JPH07324224A - Polyester-based fiber and polyester continuous filament woven fabric - Google Patents
Polyester-based fiber and polyester continuous filament woven fabricInfo
- Publication number
- JPH07324224A JPH07324224A JP6116676A JP11667694A JPH07324224A JP H07324224 A JPH07324224 A JP H07324224A JP 6116676 A JP6116676 A JP 6116676A JP 11667694 A JP11667694 A JP 11667694A JP H07324224 A JPH07324224 A JP H07324224A
- Authority
- JP
- Japan
- Prior art keywords
- polyester
- woven fabric
- fiber
- yarn
- continuous filament
- 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
- 239000000835 fiber Substances 0.000 title claims abstract description 75
- 229920000728 polyester Polymers 0.000 title claims abstract description 41
- 239000002759 woven fabric Substances 0.000 title claims abstract description 31
- 238000000034 method Methods 0.000 claims abstract description 38
- 238000009987 spinning Methods 0.000 claims abstract description 17
- 230000000704 physical effect Effects 0.000 claims abstract description 11
- 238000009835 boiling Methods 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000010438 heat treatment Methods 0.000 claims description 13
- 230000035882 stress Effects 0.000 description 21
- 238000004804 winding Methods 0.000 description 12
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 7
- 238000009998 heat setting Methods 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 6
- 238000004043 dyeing Methods 0.000 description 6
- 230000009477 glass transition Effects 0.000 description 6
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 4
- 238000010036 direct spinning Methods 0.000 description 4
- 239000004744 fabric Substances 0.000 description 4
- 230000002040 relaxant effect Effects 0.000 description 4
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 2
- MMINFSMURORWKH-UHFFFAOYSA-N 3,6-dioxabicyclo[6.2.2]dodeca-1(10),8,11-triene-2,7-dione Chemical group O=C1OCCOC(=O)C2=CC=C1C=C2 MMINFSMURORWKH-UHFFFAOYSA-N 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 235000013351 cheese Nutrition 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- BDJRBEYXGGNYIS-UHFFFAOYSA-N nonanedioic acid Chemical compound OC(=O)CCCCCCCC(O)=O BDJRBEYXGGNYIS-UHFFFAOYSA-N 0.000 description 2
- -1 polyethylene terephthalate Polymers 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- 230000008646 thermal stress Effects 0.000 description 2
- 230000004580 weight loss Effects 0.000 description 2
- FKUJGZJNDUGCFU-UHFFFAOYSA-N 2,5-dimethylterephthalic acid Chemical compound CC1=CC(C(O)=O)=C(C)C=C1C(O)=O FKUJGZJNDUGCFU-UHFFFAOYSA-N 0.000 description 1
- KLSLSJCKZBGUAJ-UHFFFAOYSA-N 4-[1-(4-carboxyphenoxy)ethoxy]benzoic acid Chemical compound C=1C=C(C(O)=O)C=CC=1OC(C)OC1=CC=C(C(O)=O)C=C1 KLSLSJCKZBGUAJ-UHFFFAOYSA-N 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 101150053899 RSH1 gene Proteins 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 239000006224 matting agent Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- RROAXNYROFIJOE-UHFFFAOYSA-N methoxycarbonyl benzenesulfonate Chemical compound COC(=O)OS(=O)(=O)C1=CC=CC=C1 RROAXNYROFIJOE-UHFFFAOYSA-N 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- HRRDCWDFRIJIQZ-UHFFFAOYSA-N naphthalene-1,8-dicarboxylic acid Chemical compound C1=CC(C(O)=O)=C2C(C(=O)O)=CC=CC2=C1 HRRDCWDFRIJIQZ-UHFFFAOYSA-N 0.000 description 1
- RXOHFPCZGPKIRD-UHFFFAOYSA-N naphthalene-2,6-dicarboxylic acid Chemical compound C1=C(C(O)=O)C=CC2=CC(C(=O)O)=CC=C21 RXOHFPCZGPKIRD-UHFFFAOYSA-N 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000012783 reinforcing fiber Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000009958 sewing Methods 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
- Woven Fabrics (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、ポリエステル系繊維、
及び該繊維が用いられた、弾発性、風合いに優れるポリ
エステル長繊維織物に関する。FIELD OF THE INVENTION The present invention relates to a polyester fiber,
And a polyester long-fiber woven fabric using the fiber, which is excellent in elasticity and texture.
【0002】[0002]
【従来の技術】ポリエステル系繊維は、その特性を生か
して衣料用途の他幅広く活用されている。特に、近年の
新合繊ブームに支えられて、その生産量は、今もって増
加している。2. Description of the Related Art Polyester fibers have been widely used in addition to clothing applications due to their characteristics. Especially, supported by the recent boom of new synthetic fibers, the production volume is still increasing.
