JPH07145511A - Polyester monofilament - Google Patents
Polyester monofilamentInfo
- Publication number
- JPH07145511A JPH07145511A JP31906193A JP31906193A JPH07145511A JP H07145511 A JPH07145511 A JP H07145511A JP 31906193 A JP31906193 A JP 31906193A JP 31906193 A JP31906193 A JP 31906193A JP H07145511 A JPH07145511 A JP H07145511A
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- Japan
- Prior art keywords
- acid
- polyester monofilament
- less
- polyester
- particle size
- 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.)
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- Compositions Of Macromolecular Compounds (AREA)
- Artificial Filaments (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、耐加水分解性及び耐屈
曲摩耗性に優れた抄紙カンバス用に好適なポリエステル
モノフィラメントに関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyester monofilament which is excellent in hydrolysis resistance and flex abrasion resistance and is suitable for papermaking canvas.
【0002】[0002]
【従来の技術】ポリエチレンテレフタレートは、強度、
耐薬品性、耐熱性、耐候性、電気絶縁性等の点で優れた
性質を有しており、工業用途にも広く使用されている。
工業用途のなかでも特に抄紙装置用に使用されるモノフ
ィラメントは、カンバス布に製織され、抄紙された湿潤
状態の紙シートを乾燥シリンダーに圧着させて乾燥しな
がら連続して運搬するベルトとして用いられるため、高
い耐加水分解性と耐屈曲摩耗性が要求される。2. Description of the Related Art Polyethylene terephthalate has strength,
It has excellent properties such as chemical resistance, heat resistance, weather resistance, and electrical insulation, and is widely used in industrial applications.
Among the industrial applications, monofilaments used especially for papermaking machines are woven into a canvas cloth and used as a belt for continuously transporting a paper sheet in a wet state, which is made by papermaking, by pressing it on a drying cylinder and drying it. , High hydrolysis resistance and bending abrasion resistance are required.
【0003】ポリエステルフィラメントの耐加水分解性
を高める方法として、あらかじめポリエステルの末端カ
ルボキシル基濃度を低下させておく方法が知られてお
り、エポキシ化合物を添加する方法(特公昭44− 27911
号、特開昭54−6051号等)、カルボジイミド化合物を添
加する方法(特公平1− 15604号、特開平3−104919号
等)、カルボジイミド化合物とフッ素化合物を添加する
方法(特開平4−149268号)等が提案されている。これ
らの方法によれば、耐加水分解性はある程度改善される
ものの、耐屈曲摩耗性が十分でないという問題点があっ
た。As a method of increasing the hydrolysis resistance of polyester filaments, a method of reducing the terminal carboxyl group concentration of polyester in advance is known, and a method of adding an epoxy compound (Japanese Patent Publication No. 44-27911).
JP-A-54-6051), a method of adding a carbodiimide compound (JP-B-1-15604, JP-A-3-104919, etc.), a method of adding a carbodiimide compound and a fluorine compound (JP-A-4-149268). No.) etc. have been proposed. According to these methods, the hydrolysis resistance is improved to some extent, but there is a problem that the flexing abrasion resistance is not sufficient.
【0004】一方、耐屈曲摩耗性を高める方法として、
金属粒子を添加する方法(特開平3− 76813号)、ケイ
素化合物でモノフィラメント表面をコーティングする方
法(特開平3−249273号、同3−269169号)、ポリエス
テルとナイロンとの芯鞘型複合糸とする方法(特開平2
−145894号)等が提案されている。これらの方法によれ
ば、耐屈曲摩耗性はある程度改善されるものの、耐加水
分解性が十分でないばかりか、ローラ表面等のベルトの
接触する部分が摩耗するといった問題点があった。On the other hand, as a method for increasing the flex wear resistance,
A method of adding metal particles (JP-A-3-76813), a method of coating the surface of a monofilament with a silicon compound (JP-A-3-249273, 3-269169), and a core-sheath composite yarn of polyester and nylon. Method (JP-A-2
No. 145894) has been proposed. According to these methods, although the flexing abrasion resistance is improved to some extent, there are problems that not only the hydrolysis resistance is insufficient, but also the contact portion of the belt such as the roller surface is abraded.
