JP4934853B2 - Method for producing fluorine resin monofilament - Google Patents

Method for producing fluorine resin monofilament Download PDF

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JP4934853B2
JP4934853B2 JP2007087990A JP2007087990A JP4934853B2 JP 4934853 B2 JP4934853 B2 JP 4934853B2 JP 2007087990 A JP2007087990 A JP 2007087990A JP 2007087990 A JP2007087990 A JP 2007087990A JP 4934853 B2 JP4934853 B2 JP 4934853B2
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monofilament
etfe
yarn
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朗 柵木
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Toray Monofilament Co Ltd
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Description

本発明は、弗素系樹脂が有する優れた耐熱性、耐薬品性、耐溶剤性、電気特性、摩擦特性、非粘着性、耐候性などの特質を遺憾なく発揮できると共に、長さ方向の線径変動が従来のエチレン−テトラフルオロエチレン共重合体からなるモノフィラメントに比べてはるかに小さく、工業織物の少なくとも一部に使用した場合に、筋、縞、段などの目ずれの発生を効果的に抑えることができるエチレン−テトラフルオロエチレン共重合体からなるモノフィラメントの製造方法に関するものである。 In the present invention, the excellent heat resistance, chemical resistance, solvent resistance, electrical characteristics, friction characteristics, non-adhesiveness, weather resistance, etc. of the fluorine-based resin can be fully exhibited, and the wire diameter in the length direction Fluctuation is much smaller than conventional monofilaments made of ethylene-tetrafluoroethylene copolymer, and effectively suppresses the occurrence of misalignments such as streaks, stripes, steps, etc. when used on at least part of industrial fabrics ethylene can be - are those concerning the Monofiramen bets manufacturing how consisting tetrafluoroethylene copolymer.

従来から、ポリアミド樹脂、ポリエステル樹脂、およびポリフェニレンサルファイド樹脂などのいわゆる汎用エンプラまたはスーパーエンプラと称される熱可塑性樹脂からなるモノフィラメントは、耐熱性、強度、剛性などの優れた特性を有することから、各種の産業資材用途に好ましく使用されてきた。   Conventionally, monofilaments made of thermoplastic resins called general-purpose engineering plastics or super engineering plastics such as polyamide resins, polyester resins, and polyphenylene sulfide resins have excellent characteristics such as heat resistance, strength, and rigidity. It has been preferably used for industrial materials.

また、近年では特に優れた耐熱性、耐薬品性、耐溶剤性、電気特性、摩擦特性、非粘着性、耐候性などの特質を有する弗素系樹脂が注目され、ポリフッ化ビニリデン樹脂などからなるモノフィラメントが、水産資材用途などに好ましく使用されている。   In recent years, fluorine resins having characteristics such as excellent heat resistance, chemical resistance, solvent resistance, electrical characteristics, friction characteristics, non-adhesiveness, and weather resistance have attracted attention, and monofilaments made of polyvinylidene fluoride resin, etc. However, it is preferably used for fishery materials.

一方、工業織物の分野においても、優れた特質を有する弗素系樹脂からなるモノフィラメントの要求が高まってきたが、特に製紙業界の製紙用具用織物用途に使用されるモノフィラメントは、織物の均質性を得るために、とりわけ長さ方向の線径の均一性が求められており、線径変動の小さいモノフィラメントを得るための種々の検討が従来よりなされてきた。   On the other hand, in the field of industrial textiles, there has been an increasing demand for monofilaments made of fluorine-based resins having excellent characteristics, but in particular, monofilaments used for textile applications for papermaking tools in the papermaking industry obtain the homogeneity of the textiles. Therefore, in particular, uniformity of the wire diameter in the length direction is required, and various studies have been made in the past to obtain a monofilament with small wire diameter fluctuation.

かかる線径変動の小さいモノフィラメントに関する従来技術としては、(A)冷却を均一に行うことによって得られる糸斑のないモノフィラメントおよびその製造方法(例えば、特許文献1参照)、および(B)線径変動率の小さい溶融液晶性ポリエステルからなる芯鞘型複合繊維およびその製造方法(例えば、特許文献2参照)などがすでに提案されている。   As prior art relating to such monofilaments having small wire diameter fluctuations, (A) monofilaments free from yarn unevenness obtained by performing cooling uniformly and a method for producing the same (for example, see Patent Document 1), and (B) wire diameter fluctuation rate A core-sheath type composite fiber made of a molten liquid crystalline polyester having a small size and a method for producing the same (for example, see Patent Document 2) have already been proposed.

また、(C)ミスト冷却によって得られる線径変動率が小さい高融点モノフィラメントおよびその製造方法(例えば、特許文献3参照)、および(D)ミスト冷却によって得られる線径変動率が小さいポリオレフィンモノフィラメントおよびその製造方法(例えば、特許文献4参照)についてもすでに提案されている。   In addition, (C) a high melting point monofilament having a small wire diameter variation rate obtained by mist cooling and a method for producing the same (for example, see Patent Document 3), and (D) a polyolefin monofilament having a small wire diameter variation rate obtained by mist cooling and A manufacturing method thereof (for example, see Patent Document 4) has already been proposed.

しかしながら、上記(A)、(B)、(C)および(D)で提案されている従来技術は、いずれも目的とする特性を付与することについては所期の効果が認められるものの、製紙業界の製紙用具用織物用途に使用されるモノフィラメントなどのように、より小さな線径変動が要求される用途においては、いずれもその効果は必ずしも満足できるものとはいいにくいものであった。   However, although the conventional techniques proposed in the above (A), (B), (C) and (D) are all expected to give the desired characteristics, the paper industry In applications where a smaller variation in wire diameter is required, such as monofilaments used in textile applications for papermaking tools, the effects are not necessarily satisfactory.

