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JP4359094B2 - Fine fiber manufacturing method and nonwoven fabric - Google Patents

Fine fiber manufacturing method and nonwoven fabric Download PDF

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JP4359094B2
JP4359094B2 JP2003272090A JP2003272090A JP4359094B2 JP 4359094 B2 JP4359094 B2 JP 4359094B2 JP 2003272090 A JP2003272090 A JP 2003272090A JP 2003272090 A JP2003272090 A JP 2003272090A JP 4359094 B2 JP4359094 B2 JP 4359094B2
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fiber
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resin component
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fine fibers
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典子 宮口
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Japan Vilene Co Ltd
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Description

本発明は細繊維の製造方法及び不織布に関する。   The present invention relates to a method for producing fine fibers and a nonwoven fabric.

繊維径が5μm以下の繊維(以下、細繊維という)からなる不織布は、濾過性能、柔軟性、隠蔽性、払拭性などの諸特性に優れているため、好適に使用することができる。このような細繊維からなる不織布を製造する1つの方法として、ある溶液によって除去可能な樹脂成分(海成分)中に、この溶液によって除去が困難な樹脂成分(島成分)が分散した繊維(いわゆる海島型繊維)を使用して、カード法やエアレイ法などにより繊維ウエブを形成し、次いでニードルや水流の作用によって繊維同士を絡合させて絡合繊維ウエブを形成した後、海島型繊維の海成分を前記溶液で溶解除去する方法がある。   Nonwoven fabrics composed of fibers having a fiber diameter of 5 μm or less (hereinafter referred to as fine fibers) are excellent in various properties such as filtration performance, flexibility, concealability, and wiping properties, and therefore can be suitably used. As one method for producing a nonwoven fabric composed of such fine fibers, fibers (so-called island components) in which a resin component (island component) that is difficult to remove by this solution is dispersed in a resin component (sea component) that can be removed by a solution. Sea-island fiber), the fiber web is formed by the card method or air lay method, etc., and then the fibers are entangled by the action of a needle or water flow to form the entangled fiber web. There is a method of dissolving and removing the components with the solution.

この方法によれば、細繊維からなる不織布を製造することができるが、細繊維が束となった状態にあるため、この細繊維束を解すため、又は形態安定性を付与するために、水流などの流体流を作用させる必要があった。しかしながら、この流体流を作用させた不織布は、地合いの点で不十分なものであった。   According to this method, a non-woven fabric made of fine fibers can be produced. However, since the fine fibers are in a bundled state, a water stream is used to unwind the fine fiber bundles or to give form stability. It was necessary to apply a fluid flow such as. However, the nonwoven fabric to which this fluid flow is applied is insufficient in terms of texture.

そこで、海島型長繊維の海成分を除去して細長繊維束とした後に、所望長さに切断して細短繊維とし、この細短繊維を用いて湿式法により繊維ウエブを形成すれば、地合の優れる不織布を製造できると考えられた。しかしながら、細長繊維束を切断する際に細短繊維同士が融着してしまい、地合いの優れる不織布を製造することが困難であった。   Therefore, after removing the sea component of the sea-island type long fiber to form a long and narrow fiber bundle, it is cut into a desired length and formed into a short and short fiber, and a fiber web is formed by a wet method using this thin and short fiber. It was thought that a superior nonwoven fabric could be produced. However, when the elongated fiber bundle is cut, the short fibers are fused with each other, and it is difficult to produce a nonwoven fabric with excellent texture.

また、細長繊維束を形成する前、つまり海島型長繊維束を切断して海島型短繊維とした後に、海島型短繊維の海成分を除去して細短繊維を形成する方法も考えられたが、この場合であっても、海島型長繊維束を切断して海島型短繊維を形成する際に、島成分同士が融着してしまい、地合いの優れる不織布を製造することが困難であるという問題点があった。   In addition, a method of forming a narrow fiber by removing the sea component of the sea-island short fiber before forming the slender fiber bundle, that is, after cutting the sea-island long fiber bundle into a sea-island short fiber was also considered. However, even in this case, when the sea-island type long fiber bundle is cut to form the sea-island type short fibers, the island components are fused with each other, and it is difficult to produce a nonwoven fabric with excellent texture. There was a problem.

そこで、本願出願人は、海島型長繊維の海成分を除去して細長繊維束とし、この細長繊維束に油剤を付与した後に切断して、細短繊維を形成する方法、を提案した(特許文献1)。この方法によれば、確かに切断する際の細短繊維同士の融着を抑えることはできたが、細短繊維同士の圧着が生じる場合があった。   Accordingly, the applicant of the present application has proposed a method of forming a narrow fiber by removing the sea component of the sea-island long fiber to obtain a slender fiber bundle, applying an oil agent to the slender fiber bundle, and then cutting it (patent). Reference 1). According to this method, although it was possible to suppress the fusion of the short fibers at the time of cutting, there was a case where the thin fibers were pressed.

特開2003−119668号公報(特許請求の範囲など)JP 2003-119668 A (claims, etc.)

本発明は上記の問題点を解決するためになされたものであり、細繊維同士の圧着を従来よりも抑えることができ、結果として地合いの優れる不織布を製造することのできる細繊維の製造方法、及びこの細繊維を用いた不織布を提供することを目的とする。   The present invention was made in order to solve the above-described problems, and the method for producing fine fibers, which can suppress the press-bonding between the fine fibers as compared with the prior art, and as a result, can produce a nonwoven fabric with excellent texture, And it aims at providing the nonwoven fabric using this fine fiber.

前述のように、海島型長繊維の海成分を除去して細長繊維束とし、この細長繊維束に油剤を付与した後に切断して、細短繊維を形成しても細短繊維同士の圧着が生じる場合がある原因を追求したところ、切断工程以前の海島型長繊維の海成分を除去して細長繊維束とした時点で既に細長繊維同士が圧着していることが判明した。これは、従来、海島型長繊維の海成分を除去する方法として、海島型長繊維を穴あきボビンに巻き付けた状態で、穴あきボビンの内側から外側へ海成分を除去できる溶液を通過させることによって海成分を溶解除去していたが、その溶液が通過する際の通液抵抗によって圧力がかかり、細長繊維同士が圧着していることを突き止めた。   As described above, sea components of the sea-island type long fibers are removed to form a slender fiber bundle, and an oil agent is applied to the slender fiber bundle and then cut to form a short fiber. In pursuit of the cause that may occur, it was found that the elongated fibers were already pressure-bonded at the time when the sea components of the sea-island long fibers before the cutting process were removed to form a bundle of elongated fibers. This is a conventional method for removing sea components of sea-island long fibers by passing a solution that can remove sea components from the inside of the perforated bobbin to the outside while the sea-island long fibers are wound around the perforated bobbin. The sea component was dissolved and removed by the pressure, but it was found that pressure was applied due to the resistance of liquid passage when the solution passed through, and the elongated fibers were pressure-bonded.

