JPH02272031A - Method for producing polyolefin crosslinked molded product - Google Patents
Method for producing polyolefin crosslinked molded productInfo
- Publication number
- JPH02272031A JPH02272031A JP9425989A JP9425989A JPH02272031A JP H02272031 A JPH02272031 A JP H02272031A JP 9425989 A JP9425989 A JP 9425989A JP 9425989 A JP9425989 A JP 9425989A JP H02272031 A JPH02272031 A JP H02272031A
- Authority
- JP
- Japan
- Prior art keywords
- polyolefin
- contact
- molded
- silane
- brought
- 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
Links
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野〕
本発明はポリオレフィン架橋成形体の製造方法に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a crosslinked polyolefin molded article.
[従来の技術]
従来から提案されているシラングラフト水架橋法による
ポリオレフィン架橋成形体の製造方法としては、ポリオ
レフィンとシラン化合物とラジカル発生剤との混合物を
加熱反応させて得たシラングラフトポリオレフィンベレ
ットを、シラノール縮合触媒を含む触媒マスターバッチ
と混合して成形加工し、水分と接触させて加温し架橋さ
せる方法が一般的に行われている。[Prior Art] As a conventionally proposed method for producing a polyolefin crosslinked molded article by the silane graft water crosslinking method, a silane grafted polyolefin pellet obtained by subjecting a mixture of a polyolefin, a silane compound, and a radical generator to a heating reaction is used. A commonly used method is to mix it with a catalyst masterbatch containing a silanol condensation catalyst, mold it, bring it into contact with water, heat it, and crosslink it.
[発明が解決しようとする課題]
しかしながら、従来技術においては架橋の度合を表すゲ
ル分率を50%以上に設定すると、シラン変成ポリオレ
フィンのメルトインデックスか原料ポリオレフィンのメ
ルトインデックスの50%前後に低下してしまい、成形
加工時の流動性の低下をもたらすという欠点があった。[Problems to be Solved by the Invention] However, in the prior art, when the gel fraction, which represents the degree of crosslinking, is set to 50% or more, the melt index of the silane-modified polyolefin decreases to around 50% of the melt index of the raw polyolefin. This has the disadvantage of causing a decrease in fluidity during molding.
本発明の目的は、前記した従来技術の欠点を解消し、成
形加工時の流動性を改善したポリオレフィン架橋成形体
の製造方法を提供することにある。An object of the present invention is to provide a method for producing a crosslinked polyolefin molded article that eliminates the drawbacks of the prior art described above and improves fluidity during molding.
[課題を解決するための手段及び作用]本発明の要旨は
、原料ポリオレフィンとして、シラングラフト後のメル
トインデックスの低下がきわめて少ない特定のポリオレ
フィンを用いたことにあり、それによって成形加工時の
流動加工性の低下を抑制したものである。[Means and effects for solving the problem] The gist of the present invention lies in the use of a specific polyolefin that exhibits an extremely small decrease in melt index after silane grafting as a raw material polyolefin, thereby making it possible to reduce flow processing during molding. This suppresses the decline in sexual performance.
本発明において、シラングラフト後のメルトインデック
スの低下がきわめて少ないポリオレフィンとしては、エ
チレン−メチルアクリレートコポリマー、エチレン−エ
チルアクリレートコポリマー (EEA) 、エチレン
−プロピルアクリレートコポリマー、エチレン−ブチル
アクリレートコポリマーなどのエチレン−アクリル酸エ
ルテル共重合体が挙げられる。In the present invention, polyolefins with extremely small decrease in melt index after silane grafting include ethylene-acrylic polyolefins such as ethylene-methyl acrylate copolymer, ethylene-ethyl acrylate copolymer (EEA), ethylene-propyl acrylate copolymer, and ethylene-butyl acrylate copolymer. Examples include acid ertel copolymers.
かかるポリオレフィンを使用することにより、架橋後の
ゲル分率を50%以上に設定した場合でも、シラン変性
後のポリマのメルトインデックスが初期のポリマのメル
トインデックスに対して80%以上の値を有するように
なり、成形加工時の流動性の低下を防止できるようにな
る。By using such a polyolefin, even when the gel fraction after crosslinking is set to 50% or more, the melt index of the silane-modified polymer is 80% or more of the melt index of the initial polymer. This makes it possible to prevent a decrease in fluidity during molding.
