JP2000328348A - Splittable type conjugate fiber and formed fiber product using the same - Google Patents
Splittable type conjugate fiber and formed fiber product using the sameInfo
- Publication number
- JP2000328348A JP2000328348A JP16485199A JP16485199A JP2000328348A JP 2000328348 A JP2000328348 A JP 2000328348A JP 16485199 A JP16485199 A JP 16485199A JP 16485199 A JP16485199 A JP 16485199A JP 2000328348 A JP2000328348 A JP 2000328348A
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- Japan
- Prior art keywords
- fiber
- splittable conjugate
- component
- resin
- cross
- 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.)
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- Multicomponent Fibers (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Nonwoven Fabrics (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、分割性に優れた分
割型複合繊維に関する。さらに詳しくはバッテリセパレ
−タ−、ワイパ−、フィルタ−などの産業資材分野、お
むつ、ナプキンなどの衛生材料分野、また衣料分野にも
好適に用いることのできる分割性に優れた分割型複合繊
維、これを用いた繊維成形体及び積層繊維成形体に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a splittable conjugate fiber having excellent splittability. More specifically, a splittable composite fiber having excellent splitting properties that can be suitably used in the field of industrial materials such as battery separators, wipers, and filters, diapers, sanitary materials such as napkins, and clothing. The present invention relates to a fiber molded article and a laminated fiber molded article using the same.
【0002】[0002]
【従来の技術】従来、極細繊維を得る方法として、海島
型や分割型の複合繊維が知られている。海島型複合繊維
を用いる方法は、複数成分を組合せて紡糸して海島型複
合繊維とし、得られた該複合繊維の1成分を溶解除去す
ることにより、極細繊維を得るものである。この方法
は、非常に細い繊維を得ることができる反面、1成分を
溶解除去するために非経済的である。一方、分割型複合
繊維を用いる方法は、複数成分の樹脂を組合せて紡糸し
て複合繊維とし、得られた該複合繊維を物理的応力や樹
脂の化学薬品に対する収縮差などを利用して、該分割型
複合繊維を多数の繊維に分割して極細繊維を得るもので
ある。2. Description of the Related Art Conventionally, sea-island type or split type composite fibers have been known as a method for obtaining ultrafine fibers. In the method using sea-island composite fibers, a plurality of components are combined and spun into sea-island composite fibers, and one component of the obtained composite fibers is dissolved and removed to obtain ultrafine fibers. Although this method can obtain very fine fibers, it is uneconomical to dissolve and remove one component. On the other hand, the method of using the splittable conjugate fiber is a method of combining and spinning a plurality of component resins to form a conjugate fiber, and using the obtained conjugate fiber by utilizing a physical stress or a difference in shrinkage of the resin against a chemical agent. An ultrafine fiber is obtained by dividing the splittable conjugate fiber into a number of fibers.
【0003】例えば、ポリエステル樹脂とポリオレフィ
ン樹脂の組み合せ、ポリエステル樹脂とポリアミド樹脂
の組み合せ、ポリアミド樹脂とポリオレフィン樹脂の組
み合わせに代表される分割型複合繊維を極細細繊化し、
不織布等に加工する際、高圧液体流処理等の分割細繊化
工程が不織布化工程の律速段階となる。また分割細繊化
に要するエネルギ−コストも大きいといった問題があっ
た。[0003] For example, a split-type composite fiber typified by a combination of a polyester resin and a polyolefin resin, a combination of a polyester resin and a polyamide resin, and a combination of a polyamide resin and a polyolefin resin is made ultrafine and fine.
When processing into a nonwoven fabric or the like, the splitting and thinning process such as high-pressure liquid flow treatment is the rate-determining step of the nonwoven fabric forming process. In addition, there is a problem that the energy cost required for dividing into fine fibers is large.
【0004】一方、ポリオレフィン系樹脂同士、ポリエ
ステル系樹脂同士、ポリアミド系樹脂同士などの同系樹
脂の組合せでは、前記異種ポリマーに比べて比較的樹脂
の相溶性が良いため、前記のような問題がさらに大きく
なり、分割細繊化させるためには、物理的衝撃をさらに
大きくする必要がある。このため、得られた不織布は、
分割された部分と分割されない部分が存在したり、繊維
が物理的衝撃で動き、目付の厚い部分と薄い部分ができ
るなど、いわゆるむらが生じて地合が悪くなったり、ま
た高圧液体流処理の加工速度を大幅に下げる必要がある
などの問題点があった。[0004] On the other hand, in the case of a combination of similar resins such as polyolefin resins, polyester resins, polyamide resins, etc., the above-mentioned problems are further increased because the compatibility of the resins is relatively better than that of the different polymers. In order to increase the size and to make the fibers finer, it is necessary to further increase the physical impact. For this reason, the obtained nonwoven fabric is
There are so-called irregularities, such as the presence of divided and undivided parts, the movement of fibers by physical impact, and the formation of thicker and thinner parts. There were problems such as a need to significantly reduce the processing speed.
【0005】この問題点を改善するために特開平4−2
8922号公報では、オルガノシロキサン及びこれらの
変成体を樹脂に添加することにより、同種ポリマー同士
の組合せの分割型複合繊維であっても容易に分割するこ
とができることが開示されている。しかしながら、分割
性は多少向上するものの、分割された繊維を用いて得ら
れた不織布は強力が低下したり、2次加工での加工性不
良などの問題点があった。To solve this problem, Japanese Patent Laid-Open No.
No. 8922 discloses that by adding an organosiloxane and a modified product thereof to a resin, it is possible to easily divide even a splittable conjugate fiber composed of a combination of polymers of the same kind. However, although the splittability is somewhat improved, the nonwoven fabric obtained by using the split fibers has problems such as reduced strength and poor workability in secondary processing.
【0006】[0006]
【発明が解決しようとする課題】本発明者らは、従来技
術の有する問題点を解決するべく、鋭意検討を重ねた。
その結果、少なくとも2成分の熱可塑性樹脂から構成さ
れ、繊維横断面において、各成分は長軸方向に交互に隣
接され、かつ該断面が屈曲、湾曲あるいは扁平形状の複
合繊維であって、該断面の長軸Lと短軸Wの比(L/
W)が3〜20を満足した分割型複合繊維とすることに
より、分割し易い分割型複合繊維となり、かつ、該分割
型複合繊維を用いると緻密で地合の良い繊維成形体及び
積層繊維成形体が得られることを見出し、この知見に基
づいて本発明を完成した。以上の記述から明らかなよう
に、本発明の目的は分割性を向上させるための添加剤を
一切添加せずに、同系樹脂同士の組み合わせであって
も、分割性に優れた分割型複合繊維を提供すると共に緻
密で地合の良い繊維成形体および該成形体を用いた製品
を提供することである。SUMMARY OF THE INVENTION The present inventors have conducted intensive studies in order to solve the problems of the prior art.
As a result, in the fiber cross-section, each component is alternately adjacent to each other in the longitudinal direction, and the cross-section is a conjugate fiber having a bent, curved or flat shape, and The ratio of the major axis L to the minor axis W (L /
By making the splittable conjugate fiber satisfying W) 3 to 20, the splittable conjugate fiber can be easily split, and when the splittable conjugate fiber is used, a dense and well-formed fiber molded article and laminated fiber molding are obtained. They found that a body could be obtained and completed the present invention based on this finding. As is apparent from the above description, the object of the present invention is to provide a splittable conjugate fiber having excellent splitting properties without adding any additives for improving splitting properties, even in the case of a combination of similar resins. An object of the present invention is to provide a dense and well-formed fiber molded product and a product using the molded product.
【0007】[0007]
【問題を解決するための手段】本発明は以下から構成さ
れる。 (1)少なくとも2成分の熱可塑性樹脂から構成され、
繊維断面において、各成分は長軸方向に交互に隣接さ
れ、かつ該断面は屈曲、湾曲もしくは扁平形状の複合繊
維であって、該断面の長軸Lと短軸Wの比(L/W)が
3〜20であることを特徴とする分割型複合繊維。The present invention comprises the following. (1) It is composed of at least two components of a thermoplastic resin,
In the fiber cross section, each component is alternately adjacent to each other in the long axis direction, and the cross section is a bent, curved or flat composite fiber, and the ratio of the long axis L to the short axis W (L / W) of the cross section Is from 3 to 20.
【0008】(2)分割型複合繊維の繊維断面におい
て、繊維を構成する1成分の繊維外周面長aと隣接成分
との接触長bの比(a/b)が0.1〜2.5である前
記第1項記載の分割型複合繊維。(2) In the fiber cross section of the splittable conjugate fiber, the ratio (a / b) of the fiber outer peripheral surface length a of one component constituting the fiber to the contact length b between adjacent components is 0.1 to 2.5. 2. The splittable conjugate fiber according to the above item 1, wherein
【0009】(3)分割型複合繊維の繊維断面におい
て、屈曲もしくは湾曲により囲まれた面積S1と該分割
型複合繊維の断面積S2の比(S1/S2)が0.2〜
1.0である前記第1項もしくは第2項のいずれか1項
記載の分割型複合繊維。(3) In the fiber cross section of the splittable conjugate fiber, the ratio (S1 / S2) of the area S1 surrounded by the bend or curve to the cross-sectional area S2 of the splittable conjugate fiber is 0.2 to 0.2.
3. The splittable conjugate fiber according to any one of the above items 1 or 2, which is 1.0.
【0010】(4)繊維成形後の該繊維を構成する少な
くとも2成分の熱可塑性樹脂のメルトフローレートがい
ずれも10〜100g/10分であり、かつ該熱可塑性
樹脂のうち、融点の最も高い樹脂成分(以下、A成分と
いう)のメルトフローレート(MFR−A)と融点が最
も低い樹脂成分(以下、B成分という)のメルトフロー
レート(MFR−B)の比(MFR−A/MFR−B)
が0.1〜5である前記第1項〜第3項のいずれか1項
記載の分割型複合繊維。(4) The thermoplastic resin of at least two components constituting the fiber after fiber molding has a melt flow rate of 10 to 100 g / 10 min, and has the highest melting point among the thermoplastic resins. The ratio (MFR-A / MFR-) of the melt flow rate (MFR-A) of the resin component (hereinafter, referred to as A component) and the melt flow rate (MFR-B) of the resin component having the lowest melting point (hereinafter, referred to as B component). B)
4. The splittable conjugate fiber according to any one of the above items 1 to 3, wherein is 0.1 to 5.
【0011】(5)少なくとも2成分の熱可塑性樹脂の
組合せが、ポリプロピレン樹脂とポリエチレン樹脂の組
合わせである前記第1項〜第4項のいずれか1項記載の
分割型複合繊維。(5) The splittable conjugate fiber according to any one of (1) to (4) above, wherein the combination of at least two thermoplastic resins is a combination of a polypropylene resin and a polyethylene resin.
【0012】(6)該複合繊維の分割前の単糸繊度が
0.5〜10デシテックス、分割後の単糸繊度が0.5
デシテックス以下である前記第1項〜第5項のいずれか
1項記載の分割型複合繊維。(6) The single fiber fineness of the conjugate fiber before splitting is 0.5 to 10 dtex, and the single fiber fineness after splitting is 0.5
6. The splittable conjugate fiber according to any one of the above items 1 to 5, which is not more than decitex.
【0013】(7)前記第1項〜の第6項いずれか1項
記載の分割型複合繊維を少なくとも30重量%以上含
み、かつ該分割型複合繊維の50%以上が分割している
繊維成形体。(7) A fiber molding containing at least 30% by weight or more of the splittable conjugate fiber according to any one of the above items 1 to 6, and wherein at least 50% of the splittable conjugate fiber is split. body.
【0014】(8)繊維成形体が繊維集合体である前記
第7項記載の繊維成形体。(8) The fiber molded article according to the above item 7, wherein the fiber molded article is a fiber aggregate.
【0015】(9)繊維成形体がスパンボンド法により
得られる繊維集合体である前記第7項もしくは第8項の
いずれか1項記載の繊維成形体。(9) The fiber molded article according to any one of the above items 7 or 8, wherein the fiber molded article is a fiber aggregate obtained by a spun bond method.
【0016】(10)前記第7項〜第9項のいずれか1
項記載の繊維成形体の片面または両面にシートを積層し
てなる積層繊維成形体。(10) Any one of the above items 7 to 9
A laminated fiber molded product obtained by laminating a sheet on one side or both surfaces of the fiber molded product according to the above item.
【0017】(11)前記第7項〜第9項のいずれか1
項記載の繊維成形体をシートの両面に積層してなる積層
繊維成形体。(11) Any one of the above items 7 to 9
A laminated fiber molded product obtained by laminating the fiber molded product according to the above item on both sides of a sheet.
【0018】(12)シートが不織布、フィルム、編
物、織物の少なくとも1種から選ばれたシ−トである前
記第10項もしくは第11項のいずれか1項記載の積層
繊維成形体。(12) The laminated fiber molded article according to any one of the above (10) or (11), wherein the sheet is a sheet selected from at least one of a nonwoven fabric, a film, a knit, and a woven fabric.
【0019】(13)前記第7項〜第9項のいずれか1
項記載の繊維成形体もしくは前記第10〜第12項にい
ずれか1項記載の積層繊維成形体を用いた吸収性物品。(13) Any one of the above items 7 to 9
13. An absorbent article using the fiber molded article according to the above item or the laminated fiber molded article according to any one of the above items 10 to 12.