本発明は上記の知見に基いてなされたもので、本発明の請求項1に係る発明は、「アルカリ水溶液によって除去可能な第1樹脂成分と、前記アルカリ水溶液によって除去が困難な第2樹脂成分とを含む連続した複合繊維を穴あきボビンに巻きつけた状態で、穴あきボビンの内側から外側へアルカリ水溶液を通過させて、又は穴あきボビンの外側から内側へアルカリ水溶液を通過させることにより、第1樹脂成分を除去し、第2樹脂成分からなる細繊維を製造する方法であり、細繊維同士の圧着を防止するために、前記アルカリ水溶液中にノニオン系界面活性剤又は両性界面活性剤、及び減量促進剤が存在していることを特徴とする、細繊維の製造方法」である。請求項1の発明によれば、アルカリ水溶液中にノニオン系界面活性剤又は両性界面活性剤が存在していることで、第2樹脂成分(細繊維)の間の第1樹脂成分が除去される際に、ノニオン系界面活性剤又は両性界面活性剤が第2樹脂成分(細繊維)間に付着していくことによって、熱と通液の圧力による細繊維同士の圧着を防止することができる。連続した複合繊維を穴あきボビンに巻きつけた状態で第1樹脂成分を除去すると、連続した複合繊維は自由度が低く、アルカリ水溶液が第2樹脂成分(細繊維)間を通過しやすいため、細繊維間にノニオン系界面活性剤又は両性界面活性剤が付着しやすい。そのため、熱と通液の圧力による細繊維同士の圧着をより効果的に防止することができる。また、第1樹脂成分を除去した後にも細繊維は複合繊維が穴あきボビンに巻かれているのと同様の状態で穴あきボビンに巻かれた状態にあり、また、穴あきボビンに巻いたコンパクトな状態で第1樹脂成分を除去することができるため、大量に効率良く細繊維を製造することができる。
The present invention has been made based on the above findings, the invention according to claim 1 of the present invention, "alkaline water a first resin component which can be removed by a solution, a second removal is difficult by the alkaline water solution Passing the alkaline aqueous solution from the inside to the outside of the perforated bobbin or passing the alkaline aqueous solution from the outside to the inside of the perforated bobbin with a continuous composite fiber containing a resin component wound around the perforated bobbin Accordingly, the first resin component is removed, a process for producing the fine fibers made of the second resin component, in order to prevent the bonding of the fine fibers, nonionic surfactants or amphoteric surfactants in the alkaline water solution A method for producing fine fibers, characterized in that an activator and a weight loss accelerator are present. According to the invention of claim 1, that the nonionic surfactant or amphoteric surfactant is present in an alkaline aqueous solution, the first resin component between the second resin component (fine fibers) is removed When the nonionic surfactant or amphoteric surfactant adheres between the second resin components (fine fibers), it is possible to prevent pressure bonding between the fine fibers due to heat and liquid flow pressure. . When the first resin component is removed in a state where the continuous conjugate fiber is wound around the perforated bobbin, the continuous conjugate fiber has a low degree of freedom, and the alkaline aqueous solution easily passes between the second resin components (fine fibers). Nonionic surfactants or amphoteric surfactants tend to adhere between the fine fibers. For this reason, it is possible to more effectively prevent the press-bonding of the fine fibers due to the heat and the pressure of liquid flow. Further, after the first resin component is removed, the fine fiber is still wound around the perforated bobbin in the same state as the composite fiber is wound around the perforated bobbin, and is wound around the perforated bobbin. Since the first resin component can be removed in a compact state, fine fibers can be efficiently produced in large quantities.

本発明の請求項2に係る発明は、「ノニオン系界面活性剤又は両性界面活性剤及び減量促進剤は、アルカリ水溶液に予め添加されたことによって、アルカリ水溶液中に存在していることを特徴とする、請求項1記載の細繊維の製造方法」である。請求項2の発明によれば、熱と通液の圧力による細繊維同士の圧着を効果的に防止することができる。
The invention according to claim 2 of the present invention, "nonionic surfactant or amphoteric surfactant, and a reduction promoter, by which is previously added to the alkaline aqueous solution, it is present in an alkaline aqueous solution The method for producing a fine fiber according to claim 1. According to invention of Claim 2, the crimping | compression-bonding of the fine fibers by the pressure of a heat | fever and a liquid flow can be prevented effectively.

本発明の請求項3に係る発明は、「ノニオン系界面活性剤又は両性界面活性剤は、ノニオン系界面活性剤又は両性界面活性剤が付与された複合繊維を用いることによって、アルカリ水溶液中に存在していることを特徴とする、請求項1又は請求項2記載の細繊維の製造方法」である。請求項3の発明によれば、熱と通液の圧力による細繊維同士の圧着を効果的に防止することができる。
The invention according to claim 3 of the present invention, "nonionic surfactant or amphoteric surfactant, by using a composite fiber nonionic surfactant or amphoteric surfactant has been applied, the alkaline water solution 3. A method for producing fine fibers according to claim 1 or 2, characterized in that it exists. According to invention of Claim 3, the crimping | compression-bonding of the fine fibers by the pressure of a heat | fever and a liquid flow can be prevented effectively.

本発明の請求項4に係る発明は、「第2樹脂成分がポリオレフィン系樹脂からなることを特徴とする、請求項1〜請求項3のいずれかに記載の細繊維の製造方法」である。請求項4の発明のように、熱変形温度が比較的低いポリオレフィン系樹脂であっても、熱と通液の圧力による細繊維同士の圧着を効果的に防止することができる。   The invention according to claim 4 of the present invention is "the method for producing fine fibers according to any one of claims 1 to 3, wherein the second resin component is made of a polyolefin resin". Even in the case of a polyolefin resin having a relatively low heat distortion temperature as in the invention of claim 4, it is possible to effectively prevent the pressure bonding between the fine fibers due to heat and the pressure of liquid flow.

本発明の請求項5に係る発明は、「細繊維の繊維径が5μm以下であることを特徴とする、請求項1〜請求項4のいずれかに記載の細繊維の製造方法」である。請求項5の発明のように、変形しやすく圧着しやすい繊維径が5μm以下の細繊維であっても、熱と通液の圧力による細繊維同士の圧着を効果的に防止することができる。   The invention according to claim 5 of the present invention is “the method for producing fine fibers according to any one of claims 1 to 4, wherein the fiber diameter of the fine fibers is 5 μm or less”. As in the fifth aspect of the invention, even if the fiber diameter is 5 μm or less, which is easily deformable and pressure-bonded, it is possible to effectively prevent the pressure-bonding of the fine fibers due to heat and liquid pressure.

