WO2003042454A1 - Polyester binder fiber for papermaking - Google Patents
Polyester binder fiber for papermaking Download PDFInfo
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- WO2003042454A1 WO2003042454A1 PCT/JP2002/011786 JP0211786W WO03042454A1 WO 2003042454 A1 WO2003042454 A1 WO 2003042454A1 JP 0211786 W JP0211786 W JP 0211786W WO 03042454 A1 WO03042454 A1 WO 03042454A1
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- polyester binder
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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
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/62—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/10—Organic non-cellulose fibres
- D21H13/20—Organic non-cellulose fibres from macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H13/24—Polyesters
Definitions
- the present invention relates to a polyester binder fiber suitable for producing a polyester fiber paper using a polyester fiber as a main fiber.
- a core-sheath type polyester-based composite fiber in which a modified polyester having a low softening point is disposed in a sheath portion and a polyester having a normal melting point is disposed in a core portion is used as one polyester-based binder fiber.
- a conjugate fiber requires complicated spinning equipment and advanced operation management, so that it becomes a high-cost binder fiber and cannot be used for applications requiring heat resistance.
- Japanese Patent Publication No. 49-8809 and Japanese Patent Application Laid-Open No. 1-104883 propose the use of undrawn polyester fibers as binder fibers.
- Japanese Unexamined Patent Publication (Kokai) No. 11-104,823 discloses, as a polyester-based binder fiber which strongly adheres to the drawn polyester fiber of the main fiber and gives a soft feeling to the obtained synthetic fiber paper, an unstretched polyester fiber.
- the intrinsic viscosity (hereinafter referred to as intrinsic viscosity) is 0.5 to 0.58
- the single-fiber fineness is 1.2 denier (about 1.3 dtex) or less
- the birefringence hereinafter referred to as ⁇ ).
- An object of the present invention is to provide a papermaking polyester binder fiber which has a small shrinkage during drying and excellent adhesiveness when producing polyester fiber paper.
- the present inventors have found that a binder fiber which can achieve the above object can be obtained by using a polyester having a very low intrinsic viscosity and selecting proper spinning conditions.
- the intrinsic viscosity is 0.35 to 0.49
- the single fiber fineness is 1.5 decitex or less
- the sheet area shrinkage defined below is 70% or less.
- Polyester binder fibers for papermaking are proposed.
- Sheet area shrinkage (%) ⁇ (Ao- Ai) / Ao ⁇ X I 0 0
- AQ is the area of the sheet before shrinkage processing
- the sheet is 80% by weight of polyester binder fiber cut to 5 mxn length and 20% by weight of NBKP. % And well mixed in water. Mix and disperse the mixture.
- the size is about 25 cm X about 25 cm and the basis weight is about 50 gm 2 .
- the polyester constituting the polyester binder fiber for papermaking of the present invention is 85 mol of the main repeating unit. /. Or more, preferably 9 5 mole 0/0 or a polyester comprising ethylene terephthalate tallates, or may be obtained by a small amount copolymerized terephthalic acid component and / or components other than E Ji render recall component.
- the intrinsic viscosity of the polyester fiber of the present invention ranges from 0.35 to 0.49, preferably from 0.40 to 0.47. If the intrinsic viscosity exceeds 0.49, the shrinkage will be too high, and the strength of the obtained polyester fiber paper will be low. On the other hand, when the intrinsic viscosity is less than 0.35, spinnability deteriorates and spinning becomes extremely difficult.
- the single fiber fineness of the polyester fiber of the present invention is 1.5 dtex or less, preferably 1.3 dtex or less. When the single fiber fineness exceeds 1.5 dtex, the strength of the obtained polyester fiber paper becomes low.
- the lower limit of the single fiber fineness is not particularly limited, but is usually about 0.2 decitex from the viewpoint of stable spinning properties.
- the polyester fiber of the present invention has a sheet area shrinkage ratio as defined above of 70% or less, and preferably 65% or less. If the area shrinkage exceeds 70%, the formation of the polyester fiber paper will be poor and the strength of the paper will be low.
- the area shrinkage can be set by adjusting physical properties of the polyester fiber, such as intrinsic viscosity, ⁇ , and specific gravity, to an appropriate range. If the intrinsic viscosity of the polyester fiber is 0.35 to 0.49, to reduce the sheet area shrinkage to 70% or less, the ⁇ of the polyester fiber should be 0.012 or less, and the specific gravity should be 1.35 or less. It is preferable to adjust it.
- the polyester fiber of the present invention can be produced by the following method. That is, pelletized polyester having an intrinsic viscosity of 0.36 to 0.51 and preferably polyethylene terephthalate is dried by an ordinary method, and then melt-spun in a spinning facility equipped with a screw-type extruder, cooled, and solidified. Take off at a rate of 700-150 OmZ.