【0020】(14)前記第7項〜第9項のいずれか1
項記載の繊維成形体もしくは前記第10項〜第12項の
いずれか1項記載の積層繊維成形体を用いたワイパー。(14) Any one of the above-mentioned items 7 to 9
Item 13. A wiper using the fiber molded product according to Item 10 or the laminated fiber molded product according to any one of Items 10 to 12.
【0021】(15)前記第7項〜第9項のいずれか1
項記載の繊維成形体もしくは前記第10項〜第12項の
いずれか1項記載の積層繊維成形体を用いたバッテリー
セパレーター。(15) Any one of the above items 7 to 9
13. A battery separator using the fiber molded article according to the above item or the laminated fiber molded article according to any one of the above items 10 to 12.
【0022】[0022]
【発明の実施の形態】以下、本発明を詳細に説明する。
本発明の分割型複合繊維に用いる熱可塑性樹脂は、溶融
紡糸工程で繊維成形性を有するものであれば特に限定さ
れないが、例えばポリエステル系樹脂、ポリアミド系樹
脂、ポリオレフィン系樹脂等を好適に使用される樹脂と
して挙げることができる。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail.
The thermoplastic resin used for the splittable conjugate fiber of the present invention is not particularly limited as long as it has fiber formability in the melt spinning step.For example, polyester resins, polyamide resins, polyolefin resins, and the like are preferably used. Resin.
【0023】ポリエステル系樹脂としては、酸成分とし
てテレフタル酸、イソフタル酸、フタル酸、2,6−ナ
フタレンジカルボン酸等の芳香族ジカルボン酸もしくは
アジピン酸、セバシン酸などの脂肪族ジカルボン酸また
はこれらのエステル類と、アルコール成分としてエチレ
ングリコール、ジエチレングリコール、1,4−ブタン
ジオール、ネオペンチルグリコール、1,4−シクロヘ
キサンジメタノール等のジオール化合物とから合成され
た単独重合体ポリエステルもしくは共重合体ポリエステ
ルであり、上記ポリエステルにパラオキシ安息香酸、5
−ナトリウムスルフォイソフタール酸、ポリアルキレン
グリコール、ペンタエリスリトール等が添加もしくは共
重合されているものも含まれる。Examples of the polyester resin include aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, phthalic acid and 2,6-naphthalenedicarboxylic acid, and aliphatic dicarboxylic acids such as adipic acid and sebacic acid, and esters thereof as an acid component. And a homopolymer polyester or a copolymer polyester synthesized from diol compounds such as ethylene glycol, diethylene glycol, 1,4-butanediol, neopentyl glycol, and 1,4-cyclohexanedimethanol as alcohol components. Paraoxybenzoic acid, 5
And those in which sodium sulfoisophthalic acid, polyalkylene glycol, pentaerythritol and the like are added or copolymerized.
【0024】ポリアミド系重合体としては、6,6−ナ
イロン、6,10−ナイロン、6−ナイロン、1,1−
ナイロン、1,2−ナイロン、4−ナイロン、4,6−
ナイロン及びこれらを主体とする共重合体等を例示する
ことができる。As the polyamide polymer, 6,6-nylon, 6,10-nylon, 6-nylon, 1,1-nylon
Nylon, 1,2-nylon, 4-nylon, 4,6-
Nylon and copolymers containing these as a main component can be exemplified.
【0025】一方、ポリオレフィン系樹脂としては、炭
素数が2〜8個の脂肪族αーオレフィン、例えばエチレ
ン、プロピレン、1−ブテン、1−ペンテン、4−メチ
ル−1−ペンテン、3−メチル−1−ブテン、1−ヘキ
セン、1−オクテン等の単独重合体もしくはこれらのα
−オレフィンの2種以上の共重合体、前記α−オレフィ
ンと他のオレフィン及び/または少量の他のエチレン系
不飽和モノマー、例えばブタジエン、イソプレン、ペン
タジエン−1、スチレン、α−メチルスチレン等の不飽
和モノマーとの共重合体及びこれらの2種以上の混合物
を挙げることができる。On the other hand, as polyolefin resins, aliphatic α-olefins having 2 to 8 carbon atoms, for example, ethylene, propylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 3-methyl-1 -Homopolymers such as butene, 1-hexene, 1-octene and the like;
-Copolymers of two or more olefins, said α-olefins and other olefins and / or small amounts of other ethylenically unsaturated monomers such as butadiene, isoprene, pentadiene-1, styrene, α-methylstyrene and the like. Copolymers with saturated monomers and mixtures of two or more thereof can be mentioned.
【0026】代表的には、ポリプロピレン系樹脂及びポ
リエチレン系樹脂を挙げることができ、該ポリプロピレ
ン系樹脂としては、例えばプロピレン単独重合体、プロ
ピレンを70重量%以上含有するプロピレンとプロピレ
ン以外の上記α−オレフィンの1種以上との共重合体、
例えばエチレン−プロピレン共重合体、エチレン−プロ
ピレン−ブテン共重合体等を挙げることができる。Representative examples include polypropylene resins and polyethylene resins. Examples of the polypropylene resins include propylene homopolymer, propylene containing 70% by weight or more of propylene, and the above-mentioned α- A copolymer with one or more olefins,
For example, an ethylene-propylene copolymer, an ethylene-propylene-butene copolymer and the like can be mentioned.
【0027】また、ポリエチレン系樹脂としては、高密
度ポリエチレン(HDPE)、低密度ポリエチレン(L
DPE)、直鎖状低密度ポリエチレン(L−LDPE)
等を挙げることができる。As the polyethylene resin, high-density polyethylene (HDPE) and low-density polyethylene (L
DPE), linear low density polyethylene (L-LDPE)
And the like.
【0028】該ポリプロピレン系樹脂のメルトフローレ
ート(230℃、2.18N、以下MFRという)及び
該ポリエチレン系樹脂のMFR(190℃、2.18
N)は、紡糸可能な範囲であれば特に限定されることは
ないが、いずれの樹脂の場合も1〜100g/10分が
好ましく、より好ましくは、5〜70g/10分であ
る。The melt flow rate of the polypropylene resin (230 ° C., 2.18 N, hereinafter referred to as MFR) and the MFR of the polyethylene resin (190 ° C., 2.18 N)
N) is not particularly limited as long as it can be spun, but is preferably 1 to 100 g / 10 min, more preferably 5 to 70 g / 10 min in any resin.
【0029】前記以外の熱可塑性樹脂としては、例えば
ビニル系重合体が用いられ、具体的には、ポリビニルア
ルコール、ポリ酢酸ビニル、ポリアクリル酸エステル、
エチレン酢酸ビニル共重合体、シンジオタクチックポリ
スチレンもしくはこれらの共重合体を使用することもで
きる。As the thermoplastic resin other than the above, for example, a vinyl polymer is used, and specifically, polyvinyl alcohol, polyvinyl acetate, polyacrylate,
Ethylene vinyl acetate copolymer, syndiotactic polystyrene or a copolymer thereof can also be used.
【0030】本発明の分割型複合繊維は、前記の中、少
なくとも2成分の熱可塑性樹脂を任意に組み合せること
が可能であるが、衣料用途など染色が必要な分野では、
例えば、ポリエステル系樹脂、ポリアミド系樹脂を主と
した組み合わせが好適である。また耐薬品性、軽量性及
び低コストが要求される産業資材分野及び衛生材料分野
等では、耐薬品性が高く、コスト的に有利なポリオレフ
ィン系樹脂を主体とした組み合わせを例示でき、中でも
耐薬品性が要求される分野には、ポリプロピレン系樹脂
及びポリエチレン系樹脂の組み合わせが好適である。The splittable conjugate fiber of the present invention can be arbitrarily combined with at least two components of the above-mentioned thermoplastic resin.
For example, a combination mainly composed of a polyester resin and a polyamide resin is preferable. In the industrial materials and sanitary materials fields where chemical resistance, light weight and low cost are required, a combination mainly composed of a polyolefin resin having high chemical resistance and being advantageous in terms of cost can be exemplified. In a field where properties are required, a combination of a polypropylene resin and a polyethylene resin is preferable.
【0031】ここで前記熱可塑性樹脂は任意の組み合わ
せが可能であるが、例えば、ポリエチレンテレフタレー
ト樹脂とポリエチレンテレフタレート樹脂の組み合わ
せ、ポリプロピレン樹脂とポリプロピレン樹脂の組み合
わせのような全く同一樹脂の組合せ及び同一構成比を有
する混合物の組み合せは本発明の範疇から除外される。Here, any combination of the above-mentioned thermoplastic resins is possible. For example, a combination of exactly the same resin such as a combination of a polyethylene terephthalate resin and a polyethylene terephthalate resin, a combination of a polypropylene resin and a polypropylene resin, and the same composition ratio Are excluded from the scope of the present invention.
【0032】本発明の分割型複合繊維に好適に使用され
るポリプロピレン系樹脂とポリエチレン系樹脂の2成分
の組み合せにあっては、該ポリプロピレン系樹脂が高融
点樹脂(A成分)となる。かかるポリプロピレン系樹脂
は具体的には、チーグラーナッタ触媒、メタロセン触媒
等で重合されたシンジオタクチックポリプロピレン、ア
イソタクチックポリプロピレンを例示できる。高融点樹
脂である該ポリプロピレン系樹脂のMFR−Aは、溶融
紡糸可能な範囲であれば良く、紡糸条件等の変更で、繊
維成形後のMFR−Aが10〜100g/10分の範囲
内であれば特に問題はない。繊維成形後のMFR−A
は、より好ましくは、10〜70g/10分である。繊
維成形後のMFR−Aが10g/10分未満、もしくは
100g/10分を超える場合は、可紡性良く、細い繊
維に紡糸することが困難となる。In the combination of the two components of the polypropylene resin and the polyethylene resin which are suitably used for the splittable conjugate fiber of the present invention, the polypropylene resin is the high melting point resin (component A). Specific examples of such a polypropylene-based resin include syndiotactic polypropylene and isotactic polypropylene polymerized with a Ziegler-Natta catalyst, a metallocene catalyst, and the like. The MFR-A of the polypropylene resin which is a high melting point resin may be in a range in which melt spinning is possible, and by changing spinning conditions and the like, the MFR-A after fiber molding is in a range of 10 to 100 g / 10 minutes. If there is no problem. MFR-A after fiber molding
Is more preferably 10 to 70 g / 10 min. When the MFR-A after fiber molding is less than 10 g / 10 minutes or more than 100 g / 10 minutes, it is difficult to spin into fine fibers with good spinnability.
【0033】ポリエチレン系樹脂は、前記ポリプロピレ
ン系樹脂の融点よりも低い低融点樹脂(B成分)であっ
て、具体的には、高密度ポリエチレン、直鎖状低密度ポ
リエチレン、低密度ポリエチレンを例示することができ
る。また、これらのポリエチレンの2種以上の混合物で
あっても良い。原料としてのポリエチレン系樹脂のMF
R−Bは溶融紡糸可能な範囲であれば良く、紡糸条件等
の変更で、繊維成形後のMFR−Bが10〜100g/
10分の範囲内であれば特に問題はない。繊維成形後の
MFR−Bは、より好ましくは、10〜60g/10分
である。MFR−Bが1g/10分未満もしくは100
g/10分を超える場合は、可紡性良く、細い繊維に紡
糸することが困難となる。The polyethylene resin is a low melting point resin (component B) lower than the melting point of the polypropylene resin, and specific examples include high density polyethylene, linear low density polyethylene, and low density polyethylene. be able to. Further, a mixture of two or more of these polyethylenes may be used. MF of polyethylene resin as raw material
RB may be in a range in which melt spinning is possible, and MFR-B after fiber molding may be 10 to 100 g / d by changing spinning conditions and the like.
There is no particular problem within the range of 10 minutes. MFR-B after fiber molding is more preferably 10 to 60 g / 10 minutes. MFR-B is less than 1 g / 10 min or 100
If it exceeds g / 10 minutes, it is difficult to spin into fine fibers with good spinnability.
【0034】本発明の分割型複合繊維を構成する少なく
とも2成分の熱可塑性樹脂のうち、最も融点の高い樹脂
をA成分としたときの該A成分のMFRをMFR−Aと
し、最も融点の低い樹脂をB成分としたときの該B成分
のMFRをMFR−Bとしたとき、該MFRの比(MF
R−A/MFR−B)は、0.1〜5であることが好ま
しく、さらに好ましくは、0.5〜3である。この値が
0.1未満であったり、5を超える場合には、溶融紡糸
時のこれら成分の口金内の流れ性、屈曲、湾曲、もしく
は扁平形状に吐出された後の溶融張力差、冷却時の粘度
上昇の差が大きくなるなどの要因上、曳糸性を維持する
ことが困難となる。When the resin having the highest melting point among the at least two thermoplastic resins constituting the splittable conjugate fiber of the present invention is the A component, the MFR of the A component is MFR-A, and the MFR-A is the lowest. When the MFR of the B component when the resin is the B component is MFR-B, the ratio (MFF) of the MFR
(RA / MFR-B) is preferably from 0.1 to 5, more preferably from 0.5 to 3. If this value is less than 0.1 or more than 5, the flowability of these components in the spinneret during melt spinning, the difference in melt tension after being discharged in a bent, curved, or flat shape, during cooling It is difficult to maintain the spinnability due to factors such as an increase in the difference in viscosity increase between the fibers.