また、これらの従来技術に、弗素系樹脂、特にエチレン−テトラフルオロエチレン共重合体を適用したとしても、線径の長さ方向の線径変動率を5%以下に押さえたモノフィラメントを得ることはできなかった。
特開平11−93015号公報 特開平9−296324号公報 特開2001−279522号公報 特開2002−88568号公報
Moreover, even if a fluorine-based resin, particularly an ethylene-tetrafluoroethylene copolymer, is applied to these conventional techniques, it is possible to obtain a monofilament in which the wire diameter variation rate in the length direction of the wire diameter is suppressed to 5% or less. could not.
Japanese Patent Laid-Open No. 11-93015 JP-A-9-296324 JP 2001-279522 A JP 2002-88568 A

本発明は、上述した従来技術における問題点の解決を課題として検討した結果、達成されたものである。   The present invention has been achieved as a result of examining the solution of the problems in the above-described prior art as an object.

したがって、本発明の目的は、弗素系樹脂が有する優れた耐熱性、耐薬品性、耐溶剤性、電気特性、摩擦特性、非粘着性、耐候性などの特質を遺憾なく発揮できると共に、長さ方向の線径変動が従来のエチレン−テトラフルオロエチレン共重合体からなるモノフィラメントに比べてはるかに小さく、工業織物の少なくとも一部に使用した場合に、筋、縞、段などの目ずれの発生を効果的に抑えることができるエチレン−テトラフルオロエチレン共重合体からなるモノフィラメントの製造方法を提供することにある。 Therefore, the object of the present invention is to display the characteristics such as excellent heat resistance, chemical resistance, solvent resistance, electrical characteristics, friction characteristics, non-adhesiveness, weather resistance, etc. possessed by the fluorine-based resin without length. The wire diameter fluctuation in the direction is much smaller than that of the conventional monofilament made of ethylene-tetrafluoroethylene copolymer, and when used in at least part of industrial fabric, streaks, streaks, steps, etc. are generated. ethylene can be effectively prevented - to provide a manufacturing how the Monofiramen bets consisting tetrafluoroethylene copolymer.

上記の目的を達成するための本発明の弗素系樹脂モノフィラメントの製造方法は、エチレン−テトラフルオロエチレン共重合体を溶融紡糸・冷却するに際して、口金面直下から冷却媒体浴中にかけての紡出糸条通路にその少なくとも下面が冷却媒体中に浸漬するよう筒状体を配置すると共にこの筒状体中へ不活性ガスを流通せしめ、口金から溶融押出した紡出糸条を直ちに前記筒状体を経て冷却媒体浴へと導いて冷却し、次いで得られた未延伸糸を5〜15m/分の速度で引き取り、引き続き少なくとも1段以上の多段で延伸または延伸/熱セット処理を行うと共に、その際の最終引き取り速度を25〜75m/分で行うことを特徴とする。 In order to achieve the above object, the method for producing a fluorine-based resin monofilament according to the present invention comprises a spinning yarn from directly under a die surface to a cooling medium bath when melt spinning and cooling an ethylene-tetrafluoroethylene copolymer. A cylindrical body is disposed in the passage so that at least its lower surface is immersed in the cooling medium, and an inert gas is circulated into the cylindrical body, and the spun yarn melt-extruded from the die is immediately passed through the cylindrical body. Then, it is led to a cooling medium bath and cooled, and then the obtained undrawn yarn is taken up at a speed of 5 to 15 m / min, and subsequently drawn or drawn / heat set in multiple stages of at least one stage. The final take-up speed is 25 to 75 m / min.

本発明の製造方法で得られるエチレン−テトラフルオロエチレン共重合体からなる弗素系樹脂モノフィラメントは、長さ方向の線径変動が、従来のエチレン−テトラフルオロエチレン共重合体からなるモノフィラメントに比べて飛躍的に改良されたものであることから、工業織物とした場合に筋、縞、段などの目ずれの発生を効果的に抑えることができ、弗素系樹脂が有する優れた耐熱性、耐薬品性、耐溶剤性、電気特性、摩擦特性、非粘着性、耐候性などの効果を良好に維持した工業織物、特に製紙用具用織物やフィルター用織物およびベルト用織物を得ることができる。 The fluorine-based resin monofilament made of an ethylene-tetrafluoroethylene copolymer obtained by the production method of the present invention has a dramatic change in the diameter in the length direction as compared with a conventional monofilament made of an ethylene-tetrafluoroethylene copolymer. Because it has been improved, it is possible to effectively suppress the occurrence of misalignment such as streaks, stripes, and steps when using industrial fabrics, and the excellent heat resistance and chemical resistance of fluorine-based resins. In addition, it is possible to obtain industrial fabrics, particularly papermaking tool fabrics, filter fabrics, and belt fabrics, which maintain good effects such as solvent resistance, electrical properties, friction properties, non-adhesiveness, and weather resistance.

以下に本発明について詳細に説明する。   The present invention is described in detail below.

本発明のエチレン−テトラフルオロエチレン共重合体からなるモノフィラメント(以下ETFEモノフィラメントと記す)は、その線径変動率が5%以下と、従来のETFEモノフィラメントに比較してきわめて小さいことを特徴とするものである。   The monofilament made of the ethylene-tetrafluoroethylene copolymer of the present invention (hereinafter referred to as ETFE monofilament) has a linear diameter fluctuation rate of 5% or less, which is extremely small compared to a conventional ETFE monofilament. It is.

ここで、本発明のETFEモノフィラメントの長さ方向の線径変動率(%)とは、モノフィラメント試料について、まずアンリツ製レーザー外径測定機KG601Aに準じた外径測定機を使用して、測定速度15m/分、測定間隔0.1秒/回、測定点1024回の条件で線径を測定し、さらにキーエンス製データー処理機NR−250&PCに準じたデーター処理機を使用して求めた値である。   Here, the variation rate (%) in the length direction of the ETFE monofilament of the present invention is the measurement speed of the monofilament sample using an outer diameter measuring machine according to an Anritsu laser outer diameter measuring machine KG601A. The wire diameter was measured under the conditions of 15 m / min, measurement interval 0.1 sec / time, and 1024 measurement points, and further obtained using a data processor according to KEYENCE data processor NR-250 & PC. .

