JP4063684B2 - Method for producing flat synthetic fiber - Google Patents

Method for producing flat synthetic fiber Download PDF

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Publication number
JP4063684B2
JP4063684B2 JP2003014388A JP2003014388A JP4063684B2 JP 4063684 B2 JP4063684 B2 JP 4063684B2 JP 2003014388 A JP2003014388 A JP 2003014388A JP 2003014388 A JP2003014388 A JP 2003014388A JP 4063684 B2 JP4063684 B2 JP 4063684B2
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Japan
Prior art keywords
fiber
synthetic fiber
spinning
flat
flatness
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JP2003014388A
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Japanese (ja)
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JP2004225194A (en
Inventor
耕司 小野
陽啓 大本
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Kaneka Corp
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Kaneka Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、合成繊維の製造方法に関するものであり、さらに詳しくは、湿式紡糸法または半乾半湿式紡糸法による合成繊維の製造工程において、扁平型の孔を有するノズルから紡出された合成繊維の扁平率をノズル交換なしで調整する方法に関するものである。
【0002】
【従来の技術】
合成繊維の製造時において、湿式紡糸法または半乾半湿式紡糸法で製造される繊維は、最終製品の扁平率に対応したノズルを使用して紡糸操作を行うことにより、様々な扁平率の合成繊維を生産している(特許文献1、2)。このため最終製品の扁平率を変更するときにはノズル交換を行なければならず、非常に手間となるだけでなく原液の損失、生産性の低下を引き起こしている。この問題点の改善策として、紡糸ドラフト、延伸倍率を調整することにより、若干の扁平率の調整は可能であるが、使用したノズルの扁平率のせいぜい4割程度までしか変化させることができず、また微妙な繊度調整が難しく、実際には実施できていないのが現状である。
【0003】
【特許文献1】
特開昭61−102410
【0004】
【特許文献2】
特開平11−222716
【0005】
【発明が解決しようとする課題】
本発明の目的は、上記のような従来の合成繊維の製造工程における品種の切り替えロスの問題点に鑑み、効率的に品種切り替えを実施することにある。
【0006】
【課題を解決するための手段】
本発明者らは上記の目的を達成するために鋭意研究を重ねた結果、合成繊維の温度を樹脂の軟化点より5℃低い温度以上、融点以下にし、かつ圧搾を行うことにより、扁平率を調整することが可能であることを見出し、本発明を完成するに至った。
【0007】
すなわち、本発明は、扁平ノズルから紡出され、湿式紡糸または半乾半湿紡糸によって得られる扁平率が1より大きいアクリル系繊維からなる繊維束を、紡糸・水洗工程において、前記アクリル系繊維を構成する樹脂の軟化点−5℃以上、融点以下の温度範囲とし、0.05〜10MPaの範囲に加圧して前記繊維束を圧搾処理することにより、前記アクリル系繊維をさらに扁平化することを特徴とする扁平合成繊維の製造方法に関する。
【0008】
その好ましい実施態様としては、圧搾処理される繊維が、扁平ノズルから紡出された繊維である上記製造方法、圧搾処理後の繊維の扁平率が、紡糸時のノズル断面の扁平率の1.5倍以上であることを特徴とする上記製造方法、または合成繊維が、湿式紡糸または半乾半湿紡糸によって得られるアクリル系繊維であることを特徴とする上記製造方法に関する。
【0009】
【発明の実施の形態】
以下に本発明をさらに詳細に説明する。
【0010】
本発明における合成繊維とは、単独重合体、または共重合体からなるものであって、具体的には、アクリルまたはモダアクリルなどのアクリル系繊維、塩化ビニル系繊維、ポリエステル系繊維、などがあげられ、特に限定されないが、アクリル系繊維が好ましい。アクリル系繊維は通常、アクリル系樹脂を有機または無機の溶媒に溶解した紡糸原液を用いて、湿式または半乾半湿式紡糸法により製造される。
【0011】
