JPS581924A - Method of producing crosslinked polyolefin wire - Google Patents
Method of producing crosslinked polyolefin wireInfo
- Publication number
- JPS581924A JPS581924A JP57104532A JP10453282A JPS581924A JP S581924 A JPS581924 A JP S581924A JP 57104532 A JP57104532 A JP 57104532A JP 10453282 A JP10453282 A JP 10453282A JP S581924 A JPS581924 A JP S581924A
- Authority
- JP
- Japan
- Prior art keywords
- polyolefin
- wire
- silane
- extruder
- stirrer
- 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
Links
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
- Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Processes Specially Adapted For Manufacturing Cables (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明はシラングラフト架橋ポリオレフィン電線の製造
方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a silane-grafted crosslinked polyolefin electric wire.
シラングラノド架橋ポリAレフイン電線の製造において
は、ポリオレフィンのベースレジンにシラン化合物や架
橋剤を添加して得たシラングラフト化ポリオレフィンと
、ポリオレフィンのベースレジンにシラノール綜合触媒
を添加して得た触媒マスターバッチとをブレンドするフ
ンバウンド工程と、これによって得たフンバウンドを押
出機に投入し、混練押出する押出工程からなる2段階方
式の製造方法が一般に採用されている。In the production of silane granod crosslinked polyA reflex wires, we use a silane grafted polyolefin obtained by adding a silane compound and a crosslinking agent to a polyolefin base resin, and a catalyst masterbatch obtained by adding a silanol integrated catalyst to a polyolefin base resin. Generally, a two-step manufacturing method is adopted, which consists of a dung bound step in which the dung bound material is blended with the dung bound material, and an extrusion step in which the dung bound obtained by this process is fed into an extruder and kneaded and extruded.
この従来の方法ではシラングラフト化ポリオレノインと
触媒マスターバッチとはそれぞれ別々に製造および保管
し、またこれらをブレンドするフンバウンド工程および
このコンパウンドの保管スペースが必要なことから次の
ような問題がふる。In this conventional method, the silane-grafted polyolenoin and the catalyst masterbatch are manufactured and stored separately, and a bounding process for blending them and storage space for this compound are required, resulting in the following problems.
0 加工費が高くなる。0 Processing costs will increase.
■ 保!!時に吸湿する可能性があり、部分架橋が開始
する。(保管時間が得られる。■ Keep! ! Sometimes moisture can be absorbed and partial crosslinking begins. (Storage time is obtained.
■ 保管スペースが必要。■ Requires storage space.
■ シランが揮発し、架橋度のむらを生ずる。■ Silane volatilizes, causing unevenness in the degree of crosslinking.
■ グラフト化ポリオレフィン及び触媒マスターバッチ
共にコンパウンド0スが発生する。■ Compound zero is generated for both the grafted polyolefin and the catalyst masterbatch.
■ 貢物混入の確率が高い。■ High probability of contamination with tribute.
■ シランの吸入、飛散の可能性があり、安全衛生状良
くない。■ There is a possibility of inhalation and scattering of silane, so the health and safety conditions are not good.
本発明は上記した従来技術の問題点を一蝉し得る架橋ポ
リオレフィン電線の製造方法を提供づるものである。The present invention provides a method for producing a crosslinked polyolefin electric wire that overcomes the problems of the prior art described above.
第1図および第2図を参照しC本発明の一実施例を説明
する。An embodiment of the present invention will be described with reference to FIGS. 1 and 2.
送出幾1、押出機2、温水槽3、引取幾4、巻取機5が
一連に配皺されていする。A delivery tube 1, an extruder 2, a hot water tank 3, a take-up tube 4, and a winder 5 are arranged in series.
この押出機2のホッパー21に近接さゼて架台60上に
攪拌器6が設置さけている二
この攪拌器6は高ぜん断ミキ勺−例えばヘンシェルミキ
サーであり、内部に供給されるポリオレフィンのレジン
を予備加熱するための予備加熱機構を備えている。A stirrer 6 is installed on a stand 60 in close proximity to the hopper 21 of the extruder 2.The stirrer 6 is a high-shear mixer, such as a Henschel mixer, and the polyolefin resin supplied therein is Equipped with a preheating mechanism for preheating.
この攪拌器6には秤量機構7を介して貯留タンク8が連
結されている。A storage tank 8 is connected to the stirrer 6 via a weighing mechanism 7.
寸なわら、原料容器9内のポリオレフィンのレジンPは
、ローダ−11により送給パイプ10を冑て吸引され、
貯留タンク8内し貯留されている。At the same time, the polyolefin resin P in the raw material container 9 is sucked through the feed pipe 10 by the loader 11.
It is stored in a storage tank 8.
貯留タンク8からは秤量機構7により一定量ずつのレジ
ント)が攪拌器6内に供給されるのである。A fixed amount of resin is supplied from the storage tank 8 into the stirrer 6 by the weighing mechanism 7.
一方、攪拌器6には、シラン化合物、シラノール縮業触
媒、架橋剤などの添加物供給装置f 2 Qが連結され
ている。On the other hand, the stirrer 6 is connected to a device f 2 Q for supplying additives such as a silane compound, a silanol condensation catalyst, and a crosslinking agent.