- the moisture content of the pellet, the drying temperature, the melt spinning temperature and the residence time of the molten polymer in the spinning machine are set and adjusted so that the intrinsic viscosity of the polyester fiber is in the range of 0.35 to 0.49. To be.
- the spinning speed is set according to each intrinsic viscosity and discharge amount, so that the ⁇ n of the polyester fiber is 0.012 or less and the specific gravity is 1.35 or less.
- the obtained polyester fiber is converged, and supplied to a dying machine while keeping the water content of 5 to 40% by weight, and cut into a predetermined fiber length. If the water content is lower than 5% by weight, the dispersibility of the fibers during papermaking deteriorates. If the moisture content exceeds 40% by weight, water scattering when cutting with a drum-type cutter increases, making it difficult to operate the cutter.
- the fiber length is 2 to 20 mm, preferably 3 to 10 mm.
- the polyester fiber produced in this manner has a small drying shrinkage in the papermaking process, has a strong adhesive force to the polyester fiber, and has excellent performance as a binder fiber for polyester fiber paper.
- the measurement was carried out in a Ubbelohde viscosity tube at a temperature of 35 ° C using orthochlorophenol as a solvent.
- a square sheet machine manufactured by Kumagai Riki Kogyo Co., Ltd. 80% by weight of polyester binder fiber and 20% by weight of NBKP cut to a length of 5 mm are thoroughly stirred and mixed in water to disperse. a size of about 25 CMX about 25 cm, a basis weight to create about 50 'gZm 2 sheet.
- the sheet is placed on a perforated Teflon sheet and subjected to a relaxation shrinkage treatment in a hot air circulating drier at 140 ° C for 5 minutes.
- the sheet area shrinkage ratio is calculated from the area ⁇ before the sheet shrinkage processing and the area ⁇ ⁇ after the sheet shrinkage processing by the following equation.
- Sheet area shrinkage (%) ⁇ (Ao-Ai) / Ao ⁇ X I 00
- the sample was charged into a density gradient tube (25 ° C) consisting of a mixed solvent of n-heptane and carbon tetrachloride, and the value after 6 hours was taken as the specific gravity.
- polyester binder fiber containing water is dried in a hot air circulating drier at 120 ° C. until it is completely dried. From the weight WQ of the sample before drying and the weight of the sample after drying, it was determined by the following equation.
- Moisture percentage (%) ⁇ (Wo-Wi) / Wi ⁇ X 100
- the adhesiveness of the polyester binder fiber was evaluated by the strength of the polyester fiber paper.
- the paper strength was measured by measuring the tensile strength according to JIS SP 8113, and expressed as the breaking length. The quality of the formation of the polyester fiber paper was visually determined.
- Level 1 The distribution of the constituent fibers is uniform, and there are very few spots
- Level 2 The distribution of the constituent fibers is slightly uneven, and the spots are slightly noticeable.
- Level 3 The distribution of constituent fibers is very uneven, and spots are noticeable.
- Polyethylene terephthalate pellets with different intrinsic viscosities are dried at 170 ° C, melted at 300 ° C, discharged through a mouthpiece with a hole count of 1192 at a discharge rate of 180 g / min.
- the yarn was drawn at a spinning speed of 1150 m / min to obtain an undrawn polyethylene terephthalate fiber having a single fiber fineness of 1.3 dtex.
- the polyethylene terephthalate fiber was made into a tow of about 200,000 decitex, and after the oil agent was applied, it was squeezed so that the water content of the toe became about 15% by weight, and cut into a length of 5 mm with a drum type cutter. An undrawn polyethylene terephthalate fiber having the properties shown in Table 1 was obtained.
- DOO fibers 6 0 disperses the weight percent in water
- the fiber is adjusted to a fiber concentration of 0.04% by weight and fed to a round paper machine. After papermaking, the fiber is dried with a Yankee dryer at 130 ° C and the basis weight is about 25 g. Zm 2 polyethylene terephthalate fiber paper was obtained.
- This paper Table 1 shows the characteristics. table 1
- polyester binder fiber of the present invention has an extremely small shrinkage during papermaking drying, it is possible to obtain a polyester fiber paper excellent in formation and firmly bonded to each other from the fiber.