本発明は、上記のような合成繊維の繊維を、その製造工程において、繊維を構成する樹脂の軟化点より5℃低い温度以上で樹脂の融点以下の範囲に加熱した条件下で圧搾処理することによって、断面形状が扁平型を有する扁平合成繊維を得るというものである。さらに、本発明においては、扁平型の孔を有するノズルから紡出された扁平合成繊維に、このような圧搾処理を行うことによって、その扁平率を任意の倍率に高めた扁平合成繊維を得ることができる。このときのノズルの形状は特に限定はしないが、長方形や楕円であることが好ましい。
【0012】
本発明でいう扁平率とは、得られる合成繊維の断面形状あるいは紡糸ノズルの断面形状において、その短径と長径の比、すなわち、断面形状の長径を短径で除した値である。本発明において圧搾処理を施される合成繊維の断面形状の扁平率は1より大きい(すなわち扁平型の断面)のが好ましく、さらに好ましくは3以上である。上限としては特に限定されないが、本発明の処理において任意の倍率の扁平合成繊維が得られることから、もとになる繊維の扁平率はそれほど高くなくてよく、例えば10以下が好ましい。
【0013】
圧搾時の合成繊維の温度は樹脂の軟化点より5℃低い温度以上であれば良いが、好ましくは樹脂の軟化点以上である方がよい。ここでいう樹脂の軟化点とは、樹脂が柔らかくなり始める温度のことであり、具体的には、示差走査熱量計により測定されるDSC曲線から読みとれるガラス転移点のことである。圧搾時の合成繊維の温度が軟化点温度より5℃以上低ければ、圧搾しても繊維の扁平率はほとんど変わらない。また融点以上では樹脂が溶け出すため、融点以下である必要がある。合成繊維をこのような温度にする手段としては特に限定されず、熱風装置やヒートロールなど公知の方法が用いられる。また、湿式または半乾半湿式紡糸法により合成繊維を製造する場合、紡糸後の水洗時に加温下で洗浄を行うことによっても、繊維束を上記温度範囲に設定することもできる。この方法は、あえて他の加温装置を必要としない点で好ましい。
【0014】
実際の繊維の製造工程においては、繊維は繊維束の状態で紡糸されその後の工程を経るため、本発明の圧搾処理も繊維束の状態でなされることになる。
【0015】
本発明における圧搾の手段としては特に限定されず、ニップロール等を用いることが出来る。また、上述した温度範囲に繊維束を加熱あるいは保温するための加熱装置を同時に有していてもよい。圧搾処理時の圧力としては、0.05MPa以上が好ましく、より好ましくは0.1MPa以上である。上限は特に限定されないが、10MPa程度までで十分である。圧力が上記範囲未満であれば圧搾の効果が得られにくくなり、上記範囲を超えると繊維が切れやすくなったり、断面形状が維持できにくくなったりする。また圧搾処理は高圧力で1回処理しても良いが、低圧力で複数回、行ってもよく、圧搾時の圧力と処理回数のバランスによって扁平率を調整すればよい。
【0016】
本発明の圧搾処理によって、繊維の扁平率は任意の倍率にすることが出来、例えば、紡糸ノズルの扁平率の1.5倍以上、好ましくは2倍以上の繊維となるように圧搾処理すればよい。上限は特に限定されないが、好ましくは10倍程度までである。
【0017】
本発明における圧搾処理は、合成繊維の製造工程において、通常、紡糸・水洗後の工程で行われる。圧搾処理後に通常の合成繊維の紡糸後処理である、延伸や熱処理などが行われる
【0018】
以下、本発明の合成繊維の断面形状を調整する好ましい方法の一例について、添付図面を引用してさらに説明する。
【0019】
図1に合成繊維の断面形状を調整する装置の一例を示す。紡糸ノズルから紡出されて凝固浴中で凝固した合成繊維の繊維束1は、ガイドロール2、3にて導かれ、所定温度の洗浄水を入れた水洗槽4に送り込まれる。そして繊維束は洗浄とともに昇温され、引き取りガイドロール6、7により水洗槽4より取り出される。その後、直ちにニップロール8で圧搾処理される。必要であれば、上記水洗と圧搾処理の一連の操作を繰り返すことにより、合成繊維の扁平率を調整する。
【0020】
【実施例】
次に実施例により本発明をさらに詳細に説明するが、本発明はこれら実施例に限定されるものではない。
【0021】
(実施例1)
アクリロニトリル49.5重量%と塩化ビニル50.0重量%、スチレンスルホン酸ソーダ0.5重量%よりなる共重合体(軟化点93℃)をアセトンに固形分濃度29.5%で溶解した紡糸原液を用いて、ノズル径0.08×0.60mm(扁平率7.5)、4000ホールの長方形ノズルから濃度30%のアセトン水溶液に押し出し、湿式紡糸法により凝固操作を行った。その後、水洗温度95℃で溶媒洗浄を行うことにより合成繊維を昇温し、ただちに0.2MPaのニップロールで圧搾操作を行った。この昇温操作と圧搾操作を交互に5回処理し、その後乾燥処理を施した結果、図2に示すような扁平率約20の扁平合成繊維を得ることができた。
【0022】
(実施例2)
実施例1と同じ条件で凝固したアクリル系繊維を、95℃の昇温操作と0.2MPaの圧搾操作を交互に10回処理し、その後乾燥処理を施した結果、図3に示すような扁平率約30の扁平合成繊維を得ることができた。
(実施例3)
実施例1と同じ条件で凝固したアクリル系繊維を、95℃の昇温操作と0.5MPaの圧搾操作を交互に1回処理し、その後乾燥処理を施した結果、図4に示すような扁平率約15の扁平合成繊維を得ることができた。
(実施例4)