【0035】本発明に使用する熱可塑性樹脂には、本発
明の効果を妨げない範囲内でさらに、酸化防止剤、光安
定剤、紫外線吸収剤、中和剤、造核剤、エポキシ安定
剤、滑剤、抗菌剤、難燃剤、帯電防止材、顔料、可塑
剤、親水剤などの添加剤を適宜必要に応じて添加しても
良い。The thermoplastic resin used in the present invention further includes an antioxidant, a light stabilizer, an ultraviolet absorber, a neutralizing agent, a nucleating agent, an epoxy stabilizer, as long as the effects of the present invention are not impaired. Additives such as a lubricant, an antibacterial agent, a flame retardant, an antistatic material, a pigment, a plasticizer, and a hydrophilic agent may be appropriately added as needed.
【0036】次に本発明の分割型複合繊維の繊維断面に
ついて説明する。本発明の分割型複合繊維は、例えば図
1に例示したような少なくとも2成分の熱可塑性樹脂か
ら構成され、繊維横断面において、各成分は長軸方向に
交互に隣接され、かつ、該断面が屈曲、湾曲もしくは扁
平形状の複合繊維であって、該断面の長軸Lと短軸Wの
比(L/W)が3〜20の分割型複合繊維である。ここ
で長軸Lとは、各成分が交互に隣接される方向で、か
つ、断面形状の最も長い部分の長さを表す(図1参
照)。短軸Wとは、各成分の接触面方向、即ち断面形状
の厚みを表す(図1参照)。L/Wの比が3以上である
と、通常の円断面分割型複合繊維、例えば放射状、積層
状分割型複合繊維と比べて、分割セグメント数および繊
度が同じである場合、表面積が大きく、また、隣接成分
同士の接触面積は小さくなるため、高圧液体流を効果的
に該複合繊維に受けることができ、同じ水圧であっても
分割し易くなる。また、20を超えると効果的に高圧液
体流を複合繊維が受けることができるが、曳糸性の維
持、口金の単位面積当たりの孔数が少なくなり、生産性
が悪くなるなどの問題が発生する。Next, the fiber cross section of the splittable conjugate fiber of the present invention will be described. The splittable conjugate fiber of the present invention is composed of, for example, at least two-component thermoplastic resin as exemplified in FIG. 1, and in the fiber cross section, each component is alternately adjacent to each other in the longitudinal direction, and the cross section is It is a conjugate fiber having a bent, curved or flattened shape, wherein the ratio (L / W) of the major axis L to the minor axis W of the cross section (L / W) is 3 to 20. Here, the major axis L represents the length of the longest portion of the cross-sectional shape in the direction in which the components are alternately adjacent to each other (see FIG. 1). The minor axis W indicates the direction of the contact surface of each component, that is, the thickness of the cross-sectional shape (see FIG. 1). When the L / W ratio is 3 or more, the surface area is large when the number of divided segments and the fineness are the same as compared with ordinary circular section splittable conjugate fibers, for example, radial and laminated splittable conjugate fibers, and Since the contact area between adjacent components is small, a high-pressure liquid flow can be effectively received by the conjugate fiber, and division is easy even at the same water pressure. In addition, when it exceeds 20, the composite fiber can receive the high-pressure liquid flow effectively, but problems such as maintaining spinnability, reducing the number of holes per unit area of the die, and reducing productivity occur. I do.
【0037】さらに、断面形状が屈曲、湾曲もしくは扁
平形状をしていることでさらに分割性が向上する。繊維
断面形状が直線であるもの(図9参照)と比べて、製糸
工程中、例えば紡糸工程で得られた未延伸糸を延伸工程
で延伸する場合、速度差のあるロール間で集束された繊
維は強い応力で延伸されるが、この時繊維同士は高い圧
力で圧迫されることとなる。また短繊維とする場合に
は、カット工程で延伸工程と同等以上の強い圧力で繊維
同士が圧迫されることとなる。このため、屈曲もしくは
湾曲した繊維断面を有する本発明の分割型複合繊維は、
直線状の断面形状と比べて、非常に潰され易く、即ち分
割が部分的に進行することとなる。また分割しなくても
該複合繊維の各成分の接触界面には歪みが加わり、より
分割しやすい状態になっており、本発明の分割型複合繊
維は非常に分割し易くなる。Further, since the cross-sectional shape is a bent, curved or flat shape, the division is further improved. In the case where the undrawn yarn obtained in the spinning step is drawn in the drawing step, for example, in the drawing step, as compared with the one in which the fiber cross-sectional shape is a straight line (see FIG. 9), the fibers bundled between rolls having a speed difference Is stretched by a strong stress, but at this time, the fibers are compressed with a high pressure. When short fibers are used, the fibers are compressed by a strong pressure equal to or higher than that in the drawing step in the cutting step. For this reason, the splittable conjugate fiber of the present invention having a bent or curved fiber cross section,
Compared to a straight cross-sectional shape, it is very easily crushed, that is, the division is partially advanced. Even without splitting, strain is applied to the contact interface of each component of the conjugate fiber, so that the conjugate fiber is more easily split, and the splittable conjugate fiber of the present invention is very easily split.
【0038】このように製糸工程中で、すでに部分的に
分割が進行しいる場合は、抄紙法が好適に使用できる。
抄紙法の場合、すでに部分的に分割が進行している方が
抄紙の段階で緻密な地合の良いウェブとなり好ましい。
また製糸工程中での分割の進行を極力抑えたい場合は、
延伸倍率を低く設定することが有効である。具体的に
は、延伸糸伸度が未延伸糸伸度の20%以上を有するこ
とが好ましい。ここで屈曲もしくは湾曲した断面形状
は、特に限定されるものではなく、例えば、C型(図1
〜5参照)、S字型(図7参照)、M字型、N字型、L
字型、V字型、W型(図8参照)、波型などを挙げるこ
とができるが、本発明はあってはこれらの断面形状に限
定されるものではない。また、種々の断面形状の混合物
であっても良い。さらに、偏平形状としては、例えばU
型、馬蹄形型や該U型、馬蹄形型の湾曲部が圧縮されて
偏平になった断面形状を挙げることができるが、本発明
はこれらの断面形状に限定されるものではない。As described above, in the case where the division has already partially progressed in the yarn making process, the papermaking method can be suitably used.
In the case of the papermaking method, it is preferred that the division has already been partially performed, since a dense and well-formed web is obtained at the papermaking stage.
Also, if you want to minimize the progress of splitting during the spinning process,
It is effective to set a low draw ratio. Specifically, the drawn yarn elongation preferably has 20% or more of the undrawn yarn elongation. Here, the bent or curved cross-sectional shape is not particularly limited.
5), S-shaped (see FIG. 7), M-shaped, N-shaped, L
Examples include a V-shape, a V-shape, a W-shape (see FIG. 8), and a corrugation, but the present invention is not limited to these cross-sectional shapes. Further, a mixture of various cross-sectional shapes may be used. Further, as the flat shape, for example, U
Molds, horseshoe-shaped, U-shaped, and horseshoe-shaped curved portions may be compressed and flattened in cross section, but the present invention is not limited to these cross sections.
【0039】前記のように本発明の分割型複合繊維の繊
維断面形状は、長軸方向に屈曲、湾曲もしくは偏平形状
をしているため、延伸、カット工程と同様な効果をカレ
ンダーロール同士の加圧によっても行うことができる。
従って、例えばスパンボンド法のような未延伸糸状態の
長繊維をそのままコンベアーに集積した場合であって
も、加圧されたカレンダーロール間を通過させることに
より、分割、細繊化された繊維集合体とすることができ
る。また従来のスパンボンド法で採用されている分割型
複合繊維の繊維断面に比べ、本発明の分割型複合繊維
は、各セグメントがほぼ同繊度のため、より均一な繊度
を有する極細繊維から構成された繊維成形体とすること
ができる。As described above, since the cross-sectional shape of the splittable conjugate fiber of the present invention is bent, curved or flat in the major axis direction, the same effect as in the drawing and cutting steps can be obtained by adding calender rolls. It can also be done by pressure.
Therefore, even when long fibers in an undrawn yarn state such as a spunbond method are directly accumulated on a conveyor, by passing between pressurized calender rolls, a divided, finely divided fiber aggregate Can be a body. Also, compared to the fiber cross section of the splittable conjugate fiber employed in the conventional spunbonding method, the splittable conjugate fiber of the present invention is composed of ultrafine fibers having more uniform fineness because each segment has almost the same fineness. Fiber molded article.
【0040】さらに本発明の分割型複合繊維を構成する
樹脂の1成分の繊維外周弧の長さaと隣接成分との接触
長さbとの比(a/b)は、0.1〜2.5を満足する
ことが好ましい。該(a/b)比が0.1未満である
と、隣接成分との接触面積が繊維外周面に比べて大きく
なり、薄片が積層した構造となり高分割率を達成するに
は、高エネルギーが必要となる。また、2.5を超える
と分割数が少なくなるか、もしくは偏平形状の厚みが薄
くなりすぎるため、可紡性良く生産することが非常に難
しくなる。Further, the ratio (a / b) of the length a of the fiber outer peripheral arc of one component of the resin constituting the splittable conjugate fiber of the present invention to the contact length b with the adjacent component is 0.1 to 2 .5 is preferably satisfied. When the (a / b) ratio is less than 0.1, the contact area with the adjacent component becomes larger than the outer peripheral surface of the fiber, and the structure becomes a laminate of flakes. Required. On the other hand, if it exceeds 2.5, the number of divisions becomes small, or the thickness of the flat shape becomes too thin, so that it becomes very difficult to produce with good spinnability.
【0041】また、本発明の分割型複合繊維の繊維断面
において、屈曲や湾曲により囲まれた面積S1と該分割
型複合繊維の断面積S2(図6参照)の比(S1/S
2)が0.2〜1.0を満足することが好ましい。ここ
でS1は、本発明の分割型複合繊維の繊維断面におい
て、長軸の両端を結んだ直線と屈曲あるいは湾曲により
囲まれた部分を表し、屈曲もしくは湾曲の度合いを表
す。即ちS1が大きくなれば長軸が大きく屈曲もしくは
湾曲することとなり、S1/S2は、0.2以上を満足
することが好ましい。0.2未満であると、屈曲や湾曲
が小さく、前記、屈曲や湾曲による効果が小さくなる。
また1.0を越えると該複合繊維の長軸が長くなりすぎ
るか、または厚みが極端に薄くなるなどの問題から生産
性を維持することが難しくなる。Further, in the fiber cross section of the splittable conjugate fiber of the present invention, the ratio (S1 / S1) of the area S1 surrounded by the bend or curve and the cross sectional area S2 (see FIG. 6) of the splittable conjugate fiber is shown.
2) preferably satisfies 0.2 to 1.0. Here, S1 represents a portion surrounded by a straight line connecting both ends of the long axis and a bend or curve in the fiber cross section of the splittable conjugate fiber of the present invention, and represents a degree of the bend or curve. That is, as S1 increases, the major axis is greatly bent or curved, and S1 / S2 preferably satisfies 0.2 or more. If it is less than 0.2, the bending or bending is small, and the effect of the bending or bending is reduced.
On the other hand, if it exceeds 1.0, it becomes difficult to maintain the productivity due to the problem that the long axis of the conjugate fiber becomes too long or the thickness becomes extremely thin.
【0042】本発明の分割型複合繊維は、前記のような
繊維断面形状を取ることにより、従来の分割型複合繊維
では、非常に分割しにくく、分割させるために高エネル
ギーが必要であった同系樹脂の組み合わせ、特にポリオ
レフィン系樹脂同士の組み合わせであっても、分割性に
優れ、容易に分割させることができる。さらに、抄紙法
で用いる短繊維で構成されたウェブであっても、地合良
く高分割率で分割させることができる。以上のことか
ら、本発明の分割型複合繊維はこれまで分割し難いとさ
れていた樹脂同士の組み合わせに好ましく用いることが
できる。ここで本発明の分割型複合繊維の繊維断面を得
るために用いる紡糸用口金は、該分割複合繊維が得られ
るものであれば特に限定されることはないが、例えば、
細孔がC型、S字型、M字型、N字型、L字型、V型、
W型、波型、U型、馬蹄形型等に配置された口金を用い
ることができる。The splittable conjugate fiber of the present invention adopts the above-mentioned fiber cross-sectional shape, so that it is extremely difficult to split with the conventional splittable conjugate fiber and high energy is required for splitting. Even in the case of a combination of resins, particularly a combination of polyolefin-based resins, it is excellent in division property and can be easily divided. Further, even a web composed of short fibers used in a papermaking method can be divided at a high division ratio with good formation. From the above, the splittable conjugate fiber of the present invention can be preferably used for a combination of resins which has been considered difficult to split. Here, the spinneret used to obtain the fiber cross section of the splittable conjugate fiber of the present invention is not particularly limited as long as the split conjugate fiber can be obtained, for example,
The pores are C type, S type, M type, N type, L type, V type,
Caps arranged in a W shape, a corrugated shape, a U shape, a horseshoe shape, or the like can be used.
