WO2006043661A1 - Hollow acrylic synthetic fiber - Google Patents
Hollow acrylic synthetic fiber Download PDFInfo
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- WO2006043661A1 WO2006043661A1 PCT/JP2005/019393 JP2005019393W WO2006043661A1 WO 2006043661 A1 WO2006043661 A1 WO 2006043661A1 JP 2005019393 W JP2005019393 W JP 2005019393W WO 2006043661 A1 WO2006043661 A1 WO 2006043661A1
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- fiber
- acrylic synthetic
- synthetic fiber
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/28—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D01F6/40—Modacrylic fibres, i.e. containing 35 to 85% acrylonitrile
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/28—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D01F6/32—Monocomponent 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
Definitions
- the present invention relates to a hollow acrylic synthetic fiber that is suitable mainly for pile applications and is lightweight, soft and has a bristle and matting effect.
- Acrylic synthetic fibers are widely used in fields such as bores, seals, fleeces, fibers, and ypiles because of their soft feel and ease of handling.
- the needles especially those used for clothing are desired to be lightweight, and various proposals have been made for light weight fibers.
- a hollow acrylic fiber having a core-sheathed two spinning stock solution and having a hollow portion between the core and sheath Patent Document 1
- 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.
- Patent Document 1 requires a complicated process of using two spinning stock solutions and using a core-sheath nozzle (Patent Document 1), and only a cross section close to a circle is possible (Patent Documents 2, 3, and 4).
- Patent Documents 2, 3, and 4 there was a problem that the tactile sensation was hard and the hair separation was not good at a thick fineness.
- Patent Document 1 JP-A-9-78355
- Patent Document 2 JP 2003-96618
- Patent Document 3 JP-A 61-28014
- Patent Document 4 Republished Patent WOOOZ70133
- An object of the present invention is to obtain an acrylic synthetic fiber that is light and soft, has good brushing properties and has a matting effect at a large fineness.
- the present invention is a cross section in which the major axis Z minor axis of the fiber cross section is 3 or more and has a hollow portion. It is a hollow acrylic synthetic fiber characterized in that 580 ⁇ ! A fiber having a light transmittance of 70% or less at ⁇ 600 nm is preferred.
- a spinning solution of acrylonitrile-based polymer is obtained by spinning using a spinneret having holes in which at least one shape selected from a circle, an ellipse, and a rhombus is connected. Is also preferable.
- the hollow acrylic synthetic fiber of the present invention is light and soft and excellent in handling the hair, and also has pores inside the fiber, so that it has a matte and so-called dull feeling expression effect. Therefore, it is particularly suitable for pile fibers having a large fineness, and a lightweight, soft and high-grade pile fabric can be obtained.
- Fig. 1 is an example of a hole shape of a spinneret used in the present invention.
- FIG. 2 is a model diagram of a skin core structure of a fiber cross section taken out of a coagulation bath in the present invention.
- FIG. 3 is a cross-sectional photograph of a fiber after undergoing a hollowing process in the present invention.
- the acrylonitrile-based copolymer in the present invention comprises 30 to 92% by weight of acrylonitrile and 8 to 70% by weight of one or more butyl group-containing monomers copolymerizable with acrylo-tolyl. A copolymerized product is used.
- Bull group-containing monomers that can be copolymerized with acrylonitrile include acrylic acid, methacrylic acid, vinyl chloride, salt vinylidene, pyrbromide bromide, vinylidene bromide, vinyl acetates such as vinyl acetate, or bull pyrrolidone. , Burpyridine and its alkyl-substituted products
- This acrylonitrile copolymer is dissolved in an organic solvent such as acetone, acetonitrile, dimethylformamide, dimethylacetamide, dimethyl sulfoxide, or an inorganic solvent such as salty zinc, nitric acid or rhodan salt.
- an organic solvent such as acetone, acetonitrile, dimethylformamide, dimethylacetamide, dimethyl sulfoxide, or an inorganic solvent such as salty zinc, nitric acid or rhodan salt.
- Spinning stock solution but use inorganic or organic pigments or stabilizers effective in anti-mold, anti-coloring, light resistance, etc., or additives that adjust inorganic or organic gloss and whiteness. May be.
- the skin core structure formed in the coagulation bath becomes a structure having a relatively large core part inside each circle, ellipse or rhombus, as shown in FIG.
- the concentration of the organic solvent or 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 preferable. Is ⁇ 10 ° C. to + 50 ° C., more preferably 0 ° C.
