JPH0368126B2 - - Google Patents
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- Publication number
- JPH0368126B2 JPH0368126B2 JP57193458A JP19345882A JPH0368126B2 JP H0368126 B2 JPH0368126 B2 JP H0368126B2 JP 57193458 A JP57193458 A JP 57193458A JP 19345882 A JP19345882 A JP 19345882A JP H0368126 B2 JPH0368126 B2 JP H0368126B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- strength
- filament
- density
- stretching
- 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
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- Compositions Of Macromolecular Compounds (AREA)
- Artificial Filaments (AREA)
Description
本発明はフイラメントの製造方法に関し、詳し
くは延伸性良好で高強度を有し、かつ柔軟性、耐
クリープ性、耐摩耗性、透明性に優れたフイラメ
ントを得ることのできるフイラメントの製造方法
に関するものである。
従来、漁網、ゴルフ場用ネツト、落石防止網な
どに用いられるフイラメント用樹脂組成物は、一
般に高密度ポリエチレンと称される密度0.950
g/cm3程度以上のエチレン共重合体(以下高密度
ポリエチレンと称する)が、多く使用されてい
る。また柔軟性が特に要求される場合には、上記
高密度ポリエチレンに適当量の高圧法低密度ポリ
エチレンがブレンドされて使用されている。
製網用原糸の樹脂組成物の場合、ロープ製網用
原糸の樹脂組成物と異なつて強度はそれ程要求さ
れず、むしろ耐クリープ性、耐摩耗性、柔軟性、
結節強度、直線強度等の諸物性が要求され、これ
らの物性がバランスしていることが重要である。
しかるに、高密度ポリエチレンでは柔軟性、耐摩
耗性、直線強度等に劣り、耐クリープ性も満足す
るまでには至つていない。
そこで、延伸倍率を中心として樹脂組成物のメ
ルトインデツクスや原糸を成形する際に用いるノ
ズルの形状、延伸温度などについて種々の検討が
なされているが、延伸倍率を低倍率に設定した場
合、柔軟性、耐摩耗性、直線伸度がある程度改良
されるもののそれ程大きなものではなく、逆に耐
クリープ性が著しく悪くなるなど満足のいく物性
は得られない。
また高密度ポリエチレンに低密度ポリエチレン
をブレンドした場合、柔軟性は改良されるが、強
度低下や耐クリープ性低下が激しく、ここにおい
ても要求特性に対しバランスし、かつ満足した物
性は得られていない。
本発明者等は上記の事情に鑑み鋭意検討した結
果、柔軟性、耐クリープ性、耐摩耗性が優れ、又
必要強度をも有し、それら諸物性がフイラメント
用としてバランスした樹脂組成物を見出し、本発
明を完成した。
本発明に使用されるフイラメント用樹脂組成物
は、密度0.930g/cm3以下、メルトインデツクス
(以下MIと称する)0.2〜10g/10minの短鎖分岐
を有する直鎖状ポリエチレン(以下樹脂Aと称す
る)5〜75重量%及び密度0.940g/cm3以上、
MI0.1〜10g/10minのポリエチレン(以下樹脂
Bと称する)25〜95重量%から成り、当該樹脂組
成物のMIは0.2〜2g/10minである。
本発明において用いられる樹脂Aは、遷移金属
化合物及び有機金属化合物からなるチーグラ型触
媒によりエチレンとプロピレン、ブテン−1、ヘ
キセン−1、4メチルペンテン−1、ヘキセン−
1、オクテン−1、デセン−1等のα−オレフイ
ンを共重合することによつて得ることのできるエ
チレンを主体とした樹脂である。重合方法、条件
は特に限定されず、気相法、スラリー法、液溶
法、溶融法等いずれの方法によつても製造するこ
とができる。
また、本発明において用いられる樹脂Aの密度
は0.930g/cm3以下であることが必要である。
密度が0.930g/cm3を越えると、所定の強度は
得られるものの耐摩耗性、耐クリープ性、柔軟性
などが悪くなり、諸物性のバランスがとれなくな
る。即ち、耐摩耗性、耐クリープ性、柔軟性は密
度0.930〜0.940g/cm3を境として急激な改良効果
が見られ、これは高密度ポリエチレンからは到底
予測できない改良効果であり、耐摩耗性、耐クリ
ープ性、柔軟性の点から特に密度0.910〜0.925
g/cm3が好ましい。
更に本発明において用いられる樹脂AのMI(温
度190℃で2160g荷重した場合の測定値)は0.2〜
10g/10minであることが必要である。このMI
が0.2g/10min未満であるときは延伸性が著し