この添加物供給装置は、図示するように1個設置するだ
けでなく、点線で例示りするように複数個設置しても口
い。This additive supply device can be installed not only as one as shown in the figure, but also as a plurality as illustrated by the dotted line.
なお、必要に応じ添加物供給装置には軽曽化機構を付属
させても良い。Note that, if necessary, the additive supply device may be attached with a lightening mechanism.
従って各添加物は混合物としてから1個の供給装置より
供給しても良いし、個々に別々の供給装置より供給して
も良い。Therefore, each additive may be supplied as a mixture from one supply device, or may be supplied individually from separate supply devices.
攪拌器6内でレジンP)よ予備加熱され且つ添加物と共
に攪拌され、レジンPに対し添加物が強制含浸ざける。The resin P) is preheated in the stirrer 6 and stirred together with the additives, so that the resin P is forcibly impregnated with the additives.
本発明においては、この攪拌器6が予備加熱機構を備え
ていることが重要な点である。In the present invention, it is important that the stirrer 6 is equipped with a preheating mechanism.
゛すなわち、(1)まず、し、却ンPを40〜90℃、
5〜50分の範囲内F予備加熱する。(2次に、この予
備加熱されたレジンに対し、添加物を供給し、40〜9
0℃、5=50分の範囲宵で両省を攪拌して、強制含浸
するという段階を経るものである。That is, (1) First, heat the temperature at 40 to 90°C.
Preheat within the range of 5 to 50 minutes. (Secondly, addi- tives are supplied to this preheated resin, and
The process involves a step of forcibly impregnating the mixture by stirring the mixture at 0° C. for 50 minutes.
このように強制含浸された」ンパウンドが、投入管6′
を経てiらに押出幾2の小ツバ−21に一投入され、押
出成型がおこなわれる。The compound thus forcibly impregnated is transferred to the input pipe 6'.
After that, it is put into the small collar 21 of the extruder 2, and extrusion molding is performed.
この押出幾2は、スラリl−長/スクリュー直径−18
〜35程瓜のものが適当であり、溶融〜混練〜計量化の
間に反応基の発生、シランによるグラフト化の開始が同
時におこなわれる。This extrusion geometry 2 is slurry l-length/screw diameter-18
Appropriately is a melon with a thickness of about 35 to 30 cm, and the generation of reactive groups and the initiation of grafting with silane occur simultaneously during melting, kneading, and metering.
次に、押出機のクロスヘッド22を通過する導線W1の
周上にシラングラノド化ポリオレフィンが被覆され、被
覆導線W2が形成される。Next, the circumference of the conducting wire W1 passing through the crosshead 22 of the extruder is coated with silane granodized polyolefin to form a coated conducting wire W2.
この被覆導[il W 2は温水槽3を通って徐冷され
ると共に架橋化され、引取機4を介して巻取機5に巻取
られる。The coated conductive material W 2 is slowly cooled through a hot water tank 3 and crosslinked, and is wound up by a winding machine 5 via a winding machine 4 .
以上説明してきた通り、本発明は1つの攪拌器におい−
(シラン化合物、シラノール縮合触媒、架橋剤などの添
加物を予備加熱されたポリオレフィンに強制含浸させて
コンパウンド化し、これを直接押出機に導入して押出機
中での溶融、混練によってシラングラフト化ポリオレフ
ィンを形成して導線上に押出被覆して後編水槽において
徐冷しながら架橋せしめる1段階方式を提供するもので
あり、従来の2段階す式に比して次のようなII著な作
用効果を秦する。As explained above, the present invention provides a single stirrer.
(Additives such as silane compounds, silanol condensation catalysts, and cross-linking agents are forcibly impregnated into preheated polyolefin to form a compound, which is then directly introduced into an extruder and melted and kneaded in the extruder to form a silane-grafted polyolefin. This method provides a one-step method in which the conductive wire is coated by extrusion and cross-linked while being slowly cooled in a post-forming water tank, and has the following remarkable effects compared to the conventional two-step method. Qin.
(1)各種添加物とポリオレフィンとは押出機への導入
直前にコンパウンド化させてがら直接押出機へ導入する
ため、シランの揮発に起因する架橋度のバラツキがなく
なり、電線の物理的特性(抗張力、伸び特性、加熱変形
特性など)が大幅に向上する。(1) Various additives and polyolefins are compounded immediately before being introduced into the extruder, and then introduced directly into the extruder. This eliminates variations in the degree of crosslinking caused by silane volatilization, and improves the physical properties of the wire (tensile strength , elongation properties, heat deformation properties, etc.) are significantly improved.
また、コンパウンド保管時における部分架橋がなくなり
、製品外観が大幅に向上する。In addition, partial crosslinking during compound storage is eliminated, and the product appearance is greatly improved.