- 90 ⁇ may be passed through saturated steam at LOO ° C!
- 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, but is dried at a low temperature of 5 to 70 ° C, preferably 20 to 50 ° C.
- the liquid content is 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.
- the yarn having the adjusted liquid content is passed through a hollowing process, and by this process, water and solvent present in the core part are instantaneously expanded and volatilized to create a void in the core part.
- the hollowing process may be a general dry heat treatment or hot heat treatment using hot air, etc., as long as the yarn can be rapidly heated, or a constant temperature bath using an organic compound such as polyethylene glycol or glycerin. . It is preferably performed at 120 to 180 ° C for dry heat and wet heat treatment, and at 100 to 140 ° C for a constant temperature bath. As a result, a fiber having voids in the core as shown in 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.
- Example 1 Example 1
- 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 100 fiber cross-sections with a porosity of 5% or more were hollowed out. And calculated by the following formula.
- Hollowing ratio (%) [(number of fibers with a porosity of 5% or more) / (number of fibers measured)] X 100 Note that the porosity is a value of a hollow portion that is a hole or a network in the fiber cross section. From the area (A) and the area (B) other than the hollow part, the following formula was used.
- the fiber strength and the point force of the texture are not preferred, so the fiber content 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.
- the light transmittance of the sample fiber was measured and evaluated at two points for each of five single fibers, for a total of 10 points.
- a transmission “bright field” neurogen lamp was used as the light source, and measurement was performed in the range of 580 to 600 nm, and the average of the transmittance at these wavelengths was defined as the light transmittance of the sample.
- 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.
- the solvent concentration in the solution from which the solvent was eluted was measured by gas chromatography (GC-14B) manufactured by Shimadzu Corporation. Fiber weight before soaking Fw, fiber weight after drying Fd, gas chromatography The solvent concentration in the solution measured from 1 was set as c, and the following formula was used.
- Liquid content (%) [(Fw-Fd) / Fd] X 100
- Solvent content (%) [C X (200 + Fw-Fd) / Fd] X 100.
- the liquid content at this stage was 95% by weight, and the acetone content was 9% by weight.
- low-temperature drying at 40 ° C for 7 minutes reduced the liquid content to 20% by weight and the acetone content to 5%.
- 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.
- the film was further stretched twice at 130 ° C and heat-treated at 145 ° C.
- 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.
- Z water 30Z70, passed through a bath at 25 ° C, where 1.5 times stretching was performed. Further, after passing through a water bath at 40 ° C, it was passed through hot water at 75 ° C where it was stretched twice. Furthermore, it 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.
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- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Artificial Filaments (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
Description
中空アクリル系合成繊維 Hollow acrylic synthetic fiber
技術分野 Technical field
[0001] 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ぐまたつや消 し効果のある、中空アクリル系合成繊維に関する。 TECHNICAL FIELD [0001] The present invention relates to a hollow acrylic synthetic fiber that is suitable mainly for pile applications and is lightweight, soft and has a bristle and matting effect.
背景技術 Background art
[0002] アクリル系合成繊維は、そのソフト感等の風合及び力卩ェの容易さから、ボア一、シ ール、フリース、ノ、ィパイル等の分野に広く使用されている。ノィル用途の中でも、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ィ匕 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。し力しながら、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ぐまた毛さばきが良 くない等の問題があった。 [0002] Acrylic synthetic fibers are widely used in fields such as bores, seals, fleeces, fibers, and ypiles because of their soft feel and ease of handling. Among the use of the needles, especially those used for clothing are desired to be lightweight, and various proposals have been made for light weight fibers. For example, a hollow acrylic fiber having a core-sheathed two spinning stock solution and having a hollow portion between the core and sheath (Patent Document 1), 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 require a complicated process of using two spinning stock solutions and using a core-sheath nozzle (Patent Document 1), and only a cross section close to a circle is possible (Patent Documents 2, 3, and 4). In particular, there was a problem that the tactile sensation was hard and the hair separation was not good at a thick fineness.
特許文献 1 :特開平 9— 78355 Patent Document 1: JP-A-9-78355
特許文献 2:特開 2003— 96618 Patent Document 2: JP 2003-96618
特許文献 3:特開昭 61 - 28014 Patent Document 3: JP-A 61-28014
特許文献 4:再公表特許 WOOOZ70133 Patent Document 4: Republished Patent WOOOZ70133
発明の開示 Disclosure of the invention
発明が解決しょうとする課題 Problems to be solved by the invention
[0003] 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ぐまたつや 消し効果のある、アクリル系合成繊維を得ることである。 [0003] An object of the present invention is to obtain an acrylic synthetic fiber that is light and soft, has good brushing properties and has a matting effect at a large fineness.