本測定法は、レーザー散乱光によってモノフィラメントの外径を長径、短径を含めて測定するものであり、従来のマルチフィラメントの繊径変動を誘電率の変化から求めた断面積の変動で測定する方法とは異なるものである。   In this measurement method, the outer diameter of the monofilament is measured by laser scattered light, including the major and minor diameters, and the variation in the diameter of the conventional multifilament is measured by the variation in the cross-sectional area obtained from the change in the dielectric constant. It is different from the method.

次に、本測定条件は、モノフィラメントの外径測定を長さ方向に約2.5cm毎に1回、約25mの長さにわたって行い、その測定点1024回分のデーターを処理して標準偏差(σ)を求め、その結果をJIS−Z8101−1で定義される変動係数[標準偏差(σ)/平均値×100]で表した線径変動率(%)を評価するものである。   Next, the measurement condition is that the outer diameter of the monofilament is measured once every about 2.5 cm in the length direction over a length of about 25 m, and the data for 1024 measurement points is processed to obtain the standard deviation (σ ) And the wire diameter variation rate (%) expressed as a coefficient of variation [standard deviation (σ) / average value × 100] defined in JIS-Z8101-1.

なお、このような測定法で測定した本発明のETFEモノフィラメントの長さ方向の線径変動率は、5%以下、好ましくは4%以下、更に好ましくは3%以下である。   It should be noted that the wire diameter variation rate in the length direction of the ETFE monofilament of the present invention measured by such a measurement method is 5% or less, preferably 4% or less, more preferably 3% or less.

上記のように線径変動率がきわめて小さい本発明のETFEモノフィラメントは、工業織物とした場合に、筋、縞、段などの目ずれの発生を効果的に抑えることができることから、線径変動率が問題とされる各種の工業織物用途に好ましく使用することができるが、なかでも製紙用具用織物やフィルター用織物およびベルト用織物として好ましく適用することができ、その場合には従来にない優れた効果を発現することができる。   As described above, the ETFE monofilament of the present invention having a very small wire diameter variation rate can effectively suppress the occurrence of misalignment such as streaks, stripes, steps, etc., when used as an industrial fabric. Can be preferably used for various industrial textile applications, which can be preferably used as a papermaking tool fabric, a filter fabric, and a belt fabric, and in that case, it has an unprecedented superiority. An effect can be expressed.

本発明のETFEモノフィラメントを形成するポリマーは、上記のようなモノフィラメントの特性を満足するエチレン−テトラフルオロエチレン共重合体樹脂であれば特に限定されるものではない。   The polymer that forms the ETFE monofilament of the present invention is not particularly limited as long as it is an ethylene-tetrafluoroethylene copolymer resin that satisfies the above-described monofilament characteristics.

なお、本発明で用いる上記エチレン−テトラフルオロエチレン共重合体樹脂には、必要に応じて、例えば顔料、染料、耐光剤、紫外線吸収剤、酸化防止剤、結晶化抑制剤および可塑剤などの各種添加剤を、目的とする性能を阻害しない範囲で、その重合行程、重合後あるいは紡糸直前に添加することができる。   The ethylene-tetrafluoroethylene copolymer resin used in the present invention includes various kinds of pigments, dyes, light-resistant agents, ultraviolet absorbers, antioxidants, crystallization inhibitors, plasticizers, and the like as necessary. Additives can be added in the polymerization process, after polymerization, or just before spinning as long as the desired performance is not impaired.

上記の特性を有する本発明のETFEモノフィラメントは、以下に説明する方法により効率的に製造することができる。   The ETFE monofilament of the present invention having the above characteristics can be efficiently produced by the method described below.

まず、上記ETFEモノフィラメントを溶融紡糸するに際しては、ETFE樹脂を先端に計量用ギヤポンプとスピンブロックを有するエクストルーダー型紡糸機に供給し、紡糸温度を285〜325℃で溶融混練した後、その溶融物を紡糸口金から溶融押出す。   First, when melt spinning the ETFE monofilament, an ETFE resin is supplied to an extruder type spinning machine having a metering gear pump and a spin block at the tip, melted and kneaded at a spinning temperature of 285 to 325 ° C., and then melted. Is melt extruded from the spinneret.

このように溶融押出した紡出糸条を冷却媒体浴に導いて冷却するに際しては、口金面直下から冷却媒体浴中にかけての紡出糸条通路にその少なくとも下面が冷却媒体中に浸漬するよう筒状体を配置して、この筒状体中へ不活性ガスを流通せしめ、紡出糸条を直ちに前記筒状体を経て冷却媒体浴へと導いて冷却し、次いで得られた未延伸糸を5〜15m/分の速度で引き取って未延伸糸を得る。   When the melt-extruded spun yarn is guided to the cooling medium bath and cooled, the tube is so arranged that at least the lower surface thereof is immersed in the cooling medium in the spun yarn passage from just below the base surface to the cooling medium bath. An inert gas is circulated through the cylindrical body, the spun yarn is immediately cooled through the cylindrical body to the cooling medium bath, and the undrawn yarn obtained is then cooled. An undrawn yarn is obtained by taking up at a speed of 5 to 15 m / min.

この筒状体中へ不活性ガスを流通せしめることにより、ポリマーの酸化を抑制し、口金孔周辺に滞留する熱変性異物等を減少させ、安定した線径の未延伸糸を得ることが可能となる。さらに、紡糸口金にはニツケル合金製口金を用いることによって、口金孔周辺に滞留する熱変性異物等の離形効果が向上する。   By allowing an inert gas to flow through the cylindrical body, it is possible to suppress the oxidation of the polymer, reduce heat-denatured foreign matter and the like remaining around the mouthpiece hole, and obtain an unstretched yarn with a stable wire diameter. Become. Further, by using a nickel alloy die for the spinneret, the effect of releasing the heat-denatured foreign matter staying around the die hole is improved.

また、未延伸糸を5〜15m/分の速度で引き取ることが重要であり、引取速度が5m/分より遅い場合は、未延伸糸が冷却媒体浴内で蛇行してしまい線経バラツキを悪化させる傾向にあるため好ましくないばかりか、隣同士の未延伸糸条が融着してしまい得ることができなくなる。   In addition, it is important to take the undrawn yarn at a speed of 5 to 15 m / min. If the take-up speed is slower than 5 m / min, the undrawn yarn will meander in the cooling medium bath, and the line-thickness variation will be worsened. This is not preferable because it tends to cause the unstretched yarns adjacent to each other to be fused.