【0003】一方で、生産性、労働力不足からの省力
化、自動化のために、従来の紡糸、延伸の2工程方式か
ら、紡糸後一旦捲取ることなく延伸する紡糸直接延伸法
(スピンドロー方式:SPD)方式への生産方式の転換
が盛んにおこなわれている。この紡糸直接延伸法による
繊維の生産は、ゴム補強用繊維をはじめとする魚網、ミ
シン糸、ロープ、ホース等の産業資材用分野のみなら
ず、衣料用分野にも拡大されている。On the other hand, in order to improve productivity, labor saving due to labor shortage, and automation, a spinning direct drawing method (spin draw method) is adopted in which spinning is carried out without being wound once from the conventional two-step method of spinning and drawing. The production method is being actively changed to the: SPD) method. The production of fibers by this spinning direct drawing method has been expanded not only to the field of industrial materials such as fish nets such as rubber-reinforcing fibers, sewing threads, ropes and hoses, but also to the field of clothing.
【0004】そして、直接紡糸延伸法は生産性の向上を
図ることを目的とするために、最近では捲取りの最終速
度が6000m/min以上の高速にまで至っている。In order to improve the productivity, the direct spinning / drawing method has recently reached a final winding speed as high as 6000 m / min or more.
【0005】[0005]
【発明が解決しようとする課題】しかしながら、高速化
にともない、熱セット時間の確保、捲取り技術の高難度
化等の問題が発生し、紡糸直接延伸法で製造されたポリ
エステル系繊維を捲取る際、従来公知の捲取条件をその
まま採用すれば、特に従来の紡糸、延伸2工程方式で得
られた糸(バーン糸)に比べて品質的に劣るという問題
があった。例えば、紡糸直接延伸法によるポリエステル
系繊維を長繊維織物の経糸に使用した場合、バーン糸に
比べ製品の膨らみが不足し、薄く手持ち感の乏しい織物
にしか仕上らないなど、風合い面で劣るという問題があ
った。However, as the speed is increased, problems such as securing the heat setting time and increasing the difficulty of the winding technique occur, and the polyester fiber produced by the spinning direct drawing method is wound up. In this case, if the conventionally known winding conditions are adopted as they are, there is a problem that the quality is inferior to that of a yarn (burn yarn) obtained by a conventional spinning and drawing two-step method. For example, when polyester fibers produced by the spinning direct drawing method are used as warp yarns for long-fiber fabrics, the product bulges are insufficient compared to burn yarns, and only thin and poorly hand-held fabrics are produced, resulting in poor texture. There was a problem.
【0006】本発明の目的は、上述した高速化に伴う問
題点を解決し、紡糸直接延伸法により得られたポリエス
テル系繊維を高速で捲取ることができ、かつ、長繊維織
物の経糸及び緯糸の少なくとも一方に使用した場合に、
優れた風合いおよび弾発性を有する長繊維織物を得るこ
とのできるポリエステル系繊維を提供することにある。
また、本発明の目的は、経糸及び緯糸の少なくとも一方
に上記ポリエステル系繊維が用いられたポリエステル長
繊維織物を提供することにある。The object of the present invention is to solve the above-mentioned problems associated with speeding up, to allow polyester fibers obtained by the spinning direct drawing method to be wound up at high speed, and for warp and weft of long fiber woven fabric. When used for at least one of
It is an object of the present invention to provide a polyester fiber capable of obtaining a long-fiber woven fabric having excellent texture and elasticity.
Another object of the present invention is to provide a polyester continuous fiber woven fabric in which the above polyester fiber is used in at least one of warp and weft.
【0007】[0007]
【課題を解決するための手段】本発明者らは、従来の紡
糸、延伸2工程方式で得られた糸と紡糸直接延伸法で得
られたポリエステル系繊維とにおける、原糸特性と風合
いの差について鋭意検討した結果、原糸の収縮特性の差
が風合い差の主因であること、直接防止延伸法で得られ
た繊維であっても、特定の構造を有し、しかも特定の収
縮挙動を有する繊維であれば、従来の2工程で得られた
繊維と同一の加工条件でも優れた風合いを有する長繊維
織物が得られ、さらに上記繊維で単糸デニールの高い繊
維を用いれば弾発性にも優れた長繊維織物が得られるこ
とを見いだし本発明に至った。DISCLOSURE OF THE INVENTION The inventors of the present invention have made a difference in the characteristics of the raw yarn and the texture between the yarn obtained by the conventional two-step spinning and drawing process and the polyester fiber obtained by the direct spinning process. As a result of diligent study, the difference in the shrinkage characteristics of the raw yarn is the main cause of the difference in texture, and even the fiber obtained by the direct prevention stretching method has a specific structure and a specific shrinkage behavior. If it is a fiber, a long fiber woven fabric having an excellent texture can be obtained even under the same processing conditions as the fiber obtained in the conventional two steps. Further, if a fiber having a high single yarn denier is used as the above fiber, it is also elastic. It was found that an excellent long-fiber woven fabric can be obtained, and the present invention has been completed.