課題を解決するための手段 Means for solving the problem
[0004] すなわち本発明は、繊維断面の長軸 Z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、 580ηπ!〜 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 、。 That is, the present invention is a cross section in which the major axis Z minor axis of the fiber cross section is 3 or more and has a hollow portion. It is a hollow acrylic synthetic fiber characterized in that 580ηπ! A fiber having a light transmittance of 70% or less at ~ 600 nm is preferred.
[0005] 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。 [0005] In addition, a spinning solution of acrylonitrile-based polymer is obtained by spinning using a spinneret having holes in which at least one shape selected from a circle, an ellipse, and a rhombus is connected. Is also preferable.
発明の効果 The invention's effect
[0006] 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。 [0006] The hollow acrylic synthetic fiber of the present invention is light and soft and excellent in handling the hair, and also has pores inside the fiber, so that it has a matte and so-called dull feeling expression effect. Therefore, it is particularly suitable for pile fibers having a large fineness, and a lightweight, soft and high-grade pile fabric can be obtained.
図面の簡単な説明 Brief Description of Drawings
[0007] [図 1]本発明に使用する紡糸口金の孔形状の例である。 [0007] Fig. 1 is an example of a hole shape of a spinneret used in the present invention.
[図 2]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。 FIG. 2 is a model diagram of a skin core structure of a fiber cross section taken out of a coagulation bath in the present invention.
[図 3]本発明にお 、て中空化工程を経た後の繊維断面写真である。 FIG. 3 is a cross-sectional photograph of a fiber after undergoing a hollowing process in the present invention.
符号の説明 Explanation of symbols
[0008] 1 :スキン層 [0008] 1: Skin layer
2 :コア層 2: Core layer
発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION
[0009] 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%、とァ クリロ-トリルと共重合可能な 1種または 2種以上のビュル基含有モノマー 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。 [0009] The acrylonitrile-based copolymer in the present invention comprises 30 to 92% by weight of acrylonitrile and 8 to 70% by weight of one or more butyl group-containing monomers copolymerizable with acrylo-tolyl. A copolymerized product is used.
アクリロニトリルと共重合可能なビュ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、塩ィ匕ビユリデン、臭化ピ ル、臭化ビ-リデン、酢酸ビニルのような ビュルエステル類、或いはビュルピロリドン、ビュルピリジン及びそのアルキル置換体 Bull group-containing monomers that can be copolymerized with acrylonitrile include acrylic acid, methacrylic acid, vinyl chloride, salt vinylidene, pyrbromide bromide, vinylidene bromide, vinyl acetates such as vinyl acetate, or bull pyrrolidone. , Burpyridine and its alkyl-substituted products
、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、ァリルスルホン酸、メタリルスルホン酸、 p—スチ レンスルホン酸、 2—アクリルアミドー 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。 , Acrylic acid ester, methacrylic acid ester, acrylic acid amide, methacrylic acid amide or their mono- and dialkyl-substituted products, allylsulfonic acid, methallylsulfonic acid, p-styrenesulfonic acid, 2-acrylamide-2-methylpropanesulfonic acid , Isoprenesulfo Examples include acids and alkali metal salts thereof.
[0010] 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、ァセトニトリル、ジメ チルホルムアミド、ジメチルァセトアミド、ジメチルスルホキシド、あるいは、無機溶媒、 例えば塩ィ匕亜鉛、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鲭、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。 [0010] This acrylonitrile copolymer is dissolved in an organic solvent such as acetone, acetonitrile, dimethylformamide, dimethylacetamide, dimethyl sulfoxide, or an inorganic solvent such as salty zinc, nitric acid or rhodan salt. Spinning stock solution, but use inorganic or organic pigments or stabilizers effective in anti-mold, anti-coloring, light resistance, etc., or additives that adjust inorganic or organic gloss and whiteness. May be.
[0011] 次に、図 1に示すような円、楕円あるいは菱形力 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°C〜 + 50°C、さらに好ましくは 0°C〜 + 30°Cである。その後、 10 〜55°Cの低温浴を通し、さらに 55〜95°C、好ましくは 60〜80°C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〜: LOO°Cの飽和水蒸気中を通してもよ!、。 [0011] Next, as shown in FIG. 1, spinning is performed in a coagulation bath through a spinneret having a hole in which three or more shapes selected from a circle, ellipse, or rhombus force are connected. By using these nozzles, the skin core structure formed in the coagulation bath becomes 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 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 preferable. Is −10 ° C. to + 50 ° C., more preferably 0 ° C. to + 30 ° C. Then, 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 Stretches 2-8 times. Then, in order to further reduce the solvent content in the wet yarn, 90 ~: may be passed through saturated steam at LOO ° C!
