JP5014799B2 - Hollow acrylic synthetic fiber - Google Patents

Hollow acrylic synthetic fiber Download PDF

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JP5014799B2
JP5014799B2 JP2006543092A JP2006543092A JP5014799B2 JP 5014799 B2 JP5014799 B2 JP 5014799B2 JP 2006543092 A JP2006543092 A JP 2006543092A JP 2006543092 A JP2006543092 A JP 2006543092A JP 5014799 B2 JP5014799 B2 JP 5014799B2
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fiber
acetone
weight
water
cross
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JPWO2006043661A1 (en
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正明 三好
陽啓 大本
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Kaneka Corp
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/28Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/40Modacrylic fibres, i.e. containing 35 to 85% acrylonitrile
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/28Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/32Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds comprising halogenated hydrocarbons as the major constituent

Description

本発明は、主にパイル用途に適した、軽量かつソフトで毛さばきがよく、またつや消し効果のある、中空アクリル系合成繊維に関する。   The present invention relates to a hollow acrylic synthetic fiber that is suitable mainly for pile applications, is lightweight, soft, has good hairiness, and has a matting effect.

アクリル系合成繊維は、そのソフト感等の風合及び加工の容易さから、ボアー、シール、フリース、ハイパイル等の分野に広く使用されている。パイル用途の中でも、特に衣料に用いられるものは、軽量であることが望まれており、従来から繊維の軽量化に向け、様々な提案がされている。例えば、2つの紡糸原液を芯鞘紡糸し、芯鞘間に中空部を有する中空アクリル繊維(特許文献1)、C字型ノズルを用いて紡糸した、略C字型断面を有するアクリル系合成繊維(特許文献2)、スキン層とコア層を形成させ、その後熱処理を行うことにより中空部を形成させるアクリル系合成繊維(特許文献3、4)などが提案されている。しかしながら、これらは2つの紡糸原液を用い芯鞘ノズルを使用するという複雑な工程を要すること(特許文献1)や、円形に近い断面しか出来ない(特許文献2、3、4)ため、特に太い繊度において触感が硬く、また毛さばきが良くない等の問題があった。
特開平9−78355 特開2003−96618 特開昭61−28014 再公表特許WO00/70133
Acrylic synthetic fibers are widely used in fields such as bores, seals, fleeces, and high piles because of their soft feel and ease of processing. Among pile applications, especially those used for apparel are desired to be lightweight, and various proposals have been made to reduce the weight of fibers. For example, a hollow acrylic fiber (Patent Document 1) in which two spinning dope solutions are spun into a core and sheath and have a hollow portion between the core and sheath, and an acrylic synthetic fiber having a substantially C-shaped cross section spun using a C-shaped nozzle Patent Document 2 proposes an acrylic synthetic fiber (Patent Documents 3 and 4) that forms a hollow portion by forming a skin layer and a core layer and then performing heat treatment. However, these are particularly thick because they require a complicated process of using two spinning dope solutions and using a core-sheath nozzle (Patent Document 1) and only a cross-section that is close to a circle (Patent Documents 2, 3, and 4). There are problems such as a feeling of fineness in touch and a poor hair separation.
JP-A-9-78355 JP2003-96618 JP 61-28014 A Republished patent WO00 / 70133

本発明の目的は、太い繊度において、軽量かつソフトで毛さばきが良く、またつや消し効果のある、アクリル系合成繊維を得ることである。   An object of the present invention is to obtain an acrylic synthetic fiber that is lightweight, soft, has good hair brushing properties and has a matting effect at a large fineness.

すなわち本発明は、繊維断面の長軸/短軸が3以上の断面でかつ中空部を有することを特徴とする中空アクリル系合成繊維であり、580nm〜600nmにおける単繊維の光透過率が70%以下であるものが好ましい。   That is, the present invention is a hollow acrylic synthetic fiber characterized in that the major axis / minor axis of the fiber cross section is a cross section of 3 or more and has a hollow portion, and the light transmittance of a single fiber at 580 nm to 600 nm is 70%. The following are preferred.

