JP2002339287A - Undrawn polyester fiber for paper-making use - Google Patents
Undrawn polyester fiber for paper-making useInfo
- Publication number
- JP2002339287A JP2002339287A JP2001138401A JP2001138401A JP2002339287A JP 2002339287 A JP2002339287 A JP 2002339287A JP 2001138401 A JP2001138401 A JP 2001138401A JP 2001138401 A JP2001138401 A JP 2001138401A JP 2002339287 A JP2002339287 A JP 2002339287A
- Authority
- JP
- Japan
- Prior art keywords
- fiber
- polyester
- water
- weight
- fibers
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Paper (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、抄紙工程での水中
分散性に優れ、且つ優れた熱接着性を有する抄紙用の未
延伸ポリエステル繊維に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an unstretched polyester fiber for papermaking which has excellent dispersibility in water in a papermaking process and has excellent heat adhesion.
【0002】[0002]
【従来の技術】従来、抄紙用の合成繊維としてビニロン
繊維、ポリアクリロニトリル繊維、ポリプロピレン繊
維、ポリエステル繊維などが使用されている。近年、機
械的特性、電気的特性、耐熱性、寸法安定性等に優れ、
かつコスト優位性の高いポリエステル繊維を抄紙用原料
の一部または全部に使用することが多くなっている。特
に、抄紙用原料の殆ど全部がポリエステル繊維から成る
ポリエステル繊維紙は、ポリエステル繊維の優れた特性
をほぼ100%生かすことができる。また、合成繊維紙
のバインダー成分としては、従来ポリエチレン系繊維、
ポリビニルアルコール繊維等のバインダー繊維が使用さ
れている。しかし、このようなバインダー繊維を主体繊
維がポリエステル繊維である抄紙に使用した場合、ポリ
エステル繊維との相溶性が不十分であるため繊維間接着
が不十分になるという問題および異種ポリマーが混在す
ることでポリエステル繊維の優れた特性を滅失するとい
う問題が生ずる。したがって、ポリエステル繊維を主体
とする抄紙バインダー繊維としては接着力を有するポリ
エステル繊維そのものが最適である。ポリエステル繊維
に接着力を付与する方法として、低融点ポリエステルを
鞘部に通常の融点を有するポリエステルを芯部にしたポ
リエステル複合繊維がある。しかし、このようなポリエ
ステル複合繊維は、複数種のポリエステル、複雑な紡糸
設備および高度な運転管理が必要であり極めて高価なバ
インダー繊維となる。一方、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試みもあるが、ポリエス
テル繊維は水中分散性が悪く、例えば特公平1−351
20号公報に提案されているような分散向上剤を付与し
なければならない。この分散向上剤がポリエステル繊維
間の接着を著しく阻害するという問題があり、未延伸ポ
リエステル繊維をそのままバインダー繊維として使用す
るのは困難であった。2. Description of the Related Art Conventionally, vinylon fibers, polyacrylonitrile fibers, polypropylene fibers, polyester fibers and the like have been used as synthetic fibers for papermaking. In recent years, mechanical properties, electrical properties, heat resistance, excellent dimensional stability, etc.,
In addition, polyester fibers having high cost advantage are often used for a part or all of papermaking raw materials. In particular, polyester fiber paper in which almost all of the papermaking raw materials are made of polyester fibers can make use of almost 100% of the excellent properties of polyester fibers. Also, as a binder component of synthetic fiber paper, conventionally polyethylene-based fibers,
Binder fibers such as polyvinyl alcohol fibers are used. However, when such a binder fiber is used in papermaking in which the main fiber is a polyester fiber, the compatibility between the polyester fiber and the polyester fiber is insufficient, so that the problem of insufficient interfiber adhesion and the mixing of heterogeneous polymers. This causes a problem that excellent characteristics of the polyester fiber are lost. Therefore, as the papermaking binder fiber mainly composed of the polyester fiber, the polyester fiber itself having an adhesive force is optimal. As a method for imparting adhesive force to polyester fibers, there is a polyester composite fiber in which a low-melting polyester is used as a sheath and polyester having a normal melting point is used as a core. However, such a polyester conjugate fiber requires a plurality of types of polyester, complicated spinning equipment and advanced operation management, and becomes an extremely expensive binder fiber. On the other hand, there has been an attempt to use unstretched polyester fibers as binder fibers, but polyester fibers have poor dispersibility in water.