一方、未延伸糸の引取速度が15m/分より速い場合は、未延伸糸が冷却媒体浴内で引き延ばされてしまい真円性が損なわれ、これまた本発明の目的とする均一な線径を有するモノフィラメントが得られにくい傾向となるため好ましくないばかりか、未延伸糸が途中で断糸してしまい得ることができなくなる。   On the other hand, when the take-up speed of the undrawn yarn is higher than 15 m / min, the undrawn yarn is stretched in the cooling medium bath and the roundness is impaired. Since it tends to be difficult to obtain a monofilament having a diameter, it is not preferable, and an undrawn yarn cannot be cut halfway.

次に、得られた未延伸糸を、少なくとも1段以上の多段で延伸または延伸/熱セット処理を行うと共に、その際の最終引き取り速度を25〜75m/分で行いETFEモノフィラメントを得る。   Next, the obtained undrawn yarn is drawn or drawn / heat set in multiple stages of at least one stage, and the final take-up speed at that time is 25 to 75 m / min to obtain an ETFE monofilament.

所望の強伸度や熱収縮特性を得るために、少なくとも1段以上の多段で延伸する。安定な延伸性を得るためには、延伸温度は、一段目の延伸温度よりも高い温度に二段目は設定し、かつ総合延伸倍率が4.0〜6.0倍になるように行う。   In order to obtain desired strength and heat shrinkage properties, the film is stretched in at least one or more stages. In order to obtain stable stretchability, the stretching temperature is set to a temperature higher than the first stretching temperature, and the total stretching ratio is set to 4.0 to 6.0 times.

これは、延伸倍率が低すぎると得られるETFEモノフィラメントに所望の強伸度や熱収縮特性が得られにくくなり、逆に高すぎると糸切れの原因となりやすいためであり、より良好な熱収縮特性を得るためには、さらに4.5〜5.5倍であることが好ましい。   This is because if the draw ratio is too low, it is difficult to obtain the desired strength and heat shrinkage characteristics of the ETFE monofilament, and conversely, if it is too high, it is likely to cause thread breakage, and better heat shrinkage characteristics. In order to obtain, it is preferable that it is 4.5 to 5.5 times.

また、延伸温度が低すぎると延伸時に高い張力が掛かり、糸切れの原因となりやすく、逆に高すぎるとETFE樹脂の融点に近くなり、延伸浴内で糸切れが発生しやすくなるため、延伸温度を80〜200℃とすることが必要であり、さらには70〜200℃とすることが好ましい。   Also, if the stretching temperature is too low, high tension is applied during stretching, which tends to cause thread breakage. Conversely, if the stretching temperature is too high, the melting point of the ETFE resin is close, and thread breakage tends to occur in the stretching bath. Must be 80 to 200 ° C., more preferably 70 to 200 ° C.

ここで、延伸工程で使用する熱媒体としては、ETFEモノフィラメントの表面から容易に除去することができ、かつETFEモノフィラメントに対して物理的、化学的な変化を本質的に与えることがない物質であれば如何なるものをも使用することができるが、本発明は比較的低い温度で一段目の延伸を行うことから、経済的には温水浴または加熱空気浴が好適である。また、二段目の延伸工程で使用する熱媒体としては、一般的に、高沸点の不活性液体を満たした液体浴、空気炉、不活性ガス炉、赤外線炉および高周波炉などの加熱装置が好適である。   Here, the heating medium used in the stretching process may be a substance that can be easily removed from the surface of the ETFE monofilament and that does not essentially give a physical or chemical change to the ETFE monofilament. Any method can be used, but the present invention performs the first-stage stretching at a relatively low temperature, and therefore, a warm water bath or a heated air bath is suitable economically. In addition, as a heat medium used in the second stretching step, generally, a heating apparatus such as a liquid bath filled with an inert liquid having a high boiling point, an air furnace, an inert gas furnace, an infrared furnace, and a high-frequency furnace is used. Is preferred.

少なくとも1段以上の多段で延伸されたETFEモノフィラメントは、延伸工程で得られた所望の強伸度や熱収縮特性をさらに向上させ、かつそれを保持するために、必要に応じて熱セット処理に供されるが、このセット処理の温度は120〜240℃とすることが必要であり、さらには140〜220℃とすることが好ましい。   The ETFE monofilament stretched in at least one or more stages is subjected to heat setting treatment as necessary in order to further improve and maintain the desired strength and heat shrinkage properties obtained in the stretching process. Although it is provided, it is necessary that the temperature of this set process be 120 to 240 ° C, and further 140 to 220 ° C is preferable.

また、セット倍率は0.85〜1.20倍で、所望の熱収縮特性を得るために必要な条件である。   The set magnification is 0.85 to 1.20 times, which is a necessary condition for obtaining desired heat shrinkage characteristics.

このセット倍率が低すぎると、得られるETFEモノフィラメントの熱収縮率が低くなるため、工業織物の熱セット後の納まりが悪くなるばかりか、筋、縞、段などの目ずれ等も発生しやすくなり、逆にセット倍率が高すぎると、糸切れの原因となりやすいため、好ましくはセット倍率を0.90〜1.05倍とすることが必要であり、さらには0.95〜1.01倍とすることがさらに好ましい。   If this set magnification is too low, the thermal shrinkage of the resulting ETFE monofilament will be low, and not only will the industrial fabrics not be stored after heat setting, but also misalignments such as streaks, stripes and steps will easily occur. On the contrary, if the set magnification is too high, thread breakage is likely to occur. Therefore, it is necessary to set the set magnification to 0.90 to 1.05 times, preferably 0.95 to 1.01 times. More preferably.

ここで、セット処理工程で使用する加熱装置としては、上述した二段目の延伸と同様な高沸点の不活性液体を満たした液体浴、空気炉、不活性ガス炉、赤外線炉および高周波炉などを挙げることができる。   Here, as the heating device used in the set processing step, a liquid bath filled with an inert liquid having a high boiling point similar to the above-described second-stage stretching, an air furnace, an inert gas furnace, an infrared furnace, a high-frequency furnace, etc. Can be mentioned.