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Abstract
Description
明 細 書 抄紙用ポリエステルバインダー繊維 技術分野 Description Polyester binder fiber for papermaking Technical field
本発明は、 主体繊維としてポリエステル繊維を用いるポリエステル繊維紙の製 造に適したポリエステルバインダー繊維に関するものである。 背景の技術 The present invention relates to a polyester binder fiber suitable for producing a polyester fiber paper using a polyester fiber as a main fiber. Background technology
近年、 機械的特性、 電気的特性、 耐熱性、 寸法安定性、 疎水性等の優れた物性 およぴコスト優位性の面から、 ポリエステル繊維を原料の一部または全部に使用 した抄紙法による合成繊維紙が多くなつている。 また該合成繊維紙のパインダ一 繊維として、 従来はポリエチレン系繊維、 ポリビニルアルコール繊維等が使用さ れていたが、 ポリエステル繊維が主体となってきた合成繊維紙の抄紙には、 同じ ポリエステル繊維が最適なバインダーとして主体的に使用されるようになってき た。 In recent years, from the viewpoint of excellent physical properties such as mechanical properties, electrical properties, heat resistance, dimensional stability, hydrophobicity, and cost advantage, and synthesis by a papermaking method using polyester fiber as part or all of the raw material Fiber paper is increasing. Conventionally, polyethylene fibers, polyvinyl alcohol fibers, etc. have been used as the binder fibers of the synthetic fiber paper. However, the same polyester fibers are most suitable for making synthetic fiber paper mainly made of polyester fibers. It has been used as an active binder.
例えば、 低軟化点の変性ポリエステルを鞘部に、 通常の融点を有するポリエス テルを芯部に配置した芯鞘型ポリエステル系複合繊維がポリエステル系バインダ 一繊維として使用されている。 しかし、 このような複合繊維は、 複雑な紡糸設備 および高度な運転管理が必要となるため、 コス トの高いバインダー繊維となり、 また、 耐熱性が要求される用途には使えないという問題がある。 For example, a core-sheath type polyester-based composite fiber in which a modified polyester having a low softening point is disposed in a sheath portion and a polyester having a normal melting point is disposed in a core portion is used as one polyester-based binder fiber. However, such a conjugate fiber requires complicated spinning equipment and advanced operation management, so that it becomes a high-cost binder fiber and cannot be used for applications requiring heat resistance.
一方、 特公昭 4 9 - 8 8 0 9号公報、 特開平 1— 1 0 4 8 2 3号公報等には未 延伸ポリエステル繊維をバインダー繊維として使用することが提案されている。 特に特開平 1一 1 0 4 8 2 3号公報には、 主体繊維のポリエステル延伸糸と強く 接着し、 得られる合成繊維紙にソフトな風合を与えるポリエステル系バインダー 繊維として、'未延伸ポリエステル繊維の極限粘度(以下固有粘度と称する) を 0 . 5 0〜0 . 5 8、 単糸繊度を 1 . 2デニール (約 1 . 3デシテックス) 以下およ び複屈折率 (以下、 Δ ηと記す) を 0 . 0 2以下、 比重を 1 . 3 5以下にするこ とが重要であるとされている。 しかしながら、 このような未延伸ポリエステル繊 維は高い収縮性を有しているため、 低い坪量 (3 0 g //m2以下) で高強力な合成 繊維紙を製造する工程、 すなわち高速で乾燥温度の高い抄紙工程で使用された場 合、 未延伸ポリエステル繊維の過度な熱収縮によって、 得られたポリエステル繊 維紙の地合が悪くなり、 紙の強力も低いものとなってしまうという問題がある。 発明の開示 On the other hand, Japanese Patent Publication No. 49-8809 and Japanese Patent Application Laid-Open No. 1-104883 propose the use of undrawn polyester fibers as binder fibers. In particular, Japanese Unexamined Patent Publication (Kokai) No. 11-104,823 discloses, as a polyester-based binder fiber which strongly adheres to the drawn polyester fiber of the main fiber and gives a soft feeling to the obtained synthetic fiber paper, an unstretched polyester fiber. The intrinsic viscosity (hereinafter referred to as intrinsic viscosity) is 0.5 to 0.58, the single-fiber fineness is 1.2 denier (about 1.3 dtex) or less, and the birefringence (hereinafter referred to as Δη). ) Is less than 0.02 and the specific gravity is less than 1.35. However, such undrawn polyester fibers Since fibers have high shrinkage, they were used in the process of producing high-strength synthetic fiber paper with a low basis weight (30 g // m 2 or less), that is, in the papermaking process at high speed and high drying temperature. In this case, excessive heat shrinkage of the undrawn polyester fiber deteriorates the texture of the obtained polyester fiber paper and lowers the strength of the paper. Disclosure of the invention
本発明の目的は、 ポリエステル繊維紙を製造する際、 乾燥時の収縮が小さく力、 つ接着性に優れた抄紙用ポリエステルバインダー繊維を提供することにある。 本発明者らは、 非常に低い固有粘度のポリエステルを用い、 しかも適正な紡糸 条件を選んだとき、 上記目的を達成できるバインダー繊維が得られることを見出 した。 An object of the present invention is to provide a papermaking polyester binder fiber which has a small shrinkage during drying and excellent adhesiveness when producing polyester fiber paper. The present inventors have found that a binder fiber which can achieve the above object can be obtained by using a polyester having a very low intrinsic viscosity and selecting proper spinning conditions.