また、アクリロニトリル系重合体の紡糸原液を円、楕円及び菱形から選択される少なくとも1種の形状を3個以上連ねた孔を有する紡糸口金を用いて紡糸して得られるものも好ましい。   Also preferred are those obtained by spinning an acrylonitrile-based polymer spinning solution using a spinneret having holes in which at least one shape selected from a circle, an ellipse and a rhombus is connected.

本発明の中空アクリル系合成繊維は、軽量かつソフトで毛さばきに優れ、また、繊維内部に空孔を有するため、つや消し、いわゆるダル感発現効果がある。このため、特に、太い繊度のパイル用繊維に適しており、軽量かつソフトで高品位なパイル布帛が出来る。   The hollow acrylic synthetic fiber of the present invention is light and soft and excellent in hair handling, and has pores inside the fiber, so that it has a matte and so-called dull feeling expression effect. For this reason, it is particularly suitable for pile fibers having a large fineness, and a lightweight, soft and high-quality pile fabric can be obtained.

本発明に使用する紡糸口金の孔形状の例である。It is an example of the hole shape of the spinneret used for this invention. 本発明における凝固浴出の繊維断面のスキンコア構造のモデル図である。It is a model figure of the skin core structure of the fiber cross section from the coagulation bath in this invention. 本発明において中空化工程を経た後の繊維断面写真である。It is a fiber cross-section photograph after passing through the hollowing process in the present invention.

符号の説明Explanation of symbols

1:スキン層
2:コア層
1: Skin layer 2: Core layer

本発明におけるアクリロニトリル系共重合体は、アクリロニトリル30〜92重量%、とアクリロニトリルと共重合可能な1種または2種以上のビニル基含有モノマー8〜70重量%を主成分として共重合してなるものを使用する。
アクリロニトリルと共重合可能なビニル基含有モノマーとしては、アクリル酸、メタクリル酸、塩化ビニル、塩化ビニリデン、臭化ビニル、臭化ビニリデン、酢酸ビニルのようなビニルエステル類、或いはビニルピロリドン、ビニルピリジン及びそのアルキル置換体、アクリル酸エステル、メタクリル酸エステル、アクリル酸アミド、メタクリル酸アミド又はそれらのモノ及びジアルキル置換体、アリルスルホン酸、メタリルスルホン酸、p−スチレンスルホン酸、2−アクリルアミド−2−メチルプロパンスルホン酸、イソプレンスルホン酸及びこれらのアルカリ金属塩等が挙げられる。
The acrylonitrile copolymer in the present invention is obtained by copolymerizing 30 to 92% by weight of acrylonitrile and 8 to 70% by weight of one or more vinyl group-containing monomers copolymerizable with acrylonitrile as main components. Is used.
Examples of vinyl group-containing monomers that can be copolymerized with acrylonitrile include vinyl esters such as acrylic acid, methacrylic acid, vinyl chloride, vinylidene chloride, vinyl bromide, vinylidene bromide, vinyl acetate, or vinyl pyrrolidone, vinyl pyridine, and the like. Alkyl substituted product, acrylic acid ester, methacrylic acid ester, acrylic acid amide, methacrylic acid amide or mono- and dialkyl substituted products thereof, allyl sulfonic acid, methallyl sulfonic acid, p-styrene sulfonic acid, 2-acrylamido-2-methyl Examples include propanesulfonic acid, isoprenesulfonic acid, and alkali metal salts thereof.