【0043】本発明の分割型複合繊維において、少なく
とも2成分の熱可塑性樹脂から構成される該複合繊維の
複合比は、10/90〜90/10重量%の範囲でその
用いた成分樹脂の合計が100重量%であれば良く、よ
り好ましくは30/70〜70/30重量%であり、最
も好ましくは、40/60〜60/40である。かかる
範囲の複合比とすることにより、少なくとも2種類の熱
可塑性樹脂が均一に配置された断面形状となり、より均
一な繊維成形体とすることができる。In the splittable conjugate fiber of the present invention, the conjugate ratio of the conjugate fiber composed of at least two-component thermoplastic resin is in the range of 10/90 to 90/10% by weight. Is preferably 100% by weight, more preferably 30/70 to 70/30% by weight, and most preferably 40/60 to 60/40. By setting the compounding ratio in such a range, a cross-sectional shape in which at least two kinds of thermoplastic resins are uniformly arranged is obtained, and a more uniform fiber molded body can be obtained.
【0044】本発明で得られる分割型複合繊維を高圧液
体流処理等で分割する場合、分割後の極細繊維の平均繊
度は0.5デシテックス以下で、特に0.3デシテック
ス以下となることが好ましい。従って分割型複合繊維の
分割セグメント数は、極細繊維の平均繊度が0.5デシ
テックス以下となるように決めれば良く、分割セグメン
ト数が多ければ分割後の繊度が小さくなる利点がある
が、実際には繊維製造上の容易さから4〜32セグメン
ト数とすることが好ましい。When the splittable conjugate fiber obtained in the present invention is split by high-pressure liquid flow treatment or the like, the average fineness of the ultrafine fiber after splitting is preferably 0.5 dtex or less, particularly preferably 0.3 dtex or less. . Therefore, the number of divided segments of the splittable conjugate fiber may be determined so that the average fineness of the ultrafine fibers is 0.5 decitex or less, and the larger the number of divided segments, the smaller the fineness after splitting. Is preferably 4 to 32 segments in terms of ease of fiber production.
【0045】分割前の単糸繊度は、特に限定されること
はないが、0.5〜10.0デシテックスであることが
好ましく、より好ましくは、1.0〜6.0デシテック
スである。また個々のセグメントの繊度は同一である必
要はなく、分割型複合繊維が完全に分割していない場合
には、未分割の分割繊維と完全に分割した極細繊維との
中間に複数の異なった繊度の繊維が混在していても良
い。The fineness of the single yarn before splitting is not particularly limited, but is preferably 0.5 to 10.0 dtex, and more preferably 1.0 to 6.0 dtex. The fineness of each segment does not need to be the same, and when the splittable conjugate fiber is not completely split, a plurality of different finenesses are set between the undivided split fiber and the completely split ultrafine fiber. May be mixed.
【0046】以下、本発明の分割型複合繊維の1例とし
て、ポリプロピレン樹脂と高密度ポリエチレン樹脂の2
成分を組み合わせた分割複合繊維の製造方法を例示す
る。通常の溶融紡糸機を用いて前記樹脂からなる長繊維
を紡出する。紡糸に際し、紡糸温度は200〜330℃
の範囲で紡糸することが好ましく、引き取り速度は40
m/分〜1500m/分程度とするのが良い。延伸は必
要に応じて行っても良く、延伸を行う場合、延伸倍率は
通常3〜9倍程度とするのが良い。さらに得られたトウ
は所定長に切断して短繊維とする。以上は短繊維の製造
工程を開示したが、トウを切断せず、長繊維トウを分繊
ガイドなどによりウェブとすることもできる。その後は
必要に応じて高次加工工程を経て、種々、用途に応じて
繊維成形体に形成される。また、紡糸延伸後、フィラメ
ント糸等として巻き取り、これを編成または織成して編
織物とした繊維成形体もしくは前記短繊維を紡績糸とし
た後、これを編成または織成して編織物とした繊維成形
体に形成しても良い。Hereinafter, as an example of the splittable conjugate fiber of the present invention, a polypropylene resin and a high-density polyethylene resin are used.
An example of a method for producing a split conjugate fiber in which components are combined will be described. A long fiber made of the resin is spun using a normal melt spinning machine. Spinning temperature is 200 ~ 330 ℃
And the take-up speed is 40
m / min to 1500 m / min. Stretching may be performed as needed, and in the case of performing stretching, the stretching ratio is usually preferably about 3 to 9 times. Further, the obtained tow is cut into a predetermined length to obtain short fibers. The above description discloses the process for producing short fibers, but it is also possible to form a long fiber tow into a web using a fiber separation guide or the like without cutting the tow. Thereafter, the fiber is formed into a fiber molded body through a high-order processing step as required, depending on various uses. Further, after spinning and drawing, the fiber molded body is wound up as a filament yarn or the like, knitted or woven to form a knitted woven fabric, or the short fiber is formed into a spun yarn, and then knitted or woven to form a knitted woven fabric. May be formed.
【0047】つまり、ここで繊維成形体とは、布状の形
態であればいかなるものでも良く、例えば織物、編物、
不織布もしくは不織繊維集合体などが挙げられる。ま
た、混綿、混紡、混繊、交撚、交編、交繊等の方法で布
状の形態にしたものも含まれる。さらに不織繊維集合体
とは、例えばカード法、エアレイド法もしくは抄紙法な
どの方法で均一にしたウェブ状物などをいう。That is, here, the fiber molded body may be any fiber-shaped form, such as a woven fabric, a knitted fabric,
Non-woven fabrics or non-woven fiber aggregates are exemplified. In addition, those in the form of a cloth by a method such as cotton blending, blending, blending, twisting, knitting, and blending are also included. Further, the nonwoven fiber aggregate refers to a web-like material made uniform by a method such as a card method, an air laid method, or a papermaking method.
【0048】かかる工程において、繊維を紡出後、繊維
の静電気防止、繊維成形体への加工性向上のための平滑
性付与などを目的として界面活性剤を繊維表面に付着さ
せることができる。界面活性剤の種類、濃度は用途に合
わせて適宜調整する。付着の方法は、ローラ法、浸漬
法、パットドライ法などを用いることができる。付着
は、紡糸工程、延伸工程、捲縮工程のいずれで付着させ
ても差し支えない。さらに短繊維、長繊維に問わず、紡
糸工程、延伸工程、捲縮工程以外の、例えば繊維成形体
に成形後、界面活性剤を付着させることもできる。In this step, after spinning the fiber, a surfactant can be adhered to the fiber surface for the purpose of preventing static electricity of the fiber and imparting smoothness for improving the processability of the fiber molded article. The type and concentration of the surfactant are appropriately adjusted according to the application. As a method of attachment, a roller method, a dipping method, a pad dry method, or the like can be used. The attachment may be performed in any of the spinning step, the stretching step, and the crimping step. Further, regardless of whether the fibers are short fibers or long fibers, a surfactant can be attached to the fiber molded body other than the spinning step, the stretching step, and the crimping step, for example, after molding the molded article.
【0049】本発明の分割型複合繊維の繊維長は、特に
限定されるものではないが、カード機を用いてウェブを
作成する場合は、一般に20〜76mmのものを用い、
抄紙法やエアレイド法では、一般に繊維長が2mm〜2
0mmのものが好ましく用いられる。繊維長が2mm未
満の場合には、物理的衝撃で繊維が動いてしまい、分割
に必要なエネルギーを繊維自体が受けにくくなってしま
う。また、繊維長が76mmを大幅に超える場合はカー
ド機等でのウェブ形成が均一にできず、均一な地合のウ
ェブとするのが難しくなる。The fiber length of the splittable conjugate fiber of the present invention is not particularly limited, but when a web is formed using a carding machine, a fiber length of 20 to 76 mm is generally used.
In the paper making method and the air laid method, the fiber length is generally 2 mm to 2 mm.
The one with 0 mm is preferably used. If the fiber length is less than 2 mm, the fiber will move due to physical impact, and the fiber itself will not easily receive the energy required for division. If the fiber length is significantly larger than 76 mm, the web cannot be formed uniformly by a carding machine or the like, and it is difficult to form a web having a uniform formation.
【0050】本発明の分割型複合繊維からなる繊維成形
体の製造方法の一例として、不織布の製造方法を例示す
る。例えば前記分割型複合繊維製造方法で製造された短
繊維を用いて、カード法、エアレイド法、あるいは抄紙
法を用いて必要な目付のウェブを作製する。またメルト
ブローン法、スパンボンド法などで直接ウェブを作製し
ても良い。前記の方法で作製したウェブを、ニードルパ
ンチ法、高圧液体流処理、加圧されたカレンダーロール
等の公知の方法で分割細繊化して繊維成形体を得ること
ができる。さらに繊維成形体を熱風あるいは熱ロール等
の公知の加工方法で処理することもできる。抄紙法など
の非常に短い繊維で構成されたウェブをニードルパンチ
法、高圧液体流処理等の公知の方法で分割細繊化する場
合に、その物理的応力で繊維が分割すると同時に繊維が
動いて地合不良となる場合があるため、予め本発明の分
割型複合繊維を構成する樹脂の融点よりも低融点で熱融
着する繊維を5〜30%重量%混綿しておき、この低融
点繊維が融着する温度で熱処理を行い、熱融着された不
織布を作成しておくことで地合不良を抑えることができ
る。As an example of the method for producing a fibrous formed article made of the splittable conjugate fiber of the present invention, a method for producing a nonwoven fabric will be described. For example, using the short fibers produced by the above-mentioned splittable composite fiber production method, a web having a required basis weight is produced by a card method, an air laid method, or a papermaking method. Alternatively, a web may be directly produced by a melt blown method, a spun bond method, or the like. The web produced by the above method can be divided and finely divided by a known method such as a needle punch method, a high-pressure liquid flow treatment, or a pressurized calender roll to obtain a fiber molded body. Further, the fiber molded body can be treated by a known processing method such as hot air or a hot roll. When a web composed of very short fibers such as a papermaking method is divided into fine fibers by a known method such as a needle punch method or a high-pressure liquid flow treatment, the fibers are divided and moved at the same time by the physical stress. Since the formation may be defective, fibers that are heat-fused at a melting point lower than the melting point of the resin constituting the splittable conjugate fiber of the present invention are mixed in advance by 5 to 30% by weight. By performing heat treatment at a temperature at which the non-woven fabric is fused to prepare a heat-sealed non-woven fabric, formation defects can be suppressed.
【0051】本発明の繊維成形体の目付は、特に限定さ
れるものではないが、10〜200g/m2のものが好
ましい。目付が10g/m2未満では、該不織布を製造
するために、分割型複合繊維を高圧液体流処理などの物
理的応力で分割、細繊化すると、地合不良な不織布とな
る場合がある。また目付が200g/m2を超えると、
目付が高く、高圧水流が必要となり、地合良く、均一な
分割を行うことが困難となる場合がある。The basis weight of the fiber molded article of the present invention is not particularly limited, but is preferably 10 to 200 g / m 2 . If the basis weight is less than 10 g / m 2 , if the splittable conjugate fiber is divided and finely divided by a physical stress such as a high-pressure liquid flow treatment to produce the nonwoven fabric, a nonwoven fabric with poor formation may be obtained. When the basis weight exceeds 200 g / m 2 ,
The basis weight is high, a high-pressure water flow is required, and it may be difficult to perform uniform and uniform division.
【0052】本発明の繊維成形体は、本発明の妨げにな
らない範囲で、必要に応じて本発明の分割型複合繊維に
他の繊維を混合して用いることができる。かかる他の繊
維としては、ポリアミド、ポリエステル、ポリオレフィ
ン、アクリルなどの合成繊維、綿、羊毛、麻などの天然
繊維、レーヨン、キュプラ、アセテートなどの再生繊
維、半合成繊維などが挙げられる。The fiber molded article of the present invention can be used by mixing other fibers with the splittable conjugate fiber of the present invention, if necessary, as long as it does not hinder the present invention. Examples of such other fibers include synthetic fibers such as polyamide, polyester, polyolefin, and acrylic; natural fibers such as cotton, wool, and hemp; regenerated fibers such as rayon, cupra, and acetate; and semi-synthetic fibers.
【0053】次に、高圧液体流処理について説明する。
高圧液体流処理に用いる高圧液体流装置としては、例え
ば、孔径が0.05〜1.5mm、特に0.1〜0.5
mmの噴射孔を孔間隔0.1〜1.5mmで一列あるい
は複数列に多数配列した装置を用いる。噴射孔から高水
圧で噴射させて得られる高圧液体流を多孔性支持部材上
に置いた前記ウェブに衝突させる。これにより本発明の
未分割の分割型複合繊維は高圧液体流により、交絡され
ると同時に細繊化される。噴射孔の配列は前記ウェブの
進行方向と直交する方向に列状に配列する。高圧液体流
としては、常温あるいは温水を用いても良し、任意に他
の液体を用いても良い。Next, the high-pressure liquid flow processing will be described.
As the high-pressure liquid flow device used for the high-pressure liquid flow treatment, for example, a hole diameter of 0.05 to 1.5 mm, particularly 0.1 to 0.5
A device in which a large number of injection holes having a diameter of 0.1 mm to 1.5 mm are arranged in a single row or in a plurality of rows is used. A high-pressure liquid stream obtained by jetting at a high water pressure from an injection hole is caused to collide with the web placed on a porous support member. Thereby, the undivided splittable conjugate fiber of the present invention is entangled and fined at the same time by the high-pressure liquid flow. The arrangement of the injection holes is arranged in a row in a direction orthogonal to the traveling direction of the web. As the high-pressure liquid flow, room temperature or hot water may be used, and other liquids may be optionally used.