【0008】すなわち、本発明のポリエステル長繊維織
物用のポリエステル系繊維は、繊維の諸物性値が、 固有粘度 IVf≦0.65、 熱収縮応力のピーク応力 σmax ≧0.35g/d、 沸水収縮率 SHW ≧12%、 熱収縮率特性値 RSH16 ≧3%、かつ、 単糸デニール dpf ≧5d であることを特徴とするものである。ここで、熱収縮率
特性値RSH16とは、繊維を10%リラックスのもと
で150℃、5秒の熱処理を施した後の160℃の乾熱
収縮率を示す。本発明において、前記ポリエステル系繊
維は、特に紡糸直接延伸法により得られたものを対象と
する。また、本発明のポリエステル長繊維織物は、経糸
及び緯糸の少なくとも一方に、前記ポリエステル系繊維
が用いられていることを特徴とするものである。That is, in the polyester fiber for the polyester continuous fiber woven fabric of the present invention, the physical properties of the fiber are as follows: intrinsic viscosity IVf ≦ 0.65, peak stress of heat shrinkage stress σ max ≧ 0.35 g / d, boiling water Shrinkage SHW ≧ 12%, thermal shrinkage characteristic value RSH16 ≧ 3%, and single yarn denier dpf ≧ 5d. Here, the heat shrinkage characteristic value RSH16 indicates a dry heat shrinkage of 160 ° C. after heat-treating the fiber at 150 ° C. for 5 seconds under 10% relaxation. In the present invention, the polyester fiber is intended to be one obtained by a direct spinning method. Further, the polyester continuous fiber woven fabric of the present invention is characterized in that the polyester fiber is used in at least one of the warp and the weft.
【0009】以下、本発明を詳しく説明する。本発明に
おいて、ポリエステル系繊維とは、エチレンテレフタレ
ート単位を主たる繰返し単位とするものであり、具体的
には全構成単位の80モル%以上がエチレンテレフタレ
ート単位であるポリエステルからなる繊維である。特に
テレフタル酸またはその機能的誘導体と、エチレングリ
コールまたはエチレンオキサイドとから製造されるポリ
エチレンテレフタレートを主な対象とするが、酸成分と
してテレフタル酸またはその機能的誘導体のほかに、酸
成分全量を基準として20モル%未満、好ましくは10
モル%未満のイソフタル酸、アジピン酸、セバチン酸、
アゼライン酸、ナフタール酸、p−オキシ安息香酸、
2,5−ジメチルテレフタル酸、ビス(p−カルボキシ
フェノキシ)エタン、2,6−ナフタレンジカルボン
酸、3,5−ジ(カルボメトキシ)ベンゼンスルホン酸
塩またはそれらの機能的誘導体を加えるか、および/ま
たはグリコール成分としてエチレングリコールの他、グ
リコール成分全量を基準として20モル%未満、好まし
くは10モル%未満のジエチレングリコール、プロピレ
ングリコール、1,4−ブタジオール、1,4−ヒドロ
キシメチルシクロヘキサン等の2価アルコールを加えて
製造される共重合体であってもよい。また、例えば難燃
性を付与するための芳香族ポリホスホネートを加えた共
重合体であってもよい。更にこれらの重合体に酸化防止
剤、艶消剤、着色剤、染色性向上剤、難燃性向上剤、制
電剤等を添加することもできる。The present invention will be described in detail below. In the present invention, the polyester-based fiber is a fiber having an ethylene terephthalate unit as a main repeating unit, and specifically, a fiber made of polyester in which 80 mol% or more of all constituent units are ethylene terephthalate units. In particular, the main target is polyethylene terephthalate produced from terephthalic acid or its functional derivative and ethylene glycol or ethylene oxide, but in addition to terephthalic acid or its functional derivative as the acid component, the total amount of the acid component is the standard. Less than 20 mol%, preferably 10
Less than mol% of isophthalic acid, adipic acid, sebacic acid,
Azelaic acid, naphthalic acid, p-oxybenzoic acid,
2,5-dimethyl terephthalic acid, bis (p-carboxyphenoxy) ethane, 2,6-naphthalenedicarboxylic acid, 3,5-di (carbomethoxy) benzenesulfonate or functional derivatives thereof, and / or In addition to ethylene glycol as the glycol component, less than 20 mol%, preferably less than 10 mol% of diethylene glycol, propylene glycol, 1,4-butadiol, 1,4-hydroxymethylcyclohexane or other dihydric alcohol based on the total amount of the glycol component. It may be a copolymer produced by adding. Further, for example, a copolymer to which an aromatic polyphosphonate for imparting flame retardancy is added may be used. Further, an antioxidant, a matting agent, a coloring agent, a dyeability improving agent, a flame retardancy improving agent, an antistatic agent, etc. can be added to these polymers.