このアクリロニトリル系共重合体を有機溶媒、例えば、アセトン、アセトニトリル、ジメチルホルムアミド、ジメチルアセトアミド、ジメチルスルホキシド、あるいは、無機溶媒、例えば塩化亜鉛、硝酸、ロダン塩等に溶解させて、紡糸原液とするが、無機又は有機の顔料あるいは防錆、着色防止、耐光性等に効果のある安定剤、あるいは無機または有機の光沢、白度を調整する添加剤等を使用してもよい。   The acrylonitrile-based copolymer is dissolved in an organic solvent such as acetone, acetonitrile, dimethylformamide, dimethylacetamide, dimethyl sulfoxide, or an inorganic solvent such as zinc chloride, nitric acid, rhodan salt, etc. Inorganic or organic pigments or stabilizers effective for rust prevention, coloring prevention, light resistance, etc., or additives for adjusting inorganic or organic gloss and whiteness may be used.

次に、図1に示すような円、楕円あるいは菱形から選択される少なくとも1種の形状を3個以上連ねた孔を有する紡糸口金を通じて凝固浴に紡出する。これらのノズルを使用することにより、凝固浴において形成されるスキンコア構造は図2のように、各々の円、楕円あるいは菱形の内部にそれぞれ比較的大きなコア部を有する構造となる。ここで、スキン層を形成させるためには、浴中の有機溶媒もしくは無機溶媒又は両者の濃度は好ましくは1〜50重量%、さらに好ましくは5〜35重量%であり、また温度は好ましくは−10℃〜+50℃、さらに好ましくは0℃〜+30℃である。その後、10〜55℃の低温浴を通し、さらに55〜95℃、好ましくは60〜80℃の熱水浴を通し、これら浴中にて、1.1〜10倍、好ましくは2〜8倍の延伸を行う。その後、さらに湿潤糸条中の溶媒含率を減少させるため、90〜100℃の飽和水蒸気中を通してもよい。     Next, it spins to a coagulation bath through the spinneret which has the hole which connected 3 or more of at least 1 sort (s) selected from a circle | round | yen, an ellipse, or a rhombus as shown in FIG. By using these nozzles, the skin core structure formed in the coagulation bath has a structure having a relatively large core part inside each circle, ellipse or rhombus, as shown in FIG. Here, in order to form the skin layer, the concentration of the organic solvent or the inorganic solvent in the bath or both is preferably 1 to 50% by weight, more preferably 5 to 35% by weight, and the temperature is preferably − It is 10 ° C to + 50 ° C, more preferably 0 ° C to + 30 ° C. Thereafter, it passes through a low temperature bath of 10 to 55 ° C, and further passes through a hot water bath of 55 to 95 ° C, preferably 60 to 80 ° C. In these baths, 1.1 to 10 times, preferably 2 to 8 times Is stretched. Thereafter, in order to further reduce the solvent content in the wet yarn, it may be passed through saturated steam at 90 to 100 ° C.

溶媒含率を減少させた方が、後の中空化工程において、中空化率が高くなる傾向がある。水洗浴出あるいは飽和水蒸気工程出の湿潤糸条は通常、含液率が60〜200重量%程度あるが、それを5〜70℃、好ましくは20〜50℃で低温乾燥を行い、含液率を5〜40重量%、好ましくは15〜30重量%にする。この時、水及び溶媒はコア部に多く存在すると考えられる。この含液率を調整した糸条を中空化工程に通すが、この工程により、コア部に存在する水及び溶媒を瞬時に膨張、揮発させ、コア部に空隙を生じさせる。従い、中空化工程は糸条を急加熱出来るものであればよく、熱風等による一般的な乾熱処理、湿熱処理、あるいはポリエチレングリコール、グリセリン等のような有機化合物を利用した恒温浴等が挙げられる。乾熱及び湿熱処理においては、120〜180℃、恒温浴においては100〜140℃で行うことが好ましい。これにより、図3のようなコア部に空隙が生じた繊維が得られる。中空化工程の後、必要に応じて、延伸、熱処理を行い、概ね扁平断面形状の中空部を有する繊維が得られる。   When the solvent content is reduced, the hollowing rate tends to increase in the subsequent hollowing step. The wet yarn from the washing bath or from the saturated steam process usually has a liquid content of about 60 to 200% by weight, and is dried at a low temperature of 5 to 70 ° C., preferably 20 to 50 ° C. 5 to 40% by weight, preferably 15 to 30% by weight. At this time, it is considered that a large amount of water and solvent are present in the core part. The yarn having the adjusted liquid content is passed through a hollowing step, and this step causes water and solvent present in the core portion to instantaneously expand and volatilize to generate voids in the core portion. Accordingly, the hollowing step is not limited as long as the yarn can be rapidly heated, and examples thereof include general dry heat treatment with hot air, wet heat treatment, or a constant temperature bath using an organic compound such as polyethylene glycol and glycerin. . The dry heat and wet heat treatment are preferably performed at 120 to 180 ° C., and the constant temperature bath is preferably performed at 100 to 140 ° C. Thereby, the fiber which the space | gap produced in the core part like FIG. 3 is obtained. After the hollowing step, if necessary, stretching and heat treatment are performed to obtain a fiber having a hollow portion having a generally flat cross-sectional shape.