No. 20 must be provided with a dispersion improver. There is a problem that the dispersing agent significantly inhibits the adhesion between the polyester fibers, and it has been difficult to use undrawn polyester fibers as binder fibers as they are.
【0003】[0003]
【発明が解決しようとする課題】本発明は、ポリエステ
ル繊維紙を製造する際、抄紙工程での水中分散性を損な
うことなく、接着性に優れた抄紙用ポリエステル未延伸
繊維を提供することを目的とする。SUMMARY OF THE INVENTION An object of the present invention is to provide an unstretched polyester fiber for papermaking which has excellent adhesion without impairing dispersibility in water during the papermaking process when producing polyester fiber paper. And
【0004】[0004]
【課題を解決するための手段】本発明者は、上記目的を
達成するために鋭意検討を重ねた結果、繊維長が2〜2
0mmの未延伸ポリエステル繊維であって、該繊維表面
には繊維重量を基準としてポリエーテル・ポリエステル
共重合体が0.03重量%以上付着していると共に、水
分保持率が5〜40重量%であることを特徴とする抄紙
用未延伸ポリエステル繊維によって達成できることを見
出した。Means for Solving the Problems The present inventor has conducted intensive studies in order to achieve the above object, and as a result, the fiber length was 2 to 2
0 mm unstretched polyester fiber having a polyether / polyester copolymer adhered to the fiber surface at 0.03% by weight or more based on the fiber weight and having a water retention of 5 to 40% by weight. It has been found that this can be achieved by an unstretched polyester fiber for papermaking, which is characterized by a certain characteristic.
【0005】[0005]
【発明の実施の形態】以下、本発明の実施形態について
詳細に説明する。本発明の抄紙用未延伸ポリエステル繊
維を構成するポリエステルは、全繰り返し単位の85モ
ル%以上、好ましくは95モル%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る。テレフタル酸成
分およびエチレングリコール成分以外の成分を少量(通
常は、テレフタル酸成分に対して15モル%以下)共重
合したものであってもよい。なお、これらのポリエステ
ルには、公知の添加剤、例えば、顔料、染料、艶消し
剤、防汚剤、抗菌剤、消臭剤、蛍光増白剤、難燃剤、安
定剤、紫外線吸収剤、滑剤等を含んでもよい。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described in detail. The polyester constituting the unstretched polyester fiber for papermaking of the present invention is a polyester in which 85 mol% or more, preferably 95 mol% or more of all repeating units are composed of ethylene terephthalate. A small amount (usually 15 mol% or less based on the terephthalic acid component) of a component other than the terephthalic acid component and the ethylene glycol component may be copolymerized. In addition, these polyesters have known additives, for example, pigments, dyes, matting agents, antifouling agents, antibacterial agents, deodorants, fluorescent brighteners, flame retardants, stabilizers, ultraviolet absorbers, lubricants Etc. may be included.
【0006】上記ポリエステルからなる本発明の未延伸
繊維は、抄紙用として使用するためにその繊維長は2〜
20mm、好ましくは2〜10mmとする必要があり、
繊維長が2mm未満の場合には、水中への分散性が低下
するだけでなく、製造時の切断抵抗が大きくなるため、
未延伸繊維が伸ばされたり単繊維同士が絡み易くなり、
安定した切断が難しくなると共に、得られる未延伸繊維
中に繊維塊が多くなって水中への分散性が極端に悪くな
るので好ましくない。一方、繊維長が20mmを超えて
長くなると、抄紙時、繊維の水中分散性が悪化するので
好ましくない。。なお、通常の抄紙用ポリエステル繊維
の繊維長の上限は30mmと言われているが、未延伸ポ
リエステル繊維の場合は、そのヤング率が低いので、繊
維同士が水中で絡みやすくなって上限の繊維長が短くな
るものと考えられる。The unstretched fiber of the present invention comprising the above polyester has a fiber length of 2 to 2 for use in papermaking.
20 mm, preferably 2-10 mm,
If the fiber length is less than 2 mm, not only does the dispersibility in water decrease, but also the cutting resistance during production increases,
Unstretched fibers are stretched or single fibers are easily entangled,
It is not preferable because stable cutting becomes difficult and the resulting unstretched fiber has a large amount of fiber lumps and dispersibility in water becomes extremely poor. On the other hand, if the fiber length is longer than 20 mm, the dispersibility of the fiber in water deteriorates during papermaking, which is not preferable. . It is said that the upper limit of the fiber length of ordinary papermaking polyester fibers is 30 mm. However, in the case of undrawn polyester fibers, since the Young's modulus is low, the fibers are easily entangled in water and the upper limit fiber length is set. Is thought to be shorter.