すなわち、本発明によれば、 固有粘度が 0 . 3 5〜 0 . 4 9、単繊維繊度が 1 . 5デシテックス以下であり、 且つ、 下記に定義するシート面積収縮率が 7 0 %以 下の抄紙用ポリエステルバインダー繊維が提案される。 That is, according to the present invention, the intrinsic viscosity is 0.35 to 0.49, the single fiber fineness is 1.5 decitex or less, and the sheet area shrinkage defined below is 70% or less. Polyester binder fibers for papermaking are proposed.
シート面積収縮率 (%) = { (Ao- Ai) /Ao} X I 0 0 Sheet area shrinkage (%) = {(Ao- Ai) / Ao} X I 0 0
ここで、 AQはシートの収縮処理前の面積、 はシートの収縮処理後の面積で あり、 シートとは 5 mxnの長さに切断されたポリエステルパインダー繊維 8 0重 量%と N B K P 2 0重量%とを水中でよく攪拌 ·混合して分散させ、 大きさが約 2 5 c m X約 2 5 c mで、坪量が約 5 0 g m2となしたものをレヽう。 シートの収 縮処理とは、 該シートを室温中で一昼夜以上乾燥させた後、 孔を開けたテフロン シートの上に载せ、 1 4 0 °Cの熱風循環式乾燥機中で 5分間弛緩収縮処理を行う 操作をレ、う。 発明を実施するための最良の形態 Here, AQ is the area of the sheet before shrinkage processing, is the area of the sheet after shrinkage processing, and the sheet is 80% by weight of polyester binder fiber cut to 5 mxn length and 20% by weight of NBKP. % And well mixed in water. Mix and disperse the mixture. The size is about 25 cm X about 25 cm and the basis weight is about 50 gm 2 . After shrinking the sheet, dry it at room temperature for one day or more, place it on a perforated Teflon sheet, and relax and shrink in a hot air circulating dryer at 140 ° C for 5 minutes. Perform the processing operation. BEST MODE FOR CARRYING OUT THE INVENTION
本発明の抄紙用ポリエステルバインダー繊維を構成するポリエステルは、 主た る繰り返し単位の 8 5モル。/。以上、 好ましくは 9 5モル0 /0以上がエチレンテレフ タレートからなるポリエステルであり、 またテレフタル酸成分および/またはェ チレンダリコール成分以外の成分を少量共重合したものであっても良い。 なお、 これらのポリエステルには、本発明の効果を阻害しない範囲で、顔料、艷消し剤、 抗菌剤、 消臭剤、 蛍光増白剤、 紫外線吸収剤等の公知の添加剤を含んでいてもよ レ、。 The polyester constituting the polyester binder fiber for papermaking of the present invention is 85 mol of the main repeating unit. /. Or more, preferably 9 5 mole 0/0 or a polyester comprising ethylene terephthalate tallates, or may be obtained by a small amount copolymerized terephthalic acid component and / or components other than E Ji render recall component. Incidentally, these polyesters, pigments, matting agents, as long as the effects of the present invention are not impaired, It may contain known additives such as antibacterial agents, deodorants, fluorescent whitening agents, and ultraviolet absorbers.
本発明のポリエステル繊維の固有粘度の範囲は 0. 35〜 0. 49であり、 好 ましくは 0. 40〜0. 47の範囲である。 固有粘度が 0. 49を越えると収縮 率が高過ぎるものとなり、 また得られたポリエステル繊維紙の強力が低くなる。 一方、 固有粘度が 0. 35より小さくなると、 曳糸性が悪化し、 紡糸が極めて難 しくなる。 The intrinsic viscosity of the polyester fiber of the present invention ranges from 0.35 to 0.49, preferably from 0.40 to 0.47. If the intrinsic viscosity exceeds 0.49, the shrinkage will be too high, and the strength of the obtained polyester fiber paper will be low. On the other hand, when the intrinsic viscosity is less than 0.35, spinnability deteriorates and spinning becomes extremely difficult.
