JP2006045737A - Artificial leather having excellent shape stability and method for producing the same - Google Patents
Artificial leather having excellent shape stability and method for producing the same Download PDFInfo
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Abstract
Description
本発明は、繊維積層絡合体を経由して人工皮革を製造することで、得られる人工皮革の折れやしわの状態や目付の斑を均一することが可能となり、また製造工程で縦伸びなどを抑制することから、形態安定性に優れ、また硬化が抑制されることによる風合いの良好な人工皮革を提供するものである。 By producing artificial leather via a fiber laminate entangled body, the present invention makes it possible to make the resulting artificial leather folds, wrinkles and uneven spots, and to achieve longitudinal elongation in the production process. Therefore, the present invention provides an artificial leather that has excellent shape stability and good texture due to suppression of curing.
従来から人工皮革の製造に際して、主として極細繊維と高分子弾性体とで構成されたものが開発されており、このような極細繊維からなる人工皮革は、スエード感や表面タッチ感、柔軟性に優れており、天然皮革に類似した素材として高く評価されてきた。また、人工皮革製造において、収縮処理を加えることで風合いの改善、繊維密度や強度の向上、あるいはバルキー性やストレッチ性付与などが提案されている。
また、繊維絡合体を形成させる方法としては、ニードルパンチ方法が一般的に用いられている。すなわち、ニードルを繊維ウェブに対し反復挿入し、ニードルの側面のバーブあるいは針先につけた凹み部分で繊維を引っ掛けて絡合せしめる方法である。しかし一般の繊維ウェブはたとえ予めクロスラッパー、ランダムウエバーまたは気液流等で均一に広げた後、それらを重ねてもニードルパンチ中に繊維ウェブからなる不織布の幅方向中央部の目付けに比べ該不織布の幅方向両端部の目付けが高くなる傾向があった。
また、人工皮革製造において様々な工程を通過する際に、縦方向に大きく張力がかかることで縦伸びしやすく、不織布の段階でいかに均一な目付けのものを製造したとしても新たな目付け斑が発生し易く、加えてスエード調人工皮革に仕上た場合、表面外観における毛羽密度の低下またはその斑が生じ、さらに得られた人工皮革は形態安定性が低下し易いといった問題を抱えていた。
Conventionally, artificial leather has been developed mainly consisting of ultrafine fibers and polymer elastic bodies. Artificial leather made of such ultrafine fibers is superior in suede, surface touch and flexibility. It has been highly evaluated as a material similar to natural leather. In addition, in the manufacture of artificial leather, it has been proposed to improve the texture, increase the fiber density and strength, or provide bulkiness and stretchability by applying a shrinkage treatment.
Moreover, as a method for forming the fiber entangled body, a needle punch method is generally used. That is, it is a method in which a needle is repeatedly inserted into a fiber web, and the fiber is hooked and entangled with a barb on the side surface of the needle or a recessed portion attached to the needle tip. However, even if a general fiber web is previously spread evenly with a cross wrapper, random web, gas-liquid flow, etc. and then overlapped, the nonwoven fabric is compared with the basis weight at the center in the width direction of the nonwoven fabric made of fiber web during needle punching. There was a tendency for the fabric weight at both ends in the width direction to become higher.
In addition, when passing through various processes in the manufacture of artificial leather, a large amount of tension is applied in the vertical direction, making it easy to stretch in the vertical direction. In addition, when finished in a suede-like artificial leather, there was a problem that the fluff density in the surface appearance was reduced or its spots were generated, and the obtained artificial leather was liable to have a low form stability.
これらの問題を解決するため従来から数多くの提案がなされてきた。例えば、紡出量を落とすことなく目付斑を防止し得るように構成された原料繊維供給装置が提案されている(例えば、特許文献1参照)。しかしながら、この装置によって繊維ウェブの目付斑は改善されるものの、その後のニードル処理での形態変化に伴う目付斑の改善までは至っていない。また、ニードル処理時に発生する目付斑改善策として、繊維を絡合することのできるショートニードルと繊維を実質的に絡合しないかあるいは前記ショートニードルの絡合能力の1/2以下であるロングニードルとで繊維ウェブをニードルパンチする方法が提案されている(例えば、特許文献2参照)。しかしながら、ロングニードルは針折れ、針曲り、更には得られる繊維絡合体に針スジを発生させやすく、また、繊維絡合体の伸びが大となりやすい傾向があった。また上記方法とは別に、短繊維ウェブに、0.01〜1.0重量%の油剤を、該ウェブの幅方向において、その中央部より端部が少ないように制御しながら付着させた後、ニードルパンチを施すことによってニードル処理時に発生する目付斑の改善方法が提案さえている(例えば、特許文献3)。しかしながら、該方法では、短繊維を作成した時点で油剤を付与するのみならず、ウェブ積層時に改めて油剤を付与せねばならず、手間がかかるばかりか、油剤がウェブの表層に多く付与され易く、厚み方向において均一に付着し難く、目付斑の改善において十分満足できるとは言い難いものであった。 Many proposals have been made to solve these problems. For example, a raw fiber supply apparatus configured to prevent spot weight without reducing the spinning amount has been proposed (see, for example, Patent Document 1). However, although this apparatus improves the unevenness of the fiber web, it has not yet improved the unevenness of the fiber due to the shape change in the needle treatment. In addition, as a measure for improving spot weight generated during needle processing, a short needle that can entangle fibers and a long needle that does not substantially entangle the fibers or that is ½ or less of the entanglement capability of the short needles. And a method of needle punching a fiber web has been proposed (see, for example, Patent Document 2). However, long needles tend to bend, bend, and easily cause needle streaks in the resulting fiber entanglement, and the fiber entanglement tends to increase in elongation. Separately from the above method, 0.01 to 1.0% by weight of the oil agent is attached to the short fiber web while controlling the web in the width direction so that the end portion is less than the center portion. There has even been proposed a method of improving the spot weight that occurs during needle processing by applying a needle punch (for example, Patent Document 3). However, in this method, not only the oil agent is applied at the time of producing the short fibers, but the oil agent must be applied again at the time of laminating the web, which is troublesome, and the oil agent is easily applied to the surface layer of the web. It was difficult to uniformly adhere in the thickness direction, and it was difficult to say that it was sufficiently satisfactory in improving the spot weight.