く低下し、低倍率しか延伸できず所定の強度が得
られない。又、MIが10g/10minを越えると高
倍率の延伸は可能になるが、達成強度が低くなり
耐摩耗性、耐クリープ性、柔軟性などとのバラン
スがとれなくなる。
本発明において用いられる樹脂Bとしてはホモ
ポリマーの他、樹脂Aについて例示したと同様の
コポリマーが挙げられる。
又本発明において用いられる樹脂Bの密度は
0.940g/cm3以上であることが必要である。密度
0.940g/cm3未満では、フイラメントの特に直線
強度が低下し、本発明所望の目的を達成し得な
い。
更に、本発明において用いられる樹脂BのMI
(温度190℃で2160g荷重した場合の測定値)は
0.1〜10g/10minであることが必要である。MI
が0.1g/10min未満では延伸性が不良になり、
ネツキングが安定せず、延伸切れ、フイラメント
の白化を生じて良質なフイラメントが得られず、
又MIが10g/10minを越えると伸度並びに結節
強度が不十分となる。
本発明に使用される樹脂組成物の樹脂Aと樹脂
Bとの混合割合については、樹脂Bが多過ぎると
即ち樹脂Aが少な過ぎると、耐摩耗性、耐クリー
プ性、柔軟性などが著しく悪くなる。逆に樹脂B
が少な過ぎると即ち樹脂Aが多過ぎると直線強
度、結節強度が低下する。樹脂Aと樹脂Bとの混
合割合は樹脂A5〜75重量%に対して樹脂B25〜
95重量%であることが必要であり、好ましくは樹
脂A10〜50重量%に対して樹脂B50〜90重量%で
ある。
当該樹脂組成物のMI(温度190℃で2160g荷重
した場合の測定値)は0.2〜2g/10minである
ことが必要である。このMIが0.2g/10min未満
であるときには延伸性が著しく低下する上に、フ
イラメントが白濁し透明度が悪くなる。又、MI
が2g/10minを越えると延伸性、透明度ともに
問題はないが、直線強度、結節強度が著しく低下
する上に、耐摩耗性、耐クリープ性も極端に悪く
なる。
本発明において用いられる樹脂A及び樹脂Bは
共に、HLMI/MI(JIS K6760)40以下であるこ
とが、本発明において紡糸性や延伸性を更に向上
させる上で好ましい。即ちのこのHLMI/MIが
40を越えるときは紡糸性、延伸性の点で問題が生
じ、かつ同一倍率での強度も弱くなるのに対し、
HLMI/MIが40以下の場合には、紡糸性及び延
伸性が良く、また同一倍率での強度も高いため、
比較的低倍率での延伸で済むことになる。
本発明に使用されるフイラメント用樹脂組成物
には、フイラメントの抗酸化性の向上を図るため
に抗酸化剤を、また、ノズルからの押出性向上を
図るために、金属石鹸を添加する。金属石鹸の具
体例としては、カルシウムテアレートが挙げられ
る。抗酸化剤の具体例としては、2,6−ジ第3
級ブチル4−メチルフエノール、チオジプロピオ
ン酸スアテリルが挙げられる。
更に本発明フイラメント用樹脂組成物には必要
に応じて、紫外線劣化防止剤、滑剤、顔料などの
補助成分を配合しても良い。
次に、本発明のフイラメントの製造方法を更に
説明するに、樹脂Aと樹脂Bとを好ましい混合割
合ブレンドし、それに抗酸化剤、金属石鹸を配合
してなるブレンド物をフイラメントに押出成形
し、冷却後にそのフイラメントを80℃以上120℃
以下の温度範囲にて6倍以上好ましくは6〜12倍
に延伸する。
詳しくは、以上ブレンド物を溶融し、例えば丸
ノズルまたは異形ノズルのいずれかを用いて、シ
エアレート400〜1800、ドラフト比1〜5で原糸
となるモノフイラメントの押出成形を行う。この
未延伸のモノフイラメントを水冷したのち、80〜
120℃の温度条件下で6倍以上の延伸倍率で延伸
を行なう。この場合、ノズルのシエアレートが
400以下であるとフイラメントに糸むらの発生が
あり、糸むらが生じると数百本以上のフイラメン
トを撚り合わせて成形するロープと異なつて、撚
り合わせ本数が数本と少ない漁網、ゴルフ場ネツ
ト、落石防止網等の類のものの原糸では問題が発
生する。また1800以上のシエアレートで押出した
ときにはフイラメント表面が荒れて延伸不能とな
るという問題がある。
本発明に用いる樹脂Aは高密度ポリエチレンよ
りもはるかにドラフト比による影響を受け易く、
設定ドラフト比は1以上で延伸性が低下しない範
囲で高い方が高強度が得られる。好ましくは1.5
〜4の範囲が良好である。ドラフト比が1以下の
場合には糸ゆれ等のトラブルが発生する。
また延伸温度は80〜120℃がよく、好ましくは
90〜100℃である。延伸温度が80℃以下の場合に
も延伸はある程度可能であるが、延伸時に白化現
象などの問題が起こり、強度や耐摩耗性、耐クリ
ープ性を著しく低下させる。更にまた延伸倍率は
6〜12倍とするが、好ましくは8〜11倍がよい。
延伸倍率が6倍より低い場合には延伸中のネツキ
ングポイントの安定性が悪く、延伸が不安定なば
かりか、一般モノフイラメントとして要求される
結節強度が低く耐クリープ性も極端に悪い。その
反対に延伸倍率が12倍を越えると、延伸切れ、白
化、耐摩耗性、伸度及び結節強度の低下のような
多くの問題が生じる。
上記はモノフイラメントの場合であるが、モノ