実施例1と同じ原液を用いて、ノズル径0.20×0.30mm(扁平率1.5)、4000ホールの楕円形ノズルから濃度30%のアセトン水溶液に押し出し、湿式紡糸法により凝固操作を行った。その後、水洗温度95℃で溶媒洗浄を行うことにより合成繊維を昇温し、ただちに0.2MPaのニップロールで圧搾操作を行った。この昇温操作と圧搾操作を交互に5回処理し、その後乾燥処理を施した結果、図5に示すような扁平率約4.5の扁平(楕円形)合成繊維を得ることができた。
(実施例5、参考例
ビニルアルコール100重量%よりなる重合体を水に固形分濃度15%で溶解した紡糸原液を用いて、ノズル径0.08×0.60mm(扁平率7.5)、2000ホールの長方形ノズルから飽和芒硝水溶液に押し出し、湿式紡糸法により凝固操作を行った。その後、乾燥、延伸、熱処理工程を経て、ホルマリン5%、硫酸20%、芒硝20%のアセタール浴により、処理温度約60℃でアセタール化処理を行う。その後、水洗温度95℃で洗浄操作を行うことにより合成繊維を昇温し、ただちに0.2MPaのニップロールで圧搾操作を行った。この昇温操作と圧搾操作を交互に5回処理し、その後乾燥処理を施した結果、図6に示すような扁平率約12の扁平合成繊維を得ることができた。
【0023】
(比較例1)
実施例1と同じ条件で凝固したアクリル系繊維を、80℃の昇温操作と0.2MPaの圧搾操作を交互に10回処理した結果、模式図7に示すような、ノズルの扁平率からわずかに高くなった程度の扁平率約8の扁平合成繊維しか得られなかった。
【0024】
【発明の効果】
以上のとおり、本発明によれば、合成繊維の製造工程において、溶媒除去時の水洗温度を樹脂の軟化点以上にし、かつ圧搾処理を行うことにより、扁平率を調整することが可能となり、ノズル交換せずに様々な扁平率の製品を製造することができ、生産性の向上に貢献しうるものである。
【図面の簡単な説明】
【図1】 本発明の合成繊維の断面形状を調整する装置の一例を示す。
【図2】 実施例1で得られた扁平合成繊維の断面形状の模式図である。
【図3】 実施例2で得られた扁平合成繊維の断面形状の模式図である。
【図4】 実施例3で得られた扁平合成繊維の断面形状の模式図である。
【図5】 実施例4で得られた扁平(楕円)合成繊維の断面形状の模式図である。
【図6】 実施例5で得られた扁平合成繊維の断面形状の模式図である。
【図7】 比較例1で得られた扁平合成繊維の断面形状の模式図である。
【符号の説明】
1:合成繊維の繊維束
2,3:ガイドロール
4:水洗槽
5:洗浄水
6、7:引き取りガイドロール
8:ニップロール
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing a synthetic fiber, and more specifically, a synthetic fiber spun from a nozzle having a flat hole in a synthetic fiber production process by a wet spinning method or a semi-dry semi-wet spinning method. It is related with the method of adjusting the flatness of this without nozzle replacement.
[0002]
[Prior art]
In the production of synthetic fibers, fibers produced by wet spinning method or semi-dry semi-wet spinning method are synthesized with various flatness ratios by spinning using a nozzle corresponding to the flatness ratio of the final product. Fibers are produced (Patent Documents 1 and 2). For this reason, when changing the flatness of the final product, it is necessary to replace the nozzle, which is not only very troublesome, but also causes a loss of stock solution and a decrease in productivity. As an improvement measure for this problem, it is possible to slightly adjust the flatness ratio by adjusting the spinning draft and the draw ratio, but it can only change the flatness ratio of the nozzle used up to about 40%. Also, it is difficult to finely adjust the fineness, and the actual situation is that it cannot be carried out.