本発明の請求項に係る発明は、「請求項1〜請求項のいずれかに記載の製造方法により製造された細繊維を含んでいることを特徴とする不織布」である。前記製造方法により製造した細繊維は圧着が少ないため、地合いの良好な不織布である。
The invention according to claim 6 of the present invention is a “nonwoven fabric characterized by including fine fibers manufactured by the manufacturing method according to any one of claims 1 to 5 ”. The fine fibers produced by the above production method are non-woven fabrics with good texture because they have little pressure bonding.

本発明の細繊維の製造方法によれば、複合繊維の第1樹脂成分を除去する所定溶液中にノニオン系界面活性剤又は両性界面活性剤が存在していることで、第2樹脂成分(細繊維)間の第1樹脂成分が除去されながら、前記界面活性剤が細繊維間に付着していくため、熱と通液の圧力による細繊維同士の圧着を防止することができる。そのため、この細繊維を使用した本発明の不織布は地合の良好なものである。   According to the method for producing fine fibers of the present invention, the presence of the nonionic surfactant or amphoteric surfactant in the predetermined solution for removing the first resin component of the composite fiber allows the second resin component (fine fiber). Since the surfactant adheres between the fine fibers while the first resin component between the fibers) is removed, it is possible to prevent the fine fibers from being pressed against each other due to heat and the pressure of liquid flow. Therefore, the nonwoven fabric of this invention using this fine fiber has a good formation.

本発明の細繊維の製造方法について、複合繊維における第1樹脂成分の除去状態を模式的に表すたて断面図である図1をもとに説明する。図1における1は複合繊維であり、2は穴あきボビンであり、3は複合繊維の第1樹脂成分を除去可能な所定の溶液である。図1においては、複合繊維1が連続した繊維で、穴あきボビン2に巻きつけられた状態にあり、この穴あきボビン2の内側2aから外側2bへ所定溶液3が通液することによって、又はこの穴あきボビン2の外側2bから内側2aへ所定溶液3が通液することによって、複合繊維1の第1樹脂成分が除去され、第2樹脂成分からなる細繊維が形成される。この所定溶液3中には、ノニオン系界面活性剤又は両性界面活性剤が存在しているため、所定溶液3が穴あきボビン2を通液する際に、ノニオン系界面活性剤又は両性界面活性剤が第2樹脂成分(細繊維)間に付着する。そのため、熱と通液の圧力による細繊維同士の圧着が防止される。なお、このような所定溶液3の通液は、例えば前記穴あきボビン2をチーズ染色機に装着して行うことができる。   The method for producing fine fibers of the present invention will be described with reference to FIG. 1 which is a vertical sectional view schematically showing the removed state of the first resin component in the composite fiber. In FIG. 1, 1 is a composite fiber, 2 is a perforated bobbin, and 3 is a predetermined solution capable of removing the first resin component of the composite fiber. In FIG. 1, the composite fiber 1 is a continuous fiber and is wound around the perforated bobbin 2, and the predetermined solution 3 is passed from the inner side 2a to the outer side 2b of the perforated bobbin 2, or By passing the predetermined solution 3 from the outer side 2b of the perforated bobbin 2 to the inner side 2a, the first resin component of the composite fiber 1 is removed, and fine fibers composed of the second resin component are formed. Since the predetermined solution 3 contains a nonionic surfactant or an amphoteric surfactant, when the predetermined solution 3 passes through the perforated bobbin 2, the nonionic surfactant or the amphoteric surfactant is used. Adheres between the second resin components (fine fibers). Therefore, the crimping | compression-bonding of the fine fibers by the pressure of heat and liquid flow is prevented. In addition, the passage of such a predetermined solution 3 can be performed, for example, by attaching the perforated bobbin 2 to a cheese dyeing machine.

このように所定溶液3中にノニオン系界面活性剤又は両性界面活性剤が存在していることによって、前記効果を奏するものであるが、ノニオン系界面活性剤又は両性界面活性剤は所定の溶液3に予め添加されたことによって、所定の溶液3中に存在しているか、複合繊維1としてノニオン系界面活性剤又は両性界面活性剤が付与されたものを用いることによって、所定の溶液3中に存在しているか、或いはこれら両方の要因によって、所定の溶液3中に存在している。所定の溶液3に予めノニオン系界面活性剤又は両性界面活性剤を添加する方法によると、所定溶液3中におけるノニオン系界面活性剤又は両性界面活性剤の濃度を調整しやすく、また、複合繊維1を巻き取る時にノニオン系界面活性剤又は両性界面活性剤を付与する手間も生じないため、より好適である。   As described above, the presence of the nonionic surfactant or amphoteric surfactant in the predetermined solution 3 provides the above-mentioned effect. However, the nonionic surfactant or amphoteric surfactant is the predetermined solution 3. Preexisting in the predetermined solution 3 by using the one added with the nonionic surfactant or amphoteric surfactant as the composite fiber 1 Or present in a given solution 3 due to both of these factors. According to the method of adding a nonionic surfactant or an amphoteric surfactant to the predetermined solution 3 in advance, the concentration of the nonionic surfactant or amphoteric surfactant in the predetermined solution 3 can be easily adjusted, and the composite fiber 1 This is more preferable because it does not require the trouble of applying a nonionic surfactant or an amphoteric surfactant when winding up.

本発明で使用する界面活性剤はノニオン系又は両性である限り特に限定するものではないが、例えば、ノニオン系界面活性剤として、ポリエチレングリコール型界面活性剤、多価アルコール型界面活性剤を挙げることができ、両性界面活性剤として、ベタイン型界面活性剤を挙げることができる。これらの中でも、ポリオキシエチレンノニルフェニルエーテル又は高級アルコール系のものが特に効果があることがわかった。なお、ノニオン系界面活性剤又は両性界面活性剤の存在量は特に限定するものではないが、細繊維同士の圧着防止性に優れているように、所定溶液3の質量100に対して、0.05%以上であるのが好ましく、0.2%以上であるのがより好ましい。他方、所定溶液3中における存在量が多くなりすぎると、第1樹脂成分の除去速度が遅くなるため、所定溶液3の質量100に対して、2%以下であるのが好ましく、1%以下であるのがより好ましい。   The surfactant used in the present invention is not particularly limited as long as it is nonionic or amphoteric. For example, examples of the nonionic surfactant include a polyethylene glycol type surfactant and a polyhydric alcohol type surfactant. Examples of amphoteric surfactants include betaine surfactants. Among these, it has been found that polyoxyethylene nonylphenyl ether or higher alcohols are particularly effective. The amount of the nonionic surfactant or the amphoteric surfactant is not particularly limited. However, the amount of nonionic surfactant or amphoteric surfactant is 0. It is preferably at least 05%, more preferably at least 0.2%. On the other hand, if the abundance in the predetermined solution 3 is too large, the removal rate of the first resin component is slowed. Therefore, it is preferably 2% or less with respect to the mass 100 of the predetermined solution 3, and preferably 1% or less. More preferably.