フイラメントの数本連結した形態よりなる並び繊
維の場合でも、成形条件を上記と同様にして製造
することができる。この並び繊維の成形にはスリ
ツトを介して連結した数本のノズルを用いる場
合、近接して設けた数本のノズルを用い押出し樹
脂のバラス効果により得る場合、更に押出した樹
脂をガイド等により溶融状態において部分的に接
着させる方法など従来周知の手段を採用すること
ができる。
本発明の方法により得られたフイラメントは直
線強度4〜8g/d、柔軟性指数5〜15、耐クリ
ープ性20%以下、耐摩耗性300以上を示し、柔軟
性、耐クリープ性、耐摩耗性が優れ、また必要強
度を備え、これら物性がバランスしたフイラメン
トである。
ところで、一般に樹脂の密度を小さくすると延
伸性が悪くなり、また強度低下が大きいと云われ
ているが、確かに高圧法ポリエチレンや高圧法ポ
リエチレンと中低圧ポリエチレンのブレンドポリ
エチレンでは延伸性が悪く、延伸性はせいぜい倍
率7〜8倍程度が限界である。しかも延伸方法特
に延伸温度を充分に考慮しての上のことであり、
通常80℃程度以下でないと延伸不可能であつた。
そして強度もせいぜい2〜4g/d程度で、漁
網、ゴルフ場用ネツト、落石防止網などに用いら
れる一般フイラメントとして耐えられる強度でな
く、加えて耐クリープ性、耐摩耗性にも難点があ
つた。しかるに本発明のモノフイラメント、並び
に繊維にあつては、上記の如く直線強度4〜8
g/d、柔軟性指数5〜15、耐クリープ性20%以
下、耐摩耗性300以上で、一般フイラメントとし
ての物性バランスを有し、漁網、ゴルフ場用ネツ
ト、落石防止網等の一般製網用原糸として最適な
ものである。
なお、本発明によるモノフイラメントは、ロー
プ用原糸としては強度の点でやや劣るが、柔軟
性、耐摩耗性、耐クリープ性に優れているため、
これらの物性が要求されるロープの原糸として使
用することもできる。
次に本発明を実施例及び比較例を以つて更に詳
説する。
実施例1〜4及び比較例1〜3
第1表に示す樹脂A−1〜A−4及びB−1、
B−2を用いて、75m/mφの押出機により下記
条件下で
C1 C2 C3 C4 AD
160 250 270 290 280
D1 D2
270 270(℃)
1.0m/mφ、150ホールノズルより押出速度
1100〜1500sec-1で押出し、エアーギヤツプ60
m/mで水冷し、水冷後100℃沸水中にして延伸
速度120m/minにより湿式延伸した。設定繊度
は400Deであつた。
なお、樹脂A及びBは、当該樹脂各100重量部
に対して
2,6−ジ−第3級ブチル4−メチルフエノール
0.1重量部
チオジプロピオン酸ステアリル 0.05 〃
カルシウムステアレート 0.15 〃
を添加してある。
The present invention relates to a method for producing a filament, and more particularly, to a method for producing a filament that can produce a filament with good drawability, high strength, and excellent flexibility, creep resistance, abrasion resistance, and transparency. It is. Conventionally, filament resin compositions used for fishing nets, golf course nets, rockfall prevention nets, etc. have a density of 0.950 and are generally referred to as high-density polyethylene.
Ethylene copolymers (hereinafter referred to as high-density polyethylene) with a density of about g/cm 3 or more are often used. When flexibility is particularly required, an appropriate amount of high-pressure low-density polyethylene is blended with the above-mentioned high-density polyethylene. In the case of a resin composition for yarn for net making, unlike a resin composition for yarn for rope net making, strength is not required as much, but rather creep resistance, abrasion resistance, flexibility,