一方、極細化可能な繊維よりなる繊維ウェブと、編織物を重ねて絡合処理して絡合一体化した後、極細化処理、高分子弾性体付与処理および立毛処理を含む処理を行って得られたシートの製造方法に関して、熱処理を行なうことによって長さ方向および/または幅方向に収縮させた後に、編織物を除去する伸縮性に優れた人工皮革の製造方法が、また、極細繊維を含む繊維絡合体と高分子弾性体からなる人工皮革の少なくとも片側の表面に、収縮処理により長さ方向に10%以上収縮する収縮性シートを接着し、該収縮性シートを収縮処理した後に収縮性シートを除去する伸縮性に優れた人工皮革の製造方法が提案されている(例えば、特許文献4および特許文献5)。しかしながら、それらの方法は、形態安定性の点では効果が認められるものの、挿入する織編物を最終的に除去する際にバフィングなどによる機械的な除去処理を行わねばならず、手間がかかるばかりか、バフィング処理の調整が困難となり表面が不必要に荒れ易くなったり、余分な工程を通すことによって処理方向に張力がかかり易くなる。さらに、製造コストに関しても非常に無駄な部分が多かった。
また、挿入する織編物として、仮に溶剤抽出可能な成分で構成されたものを用いた場合、溶剤抽出することで表面を不必要に荒らすことはなくなるものの、溶剤抽出時に繰返し行うnip処理によって製品の膨らみ感などが損なわれ、製品の風合いが劣ったものとなり易かった。
以上、従来の技術では、繊維絡合体の目付斑を抑制、また人工皮革製造において各工程通過する際に縦伸びするなど形態安定性、風合いに関して、十分満足するようなものはいまだ実現できていない。
On the other hand, a fiber web made of fibers that can be made ultrafine and a knitted fabric are entangled and integrated by entanglement, and then subjected to treatment including ultrafine treatment, polymer elastic body application treatment, and napping treatment. Regarding a method for producing a sheet obtained, a method for producing artificial leather excellent in stretchability that removes a knitted fabric after shrinking in a length direction and / or a width direction by performing a heat treatment, and also includes ultrafine fibers A shrinkable sheet that shrinks 10% or more in the length direction by shrinkage treatment is bonded to the surface of at least one side of an artificial leather composed of a fiber entangled body and a polymer elastic body. There have been proposed methods for producing artificial leather with excellent stretchability that removes water (for example, Patent Document 4 and Patent Document 5). However, although these methods are effective in terms of form stability, mechanical removal processing such as buffing must be performed when the woven or knitted fabric to be inserted is finally removed, which is troublesome. The adjustment of the buffing process becomes difficult, and the surface is easily roughened unnecessarily, or the tension is easily applied in the processing direction by passing an extra step. Furthermore, there were many very useless parts regarding manufacturing costs.
In addition, if the woven or knitted fabric to be inserted is composed of components that can be extracted with a solvent, the surface of the product will not be unnecessarily roughened by extracting the solvent, but the product may be removed by repeated nip treatment during the extraction of the solvent. The feeling of swelling was impaired and the texture of the product was inferior.
As described above, the conventional technology has not yet realized what is sufficiently satisfied with respect to form stability and texture, such as suppressing the uneven appearance of the fiber entangled body and extending longitudinally when passing through each process in the production of artificial leather. .
本発明は、繊維積層絡合体を経由して人工皮革を製造することで、得られる人工皮革の折れやしわの状態や目付の斑を均一することが可能となり、また製造工程で縦伸びなどを抑制することから、形態安定性に優れ、また硬化が抑制されることによる風合いの良好な人工皮革を提供するものである。 By producing artificial leather via a fiber laminate entangled body, the present invention makes it possible to make the resulting artificial leather folds, wrinkles and uneven spots, and to achieve longitudinal elongation in the production process. Therefore, the present invention provides an artificial leather that has excellent shape stability and good texture due to suppression of curing.
すなわち、本発明は繊維絡合体の内部に高分子弾性体が付与されてなる人工皮革を製造するに際し、以下(1)〜(4)の工程を順次行うことを特徴とする人工皮革の製造方法である。
(1)短繊維ウェブと実質的に水抽出除去可能な繊維からなる織編物を積層した後、絡合一体化処理することで繊維積層絡合体を製造する工程、
(2)繊維積層絡合体を熱収縮する工程、
(3)繊維積層絡合体の内部に高分子弾性体を付与する工程、
(4)織編物を水抽出除去する工程、
また、短繊維ウェブが水溶性高分子成分と水難溶性高分子成分からなる極細繊維発生型繊維であることが好ましく、織編物を構成する水抽出除去可能な繊維が、炭素数4以下のα―オレフィン単位および/またはビニルエーテル単位を1〜20モル%含有し、けん化度90〜99.99モル%である変性ポリビニルアルコールからなることが好ましい。
また、本発明は前述の製造方法により得られる人工皮革であり、さらに該人工皮革を起毛処理することで得られるスエード調人工皮革である。
That is, the present invention provides a method for producing artificial leather, characterized in that the following steps (1) to (4) are sequentially performed when producing an artificial leather in which a polymer elastic body is provided inside a fiber entangled body. It is.
(1) The process of manufacturing a fiber lamination entangled body by carrying out an entanglement integration process, after laminating | knitting the woven / knitted fabric which consists of a fiber which can be substantially extracted by water extraction with a short fiber web,
(2) a step of thermally shrinking the fiber laminate entangled body,
(3) A step of providing a polymer elastic body inside the fiber laminate entangled body,
(4) a step of extracting and removing the woven or knitted fabric with water,
Further, it is preferable that the short fiber web is an ultra-fine fiber generating fiber composed of a water-soluble polymer component and a poorly water-soluble polymer component, and the water extractable / removable fiber constituting the woven or knitted fabric is α- having 4 or less carbon atoms. It preferably comprises a modified polyvinyl alcohol containing 1 to 20 mol% of olefin units and / or vinyl ether units and having a saponification degree of 90 to 99.99 mol%.
Moreover, this invention is the artificial leather obtained by the above-mentioned manufacturing method, and also is a suede-like artificial leather obtained by carrying out raising treatment of this artificial leather.