【0010】本発明のポリエステル系繊維の諸物性値に
ついて説明する。まず、ポリエステル系繊維の固有粘度
IVf≦0.65である。IVfが0.65を超える
と、溶融紡糸時より高温を必要とするため紡糸操作が著
しく困難になり、そのため本発明に使用可能な良好な品
質の繊維の製造が困難になる。好ましくは固有粘度IV
f≦0.62である。Various physical properties of the polyester fiber of the present invention will be described. First, the intrinsic viscosity of the polyester fiber is IVf ≦ 0.65. When the IVf exceeds 0.65, the spinning operation becomes extremely difficult because a higher temperature is required than that during melt spinning, which makes it difficult to produce good quality fibers that can be used in the present invention. Preferably intrinsic viscosity IV
f ≦ 0.62.
【0011】繊維の熱収縮応力のピーク応力 σmax ≧
0.35g/dである。σmax が0.35g/d未満で
は、織物の特徴である巾入れによる風合いを得ることが
できず、手持ち感の乏しい織物となってしまう。好まし
くはσmax ≧0.45g/dである。Peak stress of heat shrinkage stress of fiber σ max ≧
It is 0.35 g / d. When σ max is less than 0.35 g / d, it is not possible to obtain the texture due to the width-filling, which is a characteristic of the woven fabric, and the woven fabric has a poor hand-held feeling. Preferably, σ max ≧ 0.45 g / d.
【0012】次に、繊維の沸水収縮率SHW≧12%で
ある。SHWが12%未満では、織物の丈、巾入れ特に
リラックス工程等の最初に丈、巾入れが必要な工程での
縮みが不足し、風合いの乏しい織物となってしまう。好
ましくはSHW≧15%である。Next, the boiling water shrinkage of the fiber SHW ≧ 12%. If the SHW is less than 12%, the length and width of the woven fabric, especially shrinkage in the process requiring the length and width at the beginning such as the relaxation process, will be insufficient, resulting in a poor texture. SHW ≧ 15% is preferable.
【0013】また、繊維の熱収縮率特性値RSH16≧
3%である。通常、織物を仕上げていくには、例えば、
リラックス→プレセット→減量→染色→仕上げ、といっ
た各工程を通過するが、最終の丈、巾とするために各工
程でコントロールする必要がある。これは、シワ等の工
程におけるトラブルを防止するためである。繊維の熱収
縮率特性値RSH16は、これら工程通過時の挙動を適
性化するための尺度であり、この値が3%未満であれ
ば、最終の丈、巾入れが不十分となり、風合いの乏しい
織物となってしまう。好ましくはRSH16≧6%であ
る。Further, the heat shrinkage characteristic value RSH16 ≧
3%. Usually, to finish the fabric, for example,
It goes through each process of relaxing → presetting → weight loss → dyeing → finishing, but it is necessary to control in each process to obtain the final length and width. This is to prevent troubles in the process such as wrinkles. The heat shrinkage characteristic value RSH16 of the fiber is a measure for optimizing the behavior when passing through these processes. If this value is less than 3%, the final length and width are insufficient and the texture is poor. It becomes a woven fabric. RSH16 ≧ 6% is preferable.
【0014】さらに、繊維の単糸デニールdpf≧5d
である。5d以上の単糸デニールの繊維を経糸及び緯糸
の少なくとも一方に用いることにより、弾発性の優れた
織物が得られる。単糸デニールが5d未満では、弾発性
に乏しい織物となってしまう。好ましくはdpf≧6d
である。Furthermore, the single yarn denier of the fiber dpf ≧ 5d
Is. A woven fabric having excellent elasticity can be obtained by using fibers having a single yarn denier of 5d or more for at least one of the warp and the weft. If the single yarn denier is less than 5d, the resulting fabric will have poor elasticity. Preferably dpf ≧ 6d
Is.
【0015】次に、紡糸直接延伸法による本発明のポリ
エステル系繊維の製糸工程の例を示す。溶融されたポリ
マーを紡糸口金から吐出し、紡出糸条を冷却、固化し、
この糸条に油剤付与し、引取りローラで引取る。この際
に油剤付与後引取りローラまでの間に、油剤のマイグレ
ーションをよくするために、実質的に交絡の付与されな
いインターレースを設置することも可能である。この引
取られた糸条を、捲取ることなく延伸し、熱セットす
る。更に、この糸条の配向を緩和させることなく、糸温
度をガラス転移点以下に冷却した後、若干のリラックス
で捲取る。Next, an example of the process for producing the polyester fiber of the present invention by the direct spinning method will be described. The molten polymer is discharged from the spinneret, the spun yarn is cooled and solidified,
An oil agent is applied to this yarn and the yarn is taken up by a take-up roller. At this time, in order to improve migration of the oil agent after applying the oil agent, it is possible to install an interlace to which substantially no entanglement is applied in order to improve migration of the oil agent. The yarn thus drawn is stretched without winding and heat set. Further, without relaxing the orientation of the yarn, the yarn temperature is cooled below the glass transition point and then wound up with some relaxation.