[0003]
[Patent Document 1]
JP-A-61-102410
[0004]
[Patent Document 2]
JP-A-11-222716
[0005]
[Problems to be solved by the invention]
An object of the present invention is to efficiently perform product type switching in view of the problem of product type switching loss in the conventional synthetic fiber manufacturing process as described above.
[0006]
[Means for Solving the Problems]
As a result of intensive research to achieve the above-mentioned object, the inventors have made the flatness rate by reducing the temperature of the synthetic fiber to a temperature not less than 5 ° C. below the softening point of the resin and not higher than the melting point, and performing compression. The present inventors have found that it is possible to adjust, and have completed the present invention.
[0007]
That is, the present invention provides a fiber bundle made of acrylic fibers spun from a flat nozzle and obtained by wet spinning or semi-dry semi-wet spinning and having a flatness ratio greater than 1, in the spinning / washing step, the acrylic fibers are The temperature of the softening point of the constituting resin is −5 ° C. or higher and the melting point or lower, pressurizing the fiber bundle and pressing the fiber bundle to further flatten the acrylic fiber. It is related with the manufacturing method of the flat synthetic fiber characterized.
[0008]
As a preferred embodiment thereof, the above-mentioned production method, in which the fiber to be squeezed is a fiber spun from a flat nozzle, the flatness of the fiber after the squeezing treatment is 1.5 of the flatness of the cross section of the nozzle during spinning. It is related with the said manufacturing method characterized by being more than double, or the said manufacturing method characterized by the synthetic fiber being an acrylic fiber obtained by wet spinning or semi-dry semi-wet spinning.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
The present invention is described in further detail below.
[0010]
The synthetic fiber in the present invention is composed of a homopolymer or a copolymer, and specific examples include acrylic fibers such as acrylic or modacrylic, vinyl chloride fibers, polyester fibers, and the like. Although not particularly limited, acrylic fibers are preferred. Acrylic fibers are usually produced by a wet or semi-dry semi-wet spinning method using a spinning stock solution in which an acrylic resin is dissolved in an organic or inorganic solvent.
[0011]
In the present invention, the fiber of the above-mentioned synthetic fiber is pressed in the production process under a condition where the temperature is 5 ° C. lower than the softening point of the resin constituting the fiber and is heated to a range below the melting point of the resin. Thus, a flat synthetic fiber having a flat cross-sectional shape is obtained. Furthermore, in the present invention, a flat synthetic fiber having an increased flatness ratio at an arbitrary magnification is obtained by performing such a pressing process on a flat synthetic fiber spun from a nozzle having a flat hole. Can do. The shape of the nozzle at this time is not particularly limited, but is preferably a rectangle or an ellipse.
[0012]
The flatness referred to in the present invention is the ratio of the minor axis to the major axis, that is, the value obtained by dividing the major axis of the sectional shape by the minor axis in the sectional shape of the synthetic fiber or the spinning nozzle. Is preferably flattening of the cross-sectional shape of synthetic fibers to be subjected to compression processing in the present invention is greater than 1 (i.e. flat cross-section), more preferably 3 or more. Although it does not specifically limit as an upper limit, Since the flat synthetic fiber of arbitrary magnifications is obtained in the process of this invention, the flatness of the base fiber may not be so high, for example, 10 or less is preferable.
[0013]
Although the temperature of the synthetic fiber at the time of pressing should just be 5 degreeC or more lower than the softening point of resin, it is better that it is more than the softening point of resin. The softening point of the resin here is a temperature at which the resin starts to soften, and specifically, a glass transition point that can be read from a DSC curve measured by a differential scanning calorimeter. If the temperature of the synthetic fiber at the time of pressing is 5 ° C. or more lower than the softening point temperature, the flatness of the fiber will hardly change even if the pressing is performed. Also, since the resin melts above the melting point, it must be below the melting point. The means for bringing the synthetic fiber to such a temperature is not particularly limited, and a known method such as a hot air device or a heat roll is used. Moreover, when manufacturing a synthetic fiber by a wet or semi-dry semi-wet spinning method, a fiber bundle can also be set to the said temperature range also by wash | cleaning under heating at the time of the water washing after spinning. This method is preferable in that it does not require another heating device.