本発明の所定溶液3は上述のようなノニオン系界面活性剤又は両性界面活性剤が存在するものであるが、これら界面活性剤以外に、例えば、第4級アンモニウム塩型カチオン界面活性剤などからなる減量促進剤を含んでいても良い。このような減量促進剤を含んでいても、ノニオン系界面活性剤又は両性界面活性剤の活性が損なわれないため、安定して細繊維同士の圧着を防止することができる。   The predetermined solution 3 of the present invention contains the nonionic surfactant or amphoteric surfactant as described above. In addition to these surfactants, for example, a quaternary ammonium salt type cationic surfactant is used. The weight loss promoter which becomes may be included. Even when such a weight loss accelerator is included, the activity of the nonionic surfactant or the amphoteric surfactant is not impaired, so that the pressure bonding between the fine fibers can be prevented stably.

この複合繊維1は所定の溶液3によって除去可能な第1樹脂成分と前記所定の溶液3によって除去が困難な第2樹脂成分とを含んでいる。そのため、第1樹脂成分を所定溶液3で除去することによって第2樹脂成分からなる細繊維を発生することができる。   The composite fiber 1 includes a first resin component that can be removed by the predetermined solution 3 and a second resin component that is difficult to remove by the predetermined solution 3. Therefore, by removing the first resin component with the predetermined solution 3, fine fibers composed of the second resin component can be generated.

この複合繊維1における「除去可能」とは、所定の溶液3によって樹脂成分の95mass%以上を除去できることをいい、「除去が困難」とは、第1樹脂成分を除去する条件下において樹脂成分の30mass%以下しか除去されないことをいう。   “Removable” in the composite fiber 1 means that 95% by mass or more of the resin component can be removed by the predetermined solution 3, and “difficult to remove” means that the resin component is removed under the condition of removing the first resin component. It means that only 30 mass% or less is removed.

このような複合繊維1の具体例としては、アルカリ水溶液(例えば、水酸化ナトリウム溶液)に対して除去可能なポリエステル(例えば、ポリエチレンテレフタレート、ポリエチレンテレフタレート系共重合体、ポリブチレンテレフタレート、ポリブチレンテレフタレート系共重合体、ポリグリコール酸、グリコール酸共重合体、ポリ乳酸、乳酸共重合体など)と、アルカリ水溶液に対して除去が困難なポリオレフィン系樹脂又はポリアミド系樹脂との組合せを挙げることができる。   Specific examples of such a conjugate fiber 1 include polyesters (for example, polyethylene terephthalate, polyethylene terephthalate copolymer, polybutylene terephthalate, polybutylene terephthalate) that can be removed with respect to an alkaline aqueous solution (for example, sodium hydroxide solution). A copolymer, a polyglycolic acid, a glycolic acid copolymer, a polylactic acid, a lactic acid copolymer, etc.) and a polyolefin-based resin or a polyamide-based resin that is difficult to remove with respect to an alkaline aqueous solution.

この第2樹脂成分は所定溶液3によって除去が困難な樹脂成分1種類からなる必要はなく、2種類以上から構成されていても良い。例えば、第2樹脂成分が2種類の樹脂からなると、第2樹脂成分から構成される細繊維が融着性、巻縮発現性、分割性など、各種特性を有することができるため、好適である。より具体的には、融点差のある2種類の樹脂から構成されていれば融着性と融着時の繊維形状保持性をもつ細繊維であることができ、熱収縮性の点で差のある2種類の樹脂から構成されていれば巻縮発現性をもつ細繊維であることができ、溶解度パラメーターの点で差の大きい2種類の樹脂から構成されていれば機械的に分割可能な細繊維であることができる。   The second resin component does not have to be composed of one kind of resin component that is difficult to be removed by the predetermined solution 3, and may be composed of two or more kinds. For example, it is preferable that the second resin component is made of two types of resins, because the fine fibers composed of the second resin component can have various characteristics such as fusibility, crimping and splitting properties. . More specifically, if it is composed of two types of resins having a difference in melting point, it can be a fine fiber having a fusion property and a fiber shape retention property at the time of fusion, and there is no difference in terms of heat shrinkability. If it is composed of two kinds of resins, it can be a fine fiber with a crimping property, and if it is composed of two kinds of resins having a large difference in solubility parameter, it is a fine fiber that can be mechanically divided. Can be fiber.

なお、複合繊維1の第2樹脂成分がポリオレフィン系樹脂からなる場合であっても、細繊維同士を圧着させることなく、細繊維を製造することができる。つまり、ポリプロピレンやポリエチレンは比較的熱変形温度が低く、熱と所定溶液3の通液圧力によって細繊維同士が圧着しやすいが、本発明によれば、細繊維同士を圧着させることなく、ポリオレフィン系細繊維を製造することができる。また、ポリオレフィン系樹脂は耐薬品性やエレクトレット性などの点で優れているため、各種用途に適用できる不織布を製造できるという効果も奏する。なお、第2樹脂成分がポリメチルペンテンとポリプロピレン、ポリメチルペンテンとポリエチレン、ポリプロピレンとポリエチレン、高密度ポリエチレンと低密度ポリエチレンなどの組合せからなると、融着成分と非融着成分とを備えた細繊維を製造でき、この細繊維は繊維形態を失うことなく融着できるため、脱落しにくいという特長がある。   In addition, even if it is a case where the 2nd resin component of the composite fiber 1 consists of polyolefin resin, a fine fiber can be manufactured, without making a fine fiber crimp. That is, polypropylene and polyethylene have a relatively low thermal deformation temperature, and the fine fibers are easily pressure-bonded by heat and the pressure of passing through the predetermined solution 3, but according to the present invention, the polyolefin fibers can be bonded without pressure-bonding the fine fibers. Fine fibers can be produced. In addition, since the polyolefin-based resin is excellent in terms of chemical resistance, electret properties, etc., there is also an effect that a nonwoven fabric applicable to various uses can be produced. When the second resin component is a combination of polymethylpentene and polypropylene, polymethylpentene and polyethylene, polypropylene and polyethylene, high-density polyethylene and low-density polyethylene, etc., a fine fiber having a fusion component and a non-fusion component Since this fine fiber can be fused without losing the fiber form, it has a feature that it is difficult to fall off.