【0016】かかる製糸工程において、本発明のポリエ
ステル系繊維を得るには、以下に示す方法を採用するこ
とが好ましい。すなわち、上記引取りローラで引取る際
の速度は、繊維の熱収縮率特性値RSH16に大きく影
響を与えるので、RSH16が3%以上となる速度とす
る必要がある。特に限定するものではないが、紡糸中の
結晶化(配向結晶化)が発生するまでの速度が望まし
い。このような観点から、引取り速度は好ましくは35
00m/min以下、更に好ましくは2800m/mi
n以下が良い。In order to obtain the polyester fiber of the present invention in the yarn making process, it is preferable to adopt the following method. That is, the speed at which the take-up roller pulls it out has a great influence on the heat shrinkage rate characteristic value RSH16 of the fiber, so it is necessary to set the speed at which RSH16 is 3% or more. Although not particularly limited, a speed at which crystallization (orientation crystallization) occurs during spinning is desirable. From such a viewpoint, the take-up speed is preferably 35.
00 m / min or less, more preferably 2800 m / mi
n or less is preferable.
【0017】糸条を引取り後、延伸前に、糸条に熱を付
与することが望ましい。特に限定するものではないが、
この加熱温度をガラス転移点以上とすることが染むら、
品位の点から必要であり、適性な加熱温度は好ましくは
70〜100℃である。70℃未満では延伸点が固定さ
れがたく、また100℃を越えるとローラ上での糸揺れ
が大きくなり染むら、品位の悪化だけでなく、糸切れの
増加にもつながり好ましくない。It is desirable to apply heat to the yarn after the yarn is taken up and before the drawing. Although not particularly limited,
If the heating temperature is higher than the glass transition point, uneven dyeing occurs,
It is necessary in terms of quality, and a suitable heating temperature is preferably 70 to 100 ° C. If it is less than 70 ° C., the stretching point is hard to be fixed, and if it exceeds 100 ° C., the yarn shake on the roller becomes large and uneven dyeing occurs, which not only deteriorates the quality but also increases the yarn breakage, which is not preferable.
【0018】次に、加熱された糸条を延伸し、熱セット
を施す。延伸は、必要な強伸度を得るために調整され、
更に、必要な収縮挙動を得るために調整される。特に、
熱セットは温度だけでなく、時間も重要なポイントであ
り、特に限定するものではないが、0.01〜0.1秒
付与することが望ましい。この時間未満では染むら等の
品位が悪くなる。熱セットの温度としては、70〜90
℃が好ましい。Next, the heated yarn is drawn and heat set. Stretching is adjusted to obtain the required high elongation
Furthermore, it is adjusted to obtain the required shrinkage behavior. In particular,
Not only the temperature but also the time is an important point in the heat setting, and the heat setting is not particularly limited, but it is preferable to apply the heat setting for 0.01 to 0.1 seconds. If the time is less than this time, the quality such as uneven dyeing becomes poor. The temperature of heat setting is 70 to 90
C is preferred.
【0019】熱セットされた糸条を配向緩和させること
なく糸温度をガラス転移点以下にすることが、高熱収縮
応力を得るために必須である。特に限定するものではな
いが、例えば、熱セットローラの後に、更に加熱ローラ
を設置し、両ローラの速度を同一とし、該設置ローラの
温度をガラス転移点以下の温度に設定することにより糸
条の温度をガラス転移点以下の温度とする。ここで、該
設置ローラを設置しない場合、あるいはガラス転移点以
上の温度では、捲取りの際に、パッケージの形状の調整
のために張力を下げて捲取る必要があるために、配向緩
和が著しくなり高熱収縮応力の繊維が得られない。In order to obtain a high heat shrinkage stress, it is essential to make the yarn temperature below the glass transition point without relaxing the orientation of the heat set yarn. Although not particularly limited, for example, a heating roller is further installed after the heat setting roller, the speeds of both rollers are the same, and the temperature of the installation roller is set to a temperature not higher than the glass transition point. Is set to a temperature below the glass transition point. Here, when the installation roller is not installed, or at a temperature equal to or higher than the glass transition point, it is necessary to lower the tension for winding the package in order to adjust the shape of the package. A fiber with high heat shrinkage stress cannot be obtained.
【0020】更に、単糸デニールが太くなることによ
り、従来の2工程方式では、延伸時に撚り溜まりが発生
し糸切れが多くなる。紡糸直接延伸法で紡糸、延伸を直
結することによりこの問題は解決され、単糸デニールの
太いマルチフィラメントには好適である。Furthermore, since the single yarn denier becomes thicker, in the conventional two-step system, twist accumulation occurs during drawing and more yarn breakage occurs. This problem is solved by directly connecting spinning and drawing by the spinning direct drawing method, which is suitable for a thick multifilament having a single yarn denier.