【0007】本発明の抄紙用未延伸ポリエステル繊維
は、その繊維表面に繊維重量を基準としてポリエーテル
・ポリエステル共重合体が0.03重量%以上、好まし
くは0.05重量%以上付着している必要がある。該付
着量が0.03重量%未満の場合には、抄紙工程での水
中への繊維の分散が不十分となるので好ましくない。な
お、付着量があまりに多くなりすぎる場合には、繊維間
の接着性が阻害される傾向があるだけでなく、多量のポ
リエーテル・ポリエステル共重合体は抄紙工程循環水へ
の水質負荷を増大するので、1.5重量%以下とするの
が好ましい。The unstretched polyester fiber for papermaking of the present invention has a polyether / polyester copolymer adhered to the fiber surface at 0.03% by weight or more, preferably 0.05% by weight or more based on the fiber weight. There is a need. If the amount is less than 0.03% by weight, dispersion of the fibers in water in the papermaking step becomes insufficient, which is not preferable. If the amount of adhesion is too large, not only does the adhesiveness between fibers tend to be inhibited, but also a large amount of polyether / polyester copolymer increases the water quality load on the circulating water in the papermaking process. Therefore, the content is preferably 1.5% by weight or less.
【0008】本発明で用いられる上記ポリエーテル・ポ
リエステル共重合体は、テレフタル酸および/またはイ
ソフタル酸、低級アルキレングリコール並びにポリアル
キレングリコールおよび/またはそのモノエーテルから
なる。好ましく用いられる低級アルキレングリコールと
しては、例えばエチレングリコール、プロピレングリコ
ール、テトラメチレングリコールがあげられる。一方、
ポリアルキレングリコールとしては、平均分子量が60
0〜6000のポリエチレングリコール、ポリエチレン
グリコール・ポリプロピレングリコール共重合体、ポリ
プロピレングリコールが例示できる。さらにポリアルキ
レングリコールのモノエーテルとしては、ポリエチレン
グリコール、ポリプロピレングリコール等のモノメチル
エーテル、モノエチルエーテル、モノフェニルエーテル
等があげられる。なお、該共重合体はテレフタレート単
位とイソフタレート単位のモル比が95:5〜40:6
0の範囲内が水中分散性の点から好ましいが、アルカリ
金属塩スルホイソフタル酸、アジピン酸、セバシン酸等
を少量共重合していてもよい。以上の成分からなるポリ
エーテル・ポリエステル共重合体の平均分子量は、使用
するポリアルキレングリコールの分子量にもよるが、通
常1000〜20000、好ましくは3000〜150
00である。平均分子量が1000未満では水中分散性
の向上効果が十分でなく、一方20000を越えると該
重合体の乳化分散が難しくなる。The polyether / polyester copolymer used in the present invention comprises terephthalic acid and / or isophthalic acid, lower alkylene glycol, and polyalkylene glycol and / or its monoether. Preferred examples of the lower alkylene glycol include ethylene glycol, propylene glycol, and tetramethylene glycol. on the other hand,
The polyalkylene glycol has an average molecular weight of 60
Examples thereof include polyethylene glycol of 0 to 6000, a polyethylene glycol / polypropylene glycol copolymer, and polypropylene glycol. Further, examples of the monoether of polyalkylene glycol include monomethyl ether such as polyethylene glycol and polypropylene glycol, monoethyl ether, and monophenyl ether. The copolymer had a molar ratio of terephthalate unit to isophthalate unit of 95: 5 to 40: 6.
A range of 0 is preferable from the viewpoint of dispersibility in water, but a small amount of an alkali metal salt sulfoisophthalic acid, adipic acid, sebacic acid, or the like may be copolymerized. The average molecular weight of the polyether / polyester copolymer composed of the above components depends on the molecular weight of the polyalkylene glycol used, but is usually from 1,000 to 20,000, preferably from 3,000 to 150.
00. If the average molecular weight is less than 1,000, the effect of improving dispersibility in water is not sufficient, while if it exceeds 20,000, emulsification and dispersion of the polymer become difficult.