また、 本発明のポリエステル繊維の単繊維繊度は 1. 5デシテックス以下であ り、 好ましくは 1. 3デシテックス以下である。 単繊維繊度が 1. 5デシテック スを越えると、 得られたポリエステル繊維紙の強力が低くなる。 単繊維繊度の下 限は、 特に限定'されるものではないが、 通常安定な製糸性の点から 0. 2デシテ ックス程度である。 The single fiber fineness of the polyester fiber of the present invention is 1.5 dtex or less, preferably 1.3 dtex or less. When the single fiber fineness exceeds 1.5 dtex, the strength of the obtained polyester fiber paper becomes low. The lower limit of the single fiber fineness is not particularly limited, but is usually about 0.2 decitex from the viewpoint of stable spinning properties.
さらに、本発明のポリエステル繊維は、先に定義したシート面積収縮率が 70% 以下であり、 好ましくは 65%以下である。 面積収縮率が 70%を越えると、 ポ リエステル繊維紙の地合が悪くなり、 紙の強力も低いものとなる。 該面積収縮率 は、 ポリエステル繊維の固有粘度、 Δη、 比重等の物性を適切な範囲に調整する ことによって設定することができる。 なお、 ポリエステル繊維の固有粘度が 0. 35〜0. 49の場合、 シート面積収縮率を 70%以下とするには、 ポリエステ ル繊維の Δηを 0. 012以下おょぴ比重を 1. 35以下に調節するのが好まし い。 Further, the polyester fiber of the present invention has a sheet area shrinkage ratio as defined above of 70% or less, and preferably 65% or less. If the area shrinkage exceeds 70%, the formation of the polyester fiber paper will be poor and the strength of the paper will be low. The area shrinkage can be set by adjusting physical properties of the polyester fiber, such as intrinsic viscosity, Δη, and specific gravity, to an appropriate range. If the intrinsic viscosity of the polyester fiber is 0.35 to 0.49, to reduce the sheet area shrinkage to 70% or less, the Δη of the polyester fiber should be 0.012 or less, and the specific gravity should be 1.35 or less. It is preferable to adjust it.
本発明のポリエステル繊維は以下の方法で製造できる。 即ち、 ペレット化され た固有粘度 0. 36〜0. 51のポリエステル、 好ましくはポリエチレンテレフ タレートを常法によって乾燥後、 スクリュウー式押出機等を装備した紡糸設備で 溶融紡糸し、 冷却 ,固化し、 700〜150 OmZ分の速度で引取る。 ここで、 該ぺレットの含有水分率、 乾燥温度、 溶融紡糸温度およぴ溶融ポリマーの紡糸機 内滞留時間を設定、 調節し、 ポリエステル繊維の固有粘度が 0. 35〜0. 49 の範囲となるようにする。 また、 各々の固有粘度および吐出量に応じ、 紡糸速度 を設定し、 ポリエステル繊維の Δ nが 0. 012以下おょぴ比重が 1. 35以下 となるようにする。 得られたポリエステル繊維を収束し、 5〜40重量%の水分を保持した状態で 力ッターに供給し、 所定の繊維長に切断する。 なお、 水分率が 5重量%より低い と抄紙時の繊維の分散性が悪くなる。 水分率が 40重量%を越えると、 ドラム式 カッターで切断する際の水の飛散が多くなり、 カッターの運転が困難となる。 ま た、 繊維長は 2〜20mm、 好ましくは 3〜: 1 0 mmである。 繊維長が 2mmよ り短くなると、 ドラム式力ッターでの切断抵抗が大きくなるため、 ポリエステル 繊維が伸ばされたり、 単繊維同士が絡み易くなるため、 安定した切断が難しくな る。 繊維長が 20 mmより長くなると、 抄紙時の繊維の水中分散性が悪化する。 このようにして製造されたポリエステル繊維は抄紙工程での乾燥収縮が小さく、 かつポリエステル繊維と強い接着力を有しており、 ポリエステル繊維紙用バイン ダー繊維として優れた性能を有している。 The polyester fiber of the present invention can be produced by the following method. That is, pelletized polyester having an intrinsic viscosity of 0.36 to 0.51 and preferably polyethylene terephthalate is dried by an ordinary method, and then melt-spun in a spinning facility equipped with a screw-type extruder, cooled, and solidified. Take off at a rate of 700-150 OmZ. Here, the moisture content of the pellet, the drying temperature, the melt spinning temperature and the residence time of the molten polymer in the spinning machine are set and adjusted so that the intrinsic viscosity of the polyester fiber is in the range of 0.35 to 0.49. To be. In addition, the spinning speed is set according to each intrinsic viscosity and discharge amount, so that the Δn of the polyester fiber is 0.012 or less and the specific gravity is 1.35 or less. The obtained polyester fiber is converged, and supplied to a dying machine while keeping the water content of 5 to 40% by weight, and cut into a predetermined fiber length. If the water content is lower than 5% by weight, the dispersibility of the fibers during papermaking deteriorates. If the moisture content exceeds 40% by weight, water scattering when cutting with a drum-type cutter increases, making it difficult to operate the cutter. The fiber length is 2 to 20 mm, preferably 3 to 10 mm. If the fiber length is shorter than 2 mm, the cutting resistance of the drum type power cutter will increase, and the polyester fibers will be stretched and the single fibers will easily become entangled, making stable cutting difficult. If the fiber length is longer than 20 mm, the dispersibility of the fiber in water during papermaking deteriorates. The polyester fiber produced in this manner has a small drying shrinkage in the papermaking process, has a strong adhesive force to the polyester fiber, and has excellent performance as a binder fiber for polyester fiber paper.