[0014]
In the actual fiber manufacturing process, the fiber is spun in the state of a fiber bundle and passes through the subsequent steps. Therefore, the pressing treatment of the present invention is also performed in the state of the fiber bundle.
[0015]
The pressing means in the present invention is not particularly limited, and a nip roll or the like can be used. Moreover, you may have simultaneously the heating apparatus for heating or heat-retaining a fiber bundle in the temperature range mentioned above. As a pressure at the time of a pressing process, 0.05 MPa or more is preferable, More preferably, it is 0.1 MPa or more. The upper limit is not particularly limited, but about 10 MPa is sufficient. If the pressure is less than the above range, the squeezing effect is difficult to obtain, and if it exceeds the above range, the fiber is easily cut or the cross-sectional shape is difficult to maintain. The pressing treatment may be performed once at a high pressure, but may be performed a plurality of times at a low pressure, and the flatness may be adjusted by the balance between the pressure during pressing and the number of times of processing.
[0016]
By the pressing treatment of the present invention, the flatness of the fibers can be set to an arbitrary magnification. For example, if the pressing treatment is performed so that the fibers become 1.5 times or more, preferably twice or more the spinning nozzle flatness. Good. The upper limit is not particularly limited, but is preferably about 10 times.
[0017]
The pressing treatment in the present invention is usually performed in a process after spinning and washing in the synthetic fiber manufacturing process. Stretching and heat treatment, which are post-spinning treatments of ordinary synthetic fibers, are performed after the pressing treatment .
[0018]
Hereinafter, an example of a preferable method for adjusting the cross-sectional shape of the synthetic fiber of the present invention will be further described with reference to the accompanying drawings.
[0019]
FIG. 1 shows an example of an apparatus for adjusting the cross-sectional shape of the synthetic fiber. A fiber bundle 1 of synthetic fibers spun from a spinning nozzle and solidified in a coagulation bath is guided by guide rolls 2 and 3 and fed into a washing tank 4 containing washing water of a predetermined temperature. Then, the temperature of the fiber bundle is raised with the washing, and the fiber bundle is taken out from the washing tank 4 by the take-off guide rolls 6 and 7. Thereafter, the nip roll 8 is immediately pressed. If necessary, the flatness of the synthetic fiber is adjusted by repeating a series of operations of washing with water and pressing.
[0020]
【Example】
EXAMPLES Next, although an Example demonstrates this invention further in detail, this invention is not limited to these Examples.
[0021]
Example 1
Spinning stock solution in which a copolymer (softening point 93 ° C.) composed of 49.5% by weight of acrylonitrile, 50.0% by weight of vinyl chloride and 0.5% by weight of sodium styrenesulfonate was dissolved in acetone at a solid content concentration of 29.5%. Was extruded from a rectangular nozzle having a nozzle diameter of 0.08 × 0.60 mm (flatness of 7.5) and 4000 holes into a 30% concentration aqueous acetone solution, and coagulation was performed by a wet spinning method. Thereafter, the synthetic fiber was heated by performing solvent washing at a water washing temperature of 95 ° C., and immediately subjected to a squeezing operation with a 0.2 MPa nip roll. As a result of alternately performing the temperature raising operation and the pressing operation five times and then performing a drying treatment, a flat synthetic fiber having a flatness ratio of about 20 as shown in FIG. 2 could be obtained.
[0022]
(Example 2)
As a result of subjecting the acrylic fiber solidified under the same conditions as in Example 1 to 95 ° C. heating operation and 0.2 MPa pressing operation alternately 10 times, followed by drying treatment, flattening as shown in FIG. A flat synthetic fiber having a rate of about 30 could be obtained.
(Example 3)
The acrylic fiber solidified under the same conditions as in Example 1 was subjected to a heating operation of 95 ° C. and a pressing operation of 0.5 MPa alternately once, and then subjected to a drying treatment. As a result, the flatness as shown in FIG. A flat synthetic fiber having a rate of about 15 could be obtained.
Example 4
Using the same undiluted solution as in Example 1, the nozzle diameter was 0.20 × 0.30 mm (flatness 1.5), extruded from a 4000 hole elliptical nozzle to a 30% concentration acetone aqueous solution, and coagulation operation was performed by wet spinning. went. Thereafter, the synthetic fiber was heated by performing solvent washing at a water washing temperature of 95 ° C., and immediately subjected to a squeezing operation with a 0.2 MPa nip roll. As a result of alternately performing the temperature raising operation and the pressing operation five times and then performing a drying treatment, a flat (elliptical) synthetic fiber having a flatness ratio of about 4.5 as shown in FIG. 5 was obtained.