【0054】噴射孔とウェブとの間の距離は、10〜1
50mmとするのが良い。この距離が10mm未満であ
るとこの処理により得られる繊維成形体の地合が乱れ、
一方、この距離が150mmを超えると液体流がウェブ
に与える物理的衝撃が弱くなり、交絡及び分割細繊化が
十分に施されない場合がる。この高圧液体流の処理圧力
は、製造方法及び繊維成形体の要求性能によって、制御
されるが、一般的には、20kg/cm2〜200kg
/cm2の高圧液体流を噴射するのが良い。なお処理す
る目付等にも左右されるが、前記処理圧力の範囲内にお
いて、高圧液体流は順次、低水圧から高水圧へ圧力を上
げて処理すると、ウェブの地合が乱れることなく、交絡
及び分割細繊化が可能となる。高圧液体流を施す際にウ
ェブを載せる多孔性支持部材としては、例えば50〜2
00メッシュの金網製あるいは合成樹脂製のメッシュス
クリーンや有孔板など高圧液体流が上記ウェブを貫通す
るものであれば特に限定されない。The distance between the injection hole and the web is 10 to 1
It is good to be 50 mm. If this distance is less than 10 mm, the formation of the fiber molded body obtained by this treatment is disturbed,
On the other hand, if the distance exceeds 150 mm, the physical impact of the liquid stream on the web becomes weak, and confounding and fine splitting may not be performed sufficiently. The processing pressure of the high-pressure liquid flow is controlled by the manufacturing method and the required performance of the fiber molded body, but is generally 20 kg / cm 2 to 200 kg.
/ Cm 2 of the high-pressure liquid stream is preferably injected. Although it depends on the basis weight of the treatment, etc., within the range of the treatment pressure, when the high-pressure liquid flow is treated by sequentially increasing the pressure from a low water pressure to a high water pressure, the formation of the web is not disturbed, It becomes possible to divide the fine fibers. As a porous support member on which a web is placed when applying a high-pressure liquid flow, for example, 50 to 2
There is no particular limitation as long as the high-pressure liquid flow penetrates the web, such as a 00 mesh wire mesh or a synthetic resin mesh screen or a perforated plate.
【0055】尚、ウェブの片面より高圧液体流処理を施
した後、引き続き交絡処理されたウェブを反転させて、
高圧液体流処理を施すことによって、表裏共に緻密で地
合の良い繊維成形体を得ることができる。さらに高圧液
体流処理を施した後、処理後の繊維成形体から水分を除
去する。この水分を除去するに際しては、公知の方法を
採用することができる。例えば,マングロール等の絞り
装置を用いて、水分をある程度除去した後、熱風循環式
乾燥機等の乾燥装置を用いて完全に水分を除去して本発
明の繊維成形体を得ることができる。After applying the high-pressure liquid flow treatment from one side of the web, the entangled web is subsequently inverted,
By performing the high-pressure liquid flow treatment, it is possible to obtain a fiber molded body that is dense on both sides and has good formation. After the high-pressure liquid flow treatment, moisture is removed from the treated fiber molded body. In removing the moisture, a known method can be employed. For example, after removing water to some extent using a squeezing device such as a mangrol, the water can be completely removed using a drying device such as a hot air circulation type dryer to obtain the fiber molded article of the present invention.
【0056】前記の方法で本発明の分割型複合繊維を含
むウェブに高圧液体流処理を施して分割細繊化し、緻密
な繊維成形体を得るに際し、従来の繊維断面を有する分
割型複合繊維(図9、図10)に比べ、易分割し易く、
高圧液体流による物理的衝撃が少なくて済む。このた
め、不織布加工工程の律速段階である高圧液体流処理の
高速化及び高圧液体流の低圧化による地合の改善、例え
ば高圧液体流の圧力を低くできるため、繊維成形体の地
合が乱れたり、貫通孔が開くなどの問題を改善すること
ができる。When the web containing the splittable conjugate fiber of the present invention is subjected to a high-pressure liquid flow treatment by the above-mentioned method and divided into fine fibers to obtain a dense fiber molded product, the conventional splittable conjugate fiber having a fiber cross section ( 9 and 10), it is easier to divide,
Less physical impact due to high pressure liquid flow. For this reason, the formation is improved by speeding up the high-pressure liquid flow processing, which is the rate-determining step of the nonwoven fabric processing step, and reducing the pressure of the high-pressure liquid flow. For example, the pressure of the high-pressure liquid flow can be reduced. And the problem that a through hole is opened can be improved.
【0057】以上のように最も分割し難いとされていた
同系樹脂から構成された分割型複合繊維であっても、容
易に分割させることができ、緻密で地合の良い繊維成形
体を得ることができ、これら繊維成形体を用いて、バッ
テリセパレーターやワイパー等の産業資材分野をはじ
め、衛生材料分野、衣料分野にも好適に使用することが
できる。As described above, even a splittable conjugate fiber composed of the same type of resin, which is considered to be most difficult to split, can be easily split, and a dense and well-formed fiber molded body can be obtained. The fiber molded article can be suitably used in the field of industrial materials such as battery separators and wipers, as well as in the field of sanitary materials and clothing.
【0058】さらに、本発明の繊維成形体の片面もしく
は両面に不織布、フィルム、編物、織物等から選ばれた
少なくとも1種からなるシートを積層した、積層繊維成
形体(以下Aタイプ)や、さらには該繊維成形体を逆に
前記シートの両面に積層した積層繊維成形体(以下Bタ
イプ)とすることもできる。Aタイプの場合は分割処理
した繊維成形体をシートの片面もしくは両面に積層する
方が分割効率が良く、好ましい。Bタイプの場合は積層
前後、どちらでも繊維成形体は分割されるが、特に積層
後の分割処理はシートと繊維成形体との絡合作用が得ら
れ好ましい。これらの積層繊維成形体(A)、(B)の
いずれもおむつ、ナプキン等の吸収性物品で代表される
衛生材料分野、ワイパー、バッテリセパレーター等の産
業資材分野にも好適に使用することができる。Further, a laminated fiber molded article (hereinafter referred to as A type) comprising a sheet of at least one selected from nonwoven fabrics, films, knits, and woven fabrics laminated on one or both sides of the fiber molded article of the present invention; Can be a laminated fiber molded body (hereinafter referred to as B type) in which the fiber molded body is reversely laminated on both sides of the sheet. In the case of the A type, it is preferable to laminate the fiber molded body subjected to the division treatment on one side or both sides of the sheet because the division efficiency is good. In the case of the B type, the fibrous molded body is divided before and after lamination, but the dividing treatment after lamination is particularly preferable because the entanglement action between the sheet and the fibrous molded body can be obtained. Any of these laminated fiber molded articles (A) and (B) can be suitably used in the field of sanitary materials represented by absorbent articles such as diapers and napkins, and in the field of industrial materials such as wipers and battery separators. .
【0059】[0059]
【実施例】以下、本発明を実施例及び比較例によって詳
細に説明するが、本発明はこれにより限定されるもので
はない。なお実施例、比較例における用語と物性の測定
方法は以下の通りである。EXAMPLES Hereinafter, the present invention will be described in detail with reference to Examples and Comparative Examples, but the present invention is not limited thereto. The terms used in the examples and comparative examples and methods for measuring physical properties are as follows.
【0060】(1)メルトフローレート:JIS K7
210に準拠して測定した。 原料ポリプロピレン樹脂:条件14 原料ポリエチレン樹脂 :条件4 繊維成形後のポリオレフィン系樹脂:条件14(1) Melt flow rate: JIS K7
210. Raw material polypropylene resin: Condition 14 Raw material polyethylene resin: Condition 4 Polyolefin resin after fiber molding: Condition 14
【0061】(2)L/W測定法 任意に選んだ未分割繊維10本の断面写真から、以下の
値を計算し、その平均値からL/Wを算出した。 L:各成分が交互に隣接される方向で、かつ、繊維断面
形状のもっとも長い部分を表す(図1参照) W:各成分の接触面方向、即ち断面形状の厚みを表す
(図1参照)(2) L / W Measurement Method The following values were calculated from cross-sectional photographs of 10 randomly selected undivided fibers, and the L / W was calculated from the average value. L: The direction in which each component is alternately adjacent, and represents the longest part of the fiber cross-sectional shape (see FIG. 1) W: The contact surface direction of each component, that is, the thickness of the cross-sectional shape (see FIG. 1)
【0062】(3)a/b測定法 任意に選んだ未分割繊維10本の断面写真から、以下の
値を計算し、その平均値からa/bを算出した。 a:1成分の繊維外周面の長さの平均値(図1参照) b:1成分の接触長さの平均値(図1参照)(3) a / b Measurement Method The following values were calculated from cross-sectional photographs of 10 randomly selected undivided fibers, and a / b was calculated from the average value. a: average value of the length of the fiber outer peripheral surface of one component (see FIG. 1) b: average value of the contact length of one component (see FIG. 1)
【0063】(4)S1/S2測定法 任意に選んだ未分割繊維10本の繊維断面写真から、S
1、S2の面積を計算し、その平均値からS1/S2を
算出した。(図6参照) S1:長軸の両端を結んだ直線と屈曲もしくは湾曲によ
り囲まれた部分の面積 S2:本発明の分割型複合繊維の断面積(4) S1 / S2 measurement method From the fiber cross-sectional photograph of 10 randomly selected undivided fibers,
1, the area of S2 was calculated, and S1 / S2 was calculated from the average value. (See FIG. 6) S1: Area of a portion surrounded by a straight line connecting both ends of the long axis and a bend or curve S2: Cross-sectional area of splittable conjugate fiber of the present invention
【0064】(5)曳糸性 溶融紡糸時の曳糸性を糸切れ回数の発生率により、次の
3段階で評価した。 ○:糸切れが全く発生せず、操作性が良好である。 △:糸切れが1時間当たり1〜2回 ×:糸切れが1時間当たり4回以上発生し、操作上問題
がある。(5) Spinnability The spinnability at the time of melt spinning was evaluated by the following three steps based on the occurrence rate of the number of yarn breaks. :: No breakage of yarn occurred and operability was good. Δ: Thread breaks occur 1 to 2 times per hour ×: Thread breaks occur 4 times or more per hour, causing operational problems.
【0065】(6)延伸倍率 以下の式により算出した。 延伸倍率=引取ロール速度(m/分)/供給ロール(m
/分)(6) Stretching ratio Calculated by the following equation. Stretching ratio = take-up roll speed (m / min) / supply roll (m
/ Min)
【0066】(7)繊維引張強伸度 JIS−L1013法に準じ、島津製作所(株)製オー
トグラフ AGS500Dを用い、糸長100mm、引
張速度100mm/分で測定した。(7) Tensile strength and tensile strength of fiber Measured according to JIS-L1013 method using an Autograph AGS500D manufactured by Shimadzu Corporation at a yarn length of 100 mm and a tensile speed of 100 mm / min.
【0067】(8)不織布の引張強伸度 5cm幅の不織布を島津製作所(株)製オートグラフ
AGS500Dを用い、MD方向の不織布破断強度を測
定した。試長100mm、引張速度200mm/分で測
定し、測定温度は室温とした。(8) Tensile strength and elongation of non-woven fabric A non-woven fabric having a width of 5 cm was obtained from an autograph manufactured by Shimadzu Corporation.
The breaking strength of the nonwoven fabric in the MD direction was measured using AGS500D. Measurement was performed at a test length of 100 mm and a tensile speed of 200 mm / min, and the measurement temperature was room temperature.
【0068】(9)分割率の測定 分割後の不織布をワックスにて包含し、ミクロトームで
繊維軸に対して、直角にスライスして資料片を作成す
る。これを顕微鏡で観察し、繊維の断面像を画像処理し
て、セグメントの70%以上が分割された繊維の総断面
積(A)と未分割繊維の総断面積(B)を測定し、以下
の式で算出した。 分割率(%)={A/(A+B)}×100(9) Measurement of splitting ratio The nonwoven fabric after splitting is included in wax, and sliced at right angles to the fiber axis with a microtome to prepare a data piece. This is observed with a microscope, the cross-sectional image of the fiber is image-processed, and the total cross-sectional area (A) of the fiber in which 70% or more of the segment is divided and the total cross-sectional area (B) of the undivided fiber are measured. Was calculated by the following equation. Division ratio (%) = {A / (A + B)} × 100
【0069】(10)分割後の単糸繊度 分割前の繊度と分割可能なセグメント数から、分割細繊
化後の単糸繊度を以下の式より算出した。 分割後繊度(dtex/f)=分割前繊度(dtex/
f)/分割可能セグメント数(個)(10) Single yarn fineness after division From the fineness before division and the number of segments that can be divided, the single yarn fineness after division and fineness was calculated by the following formula. Fineness after division (dtex / f) = Fineness before division (dtex /
f) / Dividable segment number (pieces)
【0070】(11)地合 10人のパネラーが分割細繊化加工後の不織布(1m
角)の繊維の分布斑を目視した結果により次のように評
価した。 ○:7人以上が斑が少なく、また貫通孔もないと感じ
た。 △:4〜6人が斑が少なく、貫通孔もないと感じた。 ×:斑が少ないと感じたのは3人以下であった。(11) Formation A panel of 10 panelists made a nonwoven fabric (1 m
The evaluation was made as follows based on the result of visually observing the distribution unevenness of the fibers of (corner). :: Seven or more felt that there were few spots and no through holes. B: Four to six persons felt that there were few spots and no through holes. X: Three or less felt that there was little unevenness.