実施例 Example
以下、 実施例により、 本発明を更に具体的に説明する。 なお、 実施例における 各項目は次の方法で測定した。 Hereinafter, the present invention will be described more specifically with reference to examples. Each item in the examples was measured by the following method.
(a) 固有粘度' (a) Intrinsic viscosity '
オルソクロロフエノールを溶媒として、 35 °Cの温度でウベローデ粘度管にて 測定し 。 The measurement was carried out in a Ubbelohde viscosity tube at a temperature of 35 ° C using orthochlorophenol as a solvent.
(b) シート面積収縮率 (b) Sheet area shrinkage
熊谷理機工業株式会社製の角型シートマシンを使って、 5mmの長さに切断さ れたポリエステルバインダー繊維 80重量%と N B K P 20重量%とを水中でよ く攪拌 ·混合して分散させ、 大きさが約 25 cmX約 25 cmで、 坪量が約 50' gZm2のシートを作成する。次に、該シートを室温中で一昼夜以上乾燥させた後、 孔を開けたテフロンシートの上に載せ、 140°Cの熱風循環式乾燥機の中で 5分 間弛緩収縮処理を行う。 シートの収縮処理前の面積 Αοと収縮処理後の面積 Αιと から次式によってシート面積収縮率を算出する。 Using a square sheet machine manufactured by Kumagai Riki Kogyo Co., Ltd., 80% by weight of polyester binder fiber and 20% by weight of NBKP cut to a length of 5 mm are thoroughly stirred and mixed in water to disperse. a size of about 25 CMX about 25 cm, a basis weight to create about 50 'gZm 2 sheet. Next, after drying the sheet at room temperature for one day or more, the sheet is placed on a perforated Teflon sheet and subjected to a relaxation shrinkage treatment in a hot air circulating drier at 140 ° C for 5 minutes. The sheet area shrinkage ratio is calculated from the area Αο before the sheet shrinkage processing and the area 収縮 ι after the sheet shrinkage processing by the following equation.
シート面積収縮率 (%) = {(Ao-Ai) /Ao} X I 00 Sheet area shrinkage (%) = {(Ao-Ai) / Ao} X I 00
(c) 複屈^率 (Δη) (c) Birefringence ^ rate (Δη)
市販の偏光顕微鏡を使って、 光源にナトリウムランプを用い、 試料をひ一プロ ムナフタリンに浸漬した状態下で B e r e kコンペンセーター法からレターデ一 ションを求めて算出した。 Using a commercially available polarizing microscope, a sodium lamp was used as the light source, and the sample was immersed in sodium pronaphthalene. Calculated.
( d ) 比重 (d) Specific gravity
n—ヘプタンと四塩化炭素の混合溶媒から成る密度勾配管 (2 5 °C) の中に試 料を投入し、 6時間経過後の値を読み比重とした。 The sample was charged into a density gradient tube (25 ° C) consisting of a mixed solvent of n-heptane and carbon tetrachloride, and the value after 6 hours was taken as the specific gravity.
( e ) 水分率 (e) Moisture percentage
水分を含んだ約 1 0 0 gのポリエステルバインダー繊維を 1 2 0 °Cの熱風循環 式乾燥機の中で絶乾になるまで乾燥する。乾燥前の試料の重量 WQと乾燥後の試料 の重量 から、 次式によって求めた。 About 100 g of polyester binder fiber containing water is dried in a hot air circulating drier at 120 ° C. until it is completely dried. From the weight WQ of the sample before drying and the weight of the sample after drying, it was determined by the following equation.