本発明の複合繊維1の横断面形状は特に限定するものではないが、例えば、海島型、多重バイメタル型、オレンジ型などを挙げることができる。また、本発明の複合繊維1における第2樹脂成分は細繊維を構成するが、濾過性能、柔軟性、隠蔽性、払拭性などの諸特性に優れる不織布を製造できるように、繊維径が5μm以下の細繊維を発生できるのが好ましく、3μm以下の細繊維を発生できるのがより好ましく、2μm以下の細繊維を発生できるのが更に好ましい。なお、細繊維の繊維径の下限は特に限定するものではないが、0.01μm以上であるのが好ましい。繊維径が小さければ小さい程、変形しやすく圧着しやすい傾向があるが、本発明の製造方法によれば、繊維径が5μm以下であるような細繊維であっても、熱と通液の圧力による細繊維同士の圧着を効果的に防止して製造できるという、効果を奏する。なお、本発明における「繊維径」は円形横断面に換算した値をいう。   The cross-sectional shape of the conjugate fiber 1 of the present invention is not particularly limited, and examples thereof include a sea-island type, a multiple bimetal type, and an orange type. In addition, the second resin component in the composite fiber 1 of the present invention constitutes a fine fiber, but the fiber diameter is 5 μm or less so that a nonwoven fabric excellent in various properties such as filtration performance, flexibility, concealability, and wiping property can be produced. It is preferable that a fine fiber of 3 μm or less can be generated, and it is more preferable that a fine fiber of 2 μm or less can be generated. In addition, although the minimum of the fiber diameter of a fine fiber is not specifically limited, It is preferable that it is 0.01 micrometer or more. The smaller the fiber diameter is, the easier it is to deform and pressure-bond. However, according to the production method of the present invention, even if the fiber diameter is 5 μm or less, the pressure of heat and liquid flow The effect that it can manufacture by preventing the crimping | compression-bonding of the fine fibers by effectively is produced. The “fiber diameter” in the present invention is a value converted into a circular cross section.

図1における複合繊維1は穴あきボビン2に巻き付けられていることからも明らかなように、連続した繊維からなる。このような連続した複合繊維1は自由度が低く、所定溶液3が第2樹脂成分(細繊維)間を通過しやすいため、細繊維間にノニオン系界面活性剤又は両性界面活性剤が付着しやすい。そのため、熱と通液の圧力による細繊維同士の圧着を効果的に防止することができる。しかしながら、複合繊維1は連続した繊維ではなく、所定長さに切断された短繊維であっても同様の効果を奏する。   The composite fiber 1 in FIG. 1 is composed of continuous fibers, as is apparent from the fact that the composite fiber 1 is wound around the bobbin 2 with holes. Such a continuous conjugate fiber 1 has a low degree of freedom, and the predetermined solution 3 easily passes between the second resin components (fine fibers), so that a nonionic surfactant or an amphoteric surfactant adheres between the fine fibers. Cheap. Therefore, it is possible to effectively prevent the pressure-bonding between the fine fibers due to heat and the pressure of liquid flow. However, even if the composite fiber 1 is not a continuous fiber but is a short fiber cut to a predetermined length, the same effect can be obtained.

以上、図1の複合繊維1を穴あきボビン2に巻き付けた状態で、所定溶液3によって第1樹脂成分を除去する態様をもとに説明したが、本発明はこの態様に限定されず、例えば、所定長さに切断した複合繊維を、ノニオン系界面活性剤又は両性界面活性剤が存在する所定溶液で満たされた容器に浸漬することによって本発明の細繊維を製造することができるし、懸垂型のかせ染色機を用い、ノニオン系界面活性剤又は両性界面活性剤が存在する所定溶液を使用して本発明の細繊維を製造することもできる。   As described above, the composite fiber 1 of FIG. 1 has been described based on the aspect in which the first resin component is removed by the predetermined solution 3 in the state where the composite fiber 1 is wound around the perforated bobbin 2, but the present invention is not limited to this aspect. The fine fiber of the present invention can be produced by immersing the composite fiber cut to a predetermined length in a container filled with a predetermined solution containing a nonionic surfactant or an amphoteric surfactant, and can be suspended. The fine fibers of the present invention can also be produced using a predetermined solution in which a nonionic surfactant or an amphoteric surfactant is present using a skein dyeing machine.

本発明の不織布は上述のような製造方法により製造した細繊維、つまり細繊維同士が圧着していない細繊維を含む不織布であるため、地合いの良好な不織布である。本発明の不織布は上述のような製造方法により製造した細繊維を含むものであるが、その含有量は不織布に必要とされる物性によって異なるため、特に限定するものではない。一般に、濾過性能、柔軟性、隠蔽性、払拭性などを高度に必要とする場合には細繊維を多く含んでいるのが好ましい。   The non-woven fabric of the present invention is a non-woven fabric having a good texture because it is a non-woven fabric containing fine fibers produced by the production method as described above, that is, fine fibers in which the fine fibers are not pressure-bonded. Although the nonwoven fabric of this invention contains the fine fiber manufactured with the above manufacturing methods, since the content changes with physical properties required for a nonwoven fabric, it does not specifically limit. Generally, it is preferable to contain a lot of fine fibers when filtration performance, flexibility, concealment, wiping properties, etc. are required at a high level.

なお、本発明の不織布は細繊維が均一に分散していることによって、地合いが優れるものであるように、水流などの外力によって細繊維を絡合させないのが好ましい。そのため、細繊維以外に融着繊維を混合しておき、融着繊維を融着させることによって不織布形態を維持させるか、細繊維を融点差のある2種類以上の樹脂から構成させ、細繊維自体を融着させることによって不織布形態を維持させるのが好ましい。   In the nonwoven fabric of the present invention, it is preferable that the fine fibers are not entangled by an external force such as a water flow so that the fine fibers are uniformly dispersed and the texture is excellent. Therefore, the fusion fiber is mixed with the fine fiber, and the non-woven fabric is maintained by fusing the fusion fiber, or the fine fiber is composed of two or more kinds of resins having different melting points, and the fine fiber itself It is preferable to maintain the non-woven fabric form by fusing.