そして、セット処理されたETFEモノフィラメントは、その表面に必要に応じて油剤が付与され、その後巻具に巻き取られる。   Then, the set ETFE monofilament is provided with an oil agent on the surface as needed, and then wound around a winding tool.

最終引き取り速度は25〜75m/分で行うことが好ましい。   The final take-up speed is preferably 25 to 75 m / min.

上記の通り、未延伸糸を5〜15m/分の速度で引き取った後、所望の強伸度や熱収縮特性を得るために少なくとも1段以上の多段で延伸または延伸/熱セット処理を行うことで長さ方向の線径変動が小さいETFEモノフィラメントを得ることができる。   As described above, after drawing the undrawn yarn at a speed of 5 to 15 m / min, the drawing or drawing / heat setting treatment is performed in multiple stages of at least one stage in order to obtain the desired strength and heat shrinkage characteristics. Thus, an ETFE monofilament with a small variation in the wire diameter in the length direction can be obtained.

この最終引き取り速度は未延伸糸引き取り速度に延伸倍率または延伸倍率/熱セット処理倍率を掛け合わせて求められるが、最終引き取り速度が25m/分より遅い場合は、延伸斑の原因となり、均一な線径を有するモノフィラメントが得られにくい傾向となるため好ましくないばかりか、所望の強伸度や熱収縮特性が不均一となりやすくなる。   This final take-up speed can be obtained by multiplying the undrawn yarn take-up speed by the draw ratio or draw ratio / heat setting treatment ratio, but if the final take-up speed is lower than 25 m / min, it will cause stretch spots and a uniform line. Since it tends to be difficult to obtain monofilaments having a diameter, it is not preferable, and the desired strength and heat shrinkage characteristics tend to be uneven.

また、最終引き取り速度が75m/分より速い場合は、糸切れの原因となりやすいためであり、より良好な均一な線径や所望の強伸度および熱収縮特性を得るには、最終引き取り速度は30〜65m/分であることが好ましい。   Further, when the final take-up speed is higher than 75 m / min, it is easy to cause thread breakage. To obtain a better uniform wire diameter and desired strength and heat shrinkage characteristics, the final take-up speed is It is preferable that it is 30-65 m / min.

こうして得られた本発明のETFEモノフィラメントは、従来のETFEモノフィラメントにはない小さい線径変動率のため、このETFEモノフィラメントを工業織物の少なくとも一部に使用することが可能となるのである。   The ETFE monofilament of the present invention thus obtained has a small wire diameter variation rate that is not found in the conventional ETFE monofilament, so that the ETFE monofilament can be used for at least a part of the industrial fabric.

また、本発明のETFEモノフィラメントからなる工業織物は、製紙用具用織物やフィルター用織物およびベルト用織物に使用することもでき、得られたこれらの各種工業織物は、筋、縞、段などの目ずれが発生しにくく安定した織面を保持することが可能であり、エチレン−テトラフルオロエチレン共重合体樹脂の持つ易成型性、耐薬品性、電気特性、高耐候性、難燃性、安全性、非粘着性、二次加工性などの優れる特性を遺憾なく発揮する。   In addition, the industrial fabric comprising the ETFE monofilament of the present invention can be used for a papermaking tool fabric, a filter fabric, and a belt fabric. It is possible to maintain a stable woven surface that is less prone to slippage, and easy moldability, chemical resistance, electrical properties, high weather resistance, flame resistance, and safety of ethylene-tetrafluoroethylene copolymer resin Exhibits excellent properties such as non-adhesiveness and secondary processability.

なお、本発明のETFEモノフィラメントは、一本の連続糸であるが、必要に応じて複数本合わせて撚糸・熱セットしたもの、および単糸を捻って熱セットしたものであってもよい。   The ETFE monofilament of the present invention is a single continuous yarn, but it may be a plurality of twisted yarns / heat set as needed, or a single yarn twisted and heat set.

また、本発明のETFEモノフィラメントの断面形状については、その用途に応じて適宜選定することができ、特に限定されるものではないが、例えば、丸、楕円、3角、T、Y、H、+、5葉,6葉,7葉,8葉などの多葉形状、正方形、長方形、菱形、繭型および馬蹄型などを挙げることができ、また、これらの形状を一部変更したものであってもよい。   In addition, the cross-sectional shape of the ETFE monofilament of the present invention can be appropriately selected according to its use and is not particularly limited. For example, the shape is round, elliptical, triangular, T, Y, H, + Multi-leaf shape such as 5 leaves, 6 leaves, 7 leaves, 8 leaves, squares, rectangles, rhombuses, saddles, and horseshoe types can be mentioned, and these shapes are partially modified Also good.

さらにまた、本発明のETFEモノフィラメントの直径についても、その用途に応じて適宜選定することができ、特に限定されるものではないが、例えば、工業織物用途としては、直径0.05〜1.50mmのものが主に使用される。   Furthermore, the diameter of the ETFE monofilament of the present invention can be appropriately selected according to its use and is not particularly limited. For example, as an industrial textile use, the diameter is 0.05 to 1.50 mm. Is mainly used.

このように、本発明の製造方法で得られる弗素系樹脂モノフィラメントは、従来のETFEモノフィラメントよりも小さい線径変動が要求される各種織物用途にきわめて有用である。 Thus, the fluorine-based resin monofilament obtained by the production method of the present invention is extremely useful for various textile applications that require smaller wire diameter fluctuations than conventional ETFE monofilaments.

次に、本発明を実施例に基づいて説明するが、実施例におけるモノフィラメントの評価は以下の方法に準じて行った。   Next, although this invention is demonstrated based on an Example, the evaluation of the monofilament in an Example was performed according to the following method.