【0005】また、ポリエステルに滑性を付与する方法
として、粒径が50μm 以下のフッ素樹脂を添加する方法
(特開昭54−124055号)が提案されている。この方法に
よれば、滑性はある程度改善されるものの、径の小さい
モノフィラメントとした場合、耐屈曲摩耗性が十分でな
いといった問題点があった。As a method of imparting lubricity to polyester, a method of adding a fluororesin having a particle size of 50 μm or less (Japanese Patent Laid-Open No. 54-124055) has been proposed. According to this method, the lubricity is improved to some extent, but when the monofilament having a small diameter is used, there is a problem that the flexing abrasion resistance is not sufficient.
【0006】[0006]
【発明が解決しようとする課題】本発明は、耐加水分解
性及び耐屈曲摩耗性に優れたポリエステルモノフィラメ
ントを提供しようとするものである。DISCLOSURE OF THE INVENTION The present invention is intended to provide a polyester monofilament having excellent hydrolysis resistance and flex abrasion resistance.
【0007】[0007]
【課題を解決するための手段】本発明は、上記の課題を
解決するもので、その要旨は、極限粘度 0.6以上、末端
カルボキシル基濃度10g当量/106g以下のポリエチレン
テレフタレート(PET)に、最大粒径5μm 以下、平
均粒径1μm 以下のポリテトラフルオロエチレン樹脂
(PTFE)粉末を全体に対して 0.1〜10重量%含有さ
せた組成物からなるポリエステルモノフィラメントにあ
る。Means for Solving the Problems The present invention is to solve the above problems, and its gist is to provide polyethylene terephthalate (PET) with an intrinsic viscosity of 0.6 or more and a terminal carboxyl group concentration of 10 g equivalent / 10 6 g or less, A polyester monofilament made of a composition containing 0.1 to 10% by weight of polytetrafluoroethylene resin (PTFE) powder having a maximum particle size of 5 μm or less and an average particle size of 1 μm or less based on the whole powder.
【0008】以下、本発明について詳細に説明する。本
発明において、PETとしては、ホモポリマーが好まし
いが、本発明の効果を損なわない範囲であれば、共重合
成分を含有していてもよい。共重合成分の具体例として
は、イソフタル酸、コハク酸、アジピン酸、スベリン
酸、ドデカン二酸、アゼライン酸、セバシン酸、1,3−
プロパンジオール、1,4−ブタンジオール、1,6−ヘキ
サンジオール、ハイドロキノン、4,4′−ジヒドロキシ
ジフェニル、ビスフェノールA、1,4−ナフタレンジカ
ルボン酸、2,4−ナフタレンジカルボン酸、2,6−ナフ
タレンジカルボン酸、4,4′−ジフェニルジカルボン
酸、ジフェノキシエタンジカルボン酸、3−ヒドロキシ
プロパン酸、4−ヒドロキシブタン酸、ε−カプロラク
トン、4−ヒドロキシ安息香酸、2−ヒドロキシ−6−
ナフトエ酸等が挙げられる。また、分子間架橋が可能な
構造を有する不飽和ジカルボン酸、不飽和ジオール及び
3官能以上のモノマー成分が共重合されていてもよく、
種々の添加剤等が含まれていてもよい。The present invention will be described in detail below. In the present invention, PET is preferably a homopolymer, but may contain a copolymerization component as long as the effects of the present invention are not impaired. Specific examples of the copolymerization component include isophthalic acid, succinic acid, adipic acid, suberic acid, dodecanedioic acid, azelaic acid, sebacic acid, 1,3-
Propanediol, 1,4-butanediol, 1,6-hexanediol, hydroquinone, 4,4'-dihydroxydiphenyl, bisphenol A, 1,4-naphthalenedicarboxylic acid, 2,4-naphthalenedicarboxylic acid, 2,6- Naphthalenedicarboxylic acid, 4,4'-diphenyldicarboxylic acid, diphenoxyethanedicarboxylic acid, 3-hydroxypropanoic acid, 4-hydroxybutanoic acid, ε-caprolactone, 4-hydroxybenzoic acid, 2-hydroxy-6-
Naphthoic acid and the like can be mentioned. Further, an unsaturated dicarboxylic acid having an intermolecular crosslinkable structure, an unsaturated diol, and a trifunctional or higher functional monomer component may be copolymerized,
Various additives may be included.