以下に実施例を示し、本発明を更に詳細に説明するが、本発明はこれらの実施例に限定されるものではない。尚、実施例の記載に先立ち、測定法等について説明する。   Examples Hereinafter, the present invention will be described in more detail with reference to Examples, but the present invention is not limited to these Examples. Prior to describing the examples, measurement methods and the like will be described.

(繊維の中空化率の測定法)
試料となる繊維束の断面形状を、走査型電子顕微鏡にて、約100個の繊維断面が入る倍率にて撮影し、100個の繊維断面において、空隙率が5%以上のものを中空化しているとみなし、次式によって算出した。
中空化率(%)=[(空隙率が5%以上の繊維数)/(測定した繊維数)]×100
なお、空隙率は、繊維断面において空孔または網目状になっている中空部分の面積(A)と中空部以外の面積(B)より、以下の式により算出した。
空隙率(%)=[Aの面積/(A+Bの面積)]
なお、中空部が破裂し、空隙部が繊維表面に向けて開口している断面については、繊維強度や風合の点から好ましくないため、このような断面の繊維の存在割合が10%を超えるものは、中空繊維として適切な性能を有しないと判断した。
また、つや消し効果の評価は、単繊維の光透過率の測定により実施した。
(Measurement method of fiber hollowing ratio)
The cross-sectional shape of the sample fiber bundle was photographed with a scanning electron microscope at a magnification at which about 100 fiber cross-sections were inserted, and the 100 fiber cross-sections having a porosity of 5% or more were hollowed out. And calculated by the following formula.
Hollowing rate (%) = [(number of fibers with a porosity of 5% or more) / (number of fibers measured)] × 100
The porosity was calculated by the following formula from the area (A) of the hollow portion that is in the form of holes or meshes in the fiber cross section and the area (B) other than the hollow portion.
Porosity (%) = [A area / (A + B area)]
In addition, about the cross section which the hollow part bursts and the space | gap part is opening toward the fiber surface, since it is unpreferable from the point of fiber strength or a feeling, the existence ratio of the fiber of such a cross section exceeds 10%. The product was judged not to have adequate performance as a hollow fiber.
The matte effect was evaluated by measuring the light transmittance of a single fiber.

(単繊維光透過率の測定法)
オリンパス株式会社製金属システム顕微鏡を用いて、試料となる繊維の光透過率を、それぞれ単繊維5本について各2箇所、合計10点で測定を行い評価した。対物レンズの倍率は50倍とし、測定領域はφ=20μmで行った。なお、光源には透過・明視野・ハロゲンランプを用い、580〜600nmの範囲で測定を行い、これら波長での透過率の平均をその試料の光透過率とした。
(Measurement method of single fiber light transmittance)
Using a metal system microscope manufactured by Olympus Corporation, the light transmittance of the sample fiber was measured and evaluated at two points for each of the five single fibers, for a total of 10 points. The magnification of the objective lens was 50 times, and the measurement area was φ = 20 μm. The light source was a transmission / bright field / halogen lamp, and measurement was performed in the range of 580 to 600 nm. The average of the transmittance at these wavelengths was taken as the light transmittance of the sample.