以下、本発明を詳細に説明する。
本発明は、短繊維ウェブと水抽出除去可能な織編物を絡合一体化処理することで繊維積層絡合体を作製し、得られる人工皮革の厚み斑、目付斑を抑制する製造方法に関するものである。また該繊維積層絡合体を経由して人工皮革を製造することで、工程通過時の人工皮革の縦伸びを抑制する製造方法に関する。すなわち、繊維積層絡合体を形成するにあたり、挿入された織編物によって繊維積層絡合体の中央部と両端部との目付斑を生じず均一な繊維積層絡合体の製造が可能となる。また織編物が挿入されていることで、繊維積層絡合体製造工程、熱収縮工程、あるいはその後の人工皮革の製造工程において縦伸びの抑制が可能であり、人工皮革の品位を損なわず、形態安定性に優れたものとなる。さらに高分子弾性体含浸後、挿入された織編物を研削処理することなく、また溶剤抽出することなく水抽出のみで除去可能なことで、風合いを柔らかくし、また表面品位を低下させることなく人工皮革を製造可能とするのである。
Hereinafter, the present invention will be described in detail.
The present invention relates to a production method for producing a fiber laminated entangled body by entangled and integrating a short fiber web and a woven or knitted fabric that can be extracted by water extraction, and suppressing the thickness unevenness and the unevenness of the artificial leather obtained. is there. Moreover, it is related with the manufacturing method which suppresses the longitudinal elongation of the artificial leather at the time of a process by manufacturing artificial leather via this fiber lamination entanglement body. That is, when forming the fiber laminate entangled body, the inserted woven or knitted fabric does not cause uneven spots between the center portion and both end portions of the fiber laminate entangled body, and a uniform fiber laminate entangled body can be produced. In addition, the insertion of the woven or knitted fabric enables the longitudinal elongation to be suppressed in the fiber laminate entanglement manufacturing process, the heat shrink process, or the subsequent artificial leather manufacturing process, and does not impair the quality of the artificial leather. Excellent in properties. Furthermore, after the polymer elastic body is impregnated, the inserted woven or knitted fabric can be removed only by water extraction without grinding and without solvent extraction, thereby softening the texture and reducing the surface quality. The leather can be manufactured.
本発明の繊維絡合体を構成する短繊維は、直接紡糸して得られる繊維、あるいは極細繊維発生型繊維から得られる繊維のいずれのタイプでもよいが、紡糸安定性の点から極細繊維発生型繊維であることが好ましい。特に極細繊維化後の繊度で好ましくは0.0003〜0.4dtexの繊度、より好ましくは0.003〜0.2dtexの繊度、さらに好ましくは0.007〜0.1dtexの繊度を有するような極細繊維発生型繊維であることが好ましい。このような極細繊維発生型繊維の繊度としては、1〜15dtexの範囲が紡糸以降の工程通過性に優れる点で好ましい。
また、短繊維は平均繊維長が18〜110mmであることが肝要である。繊維長が18mm以上のものであれば効果的な絡合が可能となり、また110mm以下であれば、カード処理などの工程通過性に優れたものとなる。ただし、その後スライス処理やバフィング処理などの後加工を行う場合、最終製品に至る前に短繊維が切断されてしまい、18mm未満になった繊維が一部含まれていることもあるが、これは効果的絡合が達成されてから後に発生した繊維であるので、本発明の効果を損なうものではない。なお、上記工程通過性の観点から平均繊維長は20〜80mmがより好ましい。
The short fiber constituting the fiber entangled body of the present invention may be either a fiber obtained by direct spinning or a fiber obtained from an ultrafine fiber generating fiber, but from the viewpoint of spinning stability, an ultrafine fiber generating fiber It is preferable that In particular, the fineness after the ultrafine fiber is preferably 0.0003 to 0.4 dtex, more preferably 0.003 to 0.2 dtex, and even more preferably 0.007 to 0.1 dtex. A fiber generating fiber is preferred. As the fineness of such an ultrafine fiber-generating fiber, a range of 1 to 15 dtex is preferable in terms of excellent processability after spinning.
It is important that the short fiber has an average fiber length of 18 to 110 mm. If the fiber length is 18 mm or more, effective entanglement is possible, and if the fiber length is 110 mm or less, the process passability such as card processing is excellent. However, when post-processing such as slicing or buffing is performed thereafter, the short fibers may be cut before reaching the final product, and some fibers that are less than 18 mm may be included. Since the fibers are generated after effective entanglement is achieved, the effect of the present invention is not impaired. In addition, the average fiber length is more preferably 20 to 80 mm from the viewpoint of the process passability.
また、極細繊維発生型繊維は、環境対応の観点から特に水溶性高分子成分と水難溶性高分子成分から構成されていることが好ましい。この水溶性高分子成分とは、該成分が水溶液により抽出除去される成分を示し、水難溶性高分子成分とは、該成分が水溶液により抽出除去されにくい成分を示す。そして、水溶性高分子成分と水難溶性高分子成分からなる極細繊維発生型繊維は少なくとも1成分が水溶液による水抽出処理で抽出除去されるものであれば、海島型複合繊維、混合紡糸型繊維などの多成分系複合繊維のいずれを使用してもよい。なお本発明で用いられる水溶性高分子成分としては、水溶液(水系溶剤と称することもある)で抽出処理できるポリマーであれば、公知のポリマーが使用できるが、水系溶剤で溶解可能なポリビニルアルコール共重合体類(以下PVAと略することもある)を用いることが好ましい。PVAは、水特に熱水で容易に溶解除去可能である点、水系溶剤で抽出除去する際の収縮挙動によって極細繊維発生型繊維の極細繊維に構造捲縮が発現し、繊維絡合体が嵩高く緻密なものとなって非常に柔軟な天然皮革のように優れた風合いの人工皮革が得られる点、また、水抽出処理する際に極細繊維成分や高分子弾性体成分の分解、溶解反応が実質的に起こらないため極細繊維成分に用いる熱可塑性樹脂および高分子弾性体成分の限定がほとんど無い点、更には環境に配慮した点等から好適に用いられる。 The ultrafine fiber generating fiber is preferably composed of a water-soluble polymer component and a poorly water-soluble polymer component from the viewpoint of environmental friendliness. The water-soluble polymer component indicates a component from which the component is extracted and removed by an aqueous solution, and the poorly water-soluble polymer component indicates a component that is difficult to extract and remove by an aqueous solution. And, as long as at least one component is extracted and removed by water extraction treatment with an aqueous solution, an ultra-fine fiber generation type fiber composed of a water-soluble polymer component and a poorly water-soluble polymer component is a sea-island type composite fiber, a mixed spinning type fiber, etc. Any of the multicomponent composite fibers may be used. As the water-soluble polymer component used in the present invention, a known polymer can be used as long as it is a polymer that can be extracted with an aqueous solution (sometimes referred to as an aqueous solvent). Polymers (hereinafter sometimes abbreviated as PVA) are preferably used. PVA can be easily dissolved and removed with water, especially hot water, and the structure of crimping is very high due to the shrinkage behavior when it is extracted and removed with an aqueous solvent. It is dense and can produce artificial leather with an excellent texture like natural leather, and the decomposition and dissolution reaction of ultra-fine fiber components and polymer elastic body components is practical during water extraction treatment. Therefore, the thermoplastic resin and the polymer elastic body component used for the ultrafine fiber component are hardly limited, and they are preferably used from the viewpoint of environmental considerations.