【0009】このようなポリエーテル・ポリエステル共
重合体は、通常水分散液として繊維表面に付着させる
が、該共重合体は比較的容易に水中へ分散させることが
できる。なお、得られる水性分散液の安定性をより向上
させるため、界面活性剤や有機溶媒を少量添加してもよ
く、また油剤等の各種処理剤を混合使用しても何ら差し
つかえない。付着方法はディップ、スプレー、ローラー
タッチ等の通常の方法が採用されるが、均一に付着させ
るためにはディップによる方法が適している。[0009] Such a polyether / polyester copolymer is usually attached to the fiber surface as an aqueous dispersion, but the copolymer can be relatively easily dispersed in water. In order to further improve the stability of the obtained aqueous dispersion, a small amount of a surfactant or an organic solvent may be added, or various kinds of treating agents such as oils may be mixed and used. An ordinary method such as dipping, spraying, or roller touching is adopted as the attaching method, but a dip method is suitable for uniform attachment.
【0010】ポリエーテル・ポリエステル共重合体が付
与された本発明の未延伸ポリエステル繊維は、上記の要
件に加えて水分の保持率が5〜40重量%である必要が
ある。該水分保持率が5重量%未満の場合には、繊維表
面に形成されたポリエーテル・ポリエステル共重合体被
膜が、抄紙工程で繊維表面から脱落しにくくなるためと
推定され、接着障害をひき起こして紙強力が低下するの
で好ましくない。一方水分保持率が40重量%を越える
場合には、紙強力の点では問題がないが、該未延伸ポリ
エステル繊維を前記繊維長に切断する際、水の飛散が多
くなって安定にカッターすることが困難となるだけでな
く、輸送コストの観点からも不経済である。The unstretched polyester fiber of the present invention to which the polyether / polyester copolymer has been imparted must have a water retention of 5 to 40% by weight in addition to the above requirements. If the water retention is less than 5% by weight, it is presumed that the polyether / polyester copolymer film formed on the fiber surface is unlikely to fall off from the fiber surface in the papermaking process, which causes adhesion failure. This is not preferred because the paper strength decreases. On the other hand, when the water retention ratio exceeds 40% by weight, there is no problem in terms of paper strength, but when the undrawn polyester fiber is cut to the fiber length, water scattering increases and the cutter is stably cut. Not only is it difficult, but also uneconomical in terms of transportation costs.
【0011】本発明の抄紙用未延伸ポリエステル繊維の
単繊維繊度は、得られる紙の用途に応じて適宜設定すれ
ばよいが、0.2〜5.0デシテックス(以下dtex
と記す)の範囲が好ましく、また、複屈折率は0.05
以下が好ましい。The single fiber fineness of the unstretched polyester fiber for papermaking of the present invention may be appropriately set according to the intended use of the paper to be obtained, and may be 0.2 to 5.0 dtex (hereinafter referred to as dtex).
And the birefringence is 0.05.
The following is preferred.
【0012】[0012]
【実施例】次に、実施例により本発明を具体的に説明す
る。なお、実施例における各項目は次の方法で測定し
た。 (a)固有粘度 オルソクロロフェノールを溶媒として、35℃の温度で
ウベローデ粘度管にて測定した。Next, the present invention will be described specifically with reference to examples. Each item in the examples was measured by the following method. (A) Intrinsic viscosity Using orthochlorophenol as a solvent, the viscosity was measured with an Ubbelohde viscosity tube at a temperature of 35 ° C.
【0013】(b)複屈折率(Δn) 市販の偏光顕微鏡によって、光源にナトリウムランプを
用い、試料をα−ブロムナフタリンに浸漬した状態下で
Berekコンペンセータ法からレターデーションを求
めて計算した。(B) Birefringence (Δn) Using a commercially available polarizing microscope, a sodium lamp was used as a light source, and the retardation was calculated from the Berk compensator method while the sample was immersed in α-bromonaphthalene.