(含液率及び含溶媒率の測定)
測定する繊維約2gを純水200g中に浸漬し、還流冷却管を使用し95℃で30分間煮沸する事より繊維中の溶媒を溶出させた。その後、浸漬していた繊維を取り出し、110℃で2時間乾燥させ、その繊維の重量を測定した。一方、溶媒を溶出させた溶液中における溶媒濃度を(株)島津製作所製ガスクロマトグラフィー(GC−14B)により測定した。浸漬前の繊維重量をFw、乾燥後の繊維重量をFd、ガスクロマトグラフィーより測定した、溶液中の溶媒濃度をCとし、次式により算出した。
含液率(%)=[(Fw−Fd)/Fd]×100
含溶媒率(%)=[C×(200+Fw−Fd)/Fd]×100 。
(Measurement of liquid content and solvent content)
About 2 g of the fiber to be measured was immersed in 200 g of pure water, and the solvent in the fiber was eluted by boiling at 95 ° C. for 30 minutes using a reflux condenser. Thereafter, the immersed fiber was taken out, dried at 110 ° C. for 2 hours, and the weight of the fiber was measured. On the other hand, the solvent concentration in the solution from which the solvent was eluted was measured by Shimadzu Corporation gas chromatography (GC-14B). The fiber weight before immersion was Fw, the fiber weight after drying was Fd, and the solvent concentration in the solution was measured by gas chromatography.
Liquid content (%) = [(Fw−Fd) / Fd] × 100
Solvent content (%) = [C × (200 + Fw−Fd) / Fd] × 100.

(実施例1)
アクリロニトリル/塩化ビニル/スチレンスルホン酸ナトリウム=49.5/50/0.5からなるアクリロニトリル系共重合体を重合体濃度29%になるようにアセトンに溶解した紡糸原液(紡糸原液A)を、直径が0.14mmの円を4つ連ねた孔形状のホール数50のノズルを通して、アセトン/水=30/70、20℃の凝固浴に紡出し、ついでアセトン/水=25/75、25℃の浴に通し、ここで1.5倍の延伸を行った。さらに、40℃の水洗浴に通した後、75℃の熱水中に通し、ここで2倍の延伸を行った。この段階における含液率は95重量%、含アセトン率は9重量%であった。次に、40℃の低温乾燥を7分間行うことにより、含液率を20重量%、含アセトン率を5%に低下させた。その後、該繊維を160℃の乾熱処理工程に10秒滞留させて、水及びアセトンを膨張揮発させ、中空部を発現させた。その後さらに、130℃で2倍に延伸し、145℃で熱処理を行った。得られた繊維は長軸/短軸=4/1の22dtexであり、中空化率は92%、光透過率は60%であった。
Example 1
A spinning stock solution (spinning stock solution A) prepared by dissolving an acrylonitrile-based copolymer of acrylonitrile / vinyl chloride / sodium styrenesulfonate = 49.5 / 50 / 0.5 in acetone to a polymer concentration of 29%, Is spun into a coagulation bath of acetone / water = 30/70, 20 ° C. through a nozzle having a hole shape of 50 holes each having four 0.14 mm circles, and then acetone / water = 25/75, 25 ° C. It was passed through a bath and stretched 1.5 times here. Furthermore, after passing through a 40 degreeC water-washing bath, it passed through 75 degreeC hot water, and stretched twice here. The liquid content at this stage was 95% by weight, and the acetone content was 9% by weight. Next, low-temperature drying at 40 ° C. was performed for 7 minutes, thereby reducing the liquid content to 20% by weight and the acetone content to 5%. Thereafter, the fiber was allowed to stay in a 160 ° C. dry heat treatment step for 10 seconds, and water and acetone were expanded and volatilized to develop a hollow portion. Thereafter, the film was further stretched twice at 130 ° C. and heat-treated at 145 ° C. The obtained fiber was 22 dtex of major axis / minor axis = 4/1, the hollowing rate was 92%, and the light transmittance was 60%.