上記PVAはホモポリマーであっても共重合単位を導入した変性ポリビニルアルコールであってもよいが、溶融紡糸性、水溶性、繊維物性および抽出処理時の収縮特性などの観点から、共重合単位を導入したPVAであることが好ましく、エチレン、プロピレン、1−ブテン、イソブテン等の炭素数4以下のα―オレフィン類、メチルビニルエーテル、エチレンビニルエーテル、n−プロピルビニルエーテル、i−プロピルビニルエーテル、n−ブチルビニルエーテル等のビニルエーテル類がより好ましい。また炭素数4以下のα−オレフィン類および/またはビニルエーテル類に由来する単位は、PVA中に1〜20モル%存在していることが好ましい。さらに、α−オレフィンがエチレンである場合において、繊維物性が高くなることから、特にエチレン単位が4〜15モル%変成されたPVAを使用することがより好ましい。
またけん化度は90〜99.99モル%が好ましく、92〜99.98モル%がより好ましく、94〜99.96モル%がさらに好ましく、95〜99.95モル%が特に好ましい。けん化度が90モル%未満の場合には、PVAの熱安定性が悪く熱分解やゲル化によって満足な複合溶融紡糸を行うことができない。一方、けん化度が99.99モル%よりも大きいPVAは安定に製造することが困難である。
また常温で水に溶出するタイプのPVAを水溶性高分子成分として用いた場合には含浸時に水溶性高分子成分が溶出し高分子弾性体水分散液を汚染してしまう場合があり、また水溶性高分子成分の一部溶出に伴い極細繊維部分が露出することによって含浸した高分子弾性体が極細繊維を直接バインドし人工皮革の風合いが硬く損なわれやすいことから60〜100℃の熱水に溶出するタイプのPVAを水溶性高分子成分として用いることが好ましい。さらに60〜100℃の熱水で水溶性高分子成分を溶出することによって、繊維絡合体の収縮挙動が発生し構造捲縮を生じやすいことから天然皮革並みの優れた風合いの人工皮革基体が得られる点で好ましい。
The PVA may be a homopolymer or a modified polyvinyl alcohol introduced with a copolymer unit. However, from the viewpoints of melt spinnability, water solubility, fiber properties, and shrinkage characteristics during extraction processing, the copolymer unit may be Preferably, the introduced PVA is an α-olefin having 4 or less carbon atoms such as ethylene, propylene, 1-butene, isobutene, methyl vinyl ether, ethylene vinyl ether, n-propyl vinyl ether, i-propyl vinyl ether, n-butyl vinyl ether. More preferred are vinyl ethers such as Moreover, it is preferable that 1-20 mol% of units derived from α-olefins having 4 or less carbon atoms and / or vinyl ethers are present in PVA. Furthermore, when the α-olefin is ethylene, the fiber physical properties are improved, and therefore, it is more preferable to use PVA in which 4 to 15 mol% of ethylene units are particularly modified.
The saponification degree is preferably 90 to 99.99 mol%, more preferably 92 to 99.98 mol%, further preferably 94 to 99.96 mol%, and particularly preferably 95 to 99.95 mol%. When the saponification degree is less than 90 mol%, the thermal stability of PVA is poor and satisfactory composite melt spinning cannot be performed by thermal decomposition or gelation. On the other hand, PVA having a saponification degree larger than 99.99 mol% is difficult to produce stably.
In addition, when PVA of the type that elutes into water at room temperature is used as the water-soluble polymer component, the water-soluble polymer component may elute during impregnation and contaminate the polymer elastic water dispersion. Because the polymer elastic body impregnated by exposing the ultrafine fiber part due to partial elution of the functional polymer component directly binds the ultrafine fiber and the texture of the artificial leather is hard and easily damaged, the hot water at 60 to 100 ° C. It is preferable to use an elution type PVA as the water-soluble polymer component. Furthermore, by eluting the water-soluble polymer component with hot water at 60 to 100 ° C., the shrinkage behavior of the fiber entanglement occurs and the structure is easily crimped, so that an artificial leather base having an excellent texture similar to that of natural leather can be obtained. This is preferable.