【0014】(c)水分率 水分を含んだ約100gの未延伸ポリエステル繊維を1
20℃の熱風循環式の乾燥機中で絶乾になるまで乾燥す
る。乾燥前の試料の重量W0と乾燥後の試料の重量W1か
ら、次式によって求めた。 水分率(%)=[(W0−W1)/W1]×100(C) Moisture content About 100 g of undrawn polyester fibers containing water
Dry until absolutely dry in a hot air circulation type dryer at 20 ° C. From the weight W 0 of the sample before drying and the weight W 1 of the sample after drying, it was determined by the following equation. Moisture percentage (%) = [(W 0 −W 1 ) / W 1 ] × 100
【0015】(d)水中分散性 1000mLのメスシリンダーに500mLの水道水を
入れ、この中に正味0.1gのポリエステル繊維を投入
する。繊維がメスシリンダーの底に達したならば、メス
シリンダーの開口部に蓋をし、上下を両手で持ち、メス
シリンダーを1回反転させて繊維を分散させ、次の基準
で水中分散性の良否を判定する。 極めて良: 未分散の繊維束がなく、単繊維1本1本が
水中にきれいに広がっている状態 良: 未分散の繊維束は殆どない。単繊維同士の絡みが
若干認められるが許容範囲 不良: 未分散の繊維束が数本以上あり、単繊維同士の
絡みも多い状態。(D) Dispersibility in water 500 mL of tap water is put into a 1000 mL measuring cylinder, and a net 0.1 g of polyester fiber is put therein. When the fibers reach the bottom of the graduated cylinder, cover the opening of the graduated cylinder, hold the top and bottom with both hands, and turn the graduated cylinder once to disperse the fibers. Is determined. Very good: No undispersed fiber bundles, and each single fiber is well spread in water. Good: Almost no undispersed fiber bundles. Slight entanglement between single fibers is observed but acceptable range is bad. There are several or more undispersed fiber bundles and many single fibers are entangled.
【0016】(e)裂断長(紙強力) 未延伸ポリエステル繊維の接着性はポリエステル繊維紙
の強力で評価した。熊谷理機工業株式会社製の角型シー
トマシンを使って、繊度が1.7dtex、繊維長が5
mmの延伸熱処理されたポリエチレンテレフタレート繊
維60%と未延伸ポリエステル繊維40%を水中で良く
攪拌混合して分散させ、大きさが約25cm×約25c
mで目付けが約50g/m2のシートを作成する。この
シートを濾紙の間に挟んで、熊谷理機工業株式会社製の
KRK高温用回転乾燥機を使って、ドラムの表面温度を
140℃、ドラムへの接触時間を2分にして乾燥及び接
着熱処理を行う。この熱処理されたシートをJIS P
8113に従って引っ張り強さを測定し、裂断長で表し
た。(E) Break length (paper strength) The adhesiveness of the undrawn polyester fiber was evaluated by the strength of the polyester fiber paper. Using a square sheet machine manufactured by Kumagai Riki Kogyo Co., Ltd., the fineness is 1.7 dtex and the fiber length is 5
60% of the polyethylene terephthalate fiber and 40% of the undrawn polyester fiber, which have been subjected to a stretching heat treatment of 40 mm, are well stirred and mixed in water to be dispersed, and have a size of about 25 cm × about 25 c.
A sheet having a basis weight of about 50 g / m 2 is prepared. This sheet is sandwiched between filter papers, and using a KRK high-temperature rotary dryer manufactured by Kumagai Riki Kogyo Co., Ltd., the surface temperature of the drum is 140 ° C., the contact time with the drum is 2 minutes, and the drying and bonding heat treatment I do. This heat treated sheet is
The tensile strength was measured according to 8113 and expressed as the breaking length.
【0017】[実施例1〜4、比較例1〜3]固有粘度
が0.64のポリエチレンテレフタレートチップを乾燥
後、300℃で溶融し、孔数が1192の紡糸口金を通
して、180g/分で吐出し、1150m/分の速度で
引取り、単繊維の繊度が約1.3dtex、Δnが0.