【0009】本発明のモノフィラメントは、極限粘度が
0.6以上、好ましくは 0.7〜0.9 で、末端カルボキシル
基濃度が10g当量/106g以下、好ましくは5g当量/10
6g以下のPETで構成される。極限粘度が 0.6未満であ
ると引張強度をはじめとする機械的特性が劣り、好まし
くない。また、末端カルボキシル基濃度が10g当量/10
6gを超えるものでは耐加水分解性が十分でない。The monofilament of the present invention has an intrinsic viscosity
0.6 or more, preferably 0.7 to 0.9, and a terminal carboxyl group concentration of 10 g equivalent / 10 6 g or less, preferably 5 g equivalent / 10
Consists of less than 6 g PET. When the intrinsic viscosity is less than 0.6, mechanical properties such as tensile strength are deteriorated, which is not preferable. Also, the terminal carboxyl group concentration is 10 g equivalent / 10
If it exceeds 6 g, hydrolysis resistance is not sufficient.
【0010】末端カルボキシル基濃度を10g当量/106g
以下にするには、溶融紡糸工程までの任意の工程で、
2,6,2′, 6′−テトライソプロピルジフェニルカ
ルボジイミド(TPC)のようなカルボジイミド化合
物、フェニルグリシジルエーテルのようなエポキシ化合
物等の末端カルボキシル基封鎖剤を添加、反応させれば
よい。例えば、末端カルボキシル基濃度20g当量/106g
以下のPETを用い、TPCをPETに対して 0.1〜3.
0 重量%添加し、エクストルーダーを用いて溶融紡糸す
ればよい。The terminal carboxyl group concentration is 10 g equivalent / 10 6 g
To the following, in any step up to the melt spinning step,
A carbodiimide compound such as 2,6,2 ′, 6′-tetraisopropyldiphenylcarbodiimide (TPC) and a terminal carboxyl group blocking agent such as an epoxy compound such as phenylglycidyl ether may be added and reacted. For example, the terminal carboxyl group concentration is 20 g equivalent / 10 6 g
The following PET is used, and TPC is 0.1 to 3.
It may be added by 0% by weight and melt-spun by using an extruder.
【0011】また、本発明のモノフィラメントには、最
大粒径が5μm 以下で、平均粒径が1μm 以下のPTF
E粉末を全体に対して 0.1〜10重量%含有させることが
必要である。PTFE粉末の最大粒径が5μm を超える
と紡糸時にフィルター詰まりを生じ、平均粒径が1μm
を超えると糸切れが多発する等の問題があり、好ましく
ない。また、PTFE粉末の含有量が 0.1重量%未満で
あると耐屈曲摩耗性向上効果が不十分であり、10重量%
を超えると引張強度はじめとする機械的特性が劣るよう
になり、好ましくない。The monofilament of the present invention has a maximum particle diameter of 5 μm or less and an average particle diameter of 1 μm or less.
It is necessary to contain the E powder in an amount of 0.1 to 10% by weight based on the whole. If the maximum particle size of PTFE powder exceeds 5 μm, filter clogging occurs during spinning and the average particle size is 1 μm.
If it exceeds, there are problems such as frequent yarn breakage, which is not preferable. Further, if the content of the PTFE powder is less than 0.1% by weight, the effect of improving the bending wear resistance is insufficient, and the content is 10% by weight.
If it exceeds, mechanical strength and other mechanical properties will deteriorate, which is not preferable.
【0012】PTFE粉末は、重合から紡糸工程までの
任意の段階でポリエステルに配合することが可能であ
り、マスターチップとして紡糸時にブレンドしてもよ
い。The PTFE powder can be blended with the polyester at any stage from the polymerization to the spinning process, and may be blended as a master chip during spinning.