(実施例2)
実施例1の紡糸原液Aを、長軸/短軸=1.5/1(長軸=0.15mm)の楕円を4つ連ねた、実施例1と同様の方法で紡糸し、低温乾燥後の含液率を20重量%、含アセトン率を4%に低下させた。その後、中空化処理、延伸熱処理を行い、得られた繊維は長軸/短軸=5/1の20dtexであり、中空化率は90%、光透過率は64%であった。
(Example 2)
The spinning dope A of Example 1 was spun by the same method as in Example 1 in which four ellipses having a major axis / minor axis = 1.5 / 1 (major axis = 0.15 mm) were connected, and after low temperature drying The liquid content was reduced to 20% by weight and the acetone content to 4%. Thereafter, hollowing treatment and stretching heat treatment were performed, and the obtained fiber was 20 dtex of major axis / minor axis = 5/1, the hollowing rate was 90%, and the light transmittance was 64%.

(実施例3)
実施例1の紡糸原液Aを、直径が0.14mmの円を4つ連ねた孔形状のホール数50のノズルを通して、アセトン/水=30/70、20℃の凝固浴に紡出し、ついでアセトン/水=35/65、25℃の浴に通し、ここで2倍の延伸を行った。さらに、40℃の水洗浴に通した後、75℃の熱水中に通し、ここで2倍の延伸を行った。この段階における含液率は87重量%、含アセトン率は7重量%であった。次に、40℃の低温乾燥を6分間行うことにより、含液率を18重量%、含アセトン率を4%に低下させた。その後、該繊維を160℃の乾熱処理工程に10秒滞留させて、水及びアセトンを膨張揮発させ、中空部を発現させた。その後さらに、130℃で1.5倍に延伸し、145℃で熱処理を行った。得られた繊維は長軸/短軸=4/1の22dtexであり、中空化率は89%、光透過率は62%であった。
(Example 3)
The spinning dope A of Example 1 was spun into a coagulation bath of acetone / water = 30/70, 20 ° C. through a nozzle having a hole number of 50 in which four circles having a diameter of 0.14 mm were connected, and then acetone. / Water = 35/65, passed through a 25 ° C. bath, where the film was stretched twice. Furthermore, after passing through a 40 degreeC water-washing bath, it passed through 75 degreeC hot water, and stretched twice here. The liquid content at this stage was 87% by weight, and the acetone content was 7% by weight. Next, low-temperature drying at 40 ° C. was performed for 6 minutes, thereby reducing the liquid content to 18% by weight and the acetone content to 4%. Thereafter, the fiber was allowed to stay in a 160 ° C. dry heat treatment step for 10 seconds, and water and acetone were expanded and volatilized to develop a hollow portion. Thereafter, the film was further stretched 1.5 times at 130 ° C. and heat-treated at 145 ° C. The obtained fiber had 22 dtex of major axis / minor axis = 4/1, the hollowing ratio was 89%, and the light transmittance was 62%.