015の未延伸ポリエステル繊維を得た。該未延伸ポリ
エステル繊維を約20万dtexのトウとなし、モル比
でテレフタル酸80モル%、イソフタル酸20モル%の
酸成分、平均分子量3000のポリエチレングリコール
70重量%(共重合体重量基準)とエチレングリコール
のグリコ−ル成分からなる平均分子量約12000のポ
リエーテル・ポリエステル共重合体の水性分散液中を7
0m/分の速度で通過させ、一対のローラーで絞り率を
調整する方法によりトウの水分率を種々変更した。ま
た、ポリエーテル・ポリエステル共重合体の水性分散液
の濃度を種々変更することにより付着量を変えた。ポリ
エーテル・ポリエステル共重合体が付与されたトウをド
ラム式カッターに供給して5mmに切断した。各々の例
におけるポリエーテル・ポリエステル共重合体付着量、
水分率、水中分散性および裂断長の測定結果をまとめて
表1に示す。[Examples 1 to 4, Comparative Examples 1 to 3] A polyethylene terephthalate chip having an intrinsic viscosity of 0.64 is dried, melted at 300 ° C., and discharged through a spinneret having 1192 holes at 180 g / min. Then, the fiber was taken up at a speed of 1150 m / min, and the fineness of the single fiber was about 1.3 dtex, and Δn was 0.3 mm.
015 undrawn polyester fiber was obtained. The unstretched polyester fiber was made into a tow of about 200,000 dtex, an acid component of 80 mol% of terephthalic acid and 20 mol% of isophthalic acid, and 70 wt% of polyethylene glycol having an average molecular weight of 3000 (based on the weight of the copolymer). In an aqueous dispersion of a polyether / polyester copolymer having an average molecular weight of about 12,000 comprising a glycol component of ethylene glycol, 7
The tow was passed at a speed of 0 m / min, and the water content of the tow was variously changed by adjusting the squeezing ratio with a pair of rollers. Further, the amount of adhesion was changed by variously changing the concentration of the aqueous dispersion of the polyether / polyester copolymer. The tow provided with the polyether / polyester copolymer was supplied to a drum type cutter and cut into 5 mm. Polyether / polyester copolymer adhesion amount in each example,
Table 1 summarizes the measurement results of the water content, dispersibility in water, and breaking length.
【0018】[0018]
【表1】 [Table 1]
【0019】ポリエーテル・ポリエステル共重合体付着
量0.04重量%、水分率14重量%の実施例1では、
ポリエステル繊維の水中分散性は良好で、カッターでの
水飛散も無く、抄紙後のポリエステル繊維紙の紙強力
(裂断長)も優れた値を示した。ポリエーテル・ポリエ
ステル共重合体付着量0.02重量%、水分率15重量
%の比較例1では、ポリエステル繊維の水中分散性が不
良で、抄紙されたポリエステル繊維紙の目面が悪く正常
品として使用する品質に達しなかった。In Example 1 in which the polyether / polyester copolymer adhesion amount was 0.04% by weight and the water content was 14% by weight,
The dispersibility in water of the polyester fiber was good, there was no water scattering with a cutter, and the paper strength (tear length) of the polyester fiber paper after papermaking showed an excellent value. In Comparative Example 1 in which the adhesion amount of the polyether / polyester copolymer was 0.02% by weight and the water content was 15% by weight, the dispersibility of the polyester fiber in water was poor, and the surface of the formed polyester fiber paper was poor, resulting in a normal product. The quality to use has not been reached.
【0020】ポリエーテル・ポリエステル共重合体付着
量0.08重量%、水分率6重量%の実施例2およびポ
リエーテル・ポリエステル共重合体付着量0.08重量
%、水分率15重量%の実施例3では、ポリエステル繊
維の水中分散性は極めて良好で、カッターでの水飛散も
無く、抄紙後のポリエステル繊維紙の紙強力(裂断長)
も優れた値を示した。ポリエーテル・ポリエステル共重
合体付着量0.15重量%、水分率35重量%の実施例
4では、トウ切断時少し水飛散が認められたがカッター
運転に支障をきたすことはなかった。ポリエステル繊維
の水中分散性は極めて良好で、ポリエステル繊維紙の紙
強力(裂断長)も優れた値を示した。ポリエーテル・ポ
リエステル共重合体付着量0.08重量%、水分率3重
量%の比較例2では、ポリエステル繊維の水中分散性は
良好で、カッターでの水飛散も無かったが、抄紙後のポ
リエステル繊維紙の紙強力(裂断長)は極めて低い値と
なった。ポリエーテル・ポリエステル共重合体付着量
0.15重量%、水分率45重量%の比較例3では、ト
ウ切断時の水飛散が非常に多く、カッター運転が不能と
なった。Example 2 with 0.08% by weight of polyether / polyester copolymer attached and 6% by weight of moisture and Example 2 with 0.08% by weight of attached polyether / polyester copolymer and 15% by weight of moisture In Example 3, the dispersibility of the polyester fiber in water was extremely good, there was no water scattering with a cutter, and the paper strength (breaking length) of the polyester fiber paper after papermaking.