Various physical properties such as nodular strength and linear strength are required, and it is important that these physical properties are balanced.
However, high-density polyethylene is inferior in flexibility, abrasion resistance, linear strength, etc., and has not yet achieved satisfactory creep resistance. Therefore, various studies have been made on the melt index of the resin composition, the shape of the nozzle used when forming the yarn, the stretching temperature, etc. with a focus on the stretching ratio, but when the stretching ratio is set to a low ratio, Although the flexibility, abrasion resistance, and linear elongation are improved to some extent, the improvement is not significant, and on the contrary, the creep resistance is significantly deteriorated, so that satisfactory physical properties cannot be obtained. Furthermore, when low-density polyethylene is blended with high-density polyethylene, the flexibility is improved, but the strength and creep resistance are significantly reduced, and here too, it is not possible to obtain physical properties that are balanced and satisfactory with respect to the required properties. . As a result of intensive studies in view of the above circumstances, the present inventors have discovered a resin composition that has excellent flexibility, creep resistance, and abrasion resistance, and also has the necessary strength, and which has a good balance of these physical properties for use in filaments. , completed the invention. The filament resin composition used in the present invention is a linear polyethylene (hereinafter referred to as resin A) having a short chain branching with a density of 0.930 g/cm 3 or less and a melt index (hereinafter referred to as MI) of 0.2 to 10 g/10 min. ) 5 to 75% by weight and a density of 0.940 g/cm 3 or more,
It consists of 25 to 95% by weight of polyethylene (hereinafter referred to as resin B) with an MI of 0.1 to 10 g/10 min, and the MI of the resin composition is 0.2 to 2 g/10 min. Resin A used in the present invention is produced by using a Ziegler type catalyst consisting of a transition metal compound and an organometallic compound to produce ethylene, propylene, butene-1, hexene-1, 4-methylpentene-1, hexene-1, and hexene-1.