またPVAを高温で紡糸すると紡糸性の悪化を招くため、本発明の水難溶性高分子成分としては公知の極細繊維となりうる、例えば、ポリアミド系、ポリエステル系およびポリオレフィン系等の成分であれば特に限定するものではない。そして、極細繊維を構成する水難溶性高分子成分の融点を適宜選択することが好ましく、極細繊維を構成する水難溶性高分子成分としては、極細繊維を形成する過程において抽出除去される水溶性高分子成分の融点から60℃上の間の融点を有する熱可塑性成分を選択することが極細繊維発生型繊維の紡糸安定性の点で好ましい。例えば、ポリエチレンテレフタレート、ポリブチレンテレフタレート、イソフタル酸を共重合したポリエチレンテレフタレートあるいはイソフタル酸を共重合したポリブチレンテレフタレートなどで代表されるポリエステル系樹脂、あるいはナイロン6、ナイロン11、ナイロン12などで代表されるポリアミド系樹脂が好ましく挙げられる。なお水溶性高分子成分の融点としては、紡糸性などの点から160〜230℃が好ましい。
なお、極細繊維発生型繊維を構成する水溶性高分子成分と水難溶性高分子成分の質量比率としては、水溶性高分子成分/水難溶性高分子成分=10/90〜60/40の範囲が、断面形成性が良好であり水溶性高分子が極細繊維を完全被覆し易いために、繊維絡合体内部での均一な浸透性が得られ均一含浸に有利である点、あるいは人工皮革基体とした場合、断面形成性が良好なため発生する極細繊維が均一であり、得られる人工皮革の風合いを損なわない点で好ましい。
In addition, since spinning of PVA at a high temperature causes deterioration of spinnability, the poorly water-soluble polymer component of the present invention can be a known ultrafine fiber. For example, it is particularly limited as long as it is a component such as polyamide, polyester and polyolefin Not what you want. The melting point of the poorly water-soluble polymer component constituting the ultrafine fiber is preferably selected as appropriate, and the poorly water-soluble polymer component constituting the ultrafine fiber is a water-soluble polymer extracted and removed in the process of forming the ultrafine fiber. From the viewpoint of spinning stability of the ultrafine fiber generating fiber, it is preferable to select a thermoplastic component having a melting point between 60 ° C. and the melting point of the component. For example, polyethylene terephthalate, polybutylene terephthalate, polyethylene terephthalate copolymerized with isophthalic acid, polyester resin typified by polybutylene terephthalate copolymerized with isophthalic acid, or nylon 6, nylon 11, nylon 12, etc. Polyamide resins are preferred. The melting point of the water-soluble polymer component is preferably 160 to 230 ° C. from the viewpoint of spinnability.
In addition, as a mass ratio of the water-soluble polymer component and the hardly water-soluble polymer component constituting the ultrafine fiber-generating fiber, the range of water-soluble polymer component / little water-soluble polymer component = 10/90 to 60/40 is When cross-section is good and water-soluble polymer is easy to completely cover ultrafine fibers, uniform penetration inside the fiber entangled body is obtained, which is advantageous for uniform impregnation, or when artificial leather base is used Since the cross-sectional formability is good, the fine fibers generated are uniform, which is preferable in that the texture of the resulting artificial leather is not impaired.
本発明の短繊維を構成する繊維は、顔料を添加していても良い。この場合、最終製品として淡色系、すなわち、薄い色や淡い色としての発色性が必要な場合顔料は少量でよく、極細繊維内部への顔料添加は低濃度である。すなわち最終製品として要求される外観の色が淡色の場合には、極細繊維内部への顔料添加量は0〜1質量%が好ましく、中色の場合には1〜2質量%が好ましく、濃色の場合には2〜5質量%が好ましく、5質量%を越えると紡糸工程性に劣り、また繊維強度が低下し、それに伴い得られる人工皮革の引裂強力が劣ったものとなってしまう。
用いる顔料としては、例えば酸化チタン、カーボンブラック、クロムレッド、モリブデンレッドなどの無機顔料や、フタロシアニン系、アントラキノン系などの有機顔料など通常ポリマー原着に使用されているものを用いることができる。特に、カーボンブラックを用いる場合、カーボンブラックが極細繊維を構成するポリマー中に混在一体化して存在し、主として極細繊維を構成するポリマー中に埋包され易い点から、カーボンブラックの平均一次粒径としては10〜60nmであることが好ましい。カーボンブラックの平均一次粒径が10nm未満の場合には、紡糸中にカーボンブラックの凝集が起こり易いことに起因して均一な繊維を得ることができにくく、色斑、物性斑等の品質安定性の問題が生じ易く、かつ紡糸性が低下する傾向がある。逆に、カーボンブラックの平均一次粒径が60nmを超える場合には、得られる人工皮革をスエード調とした際、耐光堅牢性、発色性が低下する傾向にあり、また、紡糸工程でのフィルター詰まりが起こり易く紡糸性が低下する傾向がある。そして、カーボンブラックは一般に複数の一次粒子が集合した集合体(以下、アグリゲートと呼ぶ)で存在するが、カーボンブラックが極細繊維を構成するポリマー中に混在一体化して存在し、主として極細繊維を構成するポリマー中に埋包され易く、発色性、耐光堅牢性、紡糸性が良好であることから、アグリゲートの平均粒子径としては20〜200nmであることがより好ましい。また他の無機顔料、有機顔料においても同様の理由で平均粒子径としては20〜200nmであることがより好ましい。
また、顔料の添加方法としては、極細繊維を構成するポリマー中における顔料の分散性を良好にするため、極細繊維を構成するポリマーと顔料を押出機などのコンパウンド設備を用いて混練した後ペレット化したマスターバッチ方式を採用することが好ましい。また、極細繊維成分には本発明の目的や効果を損なわない範囲で、銅化合物などの安定剤、着色剤、紫外線吸収剤、光安定剤、酸化防止剤、帯電防止剤、難燃剤、可塑剤、潤滑剤、結晶化速度遅延剤を重合反応時、またはその後の工程で添加しても良い。微粒子の種類は特に限定されず、例えばシリカ、アルミナ、酸化チタン、炭酸カルシウム、硫酸バリウムなどの不活性微粒子を添加することができ、これらは単独で使用しても2種類以上併用しても良く、紡糸性、延伸性が向上する場合がある。
The fiber constituting the short fiber of the present invention may contain a pigment. In this case, if the final product needs a light-colored system, that is, a color developability as a light color or a light color, a small amount of pigment is required, and the addition of the pigment inside the ultrafine fiber is at a low concentration. That is, when the color of the appearance required as the final product is light, the amount of pigment added to the inside of the ultrafine fibers is preferably 0 to 1% by mass, and in the case of medium color, 1 to 2% by mass is preferable, and the dark color In this case, the content is preferably 2 to 5% by mass, and if it exceeds 5% by mass, the spinning processability is inferior, the fiber strength is lowered, and the resulting tear strength of the artificial leather is inferior.