【0013】[0013]
【作用】本発明のモノフィラメントは、末端カルボキシ
ル基濃度が低いため耐加水分解性に優れ、滑性に優れた
PTFEの微粒子を含有しているため、耐屈曲摩耗性に
優れている。The monofilament of the present invention has excellent resistance to hydrolysis because it has a low concentration of terminal carboxyl groups, and since it contains fine PTFE particles having excellent lubricity, it has excellent resistance to flexing wear.
【0014】[0014]
【実施例】次に、実施例により本発明を具体的に説明す
る。なお、実施例における特性値の測定法等は次のとお
りである。 (1) 極限粘度〔η〕 フェノールと四塩化エタンとの等重量混合液を溶媒と
し、温度20℃で測定した溶液粘度から求めた。 (2) 引張強度 オリエンテック社製テンシロンUTM−4−100 型を用
い、試料長10cm、引張速度10cm/分で測定した。 (3) 耐加水分解性 オートクレーブ中、130 ℃の飽和水蒸気で15日間処理し
たサンプルの〔η〕と引張強度を測定し、処理前の値と
比較して評価した。(処理後の値が、処理前の値の共に
70%以上のものが合格。) (4) 耐屈曲摩耗性 JIS L 1095 7.10.2B法で用いられる糸摩耗試験機
により、モノフィラメントに0.2 g/dの荷重をかけ
て、摩擦速度;60回/分、摩擦角度; 110度、往復距
離;2.5cm 、試料長;20cm、摩擦子;直径 1.0mm硬質鋼
の条件で試験を行い、フィラメントが切断するまでの回
数を測定した。(6000回以上で合格。)EXAMPLES Next, the present invention will be described in detail with reference to examples. In addition, the measuring method of the characteristic value in an Example is as follows. (1) Intrinsic viscosity [η] It was determined from the solution viscosity measured at a temperature of 20 ° C using an equal weight mixture of phenol and ethane tetrachloride as a solvent. (2) Tensile strength Tensilon UTM-4-100 type manufactured by Orientec Co., Ltd. was used for measurement at a sample length of 10 cm and a tensile speed of 10 cm / min. (3) Hydrolysis resistance [η] and tensile strength of a sample treated with saturated steam at 130 ° C for 15 days in an autoclave were measured and evaluated by comparing with the value before treatment. (The value after processing is the same as the value before processing.
70% or more pass. ) (4) Bending abrasion resistance With a yarn abrasion tester used in JIS L 1095 7.10.2B method, a load of 0.2 g / d is applied to the monofilament, the friction speed is 60 times / min, the friction angle is 110 degrees, The test was conducted under the conditions of a round trip distance of 2.5 cm, a sample length of 20 cm, a friction element and a diameter of 1.0 mm hard steel, and the number of times until the filament was cut was measured. (Passed 6000 times or more.)
【0015】実施例1 ビス(β−ヒドロキシエチル)テレフタレート及びその
低重合体(BHET)の存在するエステル化反応缶にモ
ル比1/1.6 のテレフタル酸とエチレングリコールとの
スラリーを連続的に供給し、温度 250℃、圧力0.05kg/
cm2 、滞留時間8時間の条件でエステル化反応を行い、
エステル化反応率が95%のBHETを連続的に得た。こ
のBHET50kgを重合槽に移送し、280 ℃に加熱し、触
媒として三酸化アンチモンをポリエステルを構成する酸
成分1モルに対し2×10-4モルと、平均粒径0.3 μm 、
最大粒径2μm のPTFE粉末(喜多村社製KTL-500F)
の30重量%エチレングリコールスラリーをPTFEの量
が生成ポリエステル組成物の5重量%となる量で添加し
た。その後、徐々に減圧し、280 ℃で最終的に 0.1トル
の減圧下で 2.5時間重縮合反応を行い、〔η〕0.68のポ
リエステルチップを得た。このチップを減圧下、180 ℃
で固相重合することにより、〔η〕0.85、末端カルボキ
シル基濃度15.0g当量/106gの固相重合ポリエステルチ
ップを得た。得られたポリエステルチップに2重量%の
TPCを添加してエクストルーダー型溶融紡糸機に供給
し、孔径 2.4mm、孔数6の紡糸口金(直径90mm)を用
い、速度33m/分、温度 310℃で紡糸し、80℃の水浴で
急冷し、6分割して巻き取り未延伸糸を得た。得られた
未延伸糸を 5.7倍に延伸し、295 ℃で熱処理することに
より、直径0.4mm のモノフィラメントを得た。Example 1 A slurry of terephthalic acid and ethylene glycol in a molar ratio of 1 / 1.6 was continuously fed to an esterification reaction vessel containing bis (β-hydroxyethyl) terephthalate and its low polymer (BHET). , Temperature 250 ℃, pressure 0.05kg /
Perform the esterification reaction under the conditions of cm 2 and residence time of 8 hours,
BHET having an esterification reaction rate of 95% was continuously obtained. 50 kg of this BHET was transferred to a polymerization tank and heated to 280 ° C., and 2 × 10 −4 mol of antimony trioxide as a catalyst was added to 1 mol of the acid component constituting the polyester, and the average particle size was 0.3 μm.