[線径の変動率]
アンリツ製レーザー外径測定機KG601Aに準じた外径測定機を使用して、測定速度15m/分、測定間隔0.1秒/回、測定点1024回の条件で外径を測定し、さらにキーエンス製データー処理機NR−250&PCに準じたデーター処理機を使用して、前記線径の長さ方向の線径変動を評価し、その結果をJIS−Z8101−1で定義される変動係数[標準偏差(σ)/平均値×100]で表した値を線径変動率とした。
[Variation rate of wire diameter]
Using an outer diameter measuring machine according to Anritsu laser outer diameter measuring machine KG601A, the outer diameter was measured under the conditions of a measuring speed of 15 m / min, a measuring interval of 0.1 sec / time, and a measuring point of 1024 times. Using a data processor according to NR-250 & PC manufactured by the manufacturer, the wire diameter variation in the length direction of the wire diameter was evaluated, and the result was expressed as a coefficient of variation [standard deviation defined in JIS-Z8101-1. The value represented by (σ) / average value × 100] was defined as the wire diameter variation rate.

[操業性]
連続押出し紡糸を行う際の状況を観察し、糸切れや原料の紡糸機への押し込み安定性から次の3段階で評価した。
○:全く問題なく、至って良好であった、
△:糸切れがややあったが操業可能であった、
×:糸切れや原料の押し込み不良が多発するため操業性が困難であった。
[Operability]
The situation at the time of continuous extrusion spinning was observed, and the following three stages were evaluated from yarn breakage and stability of pushing the raw material into the spinning machine.
○: No problem at all, very good,
Δ: There was some yarn breakage but operation was possible.
X: The operability was difficult due to frequent occurrences of thread breakage and indentation failure of raw materials.

[目ずれ]
フィルターの目ずれ評価については、得られたフィルター1mを目視で外観(筋、縞、段)検査し、目ずれの程度を次の3段階で評価した。なお、○を外観品位が良好な水準とする。
○:筋、縞、段が判らない、
△:筋、縞、段が認められる、
×:筋、縞、段の発生が著しい。
[Missing]
For the evaluation of the misalignment of the filter, the obtained filter 1 m 2 was visually inspected (streaks, stripes, steps), and the degree of misalignment was evaluated in the following three stages. In addition, (circle) is a level with a favorable appearance quality.
○: Streaks, stripes, steps are unknown
Δ: streaks, stripes, steps are recognized,
X: Generation of streaks, stripes, and steps is remarkable.

[実施例1]
弗素系樹脂としてETFE(旭硝子(株)製 フルオンETFE−C88AXP)を使用し、これをエクストルーダー型紡糸機に供給して紡糸温度を315℃で溶融し、孔径2.0mmのニツケル合金製の紡糸口金を通して単孔当たりの吐出量12.2g/分で紡糸し、口金から溶融押出した紡出糸条を直ちに50℃の水浴中浴に導いて冷却するに際し、口金面直下から冷却媒体浴中にかけての紡出糸条通路にその少なくとも下面が冷却媒体中に浸漬するよう筒状体を配置し、この筒状体中へ窒素ガスを流通せしめて、12.3m/分で引き取って得た未延伸糸を延伸温度90℃、160℃、かつ延伸倍率を4.80倍で2段延伸し、引き続き処理温度が170℃、かつセット倍率が0.93倍のセット処理を行った。その際の最終速度を55m/分で行い、直径0.40mmかつ円形断面のETFEモノフィラメントを得た。
[Example 1]
ETFE (Full-on ETFE-C88AXP manufactured by Asahi Glass Co., Ltd.) is used as a fluorine-based resin, which is supplied to an extruder-type spinning machine, melted at a spinning temperature of 315 ° C., and made of a nickel alloy having a pore diameter of 2.0 mm. When spinning the spun yarn melted and extruded from the die through the die at a discharge rate of 12.2 g / min, immediately introduced into a 50 ° C. water bath and cooled, it was applied directly under the die surface to the cooling medium bath. A non-stretched product obtained by disposing a cylindrical body in the spinning yarn passage so that at least the lower surface thereof is immersed in a cooling medium, allowing nitrogen gas to flow through the cylindrical body and taking it up at 12.3 m / min. The yarn was stretched in two stages at stretching temperatures of 90 ° C. and 160 ° C. and a stretching ratio of 4.80 times, and subsequently set processing was performed at a processing temperature of 170 ° C. and a set ratio of 0.93 times. The final speed at that time was 55 m / min, and an ETFE monofilament having a diameter of 0.40 mm and a circular cross section was obtained.

[実施例2]
弗素系樹脂としてETFE(旭硝子(株)製 フルオンETFE−C88AXP)を使用し、これをエクストルーダー型紡糸機に供給して紡糸温度を315℃で溶融し、孔径0.8mmのニツケル合金製の紡糸口金を通して単孔当たりの吐出量0.24g/分で紡糸し、口金から溶融押出した紡出糸条を直ちに50℃の水浴中浴に導いて冷却するに際し、口金面直下から冷却媒体浴中にかけての紡出糸条通路にその少なくとも下面が冷却媒体中に浸漬するよう筒状体を配置し、この筒状体中へ窒素ガスを流通せしめて、8.2m/分で引き取って得た未延伸糸を延伸温度85℃、140℃、かつ延伸倍率を4.60倍で2段延伸し、引き続き処理温度が150℃、かつセット倍率が0.93倍のセット処理を行った。その際の最終速度を35m/分で行い、直径0.07mmかつ円形断面のETFEモノフィラメントを得た。
[Example 2]
ETFE (Fullon ETFE-C88AXP manufactured by Asahi Glass Co., Ltd.) is used as a fluorine-based resin, which is supplied to an extruder-type spinning machine, melted at a spinning temperature of 315 ° C., and a spinning made of a nickel alloy having a pore diameter of 0.8 mm. When spinning the spun yarn melt-extruded from the die through a die at a discharge rate of 0.24 g / min and immediately extruded into a 50 ° C. water bath, it is cooled immediately below the die surface into a cooling medium bath. A non-stretched product obtained by placing a cylindrical body in the spinning yarn passage of the tube so that at least the lower surface thereof is immersed in the cooling medium, circulating nitrogen gas into the cylindrical body, and taking it up at 8.2 m / min. The yarn was stretched in two stages at a stretching temperature of 85 ° C. and 140 ° C. and a draw ratio of 4.60 times, and subsequently set processing was performed at a treatment temperature of 150 ° C. and a set ratio of 0.93 times. The final speed at that time was 35 m / min, and an ETFE monofilament having a diameter of 0.07 mm and a circular cross section was obtained.