なお、シラン化合物としてはビニルトリメトキシシラン
、ビニルトリエトキシシランなどが、ラジカル発生剤と
してはジクミルパーオキサイド、過酸化ベンゾイル、過
酸化ジクロベンゾイルなどが、シラノール縮合触媒とし
てはジブチル錫ジラウレート、ジブチル錫ジアセテート
などがそれぞれ挙げられる。The silane compounds include vinyltrimethoxysilane and vinyltriethoxysilane, the radical generators include dicumyl peroxide, benzoyl peroxide, and dichlorobenzoyl peroxide, and the silanol condensation catalysts include dibutyltin dilaurate and dibutyltin. Examples include diacetate and the like.
本発明においては、必要に応じて異種のポリマー、酸化
防止剤、安定剤、難燃助剤、充てん剤、着色剤、耐候性
付与剤、熱または電気伝導性付与剤などを添加しても差
支えない。In the present invention, different polymers, antioxidants, stabilizers, flame retardant aids, fillers, colorants, weather resistance agents, thermal or electrical conductivity agents, etc. may be added as necessary. do not have.
本発明においては難燃性を付与するため、多量の難燃剤
を添加する場合もある。難燃剤としては、ハロゲン系難
燃剤、リン系難燃剤、水酸化アルミニウムや水酸化マグ
ネシウムなどの無機系難燃剤などのように添加型難燃剤
が望ましいが、これらに限定される訳ではない。In the present invention, a large amount of flame retardant may be added in order to impart flame retardancy. The flame retardant is preferably an additive flame retardant such as a halogen flame retardant, a phosphorus flame retardant, or an inorganic flame retardant such as aluminum hydroxide or magnesium hydroxide, but is not limited to these.
[実施例]
メルトインデックスが3.5.1.2.0.7(8g/
10分)の3種のエチレン−エチルアクリレートコポリ
マーのベレット100重量部にビニルトリメトキシシラ
ン1.5重量部、ジクミルパーオキサイド0.15重量
部、チオジエチレンビス(3,5−ジー第3ブチル−4
ヒドロキシ)ヒドロシンナメート0.1重量部を混合後
、40m / rn単軸スクリュー押出機のホッパーに
投入し、スクIJ、一回転数’15r、p、m、1設定
温度CI : 150℃、C2:200℃、C3:22
0℃、ヘッド=220℃の条件下で加熱反応させながら
造粒してシラン変性ポリエチレンベレットを製造した。[Example] Melt index is 3.5.1.2.0.7 (8g/
To 100 parts by weight of pellets of three types of ethylene-ethyl acrylate copolymers (10 minutes), 1.5 parts by weight of vinyltrimethoxysilane, 0.15 parts by weight of dicumyl peroxide, thiodiethylene bis(3,5-di-tert-butyl -4
After mixing 0.1 part by weight of hydroxy) hydrocinnamate, it was put into the hopper of a 40 m/rn single screw extruder, screw IJ, number of revolutions '15 r, p, m, 1 set temperature CI: 150 ° C, C2 :200℃, C3:22
Silane-modified polyethylene pellets were produced by granulating the mixture under the conditions of 0° C. and head = 220° C. while performing a heating reaction.
このペレットについて、直ちにメルトフローレートを測
定したところ、それぞれ原料EEAのメルトインデック
スとほとんど変わっていないことを確認した。When the melt flow rate of these pellets was immediately measured, it was confirmed that the melt index was almost the same as that of the raw material EEA.
次に、このペレットを水とジブチル錫ジラウレートのエ
マルジョン(温度80℃)中に16時間浸漬して絶縁体
を架橋させた。Next, the pellets were immersed in an emulsion of water and dibutyltin dilaurate (temperature: 80° C.) for 16 hours to crosslink the insulator.
こうして得られた架橋体のゲル分率の評価結果は表の下
欄に示す通りであり、60%以上の値を有していた。The evaluation results of the gel fraction of the crosslinked product thus obtained are as shown in the lower column of the table, and it had a value of 60% or more.
なおゲル分率は、110℃キシレン中で24時間抽出し
た後、十分乾燥させてからn1定した。The gel fraction was determined by n1 after extraction in xylene at 110° C. for 24 hours and thorough drying.
次に比較のため、ベースポリマーとして通常の低密度ポ
リエチレン(LDPE)を用いたところ、シラングラフ
ト後のメルトインデックスが原料LDPEのメルトイン
デックスの50〜60%とかなり低下した。Next, for comparison, when ordinary low density polyethylene (LDPE) was used as the base polymer, the melt index after silane grafting was considerably reduced to 50 to 60% of the melt index of the raw material LDPE.
〔発明の効果]
以上説明したように本発明によれば、ゲル分率を50%
以上に設定してもシラングラフト後のメルトインデック
スの低下がほとんどないので、シラン変性ポリオレフィ
ンの成形加工時の流動加工性を改善でき、すぐれた架橋
成形体を得ることができる。[Effect of the invention] As explained above, according to the present invention, the gel fraction can be reduced to 50%.