PTFE powder with a maximum particle size of 2 μm (KTL-500F manufactured by Kitamura)
30% by weight ethylene glycol slurry was added in an amount such that the amount of PTFE was 5% by weight of the resulting polyester composition. Then, the pressure was gradually reduced, and the polycondensation reaction was finally performed at 280 ° C. under a reduced pressure of 0.1 torr for 2.5 hours to obtain a polyester chip of [η] 0.68. 180 ° C under reduced pressure
By solid-state polymerization in (1), solid-state polymerized polyester chips having [η] 0.85 and terminal carboxyl group concentration of 15.0 g equivalent / 10 6 g were obtained. 2% by weight of TPC was added to the obtained polyester chips and the mixture was supplied to an extruder type melt spinning machine, and a spinneret (diameter 90 mm) having a hole diameter of 2.4 mm and 6 holes was used, a speed of 33 m / min, and a temperature of 310 ° C. Was spun, quenched in a water bath at 80 ° C., and divided into 6 to obtain undrawn yarn. The obtained undrawn yarn was drawn 5.7 times and heat-treated at 295 ° C. to obtain a monofilament having a diameter of 0.4 mm.
【0016】実施例2〜7 実施例1において、PTFE粉末の粒径、添加量を表1
に示したように変えた以外は、実施例1と同様に実施し
た。Examples 2 to 7 In Example 1, the particle size and the addition amount of the PTFE powder are shown in Table 1.
Example 1 was carried out in the same manner as in Example 1 except that the changes were made as shown in FIG.
【0017】実施例8〜9 実施例1において、TPCの添加量を表1に示したよう
に変えた以外は、実施例1と同様に実施した。Examples 8 to 9 The procedure of Example 1 was repeated, except that the amount of TPC added was changed as shown in Table 1.
【0018】実施例 10 実施例1において、TPCの代わりにフェニルグリシジ
ルエーテルを用いた以外は、実施例1と同様に実施し
た。Example 10 The procedure of Example 1 was repeated, except that phenylglycidyl ether was used instead of TPC.
【0019】実施例 11 実施例1において、〔η〕0.65のPETを用いた以外
は、実施例1と同様に実施した。Example 11 The procedure of Example 1 was repeated, except that PET having an [η] of 0.65 was used.
【0020】比較例1〜4 実施例1において、PTFE粉末の粒径、添加量を表1
に示したように変えた以外はは、実施例1と同様に実施
した。Comparative Examples 1 to 4 In Example 1, the particle size and the addition amount of the PTFE powder are shown in Table 1.
The same procedure as in Example 1 was carried out except that the changes were made as shown in FIG.
【0021】比較例5 実施例1において、TPCの添加量を表1に示したよう
に変えた以外は、実施例1と同様に実施した。Comparative Example 5 Example 1 was repeated except that the amount of TPC added was changed as shown in Table 1.