水分率 (%) = { (Wo-Wi) /Wi} X 1 0 0 Moisture percentage (%) = {(Wo-Wi) / Wi} X 100
( f ) 裂断長 (紙強力) および地合 (f) Break length (paper strength) and formation
ポリエステルバインダー繊維の接着性はポリエステル繊維紙の強力で評価した。 この紙強力は J I S P 8 1 1 3に従って引っ張り強さを測定し、 裂断長で表し た。 また、 ポリエステル繊維紙の地合の良否は目視で判定した。 The adhesiveness of the polyester binder fiber was evaluated by the strength of the polyester fiber paper. The paper strength was measured by measuring the tensile strength according to JIS SP 8113, and expressed as the breaking length. The quality of the formation of the polyester fiber paper was visually determined.
レベル 1 :構成繊維の分布が均一であり、 斑が非常に少ない Level 1: The distribution of the constituent fibers is uniform, and there are very few spots
レベル 2 :構成繊維の分布がやや不均一であり、 斑がやや目立つ Level 2: The distribution of the constituent fibers is slightly uneven, and the spots are slightly noticeable.
レベル 3 :構成繊維の分布が非常に不均一であり、 斑が目立つ。 Level 3: The distribution of constituent fibers is very uneven, and spots are noticeable.
[実施例 1〜3、 比較例 1 ] [Examples 1-3, Comparative Example 1]
固有粘度が異なるポリエチレンテレフタレートペレツトを 1 7 0 °Cで乾燥後、 3 0 0 °Cで溶融し、 孔数が 1 1 9 2の口金を通して、 吐出量 1 8 0 g /分で吐出 し、 紡糸速度 1 1 5 0 m/分の速度で引取り、 単繊維繊度が 1 . 3デシテックス の未延伸ポリエチレンテレフタレート繊維を得た。 該ポリエチレンテレフタレー ト繊維を約 2 0万デシテックスのトウとなし、 油剤を付与後、 トゥの水分率が約 1 5重量%となるように絞り、 ドラム式カッターで 5 mmの長さに切断し、 表 1 に示す特性の未延伸ポリエチレンテレフタレート繊維を得た。 Polyethylene terephthalate pellets with different intrinsic viscosities are dried at 170 ° C, melted at 300 ° C, discharged through a mouthpiece with a hole count of 1192 at a discharge rate of 180 g / min. The yarn was drawn at a spinning speed of 1150 m / min to obtain an undrawn polyethylene terephthalate fiber having a single fiber fineness of 1.3 dtex. The polyethylene terephthalate fiber was made into a tow of about 200,000 decitex, and after the oil agent was applied, it was squeezed so that the water content of the toe became about 15% by weight, and cut into a length of 5 mm with a drum type cutter. An undrawn polyethylene terephthalate fiber having the properties shown in Table 1 was obtained.
得られた未延伸ポリエチレンテレフタレート繊維 4 0重量0 /0と、 単繊維繊度が 0 . 6デシテックス、 長さが 5 mmの延伸熱処理されたポリエチレンテレフタレ ―ト繊維 6 0重量%とを水中へ分散させ、 繊維濃度が 0 . 0 4重量%となるよう に調整して円網抄紙機に供給し、 抄紙後、 1 3 0 °Cのヤンキー式ドライヤーで乾 燥し、 坪量が約 2 5 g Zm2のポリエチレンテレフタレート繊維紙を得た。 この紙 の特性を表 1に示す。 表 1 And unstretched polyethylene terephthalate obtained phthalate fibers 4 0 wt 0/0, a single fiber fineness of 0 6 dtex, length of 5 mm stretched heat-treated polyethylene terephthalate of -. DOO fibers 6 0 disperses the weight percent in water The fiber is adjusted to a fiber concentration of 0.04% by weight and fed to a round paper machine. After papermaking, the fiber is dried with a Yankee dryer at 130 ° C and the basis weight is about 25 g. Zm 2 polyethylene terephthalate fiber paper was obtained. This paper Table 1 shows the characteristics. table 1
[実施例 4〜5、 比較例 2 ] [Examples 4 and 5, Comparative Example 2]
吐出量およぴ紡糸速度の変更により収縮性の異なる未延伸繊維とする以外は実 施例 1と同じ方法、 条件で溶融紡糸を実施し、 各々表 2の特性を持つ未延伸ポリ エチレンテレフタレート繊維を得た。 これらの未延伸ポリエチレンテレフタレー ト繊維を実施例 1と同じ要領で 5 mmの長さに切断し、 該実施例と同じ条件で抄 紙した。 得られた紙の特性を表 2に示す。 表 2 Melt spinning was carried out under the same conditions and conditions as in Example 1 except that unstretched fibers differing in shrinkage were obtained by changing the discharge rate and spinning speed, and unstretched polyethylene terephthalate fibers having the properties shown in Table 2 respectively. I got These undrawn polyethylene terephthalate fibers were cut into a length of 5 mm in the same manner as in Example 1, and paper was made under the same conditions as in Example 1. Table 2 shows the properties of the obtained paper. Table 2
[実施例 6〜7、 比較例 3 ] [Examples 6 and 7, Comparative Example 3]