【0071】(12)高圧液体流処理 ローラカード機、エアレイド機、抄紙機等で作成したウ
ェブを80メッシュの平織りからなるコンベアーベルト
上に載せ、コンベアーベルト速度20m/分の速度で、
ノズル径0.1mm、ノズルピッチ1mmのノズル直下
を通過させ、高圧液体流を噴射した。まず、2MPaで
予め予備処理(2段)した後、水圧5MPaの高圧液体
流で4段処理した。ウェブを反転させ、さらに水圧5M
Paの高圧液体流で4段処理することにより、分割細繊
化した不織布を得た。ここで段とは、ノズル直下を通過
した回数のことである。(12) High-pressure liquid flow treatment A web made by a roller card machine, an air laid machine, a paper machine, or the like is placed on a conveyor belt of 80 mesh plain weave, and the conveyor belt speed is 20 m / min.
A high-pressure liquid flow was ejected by passing immediately below a nozzle having a nozzle diameter of 0.1 mm and a nozzle pitch of 1 mm. First, after a preliminary treatment (2 stages) at 2 MPa, a 4-stage treatment was performed with a high-pressure liquid flow at a water pressure of 5 MPa. Turn the web over and press 5M
By performing a four-stage treatment with a high-pressure liquid flow of Pa, a divided and finely divided nonwoven fabric was obtained. Here, the stage refers to the number of times that the ink has passed just below the nozzle.
【0072】(13)加圧(分割)ロール 誘導発熱油圧式2本ロールクリアランス機(由里ロール
(株)社製) 処理温度:雰囲気温度 処理線圧:40kg/cm 処理速度:10m/min(13) Pressurized (split) roll Induction heat-generating hydraulic two-roll clearance machine (manufactured by Yuri Roll Co., Ltd.) Processing temperature: Atmospheric temperature Processing linear pressure: 40 kg / cm Processing speed: 10 m / min
【0073】(14)耐水圧 JIS L1092に準拠して測定した。(14) Water resistance Pressure was measured in accordance with JIS L1092.
【0074】実施例1〜3 高融点樹脂(A成分)にポリプロピレン樹脂(プロピレ
ン単独重合体)、低融点樹脂(B成分)として高密度ポ
リエチレン樹脂を用い、分割型複合繊維用口金を用い
て、A成分及びB成分の両樹脂の容積比率を50/50
とし、単糸デニール7.5dtexの図1に示した繊維
断面形状を有する分割型複合繊維を紡糸した。引き取り
工程において、アルキルフォスフェートカリウム塩を付
着させた。得られた未延伸糸を90℃、4.1倍で延伸
し、抄紙用仕上げ剤を付着させた後10mmに切断し、
水分率20重量%の短繊維を得た。この短繊維にポリプ
ロピレン(芯)/低密度ポリエチレン(鞘)の鞘芯複合
繊維(EAC繊維、チッソ(株))を20重量%添加
し、角型シートマシン(25cm×25cm)を用い、
抄紙法でウェブとした。熊谷理器工業社製ヤンキードラ
イヤーを用い、105℃で3分間乾燥、予備接着を行い
ウェブを得た。このウェブに前記高圧液体流処理を行っ
た後、さらに80℃のドライヤーで乾燥させて繊維成形
体を得た。Examples 1 to 3 Using a polypropylene resin (propylene homopolymer) as the high melting point resin (component A), a high density polyethylene resin as the low melting point resin (component B), and using a splittable composite fiber die, The volume ratio of both resins of the component A and the component B is 50/50.
Then, a splittable conjugate fiber having a fiber cross-sectional shape shown in FIG. 1 and having a single yarn denier of 7.5 dtex was spun. In the take-off step, the alkyl phosphate potassium salt was deposited. The obtained unstretched yarn was stretched at 90 ° C. and 4.1 times, and after attaching a papermaking finishing agent, it was cut into 10 mm,
Short fibers having a water content of 20% by weight were obtained. 20% by weight of a sheath-core composite fiber of polypropylene (core) / low-density polyethylene (sheath) (EAC fiber, Chisso Corporation) was added to the short fiber, and a square sheet machine (25 cm × 25 cm) was used.
The web was made by the papermaking method. Using a Yankee dryer manufactured by Kumagai Riki Kogyo Co., Ltd., it was dried at 105 ° C. for 3 minutes and preliminarily bonded to obtain a web. After performing the high-pressure liquid flow treatment on the web, the web was further dried with a dryer at 80 ° C. to obtain a fiber molded body.
【0075】実施例4 高融点樹脂(A成分)としてポリプロピレン樹脂(プロ
ピレン単独重合体)、低融点樹脂(B成分)として高密
度ポリエチレン樹脂を用い、分割型複合繊維用口金を用
いて、A成分及びB成分の両樹脂の容積比率を50/5
0とし、単糸デニール7.5dtexの図2に示した繊
維断面形状を有する分割型複合繊維を紡糸した。引き取
り工程において、アルキルフォスフェートカリウム塩を
付着させた。得られた未延伸糸を90℃、1.5倍で延
伸し、捲縮を付与し、51mmに切断した。得られた短
繊維をローラカード機にてウェブとし、該ウェブに前記
高圧液体流処理を行った後、さらに80℃のドライヤー
で乾燥させて繊維成形体を得た。該繊維成形体を大人用
オムツの表面材として使用したところ、肌触り(ソフト
感)、不織布強力等に優れ、吸収性物品として非常に良
好なものであった。Example 4 A polypropylene resin (propylene homopolymer) was used as the high melting point resin (component A), a high density polyethylene resin was used as the low melting point resin (component B), and a split type composite fiber die was used. And the volume ratio of both resins of the component B is 50/5
The value was set to 0, and a splittable conjugate fiber having a single yarn denier of 7.5 dtex and having a fiber cross-sectional shape shown in FIG. 2 was spun. In the take-off step, the alkyl phosphate potassium salt was deposited. The obtained undrawn yarn was drawn at 90 ° C. and 1.5 times, crimped, and cut into 51 mm. The obtained short fibers were formed into a web by a roller card machine, and the web was subjected to the high-pressure liquid flow treatment, and then dried with a dryer at 80 ° C. to obtain a fiber molded body. When the fiber molded article was used as a surface material of an adult diaper, it was excellent in feel (soft feeling), strong strength of a nonwoven fabric, and the like, and was very good as an absorbent article.
【0076】実施例5 図3に示した繊維横断面を得るための分割型複合繊維用
口金を用いた以外は、実施例1に準拠して、分割型複合
繊維の紡糸、繊維成形体の作製を行った。Example 5 Spinning of a splittable conjugate fiber and production of a fiber molded body in accordance with Example 1 except that a splittable conjugate fiber base for obtaining a fiber cross section shown in FIG. 3 was used. Was done.
【0077】実施例6 高密度ポリエチレンの替わりに直鎖状低密度ポリエチレ
ンを用いた以外は、実施例1に準拠して、分割型複合繊
維の紡糸、繊維成形体の作製を行った。Example 6 A split type composite fiber was spun and a fiber molded product was produced in accordance with Example 1, except that a linear low-density polyethylene was used instead of the high-density polyethylene.
【0078】実施例7 高密度ポリエチレンの替わりに低密度ポリエチレンを用
いた以外は、実施例1に準拠して、分割型複合繊維の紡
糸、繊維成形体の作製を行った。Example 7 A split type composite fiber was spun and a fiber molded body was produced in accordance with Example 1, except that low-density polyethylene was used instead of high-density polyethylene.
【0079】実施例8 高融点樹脂(A成分)としてポリプロピレン樹脂(プロ
ピレン単独重合体)、低融点樹脂(B成分)として高密
度ポリエチレン樹脂を用い、分割型複合繊維用口金を用
いて、A成分及びB成分の両樹脂の容積比率を50/5
0とし、単糸デニール20.0dtexの図1に示した
繊維断面形状を有する分割型複合繊維を紡糸した。引き
取り工程において、アルキルフォスフェートカリウム塩
を付着させた。得られた未延伸糸を90℃、4.1倍で
延伸し、抄紙用仕上げ剤を付着させた後、10mmに切
断し、水分率20重量%の短繊維を得た。この短繊維に
ポリプロピレン(芯)/低密度ポリエチレン(鞘)の鞘
芯複合繊維(EAC繊維、チッソ(株))を20重量%
添加し、角型シートマシン(25cm×25cm)を用
い、抄紙法でウェブとした。熊谷理器工業社製ヤンキー
ドライヤーを用い、105℃で3分間乾燥、予備接着を
行いウェブを得た。該ウェブに前記高圧液体流処理を行
った後、さらに80℃のドライヤーで乾燥させ繊維成形
体を得た。Example 8 Using a polypropylene resin (propylene homopolymer) as the high melting point resin (component A) and a high density polyethylene resin as the low melting point resin (component B), using a die for splittable conjugate fiber, component A And the volume ratio of both resins of the component B is 50/5
The value was set to 0, and a splittable conjugate fiber having a fiber cross-sectional shape shown in FIG. 1 having a single yarn denier of 20.0 dtex was spun. In the take-off step, the alkyl phosphate potassium salt was deposited. The obtained undrawn yarn was drawn at 90 ° C. and 4.1 times to attach a papermaking finish, and then cut into 10 mm to obtain a short fiber having a water content of 20% by weight. A sheath-core composite fiber (EAC fiber, Chisso Corporation) of polypropylene (core) / low-density polyethylene (sheath) is added to the short fiber in an amount of 20% by weight.
It was added to form a web by a papermaking method using a square sheet machine (25 cm × 25 cm). Using a Yankee dryer manufactured by Kumagai Riki Kogyo Co., Ltd., it was dried at 105 ° C. for 3 minutes and preliminarily bonded to obtain a web. After performing the high-pressure liquid flow treatment on the web, the web was further dried with a dryer at 80 ° C. to obtain a fiber molded body.
【0080】実施例9 図2に示した繊維横断面を得るための分割型複合繊維用
口金をを用いた以外は、実施例8に準拠して、分割型複
合繊維の紡糸、繊維成形体の作製を行った。Example 9 Spinning of a splittable conjugate fiber and production of a fiber molded product were performed in the same manner as in Example 8 except that a splittable conjugate fiber base for obtaining a fiber cross section shown in FIG. 2 was used. Fabrication was performed.
【0081】実施例1〜9の紡糸・延伸条件、繊維物
性、形状、不織布物性、分割率等を後述の表1に示し
た。The spinning / drawing conditions, fiber properties, shape, nonwoven fabric properties, division ratio, etc. of Examples 1 to 9 are shown in Table 1 below.
【0082】実施例10 相対粘度(フェノールと四塩化エタンとの等量混合物を
溶媒とし、20℃で測定した)0.60のPET(鐘紡
(株)製、K101)を高融点樹脂(A成分)とし、低
融点樹脂(B成分)としてポリプロピレン樹脂(MF
R:16g/10分のプロピレン単独重合体)を用い、
分割型複合繊維用口金を用いて、A成分及びB成分の両
樹脂の容積比率を50/50とし、単糸デニール15.
0dtexの図1に示した繊維断面形状を有する分割型
複合繊維を紡糸した。引き取り工程において、アルキル
フォスフェートカリウム塩を付着させた。得られた未延
伸糸を90℃、3.3倍で延伸し、抄紙用仕上げ剤を付
着させた後10mmに切断し、水分率20重量%の短繊
維を得た。この短繊維にポリプロピレン(芯)/低密度
ポリエチレン(鞘)の鞘芯複合繊維(EAC繊維、チッ
ソ(株))を20重量%添加し、角型シートマシン(2
5cm×25cm)を用い、抄紙法でウェブとした。熊
谷理器工業社製ヤンキードライヤーを用い、105℃で
3分間乾燥、予備接着を行いウェブを得た。前記高圧液
体流処理を行った後、さらに80℃のドライヤーで乾燥
させ繊維成形体を得た。Example 10 PET (K101, manufactured by Kanebo KK) having a relative viscosity of 0.60 (measured at 20 ° C. using a mixture of phenol and ethane tetrachloride as a solvent) was mixed with a high melting point resin (component A). ) And polypropylene resin (MF) as the low melting point resin (component B).
R: 16 g / 10 min propylene homopolymer)
14. Using a splittable composite fiber base, the volume ratio of both the A component and the B component resins is set to 50/50, and single yarn denier is used.
A split type composite fiber having a fiber cross-sectional shape of 0 dtex and shown in FIG. 1 was spun. In the take-off step, the alkyl phosphate potassium salt was deposited. The obtained undrawn yarn was drawn at 90 ° C. and 3.3 times, and after attaching a papermaking finishing agent, cut into 10 mm to obtain short fibers having a water content of 20% by weight. 20% by weight of a sheath-core composite fiber of polypropylene (core) / low-density polyethylene (sheath) (EAC fiber, Chisso Corporation) was added to this short fiber, and a square sheet machine (2
(5 cm × 25 cm) and a web was formed by a papermaking method. Using a Yankee dryer manufactured by Kumagai Riki Kogyo Co., Ltd., it was dried at 105 ° C. for 3 minutes and preliminarily bonded to obtain a web. After performing the high-pressure liquid flow treatment, the mixture was further dried with a dryer at 80 ° C. to obtain a fiber molded body.
【0083】実施例11 図4に示した繊維断面を得るための分割型複合繊維用口
金を用いた以外は、実施例1に準拠して分割型複合繊維
の紡糸、繊維成形体の作製を行った。Example 11 Spinning of a splittable conjugate fiber and production of a fiber molded body were performed in the same manner as in Example 1 except that a splittable conjugate fiber base for obtaining a fiber cross section shown in FIG. 4 was used. Was.