It is a resin mainly composed of ethylene, which can be obtained by copolymerizing α-olefins such as 1, octene-1, and decene-1. The polymerization method and conditions are not particularly limited, and it can be produced by any method such as a gas phase method, a slurry method, a liquid solution method, or a melt method. Further, the density of resin A used in the present invention needs to be 0.930 g/cm 3 or less. When the density exceeds 0.930 g/cm 3 , although a certain level of strength can be obtained, abrasion resistance, creep resistance, flexibility, etc. deteriorate, and various physical properties become unbalanced. In other words, a rapid improvement effect on abrasion resistance, creep resistance, and flexibility was observed at a density of 0.930 to 0.940 g/cm 3 , and this is an improvement effect that could never be predicted from high-density polyethylene. Density 0.910~0.925, especially from the viewpoint of creep resistance and flexibility
g/cm 3 is preferred. Furthermore, the MI of resin A used in the present invention (measured value when loaded with 2160 g at a temperature of 190°C) is 0.2 ~
It is necessary to be 10g/10min. This MI
When the amount is less than 0.2 g/10 min, the stretchability is significantly reduced, and only a low stretching ratio is possible, making it impossible to obtain the desired strength. Furthermore, if the MI exceeds 10 g/10 min, it becomes possible to stretch at a high magnification, but the achieved strength becomes low and it becomes impossible to maintain a balance with wear resistance, creep resistance, flexibility, etc. Resin B used in the present invention includes homopolymers as well as copolymers similar to those exemplified for resin A. In addition, the density of resin B used in the present invention is
It is necessary that it is 0.940 g/cm 3 or more. density
If it is less than 0.940 g/cm 3 , the linear strength of the filament in particular decreases, making it impossible to achieve the desired object of the present invention. Furthermore, the MI of resin B used in the present invention
(Measurement value when a load of 2160g is applied at a temperature of 190℃) is
It is necessary that it is 0.1-10g/10min. MI
If it is less than 0.1g/10min, the stretchability will be poor,
Netsuking is not stable, stretching breaks, and whitening of the filament occurs, making it impossible to obtain a high-quality filament.
Furthermore, if the MI exceeds 10 g/10 min, the elongation and knot strength will be insufficient. Regarding the mixing ratio of resin A and resin B in the resin composition used in the present invention, if there is too much resin B, that is, if there is too little resin A, the abrasion resistance, creep resistance, flexibility, etc. will be significantly deteriorated. Become. On the contrary, resin B
If the amount of resin A is too small, that is, if the amount of resin A is too large, the linear strength and knot strength will decrease. The mixing ratio of resin A and resin B is 5 to 75% by weight of resin A and 25 to 75% by weight of resin B.
95% by weight, preferably 50-90% by weight of resin B to 10-50% by weight of resin A. The MI (measured value when a load of 2160 g is applied at a temperature of 190° C.) of the resin composition needs to be 0.2 to 2 g/10 min. When the MI is less than 0.2 g/10 min, the drawability is significantly reduced, and the filament becomes cloudy and its transparency deteriorates. Also, MI
If it exceeds 2 g/10 min, there is no problem with both stretchability and transparency, but linear strength and knot strength are significantly reduced, and abrasion resistance and creep resistance are also extremely poor. Both resin A and resin B used in the present invention preferably have an HLMI/MI (JIS K6760) of 40 or less in order to further improve spinnability and stretchability in the present invention. In other words, this HLMI/MI is
When it exceeds 40, problems arise in terms of spinnability and stretchability, and the strength at the same magnification becomes weak.
When HLMI/MI is 40 or less, the spinnability and stretchability are good, and the strength at the same magnification is also high.
Stretching at a relatively low magnification is sufficient. An antioxidant is added to the filament resin composition used in the present invention in order to improve the antioxidative properties of the filament, and a metal soap is added in order to improve the extrudability from a nozzle. A specific example of the metal soap is calcium tearate. Specific examples of antioxidants include 2,6-ditertiary
Examples include butyl 4-methylphenol and suateryl thiodipropionate. Furthermore, the resin composition for filaments of the present invention may contain auxiliary components such as ultraviolet deterioration inhibitors, lubricants, and pigments, if necessary. Next, to further explain the method for producing a filament of the present invention, resin A and resin B are blended at a preferable mixing ratio, an antioxidant and a metal soap are added thereto, and the blend is extruded into a filament. After cooling, the filament is heated above 80℃ to 120℃.