Also showed excellent values. In Example 4 in which the amount of the polyether / polyester copolymer attached was 0.15% by weight and the water content was 35% by weight, slight water scattering was observed when cutting the tow, but this did not hinder the operation of the cutter. The dispersibility in water of the polyester fiber was extremely good, and the paper strength (rupture length) of the polyester fiber paper also showed an excellent value. In Comparative Example 2 in which the adhesion amount of the polyether / polyester copolymer was 0.08% by weight and the moisture content was 3% by weight, the dispersibility of the polyester fiber in water was good, and there was no water scattering with a cutter. The paper strength (breaking length) of the fiber paper was extremely low. In Comparative Example 3 in which the polyether / polyester copolymer adhesion amount was 0.15% by weight and the water content was 45% by weight, water scattering during tow cutting was extremely large, and the cutter operation became impossible.
【0021】[実施例5〜8、比較例4〜5]固有粘度
が0.64のイソフタル酸を10モル%共重合ポリエチ
レンフタレートチップを乾燥後、290℃で溶融し、孔
数が1192の紡糸口金を通して200g/分で吐出
し、1100m/分の速度で引取り、繊度が約1.6d
tex、Δnが0.018の未延伸ポリエステル繊維を
得た。該未延伸ポリエステル繊維に、実施例1〜4と同
じ方法でポリエーテル・ポリエステル共重合体を0.1
0重量%付与し、水分率が15重量%となるように調整
し、ドラム式カッターに供給し、各々表2に示す繊維長
(1.5〜25mm)に切断した。各々の例におけるポ
リエステル繊維の水中分散性を測定した結果を表2に示
す。Examples 5 to 8 and Comparative Examples 4 to 5 A 10 mol% copolymerized polyethylene phthalate chip having isophthalic acid of 0.64 was dried, melted at 290 ° C., and spun with 1,192 holes. Discharged at 200g / min through a die, withdrawn at a speed of 1100m / min, and fineness of about 1.6d
An undrawn polyester fiber having a tex and Δn of 0.018 was obtained. 0.1% of a polyether / polyester copolymer was added to the undrawn polyester fiber in the same manner as in Examples 1 to 4.
0% by weight was provided, the water content was adjusted to be 15% by weight, and supplied to a drum type cutter, and cut into fiber lengths (1.5 to 25 mm) shown in Table 2 respectively. Table 2 shows the results of measuring the dispersibility in water of the polyester fibers in each example.
【0022】[0022]
【表2】 [Table 2]
【0023】[0023]
【発明の効果】本発明の抄紙用未延伸ポリエステル繊維
によれば、抄紙工程での繊維の水中分散性を損なうこと
なく、繊維同志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。According to the unstretched polyester fiber for papermaking of the present invention, it is possible to obtain a polyester fiber paper in which the fibers are firmly adhered to each other without impairing the dispersibility of the fibers in water in the papermaking process.
Claims (1)
テル繊維であって、該繊維表面には繊維重量を基準とし
てポリエーテル・ポリエステル共重合体が0.03重量
%以上付着していると共に、水分保持率が5〜40重量
%であることを特徴とする抄紙用未延伸ポリエステル繊
維。1. An undrawn polyester fiber having a fiber length of 2 to 20 mm, wherein a polyether / polyester copolymer adheres to the surface of the fiber in an amount of 0.03% by weight or more based on the weight of the fiber. An undrawn polyester fiber for papermaking, having a water retention of 5 to 40% by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001138401A JP4579445B2 (en) | 2001-05-09 | 2001-05-09 | Unstretched polyester fiber for papermaking |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001138401A JP4579445B2 (en) | 2001-05-09 | 2001-05-09 | Unstretched polyester fiber for papermaking |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2002339287A true JP2002339287A (en) | 2002-11-27 |
JP2002339287A5 JP2002339287A5 (en) | 2005-06-16 |
JP4579445B2 JP4579445B2 (en) | 2010-11-10 |
Family
ID=18985345
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001138401A Expired - Lifetime JP4579445B2 (en) | 2001-05-09 | 2001-05-09 | Unstretched polyester fiber for papermaking |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP4579445B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007107160A (en) * | 2005-10-17 | 2007-04-26 | Teijin Fibers Ltd | Method for producing short-cut nanofiber and wet nonwoven fabric |
JP2015129356A (en) * | 2014-01-06 | 2015-07-16 | 株式会社クラレ | Short-cut fiber, wet nonwoven fabric, and separator using the same |