【0022】比較例6 実施例1において、〔η〕0.55のPETを用いた以外
は、実施例1と同様に実施した。Comparative Example 6 The procedure of Example 1 was repeated, except that PET having [η] 0.55 was used.
【0023】上記の実施例及び比較例で得られたモノフ
ィラメントについて、耐加水分解性及び耐屈曲摩耗性を
測定した結果を表1に示す。Table 1 shows the results obtained by measuring the hydrolysis resistance and flex wear resistance of the monofilaments obtained in the above Examples and Comparative Examples.
【0024】[0024]
【表1】 [Table 1]
【0025】[0025]
【発明の効果】本発明によれば、耐加水分解性及び耐屈
曲摩耗性に優れた抄紙カンバス用に好適なポリエステル
モノフィラメントが提供される。また、本発明のモノフ
ィラメントは、操業性よく製造することができる。Industrial Applicability According to the present invention, there is provided a polyester monofilament which is excellent in hydrolysis resistance and bending abrasion resistance and is suitable for papermaking canvas. Further, the monofilament of the present invention can be manufactured with good operability.
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Claims (1)
濃度10g当量/106g以下のポリエチレンテレフタレート
に、最大粒径5μm 以下、平均粒径1μm 以下のポリテ
トラフルオロエチレン樹脂粉末を全体に対して 0.1〜10
重量%含有させた組成物からなるポリエステルモノフィ
ラメント。1. Polytetrafluoroethylene resin powder having a maximum particle size of 5 μm or less and an average particle size of 1 μm or less is added to polyethylene terephthalate having an intrinsic viscosity of 0.6 or more and a terminal carboxyl group concentration of 10 g equivalent / 10 6 g or less based on the total amount of 0.1. ~Ten
A polyester monofilament composed of a composition containing 100% by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31906193A JPH07145511A (en) | 1993-11-24 | 1993-11-24 | Polyester monofilament |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31906193A JPH07145511A (en) | 1993-11-24 | 1993-11-24 | Polyester monofilament |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07145511A true JPH07145511A (en) | 1995-06-06 |
Family
ID=18106066
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31906193A Pending JPH07145511A (en) | 1993-11-24 | 1993-11-24 | Polyester monofilament |
Country Status (1)
Country | Link |
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JP (1) | JPH07145511A (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0779382A1 (en) * | 1995-12-15 | 1997-06-18 | Hoechst Trevira GmbH & Co. KG | Hydrolysis resistant polyester fibres and filaments, masterbatches and production process of polyester fibres and filaments |
WO1999057346A1 (en) * | 1998-05-02 | 1999-11-11 | Dyneon Gmbh & Co.Kg | Emulsion polytetrafluorethylene micro-powder as an additive for fibre-forming plastics |
US6451914B1 (en) | 1999-04-26 | 2002-09-17 | Dyneon Gmbh & Co. Kg | Emulsion polytetrafluoroethylene micropowder additive for fiber-forming plastics |
EP1551605A1 (en) * | 2002-10-01 | 2005-07-13 | Shamrock Technologies, Inc. | Method of making synthetic melt spun fibres with polytetrafluoroethylene |
US7758959B2 (en) * | 2003-06-27 | 2010-07-20 | Rhodia Chimie | Synthetic, flame-resistant yarns, fibres and filaments |
WO2013047625A1 (en) * | 2011-09-28 | 2013-04-04 | 株式会社リケン | Resin composition and sliding member using same |
CN110139954A (en) * | 2016-12-27 | 2019-08-16 | Sabic环球技术有限责任公司 | Fiber comprising fibrillation reinforcing material |
JP2020070536A (en) * | 2018-10-29 | 2020-05-07 | ユニチカ株式会社 | Thermoplastic fiber having excellent abrasion resistance and method for producing the same |
CN113430656A (en) * | 2021-06-25 | 2021-09-24 | 江苏恒力化纤股份有限公司 | Method for preparing ultra-high strength polyester industrial yarn |