As the pigment to be used, for example, inorganic pigments such as titanium oxide, carbon black, chrome red, and molybdenum red, and organic pigments such as phthalocyanine-based and anthraquinone-based organic pigments that are usually used for polymer deposition can be used. In particular, when carbon black is used, the average primary particle size of carbon black is determined from the fact that carbon black is mixed and integrated in the polymer constituting the ultrafine fiber and is easily embedded in the polymer constituting the ultrafine fiber. Is preferably 10 to 60 nm. When the average primary particle size of the carbon black is less than 10 nm, it is difficult to obtain uniform fibers due to the tendency of the carbon black to aggregate during spinning, and the quality stability of color spots, physical spots, etc. This problem tends to occur, and the spinnability tends to decrease. Conversely, when the average primary particle size of carbon black exceeds 60 nm, when the resulting artificial leather is suede, the light fastness and color developability tend to decrease, and the filter is clogged during the spinning process. Tends to occur and the spinnability tends to decrease. Carbon black generally exists as an aggregate of a plurality of primary particles (hereinafter referred to as an aggregate), but carbon black is present in a mixed and integrated manner in the polymer constituting the ultrafine fiber, and mainly contains the ultrafine fiber. The average particle diameter of the aggregate is more preferably 20 to 200 nm because it is easily embedded in the polymer constituting it and has good color developability, light fastness and spinnability. In addition, in other inorganic pigments and organic pigments, the average particle size is more preferably 20 to 200 nm for the same reason.
In addition, as a method for adding the pigment, in order to improve the dispersibility of the pigment in the polymer constituting the ultrafine fiber, the polymer and the pigment constituting the ultrafine fiber are kneaded using a compound facility such as an extruder and then pelletized. It is preferable to adopt the master batch method. In addition, a stabilizer such as a copper compound, a colorant, an ultraviolet absorber, a light stabilizer, an antioxidant, an antistatic agent, a flame retardant, and a plasticizer are included in the ultrafine fiber component as long as the purpose and effect of the present invention are not impaired. Further, a lubricant and a crystallization rate retarder may be added during the polymerization reaction or in the subsequent steps. The type of fine particles is not particularly limited, and for example, inert fine particles such as silica, alumina, titanium oxide, calcium carbonate, and barium sulfate can be added. These may be used alone or in combination of two or more. In some cases, spinnability and stretchability may be improved.
上記の極細繊維発生型繊維は紡出した後通常延伸するが、紡糸ノズルから吐出された後一旦捲き取りその後延伸する場合と、巻き取る前に延伸する場合があり、いずれの方法でもよい。延伸方法は通常熱延伸されるが、熱風、熱板、熱ローラー、水浴などのいずれを用いて行ってもよい。ただし、極細繊維発生型繊維の一成分を水溶性高分子成分とする場合は、水分の影響の少ない熱風で延伸することが好ましい。
本発明では人工皮革の目付斑、厚み斑を改善し、さらに人工皮革の品位を損なわず、形態安定性に優れたものとするため、製造工程通過時の縦伸びを抑制する必要があり、このため織編物を挿入する必要がある。その際、形態安定性が良好となるため、短繊維と一体構造を形成しやすい織編物を用いることが重要である。また人工皮革製造にあたり繊維絡合体内部に高分子弾性体が付与されている必要があるが、高分子弾性体は空隙無く織編物を直接把持し人工皮革を硬化してしまうため、本発明では人工皮革の硬化を抑制するため、織編物を水抽出で簡便に除去できる繊維である必要がある。仮に水抽出不可能であれば、織編物除去の際、バフィングなどの研削によって処理せざるを得なくなり表面状態が不必要に荒れることで製品の表面外観を大きく損ねてしまう恐れがあり、また研削する必要の無い短繊維も研削せざるを得なくなり全体の研削量が増加しコスト高になってしまう。あるいは仮に溶剤抽出可能な織編物であれば、溶剤抽出除去の際ディップ・ニップ処理を繰り返し行う必要があり、時間が多くかかるばかりか繰返し行うディップ・ニップ処理で人工皮革が圧縮され、膨らみ感に欠け、風合いの劣ったものとなってしまう。
The above-mentioned ultrafine fiber-generating fiber is usually drawn after spinning, but may be drawn once after being discharged from the spinning nozzle and then drawn, or may be drawn before winding, and any method may be used. The stretching method is usually hot stretching, but may be performed using any of hot air, a hot plate, a hot roller, a water bath, and the like. However, when one component of the ultrafine fiber-generating fiber is a water-soluble polymer component, it is preferable to draw with hot air that is less affected by moisture.
In the present invention, it is necessary to suppress the longitudinal elongation at the time of passing through the manufacturing process in order to improve the unevenness of the artificial leather and the unevenness of the thickness of the artificial leather, and further improve the shape stability without impairing the quality of the artificial leather. Therefore, it is necessary to insert a woven or knitted fabric. At that time, it is important to use a knitted or knitted fabric that can easily form a monolithic structure with the short fibers because the shape stability becomes good. Further, in the production of artificial leather, it is necessary that a polymer elastic body is provided inside the fiber entangled body. However, since the polymer elastic body directly holds the woven or knitted fabric without voids and hardens the artificial leather, in the present invention, In order to suppress the hardening of the leather, it is necessary that the fiber can be easily removed by water extraction. If water extraction is not possible, when removing the woven or knitted fabric, it must be treated by grinding such as buffing, and the surface condition may be unnecessarily roughened, and the surface appearance of the product may be greatly impaired. Short fibers that do not need to be ground must be ground, increasing the overall grinding amount and increasing the cost. Or if it is a woven or knitted fabric that can be extracted with a solvent, it is necessary to repeat the dip / nip process when removing the solvent, and it takes a lot of time, and the repeated dip / nip process compresses the artificial leather, resulting in a feeling of swelling. It will be chipped and inferior in texture.