固有粘度が 0 . 4 7のポリエチレンテレフタレートペレットを 1 7 0 °Cで乾燥 後、 3 0 0 °Cで溶融し、 孔数が 1 1 9 2の口金を通して吐出し、 紡糸速度 1 1 5 O m/分で引き取った。 この時、 吐出量を変更して単繊維繊度の異なった未延伸 ポリエチレンテレフタレート繊維を得た。 これらの未延伸ポリエチレンテレフタ レート繊維の特性を表 3に示す。 これらの未延伸ポリエチレンテレフタレート繊 維を実施例 1と同じ要領で 5 mmの長さに切断し、 該実施例と同じ条件で抄紙し た。 得られた紙の特性を表 3に示す。 表 3 Dry polyethylene terephthalate pellets with intrinsic viscosity of 0.47 at 170 ° C Thereafter, the mixture was melted at 300 ° C., discharged through a mouthpiece having a number of holes of 119, and taken out at a spinning speed of 115 Om / min. At this time, the discharge amount was changed to obtain undrawn polyethylene terephthalate fibers having different single fiber finenesses. Table 3 shows the properties of these undrawn polyethylene terephthalate fibers. These unstretched polyethylene terephthalate fibers were cut to a length of 5 mm in the same manner as in Example 1, and paper was made under the same conditions as in Example 1. Table 3 shows the properties of the obtained paper. Table 3
産業上の利用可能性 Industrial applicability
本発明のポリエステルバインダー繊維は抄紙乾燥時の収縮が極めて小さいため、 該繊維からは、 地合に優れ且つ繊維同士が強固に接着したポリエステル繊維紙を 得ることができる。 Since the polyester binder fiber of the present invention has an extremely small shrinkage during papermaking drying, it is possible to obtain a polyester fiber paper excellent in formation and firmly bonded to each other from the fiber.
Claims
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003544260A JP4031435B2 (en) | 2001-11-14 | 2002-11-12 | Polyester binder fiber for papermaking |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001348375 | 2001-11-14 | ||
| JP2001-348375 | 2001-11-14 |
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|---|---|
| WO2003042454A1 true WO2003042454A1 (en) | 2003-05-22 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2002/011786 Ceased WO2003042454A1 (en) | 2001-11-14 | 2002-11-12 | Polyester binder fiber for papermaking |
Country Status (3)
| Country | Link |
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| JP (1) | JP4031435B2 (en) |
| TW (1) | TW200300181A (en) |
| WO (1) | WO2003042454A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012031525A (en) * | 2010-07-28 | 2012-02-16 | Nippon Ester Co Ltd | Wet short fiber nonwoven fabric |
| JP2019210566A (en) * | 2018-06-04 | 2019-12-12 | 帝人フロンティア株式会社 | Polyester-based binder fiber |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106133216B (en) | 2014-03-31 | 2021-03-30 | 可乐丽股份有限公司 | Polyester binder fibers |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0043555A1 (en) * | 1980-07-07 | 1982-01-13 | Teijin Limited | Paper-like polyester fiber sheet and process for producing the same |
| EP0117937A1 (en) * | 1983-02-01 | 1984-09-12 | Teijin Limited | Polyester binder fibers |
| JPH01104823A (en) * | 1987-10-16 | 1989-04-21 | Kuraray Co Ltd | Polyester binder yarn |
-
2002
- 2002-11-12 WO PCT/JP2002/011786 patent/WO2003042454A1/en not_active Ceased
- 2002-11-12 TW TW91133161A patent/TW200300181A/en unknown
- 2002-11-12 JP JP2003544260A patent/JP4031435B2/en not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0043555A1 (en) * | 1980-07-07 | 1982-01-13 | Teijin Limited | Paper-like polyester fiber sheet and process for producing the same |
| EP0117937A1 (en) * | 1983-02-01 | 1984-09-12 | Teijin Limited | Polyester binder fibers |
| JPH01104823A (en) * | 1987-10-16 | 1989-04-21 | Kuraray Co Ltd | Polyester binder yarn |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012031525A (en) * | 2010-07-28 | 2012-02-16 | Nippon Ester Co Ltd | Wet short fiber nonwoven fabric |
| JP2019210566A (en) * | 2018-06-04 | 2019-12-12 | 帝人フロンティア株式会社 | Polyester-based binder fiber |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4031435B2 (en) | 2008-01-09 |
| JPWO2003042454A1 (en) | 2005-03-10 |
| TW200300181A (en) | 2003-05-16 |
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