Even if it is set above, there is almost no decrease in the melt index after silane grafting, so the flow processability during molding of the silane-modified polyolefin can be improved, and an excellent crosslinked molded product can be obtained.
Claims (1)
の混合物を加熱反応させて得られるシラン変性ポリオレ
フィンをシロキサン縮合触媒と接触させて成形加工した
のち、水分と接触させて加温し架橋させるポリオレフィ
ン架橋成形体の製造方法において、前記ポリオレフィン
として、エチレン−アクリル酸エステル共重合体を用い
ることを特徴とするポリオレフィン架橋成形体の製造方
法。1. A polyolefin crosslinked molded product in which a silane-modified polyolefin obtained by heating a mixture of a polyolefin, a silane compound, and a radical generator is brought into contact with a siloxane condensation catalyst, molded and processed, and then brought into contact with water to be heated and crosslinked. A method for producing a crosslinked polyolefin molded article, characterized in that an ethylene-acrylic acid ester copolymer is used as the polyolefin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9425989A JPH02272031A (en) | 1989-04-13 | 1989-04-13 | Method for producing polyolefin crosslinked molded product |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9425989A JPH02272031A (en) | 1989-04-13 | 1989-04-13 | Method for producing polyolefin crosslinked molded product |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02272031A true JPH02272031A (en) | 1990-11-06 |
Family
ID=14105289
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9425989A Pending JPH02272031A (en) | 1989-04-13 | 1989-04-13 | Method for producing polyolefin crosslinked molded product |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02272031A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011057928A1 (en) * | 2009-11-11 | 2011-05-19 | Borealis Ag | Crosslinkable polymer composition and cable with advantageous electrical properties |
US9365708B2 (en) | 2009-11-11 | 2016-06-14 | Borealis Ag | Cable and production process thereof |
US9587043B2 (en) | 2009-11-11 | 2017-03-07 | Borealis Ag | Polymer composition and a power cable comprising the polymer composition |
US9595374B2 (en) | 2010-11-03 | 2017-03-14 | Borealis Ag | Polymer composition and a power cable comprising the polymer composition |
US10246527B2 (en) | 2009-11-11 | 2019-04-02 | Borealis Ag | Polymer composition comprising a polyolefin produced in a high pressure process, a high pressure process and an article |
-
1989
- 1989-04-13 JP JP9425989A patent/JPH02272031A/en active Pending
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10875939B2 (en) | 2009-11-11 | 2020-12-29 | Borealis Ag | Polymer composition comprising a polyolefin produced in a high pressure process, a high pressure process and an article |
US11390699B2 (en) | 2009-11-11 | 2022-07-19 | Borealis Ag | Crosslinkable polymer composition and cable with advantageous electrical properties |
EA022361B1 (en) * | 2009-11-11 | 2015-12-30 | Бореалис Аг | Crosslinkable polymer composition, cable with advantageous electrical properties and process for producing the same |
US9365708B2 (en) | 2009-11-11 | 2016-06-14 | Borealis Ag | Cable and production process thereof |
US9587043B2 (en) | 2009-11-11 | 2017-03-07 | Borealis Ag | Polymer composition and a power cable comprising the polymer composition |
US11756700B2 (en) | 2009-11-11 | 2023-09-12 | Borealis Ag | Polymer composition and a power cable comprising the polymer composition |
US10453585B2 (en) | 2009-11-11 | 2019-10-22 | Borealis Ag | Polymer composition and a power cable comprising the polymer composition |
US10246527B2 (en) | 2009-11-11 | 2019-04-02 | Borealis Ag | Polymer composition comprising a polyolefin produced in a high pressure process, a high pressure process and an article |
CN102666602A (en) * | 2009-11-11 | 2012-09-12 | 博瑞立斯有限公司 | Crosslinkable polymer composition and cable with advantageous electrical properties |
WO2011057928A1 (en) * | 2009-11-11 | 2011-05-19 | Borealis Ag | Crosslinkable polymer composition and cable with advantageous electrical properties |
US11078312B2 (en) | 2009-11-11 | 2021-08-03 | Borealis Ag | Crosslinkable polymer composition and cable with advantageous electrical properties |
US10950366B2 (en) | 2010-11-03 | 2021-03-16 | Borealis Ag | Polymer composition and a power cable comprising the polymer composition |
US10032543B2 (en) | 2010-11-03 | 2018-07-24 | Borealis Ag | Polymer composition and a power cable comprising the polymer composition |
US9595374B2 (en) | 2010-11-03 | 2017-03-14 | Borealis Ag | Polymer composition and a power cable comprising the polymer composition |
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