なお、織編物を構成する繊維としては実質的に水抽出除去可能な繊維である必要が有り、その際用いられる水抽出成分としては、水溶液(水系溶剤と称することもある)で抽出処理できるポリマーであれば、公知のポリマーが使用できるが、水系溶剤で溶解可能なポリビニルアルコール共重合体類(以下PVAと略することもある)を用いることが好ましく、短繊維ウェブに用いられている前述のPVAであることが好ましい。
さらに短繊維を構成する極細発生型繊維が水溶性高分子成分を用いている場合、織編物を構成する水溶性高分子成分と同一であることから水抽出除去の工程が1回ですみ効率がよく、不必要な負荷をかけることによる風合の低下や目付け斑の発生を抑制する点でより好ましい。
また本発明の上記の繊維から構成されている織編物は、短繊維ウェブと一体構造を形成させるため、該織編物の撚数として10〜650T/mが好ましく、15〜500T/mがより好ましい。10T/m未満では短繊維ウェブと絡合した場合に織編物の単糸が完全にばらけてしまい、損傷した糸が表面へ大きく露出してしまう。織編物は最終的に抽出除去されるため製品において織編物そのものが外観へ影響を及ぼすことは無いが、織編物が大きく露出している場合は抽出除去後に抽出跡が残るため表面に凹凸斑が発生し易く、結果的に外観を悪化させる恐れがある。また撚数が650T/mを越えると短繊維と織編物が強固に絡合した一体構造が得られにくく、収縮処理において短繊維と織編物とに収縮差が生じる場合は繊維絡合体にしわが発生する恐れがあり、加えて収縮差により目付斑を生じ、さらには織編物を抽出除去後の製品が不均一なものとなり、天然皮革ライクの風合いを得るためには不適当である。また織編物の目付けは、目的に応じて適宜設定可能であるが、20〜200g/m2であることが好ましく、30〜150g/m2がより好ましい。目付けが20g/m2未満になると織編物としての形態が極めてルーズになり、目ずれなど織物の形態安定性に欠け、また、目付けが200g/m2を越えると織編物が密になり、不織ウェブの貫通が不充分で、高絡合化が進まず不離一体化した構造物を作るのが困難になる。また、織編物の種類としては、経編、トリコット編で代表される緯編、レース編およびそれらの編み方を基本とした各種の編物、あるいは平織、綾織、朱子織およびそれらの織り方を基本とした各種の織物など特に限定されるものではない。組織、密度などいずれを選ぶかは目的により適宜決定すればよい。
The fiber constituting the woven or knitted fabric needs to be a fiber that can be substantially extracted by water extraction, and the water extraction component used at that time is a polymer that can be extracted with an aqueous solution (sometimes referred to as an aqueous solvent). In this case, known polymers can be used, but it is preferable to use polyvinyl alcohol copolymers (hereinafter sometimes abbreviated as PVA) that are soluble in an aqueous solvent, and are used for short fiber webs as described above. PVA is preferred.
Furthermore, when the ultrafine fiber that forms the short fiber uses a water-soluble polymer component, it is the same as the water-soluble polymer component that forms the woven or knitted fabric. Well, it is more preferable in that it suppresses the deterioration of texture and the occurrence of spotted spots caused by applying an unnecessary load.
Further, the woven or knitted fabric composed of the above-mentioned fibers of the present invention preferably forms 10 to 650 T / m, more preferably 15 to 500 T / m, as the number of twists of the woven or knitted fabric in order to form an integral structure with the short fiber web. . If it is less than 10 T / m, the single yarn of the knitted or knitted fabric is completely scattered when entangled with the short fiber web, and the damaged yarn is greatly exposed to the surface. Since the woven or knitted fabric is finally extracted and removed, the woven or knitted fabric itself does not affect the appearance of the product. It is likely to occur and as a result, the appearance may be deteriorated. When the twist number exceeds 650 T / m, it is difficult to obtain an integrated structure in which the short fibers and the woven or knitted fabric are entangled strongly, and when the shrinkage difference occurs between the short fibers and the woven or knitted fabric, the fiber entangled body is wrinkled. In addition, there is a texture difference due to a difference in shrinkage, and the product after extraction and removal of the woven or knitted fabric becomes non-uniform, which is inappropriate for obtaining a texture of natural leather-like. The woven or knitted fabric basis weight can be set as appropriate depending on the purpose, is preferably 20~200g / m 2, 30~150g / m 2 is more preferable. If the basis weight is less than 20 g / m 2 , the shape of the woven or knitted fabric becomes very loose, and the shape stability of the woven fabric such as misalignment is lacking. If the basis weight exceeds 200 g / m 2 , the woven or knitted fabric becomes dense, and the woven or knitted fabric becomes dense. The penetration of the woven web is insufficient, and high entanglement does not progress, making it difficult to produce a structure that is separated and integrated. As the types of woven and knitted fabrics, weft knitting represented by warp knitting and tricot knitting, lace knitting and various knittings based on these knitting methods, or plain weaving, twill weaving, satin weaving and weaving these The various woven fabrics are not particularly limited. Which one to select, such as tissue or density, may be determined appropriately according to the purpose.
そして、本発明の繊維積層絡合体としては、公知の方法を用いて絡合することができる。例えば、まず上記で得られる極細繊維発生型繊維を捲縮付与した後ステープル化し、カード、クロスラッパー、ランダムウエバー等により短繊維ウェブを形成する。そして、該短繊維ウェブの表層、下層、あるいは中間層に上記の実質的に水抽出除去可能な繊維からなる織編物を積層し、ニードルパンチにより繊維を絡ませる。ニードルパンチ条件としては、ニードル針のバーブが積層体の表面まで貫通するような条件でかつニードルパンチ数が400〜5000パンチ/cm2の条件が好ましく、より好ましくは1000〜2000パンチ/cm2の条件である。ニードルパンチは、不織布と織編物とを重ね合わせた積層物の両面から行うのが天然皮革用の外観を得る点で好ましい。すなわち、不織布の表面側に補強用織編物構成繊維をあるていど露出させるとともに織編物の表面側にも不織布構成繊維を露出させることが一体構造となった繊維積層絡合体を得やすい点で好ましい。 And it can entangle using a well-known method as a fiber lamination entanglement body of this invention. For example, the ultrafine fiber generating fiber obtained above is first crimped and then stapled, and a short fiber web is formed by a card, a cross wrapper, a random weber, or the like. Then, the woven or knitted fabric composed of the fibers that can be substantially removed by water extraction is laminated on the surface layer, the lower layer, or the intermediate layer of the short fiber web, and the fibers are entangled by needle punching. The needle punching condition is preferably such that the needle needle barb penetrates to the surface of the laminate and the number of needle punches is 400 to 5000 punch / cm 2 , more preferably 1000 to 2000 punch / cm 2 . It is a condition. Needle punching is preferably performed from both sides of a laminate in which a nonwoven fabric and a woven or knitted fabric are overlapped from the viewpoint of obtaining an appearance for natural leather. That is, it is preferable in that it is easy to obtain a fiber laminated entangled body having a monolithic structure in which the reinforcing knitted fabric constituting fibers are exposed on the surface side of the nonwoven fabric and the nonwoven fabric constituting fibers are exposed on the surface side of the woven or knitted fabric. .