It is stretched 6 times or more preferably 6 to 12 times in the following temperature range. Specifically, the above-mentioned blend is melted and extrusion molded into a monofilament to serve as a raw yarn at a shear rate of 400 to 1800 and a draft ratio of 1 to 5 using, for example, a round nozzle or an irregularly shaped nozzle. After cooling this unstretched monofilament with water,
Stretching is carried out at a temperature of 120°C at a stretching ratio of 6 times or more. In this case, the nozzle shear rate is
If it is less than 400, thread unevenness will occur in the filament, and unlike ropes that are formed by twisting hundreds or more filaments together, fishing nets, golf course nets, etc. Problems arise with raw yarn for things such as rockfall prevention nets. Further, when extruded at a shear rate of 1800 or more, there is a problem that the filament surface becomes rough and cannot be stretched. Resin A used in the present invention is much more susceptible to draft ratio than high-density polyethylene,
The set draft ratio is 1 or more, and the higher the draft ratio is, the higher the strength can be obtained as long as the drawability is not reduced. Preferably 1.5
A range of 4 to 4 is good. If the draft ratio is less than 1, troubles such as yarn wobbling will occur. In addition, the stretching temperature is preferably 80 to 120℃, preferably
The temperature is 90-100℃. Although stretching is possible to some extent even when the stretching temperature is 80° C. or lower, problems such as whitening occur during stretching, which significantly reduces strength, abrasion resistance, and creep resistance. Furthermore, the stretching ratio is 6 to 12 times, preferably 8 to 11 times.
When the stretching ratio is lower than 6 times, the stability of the netting point during stretching is poor, and not only is the stretching unstable, but the knot strength required for a general monofilament is low and the creep resistance is extremely poor. On the other hand, when the stretching ratio exceeds 12 times, many problems occur such as stretching breakage, whitening, abrasion resistance, elongation and knot strength reduction. Although the above is a case of a monofilament, even in the case of an aligned fiber formed by connecting several monofilaments, it is possible to manufacture the fiber by using the same molding conditions as above. When forming this aligned fiber, several nozzles connected through a slit are used, or several nozzles placed close together are used to obtain the extruded resin using a ballast effect, or the extruded resin is melted using a guide, etc. Conventionally known means, such as a method of partially adhering in a state, can be employed. The filament obtained by the method of the present invention has a linear strength of 4 to 8 g/d, a flexibility index of 5 to 15, a creep resistance of 20% or less, and an abrasion resistance of 300 or more, and has excellent flexibility, creep resistance, and abrasion resistance. It is a filament that has excellent properties, has the necessary strength, and has a good balance of these physical properties. By the way, it is generally said that reducing the density of the resin results in poor stretchability and a large decrease in strength, but it is true that high-pressure polyethylene and blended polyethylene of high-pressure polyethylene and medium-low pressure polyethylene have poor stretchability and are difficult to stretch. The maximum magnification is about 7 to 8 times. Moreover, the stretching method, especially the stretching temperature, must be fully considered.
Normally, stretching was not possible unless the temperature was about 80°C or lower.
Moreover, the strength was only about 2 to 4 g/d at most, which was not strong enough to withstand general filament used in fishing nets, golf course nets, rockfall prevention nets, etc., and it also had drawbacks in creep resistance and abrasion resistance. . However, the monofilament and fiber of the present invention have a linear strength of 4 to 8 as described above.
g/d, flexibility index 5 to 15, creep resistance 20% or less, abrasion resistance 300 or more, and has a good balance of physical properties as a general filament, making it suitable for general net making such as fishing nets, golf course nets, rockfall prevention nets, etc. It is most suitable as yarn for use. Although the monofilament according to the present invention is somewhat inferior in strength as a rope yarn, it has excellent flexibility, abrasion resistance, and creep resistance.