[実施例3]
弗素系樹脂としてETFE(旭硝子(株)製 フルオンETFE−C88AXP)を使用し、これをエクストルーダー型紡糸機に供給して紡糸温度を315℃で溶融し、孔径4.5mmのニツケル合金製の紡糸口金を通して単孔当たりの吐出量27.1g/分で紡糸し、口金から溶融押出した紡出糸条を直ちに50℃の水浴中浴に導いて冷却するに際し、口金面直下から冷却媒体浴中にかけての紡出糸条通路にその少なくとも下面が冷却媒体中に浸漬するよう筒状体を配置し、この筒状体中へ窒素ガスを流通せしめて、9.0m/分で引き取って得た未延伸糸を延伸温度90℃、190℃、かつ延伸倍率を5.30倍で2段延伸し、引き続き処理温度が225℃、かつセット倍率が0.93倍のセット処理を行った。その際の最終速度を40m/分で行い、直径0.70mmかつ円形断面のETFEモノフィラメントを得た。
[Example 3]
ETFE (Fullon ETFE-C88AXP manufactured by Asahi Glass Co., Ltd.) is used as a fluorine-based resin, which is supplied to an extruder-type spinning machine, melted at a spinning temperature of 315 ° C., and a spinning made of a nickel alloy having a pore diameter of 4.5 mm. When spinning the spun yarn that was spun at a discharge rate of 27.1 g / min per single hole through the die and melt-extruded from the die immediately into a 50 ° C. water bath, it was cooled immediately below the die surface into the cooling medium bath. A non-stretched product obtained by disposing a cylindrical body in the spun yarn passage so that at least the lower surface thereof is immersed in the cooling medium, allowing nitrogen gas to flow through the cylindrical body, and drawing at 9.0 m / min. The yarn was stretched in two stages at a stretching temperature of 90 ° C. and 190 ° C. and a draw ratio of 5.30 times, and subsequently a set treatment was performed at a treatment temperature of 225 ° C. and a set ratio of 0.93 times. The final speed at that time was 40 m / min, and an ETFE monofilament having a diameter of 0.70 mm and a circular cross section was obtained.

[実施例4]
弗素系樹脂としてETFE(旭硝子(株)製 フルオンETFE−C88AXP)を使用し、これをエクストルーダー型紡糸機に供給して紡糸温度を315℃で溶融し、孔径8.0mmのニツケル合金製の紡糸口金を通して単孔当たりの吐出量66.9g/分で紡糸し、口金から溶融押出した紡出糸条を直ちに50℃の水浴中浴に導いて冷却するに際し、口金面直下から冷却媒体浴中にかけての紡出糸条通路にその少なくとも下面が冷却媒体中に浸漬するよう筒状体を配置し、この筒状体中へ窒素ガスを流通せしめて、9.0m/分で引き取って得た未延伸糸を延伸温度90℃、190℃、かつ延伸倍率を4.80倍で2段延伸し、引き続き処理温度が225℃、かつセット倍率が0.93倍のセット処理を行った。その際の最終速度を40m/分で行い、直径1.10mmかつ円形断面のETFEモノフィラメントを得た。
[Example 4]
ETFE (Fullon ETFE-C88AXP manufactured by Asahi Glass Co., Ltd.) is used as a fluorine-based resin, which is supplied to an extruder-type spinning machine, melted at a spinning temperature of 315 ° C., and a spinning made of a nickel alloy having a pore diameter of 8.0 mm. When spinning the spun yarn that was spun at a discharge rate of 66.9 g / min per single hole through the die and melt-extruded from the die into a 50 ° C. water bath, it was cooled immediately below the die surface and into the cooling medium bath. A non-stretched product obtained by disposing a cylindrical body in the spun yarn passage so that at least the lower surface thereof is immersed in the cooling medium, allowing nitrogen gas to flow through the cylindrical body, and drawing at 9.0 m / min. The yarn was stretched in two stages at a stretching temperature of 90 ° C. and 190 ° C. and a stretching ratio of 4.80 times, and subsequently set processing was performed at a processing temperature of 225 ° C. and a set ratio of 0.93 times. The final speed at that time was 40 m / min, and an ETFE monofilament having a diameter of 1.10 mm and a circular cross section was obtained.

[比較例1]
実施例1において、筒状体中へ窒素ガスを流通しなかったこと以外は、実施例1と同様にして、直径0.40mmのETFEモノフィラメントを得た。
[Comparative Example 1]
In Example 1, an ETFE monofilament having a diameter of 0.40 mm was obtained in the same manner as in Example 1 except that nitrogen gas was not circulated into the cylindrical body.

[比較例2]
実施例1において、未延伸糸の引取速度を4.0m/分に、最終速度を17.9m/分に下げたこと以外は、実施例1と同様にして、直径0.40mmのETFEモノフィラメントを得た。
[Comparative Example 2]
In Example 1, an ETFE monofilament having a diameter of 0.40 mm was prepared in the same manner as in Example 1 except that the take-up speed of the undrawn yarn was lowered to 4.0 m / min and the final speed was lowered to 17.9 m / min. Obtained.

[比較例3]
実施例1において、未延伸糸の引取速度を17.5m/分に、最終速度を78.1m/分に上げたこと以外は、実施例1と同様にして、直径0.40mmのETFEモノフィラメントを得た。
[Comparative Example 3]
In Example 1, an ETFE monofilament having a diameter of 0.40 mm was prepared in the same manner as in Example 1 except that the take-up speed of the undrawn yarn was increased to 17.5 m / min and the final speed was increased to 78.1 m / min. Obtained.

[比較例4]
実施例1において、延伸倍率を4.80倍から6.80倍に上げて最終速度を77.8m/分に上げたこと以外は、実施例1と同様にして、直径0.40mmのETFEモノフィラメントを得た。
[Comparative Example 4]
An ETFE monofilament having a diameter of 0.40 mm in the same manner as in Example 1 except that the draw ratio was increased from 4.80 times to 6.80 times and the final speed was increased to 77.8 m / min. Got.