(実施例4)
アクリロニトリル/塩化ビニリデン/スチレンスルホン酸ナトリウム=50.0/490/1.0からなるアクリロニトリル系共重合体を重合体濃度30%になるようにアセトンに溶解した紡糸原液(紡糸原液B)を、直径が0.14mmの円を4つ連ねた孔形状のホール数50のノズルを通して、アセトン/水=30/70、20℃の凝固浴に紡出し、ついでアセトン/水=30/70、25℃の浴に通し、ここで1.5倍の延伸を行った。さらに、40℃の水洗浴に通した後、75℃の熱水中に通し、ここで2倍の延伸を行った。
さらに、96℃の飽和水蒸気中を2分間通し、この段階における含液率は103重量%、含アセトン率は2重量%であった。次に、40℃の低温乾燥を6分間行うことにより、含液率を21重量%、含アセトン率を1%に低下させた。その後、該繊維を165℃の乾熱処理工程に10秒滞留させて、水及びアセトンを膨張揮発させ、中空部を発現させた。その後さらに、135℃で1.5倍に延伸し、150℃で熱処理を行った。得られた繊維は長軸/短軸=4/1の22dtexであり、中空化率は95%、光透過率は57%であった。
Example 4
A spinning stock solution (spinning stock solution B) prepared by dissolving an acrylonitrile-based copolymer of acrylonitrile / vinylidene chloride / sodium styrenesulfonate = 50.0 / 490 / 1.0 in acetone so as to have a polymer concentration of 30%, Was spun into a coagulation bath of acetone / water = 30/70, 20 ° C. through a nozzle having a hole shape of 50 holes each having four 0.14 mm circles, and then acetone / water = 30/70, 25 ° C. It was passed through a bath and stretched 1.5 times here. Furthermore, after passing through a 40 degreeC water-washing bath, it passed through 75 degreeC hot water, and stretched twice here.
Further, it was passed through saturated steam at 96 ° C. for 2 minutes, and the liquid content at this stage was 103% by weight and the acetone content was 2% by weight. Next, low-temperature drying at 40 ° C. was performed for 6 minutes to reduce the liquid content to 21% by weight and the acetone content to 1%. Thereafter, the fiber was allowed to stay in a dry heat treatment step at 165 ° C. for 10 seconds, and water and acetone were expanded and volatilized to develop a hollow portion. Thereafter, the film was further stretched 1.5 times at 135 ° C. and heat-treated at 150 ° C. The obtained fiber had 22 dtex of major axis / minor axis = 4/1, the hollowing ratio was 95%, and the light transmittance was 57%.

(実施例5)
実施例4の紡糸原液Bを、直径が0.08mmの円を5つ連ねた孔形状のホール数150のノズルを通して、アセトン/水=30/70、20℃の凝固浴に紡出し、ついでアセトン/水=30/70、25℃の浴に通し、ここで1.5倍の延伸を行った。さらに、40℃の水洗浴に通した後、75℃の熱水中に通し、ここで2倍の延伸を行った。さらに、96℃の飽和水蒸気中を2分間通し、この段階における含液率は92重量%、含アセトン率は2重量%であった。次に、40℃の低温乾燥を6分間行うことにより、含液率を16重量%、含アセトン率を1%に低下させた。その後、該繊維を165℃の乾熱処理工程に10秒滞留させて、水及びアセトンを膨張揮発させ、中空部を発現させた。その後さらに、135℃で1.5倍に延伸し、150℃で熱処理を行った。得られた繊維は長軸/短軸=5/1の10dtexであり、中空化率は93%、光透過率は66%であった。
(Example 5)
The spinning dope B of Example 4 was spun into a coagulation bath of acetone / water = 30/70, 20 ° C. through a nozzle having a hole number of 150 in which five circles having a diameter of 0.08 mm were connected, and then acetone. / Water = 30/70, passed through a 25 ° C. bath, and stretched 1.5 times here. Furthermore, after passing through a 40 degreeC water-washing bath, it passed through 75 degreeC hot water, and stretched twice here. Further, it was passed through saturated steam at 96 ° C. for 2 minutes. At this stage, the liquid content was 92% by weight and the acetone content was 2% by weight. Next, low-temperature drying at 40 ° C. was performed for 6 minutes to reduce the liquid content to 16% by weight and the acetone content to 1%. Thereafter, the fiber was allowed to stay in a dry heat treatment step at 165 ° C. for 10 seconds, and water and acetone were expanded and volatilized to develop a hollow portion. Thereafter, the film was further stretched 1.5 times at 135 ° C. and heat-treated at 150 ° C. The obtained fiber had 10 dtex of major axis / minor axis = 5/1, the hollowing ratio was 93%, and the light transmittance was 66%.