It can also be used as yarn for ropes that require these physical properties. Next, the present invention will be explained in more detail with reference to Examples and Comparative Examples. Examples 1 to 4 and Comparative Examples 1 to 3 Resins A-1 to A-4 and B-1 shown in Table 1,
C 1 C 2 C 3 C 4 AD 160 250 270 290 280 D 1 D 2 270 270 (℃) 1.0 m/mφ, 150 hole nozzle using B-2 under the following conditions with an extruder of 75 m/mφ extrusion speed
Extrusion at 1100~1500sec -1 , air gap 60
After cooling with water, the film was placed in boiling water at 100° C. and wet-stretched at a stretching speed of 120 m/min. The fineness setting was 400De. In addition, resins A and B contain 2,6-di-tertiary butyl 4-methylphenol per 100 parts by weight of each resin.
0.1 part by weight of stearyl thiodipropionate 0.05 and calcium stearate 0.15 are added.
【表】
各実施例の結果を比較例の結果と共に下記第2
表に示す。[Table] The results of each example are shown in the second table below along with the results of comparative examples.
Shown in the table.
【表】【table】
【表】
比較例1では、直線及び結節強度は十分あるが
柔軟性指数が実施例1〜4と比較して高く、又、
耐摩耗性、耐クリープ性に劣る。
比較例2では、実施例1と密度はほぼ同レベル
であるがやはり柔軟性指数が高く、耐摩耗性、耐
クリープ性も劣る。又、強度も低い。[Table] Comparative Example 1 has sufficient linear and knot strength, but has a higher flexibility index than Examples 1 to 4.
Poor wear resistance and creep resistance. In Comparative Example 2, the density is almost the same as in Example 1, but the flexibility index is also high, and the abrasion resistance and creep resistance are also inferior. Also, the strength is low.
Claims (1)
0.2〜10g/10minの短鎖分岐を有する直鎖状低
密度ポリエチレン5〜75重量%及び密度0.940
g/cm3以上、メルトインデツクス0.1〜10g/
10minのポリエチレン25〜95重量%から成り、メ
ルトインデツクスが0.2〜2g/10minの樹脂組
成物に抗酸化剤および金属石鹸を配合して成るフ
イラメント用樹脂組成物からフイラメントを得る
ことを特徴とするフイラメントの製造方法。1 Density 0.930g/ cm3 or less, melt index
5-75% by weight of linear low-density polyethylene with short chain branching of 0.2-10g/10min and density 0.940
g/ cm3 or more, melt index 0.1~10g/
The method is characterized in that a filament is obtained from a resin composition for a filament, which is made of a resin composition of 25 to 95% by weight of polyethylene and has a melt index of 0.2 to 2 g/10 min, mixed with an antioxidant and a metal soap. Method of manufacturing filament.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19345882A JPS5984942A (en) | 1982-11-05 | 1982-11-05 | Resin composition for filament |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19345882A JPS5984942A (en) | 1982-11-05 | 1982-11-05 | Resin composition for filament |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5984942A JPS5984942A (en) | 1984-05-16 |
| JPH0368126B2 true JPH0368126B2 (en) | 1991-10-25 |
Family
ID=16308332
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19345882A Granted JPS5984942A (en) | 1982-11-05 | 1982-11-05 | Resin composition for filament |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5984942A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5371145A (en) * | 1993-06-08 | 1994-12-06 | Union Carbide Chemicals & Plastics Technology Corporation | High density, high molecular weight polyethylene |
| WO2011134897A2 (en) * | 2010-04-30 | 2011-11-03 | Basell Polyolefine Gmbh | Polymer filament or fiber |
| CN105008601B (en) * | 2013-03-11 | 2017-08-18 | 陶氏环球技术有限责任公司 | Fiber comprising polyethylene blend |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5130849A (en) * | 1974-09-11 | 1976-03-16 | Mitsui Petrochemical Ind | HORIECHIRENSOSEIBUTSU |
| SE454334B (en) * | 1986-09-01 | 1988-04-25 | Asea Ab | DEVICE BY INDUSTRIROBOT |
-
1982
- 1982-11-05 JP JP19345882A patent/JPS5984942A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5984942A (en) | 1984-05-16 |
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