[0012] 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 60〜20 0重量%程度あるが、それを 5〜70°C、好ましくは 20〜50°C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ぐ熱風等 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ぉ ヽて は、 120〜180°C、恒温浴においては 100〜140°C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。 実施例 [0012] 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, but is dried at a low temperature of 5 to 70 ° C, preferably 20 to 50 ° C. The liquid content is 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. The yarn having the adjusted liquid content is passed through a hollowing process, and by this process, water and solvent present in the core part are instantaneously expanded and volatilized to create a void in the core part. Therefore, the hollowing process may be a general dry heat treatment or hot heat treatment using hot air, etc., as long as the yarn can be rapidly heated, or a constant temperature bath using an organic compound such as polyethylene glycol or glycerin. . It is preferably performed at 120 to 180 ° C for dry heat and wet heat treatment, and at 100 to 140 ° C for a constant temperature bath. As a result, a fiber having voids in the core as shown in 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. Example
[0013] 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。 [0013] The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples. Prior to describing the examples, measurement methods and the like will be described.
[0014] (繊維の中空化率の測定法) [0014] (Measurement method of fiber hollowing ratio)
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。 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 100 fiber cross-sections with a porosity of 5% or more were hollowed out. And calculated by the following formula.
中空化率 (%) = [ (空隙率が 5%以上の繊維数) / (測定した繊維数) ] X 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。 Hollowing ratio (%) = [(number of fibers with a porosity of 5% or more) / (number of fibers measured)] X 100 Note that the porosity is a value of a hollow portion that is a hole or a network in the fiber cross section. From the area (A) and the area (B) other than the hollow part, the following formula was used.
空隙率 (%) = [Aの面積 Z (A+Bの面積) ] Porosity (%) = [A area Z (A + B area)]
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力も好ましくないため、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 、と判断した。 For the cross section where the hollow part is ruptured and the void part is open toward the fiber surface, the fiber strength and the point force of the texture are not preferred, so the fiber content of such a cross section exceeds 10%. The product was judged not to have adequate performance as a hollow fiber.
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。 The matte effect was evaluated by measuring the light transmittance of a single fiber.
[0015] (単繊維光透過率の測定法) [0015] (Measurement method of single fiber light transmittance)
ォ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 = 20 mで行った。なお、光源には透過'明 視野'ノヽ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。 Using a Olympus Co., Ltd. metal system microscope, the light transmittance of the sample fiber was measured and evaluated at two points for each of 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 m. A transmission “bright field” neurogen lamp was used as the light source, and measurement was performed in the range of 580 to 600 nm, and the average of the transmittance at these wavelengths was defined as the light transmittance of the sample.
[0016] (含液率及び含溶媒率の測定) [0016] (Measurement of liquid content and solvent content)
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°C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°C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 一より測定した、溶液中の溶媒濃度を cとし、次式により算出した。 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 gas chromatography (GC-14B) manufactured by Shimadzu Corporation. Fiber weight before soaking Fw, fiber weight after drying Fd, gas chromatography The solvent concentration in the solution measured from 1 was set as c, and the following formula was used.
含液率(%) = [ (Fw-Fd) /Fd] X 100 Liquid content (%) = [(Fw-Fd) / Fd] X 100
含溶媒率(%) = [C X (200 + Fw-Fd) /Fd] X 100 。 Solvent content (%) = [C X (200 + Fw-Fd) / Fd] X 100.
[0017] (実施例 1) [0017] (Example 1)
アクリロニトリル Z塩化ビュル Z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 Z水 = 30Z70、 20°Cの凝固浴に紡出し、ついでアセトン Z水 = 25Z75、 25°Cの浴に通し、ここで 1. 5倍の延伸を行った。さらに、 40°Cの水 洗浴に通した後、 75°C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°C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°C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°Cで 2倍に延伸し、 145°Cで熱処理を 行った。得られた繊維は長軸 Z短軸 =4Zlの 22dtexであり、中空化率は 92%、光 透過率は 60%であった。 A spinning stock solution (spinning stock solution A) prepared by dissolving an acrylonitrile copolymer consisting of acrylonitrile Z butyl chloride Z sodium styrenesulfonate = 49.5 / 50 / 0.5 in acetone to a polymer concentration of 29%, Acetone Z water = 30Z70, spun into a 20 ° C coagulation bath through a 50-hole nozzle with four holes with a diameter of 0.14 mm in a row and then acetone Z water = 25Z75, 25 ° C bath The film was stretched 1.5 times here. Further, after passing through a water bath at 40 ° C, it was passed through hot water at 75 ° C where it was stretched twice. 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 for 7 minutes reduced 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 with a major axis Z minor axis = 4 Zl, a hollowing rate of 92%, and a light transmittance of 60%.