【0084】実施例12 高融点樹脂(A成分)としてポリプロピレン樹脂(プロ
ピレン単独重合体)、低融点樹脂(B成分)として高密
度ポリエチレン樹脂を用い、分割型複合繊維用口金を用
いて、A成分及びB成分の両樹脂の容積比率を50/5
0とし、単糸デニール7.5dtexの図1に示した繊
維断面形状を有する分割型複合繊維を紡糸した。引き取
り工程において、アルキルフォスフェートカリウム塩を
付着させた。得られた未延伸糸を90℃、4.1倍で延
伸し、抄紙用仕上げ剤を付着させた後10mmに切断
し、水分率20重量%の短繊維を得た。この短繊維にポ
リプロピレン(芯)/低密度ポリエチレン(鞘)の鞘芯
複合繊維(EAC繊維、チッソ(株))を20重量%添
加し、角型シートマシン(25cm×25cm)を用
い、抄紙法でウェブとした。該Webを熊谷理器工業社
製ヤンキードライヤーを用い、105℃で3分間乾燥、
予備接着を行いウェブを得た。該ウェブに前記高圧液体
流処理を行った後、さらに80℃のドライヤーで乾燥さ
せて繊維成形体を得た。Example 12 Using a polypropylene resin (propylene homopolymer) as the high melting point resin (component A) and a high density polyethylene resin as the low melting point resin (component B), using a die for splittable conjugate fiber, component A And the volume ratio of both resins of the component B is 50/5
The value was set to 0, and a splittable conjugate fiber having a single yarn denier of 7.5 dtex and having a fiber cross-sectional shape shown in FIG. 1 was spun. In the take-off step, the alkyl phosphate potassium salt was deposited. The obtained undrawn yarn was drawn at 90 ° C. and 4.1 times, and after attaching a papermaking finish, it was cut into 10 mm to obtain short fibers having a water content of 20% by weight. 20% by weight of a sheath-core composite fiber (EAC fiber, Chisso Corporation) of polypropylene (core) / low-density polyethylene (sheath) was added to the short fiber, and a papermaking method was performed using a square sheet machine (25 cm × 25 cm). And made it web. The Web was dried at 105 ° C. for 3 minutes using a Yankee dryer manufactured by Kumagai Riki Kogyo Co., Ltd.
Preliminary bonding was performed to obtain a web. After performing the high-pressure liquid flow treatment on the web, the web was further dried with a dryer at 80 ° C. to obtain a fiber molded body.
【0085】実施例13 高融点樹脂(A成分)にポリプロピレン樹脂(プロピレ
ン単独重合体)、低融点樹脂(B成分)として高密度ポ
リエチレン樹脂を用い、分割型複合繊維用口金を用い
て、A成分及びB成分の両樹脂の容積比率を50/50
とし、図1に示した繊維断面形状を有する分割型複合繊
維をスパンボンド法にて紡糸した。紡糸口金より吐出し
た複合繊維群をエアーサッカーに導入して牽引延伸し、
単糸デニール2.0dtexの複合長繊維を得、続い
て、エアーサッカーより排出された前記長繊維群を、帯
電装置により同電荷を付与せしめ帯電させた後、反射板
に衝突させて開繊し、開繊した長繊維群を裏面に吸引装
置を設けた無端ネット状コンベヤー上に、長繊維ウェブ
として捕集する。該長繊維ウェブを加圧ロールで分割処
理した後、120℃に加熱した面積率15%のエンボス
ロール機にて処理し、繊維成形体を得た。Example 13 Using a polypropylene resin (propylene homopolymer) as the high melting point resin (component A), a high density polyethylene resin as the low melting point resin (component B), and a split type composite fiber base, And the volume ratio of both resins of component B is 50/50.
A splittable conjugate fiber having a fiber cross-sectional shape shown in FIG. 1 was spun by a spun bond method. The composite fiber group discharged from the spinneret is introduced into air soccer and drawn and stretched.
After obtaining a composite filament having a single yarn denier of 2.0 dtex, the same group of filaments discharged from the air soccer was charged with the same electric charge by a charging device, and then collided with a reflecting plate to spread the fiber. Then, the opened filament group is collected as a filament web on an endless net-shaped conveyor provided with a suction device on the back surface. After splitting the long fiber web with a pressure roll, the web was processed with an embossing roll machine heated to 120 ° C. and having an area ratio of 15% to obtain a fiber molded body.
【0086】実施例10〜13の紡糸・延伸条件、繊維
物性、形状、不織布物性、分割率等を後述の表2示し
た。The spinning / drawing conditions, fiber properties, shape, nonwoven fabric properties, division ratio, etc. of Examples 10 to 13 are shown in Table 2 below.
【0087】比較例1、2 高融点樹脂(A成分)としてポリプロピレン樹脂(プロ
ピレン単独重合体)、低融点樹脂(B成分)として高密
度ポリエチレン樹脂を用い、分割型複合繊維用口金を用
いて、A成分及びB成分の両樹脂の容積比率を50/5
0とし、単糸デニール7.5dtexの図1に示した繊
維断面形状を有する分割型複合繊維を紡糸した。引き取
り工程において、アルキルフォスフェートカリウム塩を
付着させた。得られた未延伸糸を90℃、4.1倍で延
伸し、抄紙用仕上げ剤を付着させた後10mmに切断
し、水分率20重量%の短繊維を得た。この短繊維にポ
リプロピレン(芯)/低密度ポリエチレン(鞘)の鞘芯
複合繊維(EAC繊維、チッソ(株))を20重量%添
加し、角型シートマシン(25cm×25cm)を用
い、抄紙法でウェブとした。これを、熊谷理器工業社製
ヤンキードライヤーを用い、105℃で3分間乾燥、予
備接着を行いウェブを得た。該ウェブに前記高圧液体流
処理を行った後、さらに80℃のドライヤーで乾燥させ
繊維成形体を得た。紡糸・延伸条件、繊維物性、形状、
不織布物性、分割率等を後述の表2に示した。Comparative Examples 1 and 2 A polypropylene resin (propylene homopolymer) was used as the high melting point resin (component A), a high density polyethylene resin was used as the low melting point resin (component B), and a split type composite fiber die was used. The volume ratio of both resins of component A and component B is 50/5
The value was set to 0, and a splittable conjugate fiber having a single yarn denier of 7.5 dtex and having a fiber cross-sectional shape shown in FIG. 1 was spun. In the take-off step, the alkyl phosphate potassium salt was deposited. The obtained undrawn yarn was drawn at 90 ° C. and 4.1 times, and after attaching a papermaking finish, it was cut into 10 mm to obtain short fibers having a water content of 20% by weight. 20% by weight of a sheath-core composite fiber (EAC fiber, Chisso Corporation) of polypropylene (core) / low-density polyethylene (sheath) was added to the short fiber, and a papermaking method was performed using a square sheet machine (25 cm × 25 cm). And made it web. This was dried at 105 ° C. for 3 minutes using a Yankee dryer manufactured by Kumagai Riki Kogyo Co., Ltd., and preliminarily bonded to obtain a web. After performing the high-pressure liquid flow treatment on the web, the web was further dried with a dryer at 80 ° C. to obtain a fiber molded body. Spinning / drawing conditions, fiber properties, shape,
The physical properties of the nonwoven fabric, the division ratio, and the like are shown in Table 2 below.
【0088】比較例3 図9に示した繊維断面を得るための分割型複合繊維用口
金を用いた以外は、実施例1に準拠して、分割型複合繊
維の紡糸、繊維成形体の作製を行った。紡糸・延伸条
件、繊維物性、形状、不織布物性、分割率等を後述の表
2に示した。Comparative Example 3 Spinning of a splittable conjugate fiber and production of a fiber molded body were carried out in the same manner as in Example 1 except that a die for a splittable conjugate fiber for obtaining a fiber cross section shown in FIG. 9 was used. went. The spinning / drawing conditions, fiber properties, shape, nonwoven fabric properties, division ratio and the like are shown in Table 2 below.
【0089】比較例4 図10に示した繊維断面を得るための分割型複合繊維用
口金を用いた以外は、実施例1に準拠して、分割型複合
繊維の紡糸、繊維成形体の作製を行った。紡糸・延伸条
件、繊維物性、形状、不織布物性、分割率等を後述の表
2に示した。Comparative Example 4 Spinning of a splittable conjugate fiber and production of a fiber molded body were carried out in the same manner as in Example 1, except that a die for a splittable conjugate fiber for obtaining a fiber cross section shown in FIG. 10 was used. went. The spinning / drawing conditions, fiber properties, shape, nonwoven fabric properties, division ratio and the like are shown in Table 2 below.
【0090】比較例5 図10に示した繊維断面を得るための分割型複合繊維用
口金を用いた以外は、実施例13に準拠して、分割型複
合繊維の紡糸、繊維成形体の作製を行った。紡糸・延伸
条件、繊維物性、形状、不織布物性、分割率等を後述の
表2に示した。Comparative Example 5 Spinning of a splittable conjugate fiber and production of a fiber molded body were carried out in the same manner as in Example 13 except that a die for a splittable conjugate fiber for obtaining a fiber cross section shown in FIG. 10 was used. went. The spinning / drawing conditions, fiber properties, shape, nonwoven fabric properties, division ratio and the like are shown in Table 2 below.
【0091】実施例14、15 実施例1に準拠して繊維成形体を得る前工程(高圧液体
流処理前)の目付10g/m2のウェブ(Aと略す)を得
た。次に高密度ポリエチレン(鞘)/ポリプロピレン
(芯)の鞘芯型複合繊維(ESC繊維、チッソ(株))
2.2dtex×51mmの短繊維を用い、目付10g/
m2のカードウェブ(Bと略す)を得た。Aを上層、B
を下層に積層したもの(実施例14)及びAを上下層、
Bを中層に積層したもの(実施例15)を各々、前記高
圧液体流処理を行った後、80℃のドライヤーで乾燥さ
せて積層繊維成形体を得た。さらに、この積層繊維成形
体を拭き取り用ワイパーに使用したところ、実施例14
および15ともに非常に優れた拭き取り性を示した。Examples 14 and 15 According to Example 1, a web (abbreviated as A) having a basis weight of 10 g / m 2 in a pre-process (before high-pressure liquid flow treatment) for obtaining a fiber molded body was obtained. Next, sheath-core type composite fiber of high-density polyethylene (sheath) / polypropylene (core) (ESC fiber, Chisso Corporation)
Using short fibers of 2.2 dtex x 51 mm, the basis weight is 10 g /
An m 2 card web (abbreviated as B) was obtained. A is the upper layer, B
Are laminated on the lower layer (Example 14) and A is the upper and lower layers,
After laminating B in the middle layer (Example 15), each was subjected to the high-pressure liquid flow treatment, and dried with a dryer at 80 ° C. to obtain a laminated fiber molded body. Further, when this laminated fiber molded product was used for a wiper for wiping, Example 14 was repeated.
And No. 15 exhibited very excellent wiping properties.
【0092】実施例16 高融点樹脂(A成分)としてポリプロピレン樹脂(プロ
ピレン単独重合体)、低融点樹脂(B成分)として高密
度ポリエチレン樹脂を用い、分割型複合繊維用口金を用
いて、A成分及びB成分の両樹脂の容積比率を50/5
0とし、単糸デニール2.0dtexの図1に示した繊
維断面形状を有する分割型複合繊維をスパンボンド法で
紡糸して、中層用の目付10g/m2のウェブを得た。次
に、該樹脂の組み合わせにおいて、鞘芯型複合繊維用口
金を用いて、A成分を芯側、B成分を鞘側として、A及
びBの両樹脂の容積比率を50/50とし、単糸デニー
ル2.0dtexの複合繊維をスパンボンド法で紡糸し
て、目付5.0g/m2のウェブを上下層として上記中層
用のウェブに積層し、加圧ロールで分割処理した後、1
20℃に加熱した面積率15%のエンボス機にて処理
し、積層繊維成形体を得た。さらに、該繊維成形体を大
人用オムツの表面材として使用したところ、耐水圧、不
織布強力等に優れ、吸収性物品として非常に良好なもの
であった。Example 16 Using a polypropylene resin (propylene homopolymer) as the high-melting resin (component A), a high-density polyethylene resin as the low-melting resin (component B), And the volume ratio of both resins of the component B is 50/5
The split conjugate fiber having a fiber cross-sectional shape shown in FIG. 1 and having a single denier of 2.0 dtex was spun by a spun bond method to obtain a web having a basis weight of 10 g / m 2 for the middle layer. Next, in the combination of the resins, the volume ratio of both the A and B resins is set to 50/50 by using the core for the sheath-core type composite fiber, the component A as the core side, and the component B as the sheath side. A composite fiber having a denier of 2.0 dtex is spun by a spun bond method, and a web having a basis weight of 5.0 g / m 2 is laminated as an upper and lower layer on the above-mentioned intermediate layer web.
This was treated with an embossing machine heated to 20 ° C. and having an area ratio of 15% to obtain a laminated fiber molded body. Further, when the fiber molded article was used as a surface material of an adult diaper, it was excellent in water pressure resistance, nonwoven fabric strength, etc., and was very good as an absorbent article.