【0021】[0021]
【作用】スピンドロー(SPD)方式では、熱セット時
間の確保等の理由から通常最終ローラは加熱ローラであ
り、しかも、その温度は他のローラに比べて最も高く設
定されている。一方、捲取りの観点からは、捲形状、捲
締めを考慮して、比較的低テンションで捲取られる。こ
のため、通常は、捲取り速度を最終ローラの速度より遅
くしてテンションをコントロールしている。その結果、
従来のスピンドロー方式で得られた糸(SPD糸)は実
質的に、最終ローラでリラックスを受けることになり、
非晶部の配向が緩和されていた。In the spin draw (SPD) system, the final roller is usually the heating roller for the reason of ensuring the heat setting time, and the temperature thereof is set to be the highest as compared with the other rollers. On the other hand, from the viewpoint of winding, taking into consideration the winding shape and tightening, the winding is performed with a relatively low tension. Therefore, usually, the winding speed is set lower than the speed of the final roller to control the tension. as a result,
The yarn obtained by the conventional spin draw method (SPD yarn) is substantially subjected to relaxation on the final roller,
The orientation of the amorphous part was relaxed.
【0022】本発明ではこの非晶部の配向緩和をなくし
て、高熱収縮応力の繊維を得るとともに、2工程で発生
する延伸時のトラブル(例えば、放置時間オーバー、延
撚機への仕掛けまちがい等)もなく、しかも、後加工工
程(特に、染加工)での収縮特性をコントロールするこ
とにより、スピンドロー方式でも、従来の2工程で得ら
れた繊維と同一の工程条件でも、優れた風合いを持ち、
且つ弾発性に優れた織物を得ることができる。In the present invention, the orientation relaxation of the amorphous portion is eliminated to obtain a fiber having a high heat shrinkage stress, and a trouble occurs during the stretching which occurs in two steps (for example, the standing time is exceeded, a mistake in setting the twisting machine, etc.). ), And by controlling the shrinkage characteristics in the post-processing steps (especially dyeing processing), excellent texture can be obtained even with the spin draw method and the same process conditions as the fibers obtained in the conventional two steps. Have,
Moreover, a woven fabric excellent in elasticity can be obtained.
【0023】[0023]
【実施例】以下に、実施例をあげて本発明をさらに詳述
する。なお、各実施例、比較例における物性値は以下の
方法で測定した。 <固有粘度>フェノール/テトラクロロエタン 60/
40の混合溶液を用いて、30℃で測定する。EXAMPLES The present invention will be described in more detail below with reference to examples. In addition, the physical-property value in each Example and a comparative example was measured by the following method. <Intrinsic viscosity> Phenol / tetrachloroethane 60 /
It measures at 30 degreeC using the mixed solution of 40.
【0024】<熱収縮応力のピーク応力σmax >熱収縮
応力のピーク応力σmax とは、以下の方法で測定され
る、温度〜収縮応力のカーブの中で、最も高い応力値
(ピーク応力)をいう。熱応力測定機(例えば、SII
製TMA/SS100)とこれに連動した記録装置を用
いて測定する。測定する試料は、全デニールが75〜1
25dの範囲に入るように引き揃えチャック間が2cm
の長さになるように両端を挟み込み、熱応力測定機にセ
ットする。試料にデニールあたり1/30gの初荷重を
掛け定長に保ちながら、室温〜300℃まで、昇温速度
20℃/分で昇温する。この際に発生する応力を記録
し、最大応力点(ピーク応力)を読み取る。[0024] The peak stress sigma max thermal shrinkage stress <peak stress sigma max thermal shrinkage stress>, is measured by the following method, in the curve of the temperature-shrinkage stress, the highest stress value (peak stress) Say. Thermal stress measuring machine (eg SII
(TMA / SS100 manufactured by Mitsui Chemical Co., Ltd.) and a recording device linked to the measurement. The sample to be measured has a total denier of 75 to 1
2cm between the alignment chucks so that it falls within the range of 25d
Insert both ends so that the length becomes, and set it in the thermal stress measuring machine. While maintaining a constant length by applying an initial load of 1/30 g per denier to the sample, the temperature is raised from room temperature to 300 ° C. at a temperature rising rate of 20 ° C./min. The stress generated at this time is recorded and the maximum stress point (peak stress) is read.
【0025】<沸水収縮率SHW>JIS−L1013
に準じて測定する。<Shrinkage rate SHW> JIS-L1013
Measure according to.
【0026】<熱収縮率特性値RSH16>繊維を延撚
機等を用いて、10%リラックスのもとで150℃×5
秒の熱処理を施した後、160℃乾熱下での乾熱収縮率
を測定する。<Heat Shrinkage Characteristic Value RSH16> Using a twisting machine or the like for fibers, 150 ° C. × 5 under 10% relaxation
After heat treatment for 2 seconds, the dry heat shrinkage rate under dry heat at 160 ° C. is measured.
【0027】次に、各実施例、比較例で用いたローラの
配置について、図1および図2を参照して説明する。図
1において、(NZ)は紡糸口金であり、糸条(1) の進行方
向に見て、加熱ローラ(GR1) 、加熱ローラ(GR2) 、加熱
ローラ(GR3) 、および巻取ローラ(2) 、巻取チーズ(3)
が、この順で配置されている。図2においては、図1の
加熱ローラ(GR3) が配置されていない以外は、図1と同
様である。Next, the arrangement of the rollers used in each of the examples and comparative examples will be described with reference to FIGS. 1 and 2. In FIG. 1, (NZ) is a spinneret, and viewed in the traveling direction of the yarn (1), a heating roller (GR1), a heating roller (GR2), a heating roller (GR3), and a winding roller (2). , Rolled cheese (3)
However, they are arranged in this order. 2 is the same as FIG. 1 except that the heating roller (GR3) of FIG. 1 is not arranged.