[0018] (実施例 2) [0018] (Example 2)
実施例 1の紡糸原液 Aを、長軸 Z短軸 = 1. 5Z1 (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%、含ァセ 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 Z短軸 = 5Zlの 20dtexであり、中空化率は 90%、光透過率は 64%であつ た。 Spinning stock solution A of Example 1 was spun in the same manner as in Example 1 in which four ellipses with a major axis Z minor axis = 1.5 Z1 (major axis = 0.15 mm) were connected, and contained after low-temperature drying. The liquid ratio was reduced to 20% by weight and the acetone content was reduced to 4%. Thereafter, hollowing treatment and drawing heat treatment were performed, and the obtained fiber was 20 dtex with a major axis Z minor axis = 5 Zl, a hollowing rate of 90%, and a light transmittance of 64%.
[0019] (実施例 3) [Example 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 Z水 = 30Z70、 20°Cの凝固浴に紡出し、ついでアセトン Z水 = 35Z65、 25°Cの浴に通し、ここで 2倍の延伸を行った。さらに、 40°Cの水洗 浴に通した後、 75°C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°Cの低温乾燥を 6 分間行うことにより、含液率を 18重量0 /0、含アセトン率を 4%に低下させた。その後、 該繊維を 160°C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°Cで 1. 5倍に延伸し、 145°Cで熱処理 を行った。得られた繊維は長軸 Z短軸 =4Zlの 22dtexであり、中空化率は 89%、 光透過率は 62%であった。 Spinning stock solution A of Example 1 was spun into a coagulation bath of acetone Z water = 30Z70, 20 ° C through a nozzle with a hole shape of four circles each having a diameter of 0.14 mm, and then acetone Z It passed through a bath of water = 35Z65, 25 ° C., and was stretched twice here. Further, after passing through a water bath at 40 ° C, it was passed through hot water at 75 ° C, where it was stretched twice. At this stage, the liquid content was 87% by weight and the acetone content was 7% by weight. Next, dry at 40 ° C at low temperature 6 By performing minutes, the liquid content 18 weight 0/0 decreased the containing acetone ratio of 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 was 22 dtex with a major axis Z minor axis = 4 Zl, a hollowing ratio of 89%, and a light transmittance of 62%.
[0020] (実施例 4) [0020] (Example 4)
アクリロニトリル Z塩化ビ-リデン Z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 Z水 = 30Z70、 20°Cの凝固浴に紡出し、ついでァ セトン Z水 = 30Z70、 25°Cの浴に通し、ここで 1. 5倍の延伸を行った。さらに、 40 °Cの水洗浴に通した後、 75°Cの熱水中に通し、ここで 2倍の延伸を行った。 A spinning stock solution (spinning stock solution B) in which an acrylonitrile copolymer consisting of acrylonitrile Z vinylidene chloride Z sodium styrenesulfonate = 50.0 / 490/1. , It was spun into a coagulation bath of acetone Z water = 30Z70, 20 ° C through a nozzle with a hole shape consisting of four circles with a diameter of 0.14 mm and a number of holes of 50, followed by caseon Z water = 30Z70, 25 ° C. Then, the film was stretched 1.5 times. Further, after passing through a water bath at 40 ° C., it was passed through hot water at 75 ° C., where it was stretched twice.
さらに、 96°C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°C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°C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°Cで 1. 5倍に延伸し、 150°Cで熱処理を行った。得られた 繊維は長軸 Z短軸 =4Zlの 22dtexであり、中空化率は 95%、光透過率は 57%で めつに。 Further, it 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. for 6 minutes reduced 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 resulting fiber is 22 dtex with a major axis Z minor axis = 4 Zl, hollowing rate of 95%, and light transmittance of 57%.