【0093】[0093]
【表1】 [Table 1]
【0094】[0094]
【表2】 [Table 2]
【0095】表1、表2から明らかなように、本発明の
実施例各例で得られた繊維成形体および積層繊維成形体
は、比較各例に比べて同条件でも高分割率で分割してい
る。即ち、従来のような高水圧の高圧液体流処理を行わ
なくても、分割、細繊化が容易に進行するため、比較的
低目付の不織布でも地合が乱れることなく製造すること
ができ、さらに高圧液体流処理のコストも大幅に削減す
ることができる。As is clear from Tables 1 and 2, the fiber molded product and the laminated fiber molded product obtained in each example of the present invention were divided at a higher division ratio under the same conditions as in the comparative examples. ing. That is, even without performing the high-pressure liquid flow treatment of the conventional high water pressure, because the division, fineness easily proceeds, even a relatively low-weight nonwoven fabric can be produced without disturbing formation, Furthermore, the cost of high pressure liquid flow processing can be significantly reduced.
【0096】[0096]
【発明の効果】本発明の分割型複合繊維は、非常に分割
し易いため、特別に易分割させるための添加剤を一切添
加せずに、物理衝撃を大きくしなくても極細繊維化が容
易に行える。このため、本発明の分割複合繊維を用いる
と緻密で地合いの良い繊維成形体および積層繊維成形体
が得られる。The splittable conjugate fiber of the present invention is very easy to split, so that it is easy to make ultrafine fibers without increasing the physical impact without adding any additives for easy splitting. Can be done. Therefore, when the split conjugate fiber of the present invention is used, a dense and well-formed fiber molded product and a laminated fiber molded product can be obtained.
【図1】本発明に用いられる分割型複合繊維の繊維断面
の1模式図FIG. 1 is a schematic view of a fiber cross section of a splittable conjugate fiber used in the present invention.
【図2】本発明に用いられる分割型複合繊維の繊維断面
の1模式図FIG. 2 is a schematic view of a fiber cross section of a splittable conjugate fiber used in the present invention.
【図3】本発明に用いられる分割型複合繊維の繊維横断
面の1模式図FIG. 3 is a schematic diagram of a cross section of a fiber of a splittable conjugate fiber used in the present invention.
【図4】本発明に用いられる分割型複合繊維の繊維横断
面の1模式図FIG. 4 is a schematic view of a fiber cross section of a splittable conjugate fiber used in the present invention.
【図5】本発明に用いられる分割型複合繊維の繊維横断
面の1模式図FIG. 5 is a schematic view of a cross section of a fiber of a splittable conjugate fiber used in the present invention.
【図6】屈曲もしくは湾曲により囲まれた面積(S1)
と分割型複合繊維の断面積(S2)を示した模式図FIG. 6 is an area surrounded by a bend or a curve (S1).
And schematic diagram showing the cross-sectional area (S2) of the splittable conjugate fiber
【図7】本発明に用いられる分割型複合繊維の繊維横断
面の1模式図FIG. 7 is a schematic diagram of a cross section of a fiber of a splittable conjugate fiber used in the present invention.
【図8】本発明に用いられる分割型複合繊維の繊維横断
面の1模式図FIG. 8 is a schematic view of a fiber cross section of a splittable conjugate fiber used in the present invention.
【図9】比較例に用いられる分割型複合繊維の繊維横断
面の1模式図FIG. 9 is a schematic view of a fiber cross section of a splittable conjugate fiber used in a comparative example.
【図10】比較例に用いられる分割型複合繊維の繊維横
断面の1模式図FIG. 10 is a schematic diagram of a fiber cross section of a splittable conjugate fiber used in a comparative example.
L:複合繊維の各成分が交互に隣接される方向で、か
つ、断面形状の最も長い部分の長さを表す。 W:複合繊維の各成分の接触面方向で断面形状の厚みを
表す。 a:複合繊維を構成する1成分の繊維外周面の長さを表
す。 b:複合繊維を構成する1成分の隣接成分との接触長さ
を表す。 S1:長軸の両端を結んだ直線と屈曲あるいは湾曲によ
り囲まれた部分の面積を表す。 S2:複合繊維の繊維横断面積を表す。L: The length of the longest part of the cross-sectional shape in the direction in which the components of the composite fiber are alternately adjacent to each other. W: The thickness of the cross-sectional shape in the contact surface direction of each component of the conjugate fiber. a: The length of the outer peripheral surface of one component fiber constituting the composite fiber. b: Represents the contact length of one component constituting the conjugate fiber with an adjacent component. S1: represents the area of a portion surrounded by a straight line connecting both ends of the long axis and bending or bending. S2: represents the fiber cross-sectional area of the composite fiber.
フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) D04H 1/56 D04H 1/56 Fターム(参考) 4L041 AA07 AA19 AA20 BA04 BA05 BA11 BA33 BA48 BA49 BA59 BD06 BD07 BD11 BD20 CA06 CA37 CA38 DD01 DD06 DD14 EE06 EE20 4L045 AA05 BA03 BA06 BA21 BA34 BA39 BA54 BA60 DA42 4L047 AA14 AA27 AB02 AB08 AB09 BA04 BA09 BA21 BA22 BB09 CC01 CC03 CC04 CC05 CC12 CC16 Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat II (reference) D04H 1/56 D04H 1/56 F term (reference) 4L041 AA07 AA19 AA20 BA04 BA05 BA11 BA33 BA48 BA49 BA59 BD06 BD07 BD11 BD20 CA06 CA37 CA38 DD01 DD06 DD14 EE06 EE20 4L045 AA05 BA03 BA06 BA21 BA34 BA39 BA54 BA60 DA42 4L047 AA14 AA27 AB02 AB08 AB09 BA04 BA09 BA21 BA22 BB09 CC01 CC03 CC04 CC05 CC12 CC16
Claims (15)
され、繊維断面において、各成分は長軸方向に交互に隣
接され、かつ該断面は屈曲、湾曲もしくは扁平形状の複
合繊維であって、該断面の長軸Lと短軸Wの比(L/
W)が3〜20であることを特徴とする分割型複合繊
維。1. A composite fiber comprising at least two components of a thermoplastic resin, wherein, in a fiber cross section, each component is alternately adjacent to each other in a longitudinal direction, and the cross section is a bent, curved or flat composite fiber. The ratio (L /
W) is 3 to 20;
を構成する1成分の繊維外周面長aと隣接成分との接触
長bの比(a/b)が0.1〜2.5である請求項1記
載の分割型複合繊維。2. In the fiber cross section of the splittable conjugate fiber, the ratio (a / b) of the fiber outer peripheral surface length a of one component constituting the fiber to the contact length b of the adjacent component is 0.1 to 2.5. The splittable conjugate fiber according to claim 1.
もしくは湾曲により囲まれた面積S1と該分割型複合繊
維の断面積S2の比(S1/S2)が0.2〜1.0で
ある請求項1もしくは請求項2のいずれか1項記載の分
割型複合繊維。3. A ratio (S1 / S2) of an area S1 surrounded by a bend or a curve to a cross-sectional area S2 of the splittable conjugate fiber in the cross section of the splittable conjugate fiber is 0.2 to 1.0. The splittable conjugate fiber according to claim 1.
2成分の熱可塑性樹脂のメルトフローレートがいずれも
10〜100g/10分であり、かつ該熱可塑性樹脂の
うち、融点の最も高い樹脂成分(以下、A成分という)
のメルトフローレート(MFR−A)と融点が最も低い
樹脂成分(以下、B成分という)のメルトフローレート
(MFR−B)の比(MFR−A/MFR−B)が0.
1〜5である請求項1〜3のいずれか1項記載の分割型
複合繊維。4. A resin having a highest melting point among the thermoplastic resins having a melt flow rate of at least 10 to 100 g / 10 minutes for each of the thermoplastic resins of at least two components constituting the fibers after fiber molding. Component (hereinafter referred to as A component)
The ratio (MFR-A / MFR-B) of the melt flow rate (MFR-A) of the resin component having the lowest melting point (MFR-B) to the resin component having the lowest melting point (hereinafter referred to as B component) is 0.
The splittable conjugate fiber according to any one of claims 1 to 3, which is 1 to 5.
が、ポリプロピレン系樹脂とポリエチレン系樹脂である
請求項1〜4のいずれか1項記載の分割型複合繊維。5. The splittable conjugate fiber according to claim 1, wherein the combination of at least two thermoplastic resins is a polypropylene resin and a polyethylene resin.
5〜10デシテックス、分割後の単糸繊度が0.5デシ
テックス以下である請求項1〜5のいずれか1項記載の
分割型複合繊維。6. The split conjugate fiber has a single fiber fineness before splitting of 0.1.
The splittable conjugate fiber according to any one of claims 1 to 5, wherein the single yarn fineness after splitting is 5 decitex or less and 0.5 dentex or less.
合繊維を少なくとも30重量%以上含み、かつ該分割型
複合繊維の50%以上が分割している繊維成形体。7. A fibrous article comprising at least 30% by weight or more of the splittable conjugate fiber according to claim 1, and 50% or more of the splittable conjugate fiber is split.
載の繊維成形体。8. The fiber molding according to claim 7, wherein the fiber molding is a fiber aggregate.
る繊維集合体である請求項7もしくは請求項8のいずれ
か1項記載の繊維成形体。9. The fiber molded article according to claim 7, wherein the fiber molded article is a fiber aggregate obtained by a spun bond method.
成形体の片面または両面にシートを積層してなる積層繊
維成形体。10. A laminated fiber molded product obtained by laminating a sheet on one or both surfaces of the fiber molded product according to any one of claims 7 to 9.
成形体をシートの両面に積層してなる積層繊維成形体。11. A laminated fiber molded product obtained by laminating the fiber molded product according to any one of claims 7 to 9 on both sides of a sheet.
の少なくとも1種から選ばれたシ−トである請求項10
もしくは請求項11記載の積層繊維成形体。12. The sheet according to claim 10, wherein the sheet is a sheet selected from at least one of a nonwoven fabric, a film, a knitted fabric, and a woven fabric.
Alternatively, the laminated fiber molded product according to claim 11.
成形体もしくは請求項10〜12のいずれか1項記載の
積層繊維成形体を用いた吸収性物品。13. An absorbent article using the fiber molded article according to any one of claims 7 to 9 or the laminated fiber molded article according to any one of claims 10 to 12.
成形体もしくは請求項10〜12のいずれか1項記載の
積層繊維成形体を用いたワイパー。14. A wiper using the fiber molded article according to any one of claims 7 to 9 or the laminated fiber molded article according to any one of claims 10 to 12.
成形体もしくは請求項10〜12のいずれか1項記載の
積層繊維成形体を用いたバッテリーセパレーター。15. A battery separator using the fiber molded article according to any one of claims 7 to 9 or the laminated fiber molded article according to any one of claims 10 to 12.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16485199A JP4026279B2 (en) | 1999-03-17 | 1999-06-11 | Split type composite fiber and fiber molded body using the same |
DE10080786.0T DE10080786B3 (en) | 1999-03-08 | 2000-02-29 | Cleavable multicomponent fiber and fibrous article comprising it |
PCT/JP2000/001180 WO2000053831A1 (en) | 1999-03-08 | 2000-02-29 | Split type conjugate fiber, method for producing the same and fiber formed article using the same |
US09/674,384 US6410139B1 (en) | 1999-03-08 | 2000-02-29 | Split type conjugate fiber, method for producing the same and fiber formed article using the same |
US10/153,133 US6617023B2 (en) | 1999-03-08 | 2002-05-21 | Splittable multi-component fiber, method for producing it, and fibrous article comprising it |
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JP7258399 | 1999-03-17 | ||
JP11-72583 | 1999-03-17 | ||
JP16485199A JP4026279B2 (en) | 1999-03-17 | 1999-06-11 | Split type composite fiber and fiber molded body using the same |
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JP2000328348A true JP2000328348A (en) | 2000-11-28 |
JP4026279B2 JP4026279B2 (en) | 2007-12-26 |
Family
ID=26413713
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JP16485199A Expired - Fee Related JP4026279B2 (en) | 1999-03-08 | 1999-06-11 | Split type composite fiber and fiber molded body using the same |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003020524A (en) * | 2001-07-10 | 2003-01-24 | Kuraray Co Ltd | Joining-type conjugated staple fiber |
WO2008038536A1 (en) * | 2006-09-25 | 2008-04-03 | Mitsui Chemicals, Inc. | Split type composite long fiber, nonwoven fabric made of split type composite long fiber, and split-fiber nonwoven fabric |
WO2014139731A1 (en) * | 2013-03-11 | 2014-09-18 | Basell Polyolefine Gmbh | Multilayer fibers |
-
1999
- 1999-06-11 JP JP16485199A patent/JP4026279B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003020524A (en) * | 2001-07-10 | 2003-01-24 | Kuraray Co Ltd | Joining-type conjugated staple fiber |
WO2008038536A1 (en) * | 2006-09-25 | 2008-04-03 | Mitsui Chemicals, Inc. | Split type composite long fiber, nonwoven fabric made of split type composite long fiber, and split-fiber nonwoven fabric |
JPWO2008038536A1 (en) * | 2006-09-25 | 2010-01-28 | 三井化学株式会社 | Split composite long fiber, non-woven fabric composed of split composite long fiber, and split fiber non-woven fabric |
JP5334583B2 (en) * | 2006-09-25 | 2013-11-06 | 三井化学株式会社 | Split composite long fiber, non-woven fabric composed of split composite long fiber, and split fiber non-woven fabric |
WO2014139731A1 (en) * | 2013-03-11 | 2014-09-18 | Basell Polyolefine Gmbh | Multilayer fibers |
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