(比較例1)
実施例1の紡糸原液Aを、長軸/短軸=8/1(長軸=0.66mm)の、実施例1と同様の方法で紡糸し、低温乾燥後の含液率を15重量%、含アセトン率を4%に低下させた。その後、160℃で中空化処理を行ったが、中空部の破裂が起こり、大部分が扁平形状をとどめない断面となった。その後、延伸熱処理を行ったが、最終繊維においても扁平形状をとどめない断面が大部分となり、中空部が破裂した繊維の存在割合は55%、光透過率は60%であった。
(Comparative Example 1)
Spinning stock solution A of Example 1 was spun by the same method as in Example 1 with the major axis / minor axis = 8/1 (major axis = 0.66 mm), and the liquid content after low-temperature drying was 15% by weight. The acetone content was reduced to 4%. Thereafter, the hollowing treatment was performed at 160 ° C., but the hollow portion was ruptured, and most of the cross-sections did not remain flat. Thereafter, a drawing heat treatment was performed, but the cross-section that did not retain the flat shape was also large in the final fiber, and the existence ratio of the fiber in which the hollow portion was ruptured was 55%, and the light transmittance was 60%.

(比較例2)
実施例1の紡糸原液Aを、長軸/短軸=8/1(長軸=0.66mm)の、実施例1と同様の方法で紡糸し、低温乾燥後の含液率を5重量%、含アセトン率を2%に低下させた。その後、160℃で中空化処理を行ったが、中空化率は27%と低く、光透過率は81%であった。
(Comparative Example 2)
Spinning stock solution A of Example 1 was spun by the same method as in Example 1 with the major axis / minor axis = 8/1 (major axis = 0.66 mm), and the liquid content after low-temperature drying was 5% by weight. The acetone content was reduced to 2%. Thereafter, hollowing treatment was performed at 160 ° C., but the hollowing rate was as low as 27% and the light transmittance was 81%.

得られた中空化率、光透過率及び中空部が破裂した断面の存在割合について表1に示した。   Table 1 shows the obtained hollowing ratio, light transmittance, and the existence ratio of the cross-section where the hollow portion was ruptured.

Figure 0005014799
Figure 0005014799

Claims (1)

アクリロニトリル系重合体の紡糸原液を円、楕円及び菱形から選択される少なくとも1種の形状を3個以上連ねた孔を有する紡糸口金を用いて紡糸してなり、繊維断面の長軸/短軸が3以上の断面でかつ中空部を有し、580nm〜600nmにおける単繊維の光透過率が70%以下であることを特徴とする中空アクリル系合成繊維。 Spinning stock solution of acrylonitrile polymer is spun using a spinneret having holes in which at least one kind selected from circle, ellipse and rhombus is connected, and the major / minor axis of the fiber cross section is A hollow acrylic synthetic fiber having a cross section of 3 or more and a hollow part, wherein the light transmittance of a single fiber at 580 nm to 600 nm is 70% or less.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6128014A (en) * 1984-07-18 1986-02-07 Kanegafuchi Chem Ind Co Ltd Production of fiber containing acrylonitrile
JPS62177255A (en) * 1985-10-24 1987-08-04 鐘淵化学工業株式会社 Pile composition containing foamed fiber
JPS6375113A (en) * 1986-09-12 1988-04-05 Teijin Ltd Polyester yarn for flock processing

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6128014A (en) * 1984-07-18 1986-02-07 Kanegafuchi Chem Ind Co Ltd Production of fiber containing acrylonitrile
JPS62177255A (en) * 1985-10-24 1987-08-04 鐘淵化学工業株式会社 Pile composition containing foamed fiber
JPS6375113A (en) * 1986-09-12 1988-04-05 Teijin Ltd Polyester yarn for flock processing

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