear from the effects of the above embodiments, the present invention is capable of producing a film by feeding atomized silanol condensation catalyst into a tube together with expanded air.
It was able to prevent the occurrence of surface plucking and burning on the surface of the hair, and its industrial value is extremely large.

【図面の簡単な説明】[Brief explanation of the drawing]

図は本発明のシラン架橋有機重合体フィルムの製造方法
の一実施例を示した図である。 6−−−−−−−−チユーブ ?  −−−−−−−−シラノール縮合触媒を含む空気
8 −−−−−−−−フイルム
The figure shows an example of the method for producing a silane crosslinked organic polymer film of the present invention. 6------------Tube? ----------Air containing silanol condensation catalyst 8 ----------Film

Claims (1)

【特許請求の範囲】[Claims] 1、加水分解し得る有機基をもつ不飽和シラン、遊離ラ
ジカル発生剤および有機重合体ベースの混合物を、押出
機に供給し、前記押出機内で前記不飽和シランを有機重
合体へグラフト化させた後、これを薄肉チューブ状に押
し出しながら、前記チューブ内にシラノール縮合触媒を
含む空気を送り込み所定サイズにまでふくらませつつ連
続的にフィルムを巻き取ることを特徴とするシラン架橋
有機重合体フィルムの製造方法。
1. A mixture based on an unsaturated silane with hydrolysable organic groups, a free radical generator and an organic polymer was fed into an extruder, in which the unsaturated silane was grafted onto the organic polymer. Thereafter, while extruding the film into a thin-walled tube, air containing a silanol condensation catalyst is fed into the tube to inflate it to a predetermined size, and the film is continuously wound up. .
JP59132717A 1984-06-27 1984-06-27 Manufacture of silane-bridged organic polymer film Pending JPS6111223A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59132717A JPS6111223A (en) 1984-06-27 1984-06-27 Manufacture of silane-bridged organic polymer film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59132717A JPS6111223A (en) 1984-06-27 1984-06-27 Manufacture of silane-bridged organic polymer film

Publications (1)

Publication Number Publication Date
JPS6111223A true JPS6111223A (en) 1986-01-18

Family

ID=15087928

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59132717A Pending JPS6111223A (en) 1984-06-27 1984-06-27 Manufacture of silane-bridged organic polymer film

Country Status (1)

Country Link
JP (1) JPS6111223A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017081093A (en) * 2015-10-30 2017-05-18 大日本印刷株式会社 Composite preform, composite container, plastic member and manufacturing method of plastic member

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017081093A (en) * 2015-10-30 2017-05-18 大日本印刷株式会社 Composite preform, composite container, plastic member and manufacturing method of plastic member

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