[0021] (実施例 5) [Example 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 15 0のノズルを通して、アセトン Z水 = 30Z70、 20°Cの凝固浴に紡出し、ついでァセト ン Z水 = 30Z70、 25°Cの浴に通し、ここで 1. 5倍の延伸を行った。さらに、 40°Cの 水洗浴に通した後、 75°Cの熱水中に通し、ここで 2倍の延伸を行った。さらに、 96°C 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°C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°C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°Cで 1. 5倍に延伸し、 150°Cで熱処理を行った。得られた繊維は長軸 Z短 軸 = 5Zlの lOdtexであり、中空化率は 93%、光透過率は 66%であった。 Spinning stock solution B of Example 4 was spun into a coagulation bath of acetone Z water = 30Z70, 20 ° C through a nozzle with a hole shape of 150 holes having a diameter of 0.08 mm and connected in series to a 20 ° C coagulation bath. Z water = 30Z70, passed through a bath at 25 ° C, where 1.5 times stretching was performed. Further, after passing through a water bath at 40 ° C, it was passed through hot water at 75 ° C where it was stretched twice. Furthermore, it 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 for 6 minutes reduced the liquid content to 16% by weight and the acetone content to 1%. Thereafter, the fiber was allowed to stay in a 165 ° C. dry heat treatment step for 10 seconds, and water and acetone were expanded and volatilized to develop a hollow portion. After that The film was stretched 1.5 times at 135 ° C and heat-treated at 150 ° C. The obtained fiber was lOdtex having a major axis Z minor axis = 5 Zl, a hollowing ratio of 93%, and a light transmittance of 66%.
[0022] (比較例 1) [0022] (Comparative Example 1)
実施例 1の紡糸原液 Aを、長軸 Z短軸 = 8Zl (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°C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。 Spinning stock solution A of Example 1 was spun by the same method as in Example 1 with a major axis Z minor axis = 8 Zl (major axis = 0.66 mm), and the liquid content after low-temperature drying was 15 wt%. The acetone content was reduced to 4%. After that, hollowing treatment was performed at 160 ° C. However, the hollow portion burst, and most of the cross-sections did not remain flat. After that, drawing heat treatment was performed, but the cross-section that did not retain the flat shape was the majority even in the final fiber, the presence ratio of the fiber with the hollow portion ruptured was 55%, and the light transmittance was 60%.
[0023] (比較例 2) [0023] (Comparative Example 2)
実施例 1の紡糸原液 Aを、長軸 Z短軸 = 8Zl (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°Cで中空化処理を行った力 中空化率は 27%と低ぐ光透過率は 8 1%であった。 Spinning stock solution A of Example 1 was spun by the same method as in Example 1 with a major axis Z minor axis = 8 Zl (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, the hollowing rate at 160 ° C was 27%, and the light transmittance was 81%.
[0024] 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 [0024] The obtained hollowing ratio, light transmittance, and the existence ratio of the cross-section in which the hollow portion is ruptured are shown.
1に示した。 Shown in 1.
[0025] [表 1] 中空化率 光透過率 中空部が破裂した断面の [0025] [Table 1] Hollowing rate Light transmittance Cross section of hollow part ruptured
% % 存在割合 (%) %% Existence (%)
実施例 1 9 2 6 0 1 Example 1 9 2 6 0 1
実施例 2 9 0 6 4 0 Example 2 9 0 6 4 0
実施例 3 8 9 6 2 0 Example 3 8 9 6 2 0
実施例 4 9 5 5 7 0 Example 4 9 5 5 7 0
実施例 5 9 3 6 6 1 Example 5 9 3 6 6 1
比較例 1 3 2 6 0 5 5 Comparative Example 1 3 2 6 0 5 5
比較例 2 2 7 8 1 0 Comparative Example 2 2 7 8 1 0
Claims
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| Application Number | Priority Date | Filing Date | Title |
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| JP2006543092A JP5014799B2 (en) | 2004-10-22 | 2005-10-21 | Hollow acrylic synthetic fiber |
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| JP2004-308471 | 2004-10-22 |
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| Application Number | Title | Priority Date | Filing Date |
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| WO (1) | WO2006043661A1 (en) |
Citations (3)
| 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 |
-
2005
- 2005-10-21 WO PCT/JP2005/019393 patent/WO2006043661A1/en not_active Ceased
- 2005-10-21 JP JP2006543092A patent/JP5014799B2/en not_active Expired - Fee Related
Patent Citations (3)
| 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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| JPWO2006043661A1 (en) | 2008-05-22 |
| JP5014799B2 (en) | 2012-08-29 |
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