(Example 5 , Reference example )
Saturated from a rectangular nozzle with a nozzle diameter of 0.08 × 0.60 mm (flatness of 7.5) and 2000 holes using a spinning stock solution in which a polymer composed of 100% by weight of vinyl alcohol is dissolved in water at a solid content concentration of 15%. It was extruded into an aqueous solution of sodium sulfate and solidified by a wet spinning method. Thereafter, after a drying, stretching, and heat treatment process, an acetalization treatment is performed at a treatment temperature of about 60 ° C. in an acetal bath of 5% formalin, 20% sulfuric acid, and 20% sodium sulfate. Then, the synthetic fiber was heated by performing a washing operation at a water washing temperature of 95 ° C., and immediately, the squeezing operation was performed with a 0.2 MPa nip roll. As a result of alternately performing the temperature raising operation and the pressing operation five times and then performing a drying treatment, a flat synthetic fiber having a flatness ratio of about 12 as shown in FIG. 6 was obtained.
[0023]
(Comparative Example 1)
As a result of treating the acrylic fiber solidified under the same conditions as in Example 1 10 times alternately with a temperature rising operation of 80 ° C. and a pressing operation of 0.2 MPa, the flatness of the nozzle as shown in FIG. Only a flat synthetic fiber having a flatness ratio of about 8 was obtained.
[0024]
【The invention's effect】
As described above, according to the present invention, in the synthetic fiber manufacturing process, the water washing temperature at the time of solvent removal is set to be equal to or higher than the softening point of the resin, and the flattening rate can be adjusted by performing the pressing treatment. Products with various flatness ratios can be manufactured without replacement, which can contribute to the improvement of productivity.
[Brief description of the drawings]
FIG. 1 shows an example of an apparatus for adjusting the cross-sectional shape of a synthetic fiber of the present invention.
2 is a schematic diagram of a cross-sectional shape of a flat synthetic fiber obtained in Example 1. FIG.
3 is a schematic diagram of a cross-sectional shape of a flat synthetic fiber obtained in Example 2. FIG.
4 is a schematic diagram of a cross-sectional shape of a flat synthetic fiber obtained in Example 3. FIG.
5 is a schematic diagram of a cross-sectional shape of a flat (elliptical) synthetic fiber obtained in Example 4. FIG.
6 is a schematic diagram of a cross-sectional shape of a flat synthetic fiber obtained in Example 5. FIG.
7 is a schematic view of a cross-sectional shape of a flat synthetic fiber obtained in Comparative Example 1. FIG.
[Explanation of symbols]
1: Fiber bundle of synthetic fibers 2, 3: Guide roll 4: Washing tank 5: Washing water 6, 7: Take-off guide roll 8: Nip roll

Claims (2)

扁平ノズルから紡出され、湿式紡糸または半乾半湿紡糸によって得られる扁平率が1より大きいアクリル系繊維からなる繊維束を、
紡糸・水洗工程において、前記アクリル系繊維を構成する樹脂の軟化点−5℃以上、融点以下の温度範囲とし、0.05〜10MPaの範囲に加圧して前記繊維束を圧搾処理することにより、前記アクリル系繊維をさらに扁平化することを特徴とする扁平合成繊維の製造方法。
A fiber bundle composed of acrylic fibers spun from a flat nozzle and obtained by wet spinning or semi-dry semi-moist spinning, with a flatness ratio greater than 1.
In the spinning / washing step, the temperature of the softening point of the resin constituting the acrylic fiber is −5 ° C. or higher and the melting point or lower , and pressurizing the fiber bundle by pressing in the range of 0.05 to 10 MPa , A method for producing a flat synthetic fiber, wherein the acrylic fiber is further flattened .
前記圧搾処理後の繊維の扁平率が、紡糸時のノズル断面の扁平率の1.5倍以上である請求項1に記載の扁平合成繊維の製造方法。 The pressed fiber flattening of the after treatment, a manufacturing method of the flat synthetic fiber according to Motomeko 1 Ru der 1.5 times or more the flattening of the nozzle section during spinning.
JP2003014388A 2003-01-23 2003-01-23 Method for producing flat synthetic fiber Expired - Fee Related JP4063684B2 (en)

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