本発明の不織布の具体的な製造方法としては、前述のようにして細繊維を製造した後、細繊維が連続繊維である場合には、所望長さに切断する。なお、この切断の際に、細繊維同士が融着してしまう場合があるため、細繊維同士の融着が生じないように、特開2003−119668号公報に開示されている方法により切断するのが好ましい。つまり、連続細繊維束に油剤(アニオン系、カチオン系、ノニオン系界面活性剤等)を付与(連続細繊維束の質量100に対して15%以上であるのが好ましく、20%以上であるのがより好ましい、また、50%以下であるのが好ましい)した後、連続細繊維束にフィルムを巻きつけて連続細繊維束を固定した状態で、常法の切断装置(例えば、ギロチンカッターなど)を使用して、連続細繊維束を所望長さに切断するのが好ましい。なお、連続細繊維束に油剤(アニオン系、カチオン系、ノニオン系界面活性剤等)を付与(連続細繊維束の質量100に対して15%以上であるのが好ましく、20%以上であるのがより好ましい、また、50%以下であるのが好ましい)した場合には、フィルムで固定することなく、ロータリーカッターによって、連続細繊維束を所望長さに切断することができる。   As a specific method for producing the nonwoven fabric of the present invention, after producing fine fibers as described above, if the fine fibers are continuous fibers, they are cut to a desired length. In addition, since the fine fibers may be fused at the time of this cutting, cutting is performed by the method disclosed in Japanese Patent Application Laid-Open No. 2003-119668 so that the fine fibers are not fused. Is preferred. That is, an oil agent (anionic, cationic, nonionic surfactant, etc.) is given to the continuous fine fiber bundle (preferably 15% or more with respect to the mass 100 of the continuous fine fiber bundle, and 20% or more. Is more preferable, and is preferably 50% or less), and a conventional cutting device (for example, a guillotine cutter) in a state where the continuous fine fiber bundle is fixed by winding the film around the continuous fine fiber bundle. Is preferably used to cut the continuous fine fiber bundle to a desired length. It should be noted that an oil agent (anionic, cationic, nonionic surfactant, etc.) is imparted to the continuous fine fiber bundle (preferably 15% or more with respect to the mass 100 of the continuous fine fiber bundle, and 20% or more. Is more preferable and 50% or less is preferable), the continuous fine fiber bundle can be cut into a desired length by a rotary cutter without fixing with a film.

次いで、細短繊維を用い、必要であれば融着繊維も用いて、常法により繊維ウエブを製造する。この繊維ウエブの製造方法としては細短繊維を扱いやすく、細短繊維が均一に分散した地合いの優れる不織布を製造しやすい湿式法により繊維ウエブを製造するのが好ましい。   Subsequently, a fiber web is produced by a conventional method using short and short fibers, and if necessary, using fused fibers. As a method for producing this fiber web, it is preferable to produce the fiber web by a wet method that facilitates the production of a nonwoven fabric excellent in texture in which the fine fibers are easily handled and the fine fibers are uniformly dispersed.

その後、繊維ウエブを結合して本発明の不織布を製造できる。繊維ウエブの結合方法は特に限定するものではないが、地合いの優れる不織布を製造できるように、水流などによって絡合させることなく、細短繊維を融着させることによって、混合した融着繊維を融着させることによって、或いはエマルジョン状又はサスペンジョン状のバインダーで接着させることによって結合する方法を例示できる。   Thereafter, the nonwoven fabric of the present invention can be produced by bonding the fiber web. The bonding method of the fiber web is not particularly limited, but the mixed fused fibers can be fused by fusing the short fibers without being entangled by a water flow or the like so that a nonwoven fabric having excellent texture can be produced. Examples thereof include a method of bonding by attaching, or by adhering with an emulsion-like or suspension-like binder.

以下に本発明の実施例を記載するが、本発明は以下の実施例に限定されるものではない。   Examples of the present invention will be described below, but the present invention is not limited to the following examples.

(実施例1)
第1樹脂成分であるポリエチレンテレフタレート(海成分)中に、第2樹脂成分であるポリプロピレン(島成分)が点在した海島型複合連続繊維を集束した、繊度が14万dtexの海島型複合連続繊維束を用意した。次いで、この海島型複合連続繊維束を穴あきボビン2に約140m巻きつけた後、チーズ染色機に装着した。
(Example 1)
A sea-island composite continuous fiber having a fineness of 140,000 dtex, in which the sea-island composite continuous fibers interspersed with the first resin component, polyethylene terephthalate (sea component), is dispersed with the second resin component, polypropylene (island component). A bundle was prepared. Next, this sea-island type composite continuous fiber bundle was wound around a bobbin 2 with a hole of about 140 m and mounted on a cheese dyeing machine.

他方、前記第1樹脂成分を除去できる所定溶液3である水酸化ナトリウム溶液(60g/L)に、第4級アンモニウム塩型カチオン界面活性剤(減量促進剤、3g/L)、及びポリオキシエチレンノニルフェニルエーテル(所定溶液3の質量100に対して、0.3%)を加えて、混合所定溶液3を調製した。   On the other hand, a sodium hydroxide solution (60 g / L) which is the predetermined solution 3 capable of removing the first resin component, a quaternary ammonium salt type cationic surfactant (weight loss accelerator, 3 g / L), and polyoxyethylene Nonylphenyl ether (0.3% with respect to 100 mass of the predetermined solution 3) was added to prepare a mixed predetermined solution 3.

次いで、混合所定溶液3を温度98℃に加温した状態で、前記混合所定溶液3を穴あきボビン2の内側2aから外側2bへ通過させることにより、海島型複合連続繊維の第1樹脂成分であるポリエチレンテレフタレートを除去して、繊維径2μmのポリプロピレン細連続繊維束を製造した。   Next, with the mixed predetermined solution 3 heated to a temperature of 98 ° C., the mixed predetermined solution 3 is passed from the inner side 2a of the perforated bobbin 2 to the outer side 2b, whereby the first resin component of the sea-island type composite continuous fiber is obtained. A certain polyethylene terephthalate was removed to produce a polypropylene fine continuous fiber bundle having a fiber diameter of 2 μm.

次いで、このポリプロピレン細連続繊維束に油剤(ノニオン系界面活性剤)を繊維束の質量100に対して5%付与した後、ロータリーカッターで長さ3mmに切断し、ポリプロピレン細短繊維を製造した。   Next, 5% of the oil agent (nonionic surfactant) was applied to the polypropylene fine continuous fiber bundle with respect to the mass 100 of the fiber bundle, and then cut into a length of 3 mm with a rotary cutter to produce polypropylene fine fibers.

このポリプロピレン細短繊維70mass%と、別途用意した芯鞘型融着繊維(ポリプロピレン芯成分と低密度ポリエチレン鞘成分から構成、繊維径:17.5μm、繊維長:10mm)30mass%とを攪拌機で混合させるとともに分散させた後、湿式抄紙して湿式繊維ウエブを形成した。その後、湿式繊維ウエブを温度120℃に設定されたオーブンへ供給し、芯鞘型融着繊維の低密度ポリエチレンのみを融着させて不織布(目付:40g/m、厚さ:0.22mm)を製造した。この不織布表面の電子顕微鏡写真を図2に示す。この図2から明らかなように、ポリプロピレン細短繊維が1本づつにほぐれており、均一に分散した、地合いの良好なものであった。これは、ポリプロピレン細短繊維同士が圧着していないことに起因するものであった。 70 mass% of this polypropylene short staple fiber and 30 mass% of separately prepared core-sheath-type fusion fibers (composed of a polypropylene core component and a low-density polyethylene sheath component, fiber diameter: 17.5 μm, fiber length: 10 mm) are mixed with a stirrer. And dispersed, and then wet paper making to form a wet fiber web. Thereafter, the wet fiber web is supplied to an oven set at a temperature of 120 ° C., and only the low-density polyethylene of the core-sheath type fused fiber is fused to form a nonwoven fabric (weight per unit: 40 g / m 2 , thickness: 0.22 mm). Manufactured. An electron micrograph of the nonwoven fabric surface is shown in FIG. As apparent from FIG. 2, the polypropylene short fibers were loosened one by one, and were uniformly dispersed and had good texture. This was due to the fact that the polypropylene short fibers were not pressure-bonded.