(2) 予備加熱されたポリオレフィン中に添加物が
供給されて強制含浸が行われるため、添加物は均一かつ
効果的にポリオレフィン中に含浸され、架橋度が大幅に
向上する。(2) Since the additive is supplied into the preheated polyolefin and forced impregnation is performed, the additive is uniformly and effectively impregnated into the polyolefin, and the degree of crosslinking is greatly improved.
(3架橋は冷却を兼ねた温水槽中で行われるため、これ
によっても架橋度が向上する。(3) Since crosslinking is performed in a hot water bath that also serves as cooling, this also improves the degree of crosslinking.
(4) コンパウンド化は1個゛の操作により行われ
るため、コンパウンドのロスがなくなると共に、異物混
入の危険がなくなり、またシランの吸入、飛散もなくな
る。(4) Since compounding is performed in one operation, there is no loss of compound, there is no danger of foreign matter contamination, and there is no inhalation or scattering of silane.
(5) コンパウンド化から架橋化まで一連の工程で
行われるため、保管スペースを最少銀にできると共に製
造能率を大幅に向上eき、加工費番安価にできる。(5) Since the process from compounding to crosslinking is carried out in a series, storage space can be minimized, manufacturing efficiency can be greatly improved, and processing costs can be reduced.
第1図および第2図は本発明を実施するための順造設備
の一実施例を示し、第1図はライン全体を示す説明図、
第2図は押出機周辺の要部のみを示す説明図ぐある。
1:送出機、2:押出機、3:温水槽、4:引取機、5
:巻取機、6:攪拌器、7:秤量機構、8:貯留タンク
、9:原料容器、P:ポリオレフィンのレジン、
20:添加物供給装置。FIGS. 1 and 2 show an embodiment of the manufacturing equipment for carrying out the present invention, and FIG. 1 is an explanatory diagram showing the entire line;
FIG. 2 is an explanatory diagram showing only the main parts around the extruder. 1: Delivery machine, 2: Extrusion machine, 3: Hot water tank, 4: Taking machine, 5
: Winder, 6: Stirrer, 7: Weighing mechanism, 8: Storage tank, 9: Raw material container, P: Polyolefin resin, 20: Additive supply device.
Claims (1)
化合物、シラノール綜合触媒、架橋剤などの添加物供給
@置を連結すると共に秤量1141を介してポリオレフ
ィン貯留タンクを連結し、上記攪拌器内で予価加熱され
たポリオレフィンに添加物を強III含浸させて得たフ
ンバウンドを直接押出機内へ導入してシラングラフト化
ポリオレフィンを形成し、これを導線同上に押出被覆し
てから温水槽に導いて徐冷させつつ架橋せしめることを
特徴とする架橋ポリオレフィン電線の製造方法。A stirrer is installed near the extruder, and a supply of additives such as a silane compound, a silanol synthesis catalyst, and a crosslinking agent is connected to this stirrer, and a polyolefin storage tank is also connected via a weighing device 1141, and the above-mentioned stirring The polyolefin preheated in the vessel is impregnated with strong III additives, and the resulting filtrate is directly introduced into the extruder to form a silane-grafted polyolefin, which is extruded and coated on the conductor wire, and then placed in a hot water bath. 1. A method for producing a crosslinked polyolefin electric wire, which comprises crosslinking the wire while slowly cooling the wire.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57104532A JPS581924A (en) | 1982-06-17 | 1982-06-17 | Method of producing crosslinked polyolefin wire |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57104532A JPS581924A (en) | 1982-06-17 | 1982-06-17 | Method of producing crosslinked polyolefin wire |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS581924A true JPS581924A (en) | 1983-01-07 |
| JPS6116147B2 JPS6116147B2 (en) | 1986-04-28 |
Family
ID=14383099
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57104532A Granted JPS581924A (en) | 1982-06-17 | 1982-06-17 | Method of producing crosslinked polyolefin wire |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS581924A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4446279A (en) * | 1982-02-22 | 1984-05-01 | Union Carbide Corporation | Compositions based on a polysiloxane and an organo titanate and the use thereof in the preparation of water curable, silane modified alkylene-alkyl acrylate copolymers |
| US4489029A (en) * | 1983-06-01 | 1984-12-18 | Union Carbide Corporation | Compositions based on alkylene-alkyl acrylate copolymers and silanol condensation catalysts; and the use thereof in the production of covered wires and cables |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63137648U (en) * | 1987-03-03 | 1988-09-09 | ||
| JPH0210861U (en) * | 1988-07-06 | 1990-01-24 | ||
| JPH0422968U (en) * | 1990-06-15 | 1992-02-25 |
-
1982
- 1982-06-17 JP JP57104532A patent/JPS581924A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4446279A (en) * | 1982-02-22 | 1984-05-01 | Union Carbide Corporation | Compositions based on a polysiloxane and an organo titanate and the use thereof in the preparation of water curable, silane modified alkylene-alkyl acrylate copolymers |
| US4489029A (en) * | 1983-06-01 | 1984-12-18 | Union Carbide Corporation | Compositions based on alkylene-alkyl acrylate copolymers and silanol condensation catalysts; and the use thereof in the production of covered wires and cables |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6116147B2 (en) | 1986-04-28 |
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