KR20160012225A (en) * | 2013-05-30 | 2016-02-02 | 데이진 가부시키가이샤 | Organic resin non-crimped staple fiber |
WO2018139651A1 (en) * | 2017-01-30 | 2018-08-02 | 帝人フロンティア株式会社 | Method for producing uncrimped short fibers and wet-laid nonwoven fabric comprising obtained uncrimped short fibers |
-
2001
- 2001-05-09 JP JP2001138401A patent/JP4579445B2/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007107160A (en) * | 2005-10-17 | 2007-04-26 | Teijin Fibers Ltd | Method for producing short-cut nanofiber and wet nonwoven fabric |
KR20160012225A (en) * | 2013-05-30 | 2016-02-02 | 데이진 가부시키가이샤 | Organic resin non-crimped staple fiber |
US20160177476A1 (en) * | 2013-05-30 | 2016-06-23 | Teijin Limited | Organic resin non-crimped staple fiber |
KR102184471B1 (en) * | 2013-05-30 | 2020-11-30 | 데이진 가부시키가이샤 | Organic resin non-crimped staple fiber |
JP2015129356A (en) * | 2014-01-06 | 2015-07-16 | 株式会社クラレ | Short-cut fiber, wet nonwoven fabric, and separator using the same |
WO2018139651A1 (en) * | 2017-01-30 | 2018-08-02 | 帝人フロンティア株式会社 | Method for producing uncrimped short fibers and wet-laid nonwoven fabric comprising obtained uncrimped short fibers |
Also Published As
Publication number | Publication date |
---|---|
JP4579445B2 (en) | 2010-11-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101421317B1 (en) | Wet-laid non-woven fabric and filter | |
KR101441723B1 (en) | Thin paper | |
KR950007814B1 (en) | Wet-process monwoven fabric and ultrafine polyester fibers therefor | |
JP6548634B2 (en) | Polyester binder fiber | |
JP2009221611A (en) | Polyethylene naphthalate fibers and staple fiber nonwoven fabric formed of the same | |
JP2002339287A (en) | Undrawn polyester fiber for paper-making use | |
JP2003089954A (en) | Acoustic vibration member | |
JP2002227089A (en) | Polyester-based binder fiber for wet papermaking and method for producing the same | |
JP2004181341A (en) | Wet nonwoven fabric for filter and polyester binder fiber for use therein | |
JP2003138424A (en) | Polyester fiber for binder | |
JP2012067409A (en) | Heat-adhesive polyester composite fiber | |
JP2012067408A (en) | Wet type polyester nonwoven fabric | |
JP2765947B2 (en) | Bulky paper | |
EP3561161B1 (en) | Polyester binder fiber | |
JP2002339287A5 (en) | ||
JP6534885B2 (en) | Stretched polyester-based fiber and fiber structure containing the fiber | |
JP4031435B2 (en) | Polyester binder fiber for papermaking | |
JP4874014B2 (en) | Polyester staple fiber | |
JP5563343B2 (en) | Polyester fiber for papermaking and method for producing the same | |
JP2002339257A (en) | Ultrafine polyester drawn fiber for papermaking | |
JP4336551B2 (en) | Shoji paper | |
JP2011074506A (en) | Thermally adhesive conjugated fiber for wet nonwoven fabric | |
JPH0327195A (en) | Bulky paper having water-dispersing and dissolving performance and preparation thereof | |
JPH03241087A (en) | Method for making bulky paper | |
JP2667836B2 (en) | Polyester blend paper and method for producing the same |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A711 | Notification of change in applicant |
Free format text: JAPANESE INTERMEDIATE CODE: A712 Effective date: 20040818 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20040909 |
|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20040909 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20060630 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20060725 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20070814 |
|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20100826 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130903 Year of fee payment: 3 |
|
R150 | Certificate of patent or registration of utility model |
Free format text: JAPANESE INTERMEDIATE CODE: R150 Ref document number: 4579445 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130903 Year of fee payment: 3 |
|
S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130903 Year of fee payment: 3 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313111 |
|
S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
EXPY | Cancellation because of completion of term |