以上、上記実施例1〜4および比較例1〜4で得られた各ETFEモノフィラメントの線経変動率結果を表1に併せて示す。   Table 1 also shows the results of the rate of variation of the wire diameter of each ETFE monofilament obtained in Examples 1-4 and Comparative Examples 1-4.

Figure 0004934853
Figure 0004934853

表1の結果から明らかなように、本発明の製造方法で得られたETFEモノフィラメント(実施例1〜4)は、いずれも長さ方向の線径の変動率が5%以下と極めて小さいものである。 As is clear from the results of Table 1, the ETFE monofilaments (Examples 1 to 4) obtained by the production method of the present invention have extremely small fluctuation rates of the wire diameter in the length direction of 5% or less. is there.

一方、口金面直下での窒素ガスの流通、未延伸糸の引取速度、モノフィラメントの最終速度が本発明の条件を満たさない製法により製造されたETFEモノフィラメント(比較例1〜4)は、いずれも操業性が悪く、長さ方向の線径の変動率が大きいもの(比較例1〜2)や、延伸切れ(比較例3〜4)して製糸できなく、本発明が目的とする効果を十分に満たすものではなかった。   On the other hand, all of the ETFE monofilaments (Comparative Examples 1 to 4) manufactured by a production method in which the flow of nitrogen gas directly under the die surface, the take-up speed of undrawn yarn, and the final speed of the monofilament do not satisfy the conditions of the present invention are operated. Inferior in properties, the variation rate of the wire diameter in the length direction is large (Comparative Examples 1 and 2), and the yarn is not drawn by being stretched (Comparative Examples 3 and 4). It did not meet.

また、実施例1および比較例1〜2で得られた直径0.40mmのETFEモノフィラメントをそれぞれ経糸、緯糸に使用して平織物を製織し、さらにこの織物を190℃で熱セットして目付500g/mのフィルターを作製したところ、長さ方向の線径変動率が小さくかった実施例1のETFEモノフィラメントをフィルター構成線材として使用したフィルターは、目ずれが発生しなかったのに対し、比較例1、2のETFEモノフィラメントは、筋、縞、段が認められるなどの目ずれが発生した。 A plain woven fabric was woven using the ETFE monofilaments of 0.40 mm in diameter obtained in Example 1 and Comparative Examples 1 and 2 for warp and weft, respectively, and this fabric was heat-set at 190 ° C. to give a basis weight of 500 g. / M 2 filter was produced, and the filter using the ETFE monofilament of Example 1 as a filter constituent wire, which had a small variation in the diameter in the length direction, did not cause misalignment. In the ETFE monofilaments of Examples 1 and 2, misalignments such as streaks, stripes and steps were observed.

以上説明したように、本発明の製造方法で得られるETFEモノフィラメントは、長さ方向の線径変動が従来のETFEモノフィラメントに比べて飛躍的に改良されたものであることから、例えば製紙用具用織物やフィルター用織物およびベルト用織物などの工業織物用としての使用が極めて有用である。 As described above, the ETFE monofilament obtained by the production method of the present invention has a drastic improvement in the wire diameter variation in the length direction as compared with the conventional ETFE monofilament. Further, it is very useful for industrial fabrics such as filter fabrics and belt fabrics.

また、本発明の製造方法によれば、長さ方向の線径変動率が極めて小さいETFEモノフィラメントを効率的に製造することができる。   Moreover, according to the manufacturing method of the present invention, an ETFE monofilament having a very small wire diameter variation rate in the length direction can be efficiently manufactured.

さらに、本発明の製造方法で得られるETFEモノフィラメントを用いた工業織物は、製紙用具用織物やフィルター用織物およびベルト用織物などに使用することもでき、得られたこれらの各種工業織物は、その織面の筋、縞、段などの目ずれが発生しにくく安定した織面を保持することが可能であり、さらに弗素系樹脂が有する優れた耐熱性、耐薬品性、耐溶剤性、電気特性、摩擦特性、非粘着性、耐候性などの効果を遺憾なく発揮する。 Furthermore, the industrial fabric using the ETFE monofilament obtained by the production method of the present invention can also be used for a papermaking tool fabric, a filter fabric, a belt fabric, and the like. It is possible to maintain a stable woven surface that is less prone to misalignment such as streaks, stripes and steps on the woven surface, and also has excellent heat resistance, chemical resistance, solvent resistance, and electrical properties possessed by fluorine-based resins. It exhibits the effects such as friction characteristics, non-adhesiveness, and weather resistance.

Claims (1)

エチレン−テトラフルオロエチレン共重合体を溶融紡糸・冷却するに際して、口金面直下から冷却媒体浴中にかけての紡出糸条通路にその少なくとも下面が冷却媒体中に浸漬するよう筒状体を配置すると共にこの筒状体中へ不活性ガスを流通せしめ、口金から溶融押出した紡出糸条を直ちに前記筒状体を経て冷却媒体浴へと導いて冷却し、次いで得られた未延伸糸を5〜15m/分の速度で引き取り、引き続き少なくとも1段以上の多段で延伸または延伸/熱セット処理を行うと共に、その際の最終引き取り速度を25〜75m/分で行うことを特徴とする弗素系樹脂モノフィラメントの製造方法。When melt-spinning and cooling the ethylene-tetrafluoroethylene copolymer, a cylindrical body is arranged in the spinning yarn passage from directly under the die surface to the cooling medium bath so that at least the lower surface thereof is immersed in the cooling medium. An inert gas is allowed to flow through the cylindrical body, and the spun yarn melt-extruded from the die is immediately led to the cooling medium bath through the cylindrical body to be cooled, and the obtained undrawn yarn is A fluorine-based resin monofilament characterized by being drawn at a speed of 15 m / min and subsequently subjected to stretching or stretching / heat setting treatment in at least one or more stages, and the final take-up speed at that time is 25 to 75 m / min. Manufacturing method.
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