CN113430658A (en) * | 2021-06-25 | 2021-09-24 | 江苏恒力化纤股份有限公司 | Low-pressure spinning method of polyester industrial yarn |
CN113430657A (en) * | 2021-06-25 | 2021-09-24 | 江苏恒力化纤股份有限公司 | Method for reducing spinning temperature of polyester industrial yarn |
CN114481335A (en) * | 2021-12-17 | 2022-05-13 | 桐昆集团浙江恒通化纤有限公司 | High-strength sunlight-resistant anti-aging terylene pre-oriented yarn for curtain and preparation method thereof |
-
1993
- 1993-11-24 JP JP31906193A patent/JPH07145511A/en active Pending
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0779382A1 (en) * | 1995-12-15 | 1997-06-18 | Hoechst Trevira GmbH & Co. KG | Hydrolysis resistant polyester fibres and filaments, masterbatches and production process of polyester fibres and filaments |
US5811508A (en) * | 1995-12-15 | 1998-09-22 | Hoechst Trevira Gmbh & Co Kg | Hydrolysis-resistant polyester fibers and filaments, masterbatches and processes for the production of polyester fibers and filaments |
WO1999057346A1 (en) * | 1998-05-02 | 1999-11-11 | Dyneon Gmbh & Co.Kg | Emulsion polytetrafluorethylene micro-powder as an additive for fibre-forming plastics |
US6451914B1 (en) | 1999-04-26 | 2002-09-17 | Dyneon Gmbh & Co. Kg | Emulsion polytetrafluoroethylene micropowder additive for fiber-forming plastics |
EP1551605A1 (en) * | 2002-10-01 | 2005-07-13 | Shamrock Technologies, Inc. | Method of making synthetic melt spun fibres with polytetrafluoroethylene |
EP1551605A4 (en) * | 2002-10-01 | 2006-06-07 | Shamrock Tech Inc | Method of making synthetic melt spun fibres with polytetrafluoroethylene |
US7758959B2 (en) * | 2003-06-27 | 2010-07-20 | Rhodia Chimie | Synthetic, flame-resistant yarns, fibres and filaments |
JP5568184B2 (en) * | 2011-09-28 | 2014-08-06 | 株式会社リケン | Seal ring |
WO2013047625A1 (en) * | 2011-09-28 | 2013-04-04 | 株式会社リケン | Resin composition and sliding member using same |
US9085690B2 (en) | 2011-09-28 | 2015-07-21 | Kabushiki Kaisha Riken | Resin composition and sliding member using same |
CN110139954A (en) * | 2016-12-27 | 2019-08-16 | Sabic环球技术有限责任公司 | Fiber comprising fibrillation reinforcing material |
JP2020070536A (en) * | 2018-10-29 | 2020-05-07 | ユニチカ株式会社 | Thermoplastic fiber having excellent abrasion resistance and method for producing the same |
CN113430656A (en) * | 2021-06-25 | 2021-09-24 | 江苏恒力化纤股份有限公司 | Method for preparing ultra-high strength polyester industrial yarn |
CN113430658A (en) * | 2021-06-25 | 2021-09-24 | 江苏恒力化纤股份有限公司 | Low-pressure spinning method of polyester industrial yarn |
CN113430657A (en) * | 2021-06-25 | 2021-09-24 | 江苏恒力化纤股份有限公司 | Method for reducing spinning temperature of polyester industrial yarn |
CN113430656B (en) * | 2021-06-25 | 2022-05-06 | 江苏恒力化纤股份有限公司 | Method for preparing ultra-high strength polyester industrial yarn |
CN113430657B (en) * | 2021-06-25 | 2022-05-24 | 江苏恒力化纤股份有限公司 | Method for reducing spinning temperature of polyester industrial yarn |
CN114481335A (en) * | 2021-12-17 | 2022-05-13 | 桐昆集团浙江恒通化纤有限公司 | High-strength sunlight-resistant anti-aging terylene pre-oriented yarn for curtain and preparation method thereof |
CN114481335B (en) * | 2021-12-17 | 2023-06-27 | 桐昆集团浙江恒通化纤有限公司 | High-strength sun-resistant anti-aging polyester pre-oriented yarn for curtain and preparation method thereof |
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