(実施例2)
海島型複合連続繊維束として、第1樹脂成分がポリエチレンテレフタレート(海成分)からなり、第2樹脂成分が低密度ポリエチレン(島成分)からなる海島型複合連続繊維を集束して、繊度を14万dtexとした海島型複合連続繊維束を用いたこと以外は、実施例1と全く同様に、繊維径2μmの高密度ポリエチレン細連続繊維束の製造、繊維長3mmの高密度ポリエチレン細短繊維の製造を実施した。
(Example 2)
As a sea-island type composite continuous fiber bundle, the sea-island type composite continuous fibers in which the first resin component is made of polyethylene terephthalate (sea component) and the second resin component is made of low-density polyethylene (island component) are bundled to obtain a fineness of 140,000. Except for using a sea-island type continuous fiber bundle made of dtex, exactly as in Example 1, production of a high-density polyethylene fine continuous fiber bundle having a fiber diameter of 2 μm and production of a high-density polyethylene fine short fiber having a fiber length of 3 mm Carried out.

次いで、この高密度ポリエチレン細短繊維100mass%を攪拌機で分散させた後、湿式抄紙して湿式繊維ウエブを形成した。その後、湿式繊維ウエブを温度120℃に設定されたオーブンへ供給し、高密度ポリエチレン細短繊維を融着させて不織布(目付:30g/m、厚さ:0.15mm)を製造した。この不織布表面の電子顕微鏡写真を観察したところ、実施例1の不織布(図2)と同様に、高密度ポリエチレン細短繊維が1本づつにほぐれており、均一に分散した、地合いの良好なものであった。これは、高密度ポリエチレン細短繊維同士が圧着していないことに起因するものであった。 Next, 100 mass% of the high-density polyethylene fine fibers were dispersed with a stirrer, and then wet papermaking was performed to form a wet fiber web. Thereafter, the wet fiber web was supplied to an oven set at a temperature of 120 ° C., and the high density polyethylene fine fibers were fused to produce a nonwoven fabric (weight per unit: 30 g / m 2 , thickness: 0.15 mm). Observation of an electron micrograph of the surface of this nonwoven fabric revealed that, like the nonwoven fabric of Example 1 (FIG. 2), the high-density polyethylene fine fibers were loosened one by one, uniformly dispersed, and with good texture Met. This was due to the fact that the high-density polyethylene thin fibers were not pressure-bonded.

(実施例3)
混合所定溶液3として、水酸化ナトリウム溶液(60g/L)に、第4級アンモニウム塩型カチオン界面活性剤(減量促進剤、3g/L)、及び高級アルコールノニオン系界面活性剤(所定溶液3の質量100に対して0.3%)を加えた混合所定溶液3を用いたこと以外は実施例1と同様に、繊維径2μmのポリプロピレン細連続繊維束の製造、繊維長3mmのポリプロピレン細短繊維の製造、湿式繊維ウエブの形成、及び不織布(目付:40g/m、厚さ:0.20mm)の製造を実施した。この不織布表面の電子顕微鏡写真を図3に示す。この図3から明らかなように、ポリプロピレン細短繊維が1本づつにほぐれており、均一に分散した、地合いの良好なものであった。これは、ポリプロピレン細短繊維同士が圧着していないことに起因するものであった。
(Example 3)
As the mixed predetermined solution 3, a sodium hydroxide solution (60 g / L), a quaternary ammonium salt type cationic surfactant (weight loss accelerator, 3 g / L), and a higher alcohol nonionic surfactant (of the predetermined solution 3) Production of a polypropylene continuous fiber bundle having a fiber diameter of 2 μm, and polypropylene short fibers having a fiber length of 3 mm, except that the mixed predetermined solution 3 added with 0.3% of mass 100) was used. , Formation of a wet fiber web, and manufacture of a nonwoven fabric (weight per unit: 40 g / m 2 , thickness: 0.20 mm). An electron micrograph of the nonwoven fabric surface is shown in FIG. As is apparent from FIG. 3, the polypropylene short fibers were loosened one by one, and were uniformly dispersed and had good texture. This was due to the fact that the polypropylene short fibers were not pressure-bonded.

(実施例4)
第1樹脂成分であるポリエチレンテレフタレート(海成分)中に、第2樹脂成分であるポリプロピレン(島成分)が点在した海島型複合連続繊維に対して、ポリオキシエチレンノニルフェニルエーテル4.5mass%溶液を、付与しながら集束した、繊度が14万dtexの海島型複合連続繊維束(ポリオキシエチレンノニルフェニルエーテル溶液は海島型複合連続繊維束の質量に対して30%付着)を用意した。次いで、このノニオン系界面活性剤を付与した海島型複合連続繊維束を穴あきボビン2に約140m巻きつけた後、チーズ染色機に装着した。
(Example 4)
Polyoxyethylene nonylphenyl ether 4.5 mass% solution for sea-island type composite continuous fiber in which polypropylene (island component) as second resin component is interspersed in polyethylene terephthalate (sea component) as first resin component A sea-island type composite continuous fiber bundle having a fineness of 140,000 dtex (30% adhered to the mass of the sea-island type composite continuous fiber bundle) was prepared. Next, the sea-island type composite continuous fiber bundle to which the nonionic surfactant was added was wound around a bobbed bobbin 2 for about 140 m, and then mounted on a cheese dyeing machine.

他方、前記第1樹脂成分を除去できる所定溶液3である水酸化ナトリウム溶液(60g/L)に、第4級アンモニウム塩型カチオン界面活性剤(減量促進剤、3g/L)のみを加えて、混合所定溶液3を調製した。   On the other hand, only the quaternary ammonium salt type cationic surfactant (weight loss accelerator, 3 g / L) is added to the sodium hydroxide solution (60 g / L) which is the predetermined solution 3 capable of removing the first resin component, A mixed predetermined solution 3 was prepared.