【0028】[実施例1〜4]固有粘度IVp=0.6
35のポリエチレンテレフタレートを紡糸温度280℃
で押出し、図1に示すローラの配置で、表1に示すそれ
ぞれの条件を用いて、30d/5fの完成糸を得た。得
られた糸の物性を表2に示す。次に、得られた繊維と3
0d/18fの自己伸長糸とを混繊し、500T/mの
撚りを加えた後、糊付け、整経し経糸とした。緯糸に7
5d/72fの強撚糸を用い生機とし、120℃の温熱
下でのリラックス、190℃の乾熱下でのプレセット、
減量染色を経た後に、仕上げ加工して織物を得た。この
織物の緯糸密度、風合い、弾発性を表2に併せて示す。[Examples 1 to 4] Intrinsic viscosity IVp = 0.6
35 polyethylene terephthalate spinning temperature 280 ℃
Was extruded in accordance with the conditions shown in Table 1 with the arrangement of the rollers shown in FIG. 1 to obtain a finished yarn of 30d / 5f. Table 2 shows the physical properties of the obtained yarn. Then, the obtained fiber and 3
The yarn was mixed with 0d / 18f self-stretching yarn, twisted at 500 T / m, sized and warped. 7 for weft
Using 5d / 72f strong twist yarn as a raw material, relaxing under heat of 120 ° C, presetting under dry heat of 190 ° C,
After undergoing weight loss dyeing, finishing processing was carried out to obtain a woven fabric. Table 2 also shows the weft density, texture and elasticity of this woven fabric.
【0029】[比較例1〜4]図1に示すローラの配置
で、表1に示すようにそれぞれ条件を変更した以外は、
実施例と同様にして、30d/5fの完成糸を得た。得
られた糸の物性を表2に示す。次に、得られた繊維か
ら、実施例と同様にして織物を得た。この織物の緯糸密
度、風合い、弾発性を表2に併せて示す。[Comparative Examples 1 to 4] With the arrangement of the rollers shown in FIG. 1, the conditions were changed as shown in Table 1, except that
A finished yarn of 30d / 5f was obtained in the same manner as in the example. Table 2 shows the physical properties of the obtained yarn. Next, a woven fabric was obtained from the obtained fibers in the same manner as in the example. Table 2 also shows the weft density, texture and elasticity of this woven fabric.
【0030】[比較例5〜6]図2に示すローラの配置
で、表1に示すようにそれぞれ条件を変更した以外は、
実施例と同様にして、30d/5fの完成糸を得た。得
られた糸の物性を表2に示す。次に、得られた繊維か
ら、実施例と同様にして織物を得た。この織物の緯糸密
度、風合い、弾発性を表2に併せて示す。[Comparative Examples 5 to 6] With the arrangement of the rollers shown in FIG. 2, the conditions were changed as shown in Table 1, except that
A finished yarn of 30d / 5f was obtained in the same manner as in the example. Table 2 shows the physical properties of the obtained yarn. Next, a woven fabric was obtained from the obtained fibers in the same manner as in the example. Table 2 also shows the weft density, texture and elasticity of this woven fabric.
【0031】実施例1〜4により得られたポリエステル
系繊維はいずれも、固有粘度、熱収縮応力のピーク応力
σmax 、沸水収縮率SHW、熱収縮率特性値RSH1
6、および単糸デニールの各物性値に優れており、該繊
維から製造されたポリエステル長繊維織物は、優れた風
合いを有すると共に、弾発性にも優れている。これに対
して、比較例1〜6により得られたポリエステル系繊維
はいずれも、σmax 、SHW、RSH16、および単糸
デニールの物性値のいずれかに劣っているため、該繊維
から製造されたポリエステル長繊維織物は、風合い、弾
発性に劣っている。The polyester fibers obtained in Examples 1 to 4 all have an intrinsic viscosity, a peak stress σ max of heat shrinkage stress, a boiling water shrinkage SHW, and a heat shrinkage characteristic value RSH1.
6 and single yarn denier have excellent physical property values, and the polyester long-fiber woven fabric produced from the fiber has excellent texture and elasticity. On the other hand, all of the polyester fibers obtained in Comparative Examples 1 to 6 were inferior to any of the physical properties of σ max , SHW, RSH16, and single yarn denier, and thus were produced from the fibers. The polyester long-fiber woven fabric is inferior in texture and elasticity.