次いで、混合所定溶液3を温度98℃に加温した状態で、前記混合所定溶液3を穴あきボビン2の内側2aから外側2bへ通過させることにより、海島型複合連続繊維の第1樹脂成分を除去して、繊維径2μmのポリプロピレン細連続繊維束を製造した。この第1樹脂成分を除去時における、混合所定溶液3中におけるポリオキシエチレンノニルフェニルエーテルの濃度は、混合所定溶液の質量100の0.2%であった。   Next, with the mixed predetermined solution 3 heated to a temperature of 98 ° C., the mixed predetermined solution 3 is passed from the inner side 2a of the perforated bobbin 2 to the outer side 2b, whereby the first resin component of the sea-island type composite continuous fiber is obtained. After removing, a fine polypropylene continuous fiber bundle having a fiber diameter of 2 μm was produced. At the time of removing the first resin component, the concentration of polyoxyethylene nonylphenyl ether in the mixed predetermined solution 3 was 0.2% of the mass 100 of the mixed predetermined solution.

その後、実施例1と同様に、長さ3mmのポリプロピレン細短繊維の製造、湿式繊維ウエブの形成、及び不織布(目付:40g/m、厚さ:0.21mm)の製造を実施した。この不織布表面の電子顕微鏡写真を観察したところ、実施例1の不織布(図2)と同様に、ポリプロピレン細短繊維が1本づつにほぐれており、均一に分散した、地合いの良好なものであった。これは、ポリプロピレン細短繊維同士が圧着していないことに起因するものであった。 Thereafter, in the same manner as in Example 1, production of polypropylene short fibers having a length of 3 mm, formation of a wet fiber web, and production of a nonwoven fabric (weight per unit: 40 g / m 2 , thickness: 0.21 mm) were performed. When an electron micrograph of the surface of this nonwoven fabric was observed, it was found that, as with the nonwoven fabric of Example 1 (FIG. 2), the polypropylene short fibers were loosened one by one and were uniformly dispersed and had good texture. It was. This was due to the fact that the polypropylene short fibers were not pressure-bonded.

(比較例1)
混合所定溶液3として、水酸化ナトリウム溶液(60g/L)に、第4級アンモニウム塩型カチオン界面活性剤(減量促進剤、3g/L)のみを加えた混合所定溶液3を用いたこと以外は実施例1と同様に、繊維径2μmのポリプロピレン細連続繊維束の製造、繊維長3mmのポリプロピレン細短繊維の製造、湿式繊維ウエブの形成、及び不織布(目付:39g/m、厚さ:0.18mm)の製造を実施した。この不織布表面の電子顕微鏡写真を図4に示す。この図4から明らかなように、ポリプロピレン細短繊維同士が圧着した、地合いの悪いものであった。
(Comparative Example 1)
As the mixed predetermined solution 3, except that the mixed predetermined solution 3 in which only a quaternary ammonium salt type cationic surfactant (weight loss accelerator, 3 g / L) was added to a sodium hydroxide solution (60 g / L) was used. In the same manner as in Example 1, production of a polypropylene fine continuous fiber bundle having a fiber diameter of 2 μm, production of a polypropylene fine fiber having a fiber length of 3 mm, formation of a wet fiber web, and a nonwoven fabric (weight per unit: 39 g / m 2 , thickness: 0) .18 mm) was carried out. An electron micrograph of the nonwoven fabric surface is shown in FIG. As is apparent from FIG. 4, the polypropylene short fibers were pressed together and had poor texture.

複合繊維における第1樹脂成分の除去状態を模式的に表すたて断面図Vertical sectional view schematically showing the removal state of the first resin component in the conjugate fiber 実施例1の不織布表面の電子顕微鏡写真Electron micrograph of the nonwoven fabric surface of Example 1 実施例3の不織布表面の電子顕微鏡写真Electron micrograph of the nonwoven fabric surface of Example 3 比較例1の不織布表面の電子顕微鏡写真Electron micrograph of the nonwoven fabric surface of Comparative Example 1

符号の説明Explanation of symbols

1 複合繊維
2 穴あきボビン
2a 穴あきボビンの内側
2b 穴あきボビンの外側
3 所定溶液
DESCRIPTION OF SYMBOLS 1 Composite fiber 2 Perforated bobbin 2a Inner side of perforated bobbin 2b Outer side of perforated bobbin 3 Predetermined solution

Claims (6)

アルカリ水溶液によって除去可能な第1樹脂成分と、前記アルカリ水溶液によって除去が困難な第2樹脂成分とを含む連続した複合繊維を穴あきボビンに巻きつけた状態で、穴あきボビンの内側から外側へアルカリ水溶液を通過させて、又は穴あきボビンの外側から内側へアルカリ水溶液を通過させることにより、第1樹脂成分を除去し、第2樹脂成分からなる細繊維を製造する方法であり、細繊維同士の圧着を防止するために、前記アルカリ水溶液中にノニオン系界面活性剤又は両性界面活性剤、及び減量促進剤が存在していることを特徴とする、細繊維の製造方法。 A first resin component which can be removed by alkaline aqueous solution, in a state where the continuous composite fiber containing said alkaline water solution second resin component removal is difficult by wound on perforated bobbin, from the inside of the perforated bobbin outside to be passed through an aqueous alkaline solution, or by making the outside of the perforated bobbin to pass through the alkaline aqueous solution to the inside, the first resin component is removed, a process for producing the fine fibers made of the second resin component, fine to prevent crimping between fibers, characterized in that the nonionic surfactant or amphoteric surfactant in the alkaline water solution, and weight loss enhancers are present, the production method of the fine fibers. ノニオン系界面活性剤又は両性界面活性剤及び減量促進剤は、アルカリ水溶液に予め添加されたことによって、アルカリ水溶液中に存在していることを特徴とする、請求項1記載の細繊維の製造方法。 Nonionic surface active agents or amphoteric surface active agent, and a reduction promoter, by which is previously added to the alkaline water solution, characterized in that present in alkaline water solution, fine fibers according to claim 1, wherein Manufacturing method. ノニオン系界面活性剤又は両性界面活性剤は、ノニオン系界面活性剤又は両性界面活性剤が付与された複合繊維を用いることによって、アルカリ水溶液中に存在していることを特徴とする、請求項1又は請求項2記載の細繊維の製造方法。 Nonionic surfactants or amphoteric surfactants, characterized in that by using a composite fiber nonionic surfactant or amphoteric surfactant has been applied, is present in an alkaline aqueous solution, claim A method for producing a fine fiber according to claim 1. 第2樹脂成分がポリオレフィン系樹脂からなることを特徴とする、請求項1〜請求項3のいずれかに記載の細繊維の製造方法。 The method for producing fine fibers according to any one of claims 1 to 3, wherein the second resin component comprises a polyolefin resin. 細繊維の繊維径が5μm以下であることを特徴とする、請求項1〜請求項4のいずれかに記載の細繊維の製造方法。 The method for producing a fine fiber according to any one of claims 1 to 4, wherein the fiber diameter of the fine fiber is 5 µm or less. 請求項1〜請求項のいずれかに記載の製造方法により製造された細繊維を含んでいることを特徴とする不織布。 A non-woven fabric comprising fine fibers produced by the production method according to any one of claims 1 to 5 .
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