【0032】[0032]
【発明の効果】上述のように、本発明のポリエステル系
繊維は、固有粘度、熱収縮応力のピーク応力σmax 、沸
水収縮率SHW、熱収縮率特性値RSH16、および単
糸デニールの各物性値に優れている。従って、本発明の
ポリエステル系繊維はスピンドロー方式で得られたもの
であっても、該繊維から、従来の2工程方式で得られた
繊維と同一の工程条件でも、優れた風合いを持ち、且つ
弾発性に優れたポリエステル長繊維織物を製造すること
ができる。このように本発明によると、スピンドロー方
式によるポリエステル系繊維の高生産性と、それから得
られるポリエステル長繊維織物の品質とを両立すること
ができる。As described above, the polyester fiber of the present invention has various physical properties such as intrinsic viscosity, peak stress σ max of heat shrinkage stress, boiling water shrinkage SHW, heat shrinkage characteristic value RSH16, and single yarn denier. Is excellent. Therefore, even if the polyester fiber of the present invention is obtained by the spin draw method, it has an excellent texture even under the same process conditions as the fiber obtained by the conventional two-step method from the fiber, and It is possible to produce a polyester long-fiber woven fabric having excellent elasticity. As described above, according to the present invention, it is possible to achieve both high productivity of the polyester fiber by the spin draw method and quality of the polyester continuous fiber woven fabric obtained therefrom.
【0033】[0033]
【表1】 [Table 1]
【0034】[0034]
【表2】 [Table 2]
【図1】実施例1〜4および比較例1〜4で用いたロー
ラの配置を示す図である。FIG. 1 is a diagram showing the arrangement of rollers used in Examples 1 to 4 and Comparative Examples 1 to 4.
【図2】比較例5〜6で用いたローラの配置を示す図で
ある。FIG. 2 is a diagram showing the arrangement of rollers used in Comparative Examples 5 and 6.
(NZ)…紡糸口金 (GR1) …加熱ローラ (GR2) …加熱ローラ (GR3) …加熱ローラ (1) …糸条 (2) …巻取ローラ (3) …巻取チーズ (NZ)… Spinneret (GR1)… Heating roller (GR2)… Heating roller (GR3)… Heating roller (1)… Yarn (2)… Winding roller (3)… Winding cheese
Claims (3)
ル系繊維であって、繊維の諸物性値が、 固有粘度 IVf≦0.65、 熱収縮応力のピーク応力 σmax ≧0.35g/d、 沸水収縮率 SHW ≧12%、 熱収縮率特性値 RSH16 ≧3%、かつ、 単糸デニール dpf ≧5d であることを特徴とする、ポリエステル系繊維;ここ
で、熱収縮率特性値RSH16とは、繊維を10%リラ
ックスのもとで150℃、5秒の熱処理を施した後の1
60℃の乾熱収縮率を示す。1. A polyester fiber for polyester long-fiber woven fabric, wherein the physical properties of the fiber are: intrinsic viscosity IVf ≦ 0.65, peak stress of thermal shrinkage σ max ≧ 0.35 g / d, boiling water shrinkage Rate SHW ≧ 12%, heat shrinkage characteristic value RSH16 ≧ 3%, and single yarn denier dpf ≧ 5d polyester fiber; wherein heat shrinkage characteristic value RSH16 means a fiber 1 after heat treatment at 150 ° C for 5 seconds under 10% relaxation
The dry heat shrinkage ratio at 60 ° C. is shown.
1記載のポリエステル系繊維。2. The polyester fiber according to claim 1, which is obtained by a spinning direct drawing method.
項1または2記載のポリエステル系繊維が用いられてい
ることを特徴とする、ポリエステル長繊維織物。3. A polyester continuous fiber woven fabric, wherein the polyester fiber according to claim 1 is used in at least one of warp and weft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11667694A JP3438322B2 (en) | 1994-05-30 | 1994-05-30 | Polyester fiber, method for producing the same, and polyester continuous fiber woven fabric |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11667694A JP3438322B2 (en) | 1994-05-30 | 1994-05-30 | Polyester fiber, method for producing the same, and polyester continuous fiber woven fabric |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07324224A true JPH07324224A (en) | 1995-12-12 |
| JP3438322B2 JP3438322B2 (en) | 2003-08-18 |
Family
ID=14693129
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11667694A Expired - Fee Related JP3438322B2 (en) | 1994-05-30 | 1994-05-30 | Polyester fiber, method for producing the same, and polyester continuous fiber woven fabric |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3438322B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012505324A (en) * | 2008-10-13 | 2012-03-01 | ビーエーエスエフ ソシエタス・ヨーロピア | Monofilament manufacturing method and use of monofilament |
| CN105525417A (en) * | 2016-02-23 | 2016-04-27 | 广东溢达纺织有限公司 | Polyester woven label and preparation method thereof |
-
1994
- 1994-05-30 JP JP11667694A patent/JP3438322B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012505324A (en) * | 2008-10-13 | 2012-03-01 | ビーエーエスエフ ソシエタス・ヨーロピア | Monofilament manufacturing method and use of monofilament |
| CN105525417A (en) * | 2016-02-23 | 2016-04-27 | 广东溢达纺织有限公司 | Polyester woven label and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3438322B2 (en) | 2003-08-18 |
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