得られた繊維積層絡合体は、繊維積層絡合体を熱収縮処理することで繊維の毛羽密度を増加させ風合い良好なものを得るにあたり収縮処理が必要であり、また必要に応じ熱プレスすることが好ましく、この収縮処理により布帛の面積を収縮前の40〜90%にする。この収縮処理により緻密構造が得られ、収縮の程度が収縮前の面積の90%以上となるような低い収縮では緻密感が得られず、風合い劣化となり、逆に収縮前の面積の40%未満となるような大きな収縮の場合には風合いが硬化し好ましくない。なお収縮処理は、上記絡合体を160〜200℃の雰囲気に0.5〜3分放置することにより好適に行なわれる。また前記したように、一般に収縮処理において短繊維と織編物とに収縮差が生じる場合は繊維絡合体にしわが発生する恐れがあるが、織編物が挿入され一体構造を有する場合はしわの発生を抑制できる利点があり、さらには織編物によって工程通過時の縦方向テンションによる縦伸びが抑制され、横のみならず縦方向の収縮が可能になるに伴い、横方向のみの過剰な収縮が抑制され均一に収縮しやすくなり、これに伴い厚み斑や目付斑の発生も抑制することが可能となる。 The obtained fiber laminate entangled body needs to be subjected to shrinkage treatment in order to increase the fluff density of the fiber by heat shrinking the fiber laminate entangled body to obtain a good texture, and may be hot pressed as necessary. Preferably, the area of the fabric is reduced to 40 to 90% before shrinkage by this shrinkage treatment. This shrinking treatment provides a dense structure, and the shrinkage is so low that the degree of shrinkage is 90% or more of the area before shrinkage, the feeling of denseness is not obtained, and the texture is deteriorated. Conversely, less than 40% of the area before shrinkage In the case of such large shrinkage, the texture is hardened, which is not preferable. The shrinkage treatment is preferably performed by leaving the entangled body in an atmosphere of 160 to 200 ° C. for 0.5 to 3 minutes. In addition, as described above, when there is a shrinkage difference between the short fiber and the woven or knitted fabric in the shrinking treatment, wrinkles may occur in the fiber entangled body. However, when the woven or knitted fabric has an integral structure, wrinkles are generated. There is an advantage that it can be suppressed, and further, the woven or knitted fabric suppresses the longitudinal elongation due to the longitudinal tension during the process passage, and the shrinkage not only in the transverse direction but also in the longitudinal direction is enabled, so that excessive shrinkage only in the transverse direction is suppressed. It becomes easy to shrink uniformly, and accordingly, it is possible to suppress the occurrence of thickness spots and spotted spots.
織編物を構成する各単繊維の表面露出度、すなわち織編物と短繊維からなる不織布とのの該織編物と接する反対側の面において、織編物を構成する各単繊維の表面露出度は0.3〜20%であることが好ましく、1〜15%がより好ましく、2〜10%がさらにより好ましい。0.3%未満では短繊維と織編物の絡合状態が弱く、強固に絡合された一体構造を有する絡合体とは異なり、収縮時にしわが発生しやすい。一方20%を越えると強固に絡合された一体構造を有する繊維積層絡合体は得られるものの外観は低下し易く、さらには織編物の損傷が大きいことから、織編物抽出後の最終製品において外観が低下しやすくなる。 The surface exposure degree of each single fiber constituting the woven or knitted fabric, that is, the surface exposure degree of each single fiber constituting the woven or knitted fabric is 0 on the surface opposite to the woven or knitted fabric between the woven and knitted fabric and the nonwoven fabric composed of short fibers. It is preferably 3 to 20%, more preferably 1 to 15%, still more preferably 2 to 10%. If it is less than 0.3%, the entangled state of the short fiber and the woven or knitted fabric is weak, and unlike an entangled body having a tightly entangled integral structure, wrinkles are likely to occur during shrinkage. On the other hand, if it exceeds 20%, a fiber laminated entangled body having a tightly entangled monolithic structure can be obtained, but the appearance tends to deteriorate, and the damage to the woven or knitted fabric is great, so the appearance in the final product after extraction of the woven or knitted fabric Tends to decrease.
なお、本発明で言う表面露出度の評価方法を次に説明する。
<減圧パラフィン包埋>
パラフィン mp68〜70℃
ホットプレート iuchi NHP−1
<ミクロトーム>
装置 MICROM社製 HM360
<顕微鏡>
装置 Nikon社製 SMZ1000
<方法>
1)得られた短繊維からなる不織布(A)と織編物(B)の絡合一体化物を減圧パラフィン包埋(約80℃ アスピレーター減圧)する。もちろん高分子弾性体が付与されていても良い。
2)ミクロトームで表層より約100μ程度、切削する。
3)光学顕微鏡で100倍に拡大し、さらにそれを2倍に拡大して写真を撮影
4)パソコンにて画像解析を実施し、不織布(A)側の面に存在する織編物構成繊維の面積(P)を計測する。(1cm×1cm)
表面露出度=100×P/(短繊維からなる不織布構成繊維+織編物構成繊維)面積
分母の(短繊維からなる不織布構成繊維+織編物構成繊維)面積の求め方としては、繊維絡合体の見かけ密度と繊維絡合体構成繊維の比重から構成繊維の占有割合を計算により求め、計算により求められた値を(短繊維からなる不織布構成繊維+織編物構成繊維)面積とする。なお、写真に織編物構成繊維が繊維断面としてではなく横方向に寝た状態で写っている場合には、その繊維は除外して面積を求める。
In addition, the evaluation method of the surface exposure degree said by this invention is demonstrated next.
<Embedded paraffin under reduced pressure>
Paraffin mp68-70 ° C
Hot plate uchi NHP-1
<Microtome>
Device HM360 manufactured by MICROM
<Microscope>
Device SMZ1000 manufactured by Nikon
<Method>
1) The entangled integrated product of the obtained nonwoven fabric (A) and woven or knitted fabric (B) is embedded in reduced-pressure paraffin (approximately 80 ° C., aspirator reduced pressure). Of course, a polymer elastic body may be provided.
2) Cut about 100μ from the surface with a microtome.
3) Magnify 100 times with an optical microscope, and further magnify it 2 times and take a picture 4) Perform image analysis with a personal computer, and the area of the woven / knitted fabric fibers on the nonwoven fabric (A) side (P) is measured. (1cm x 1cm)
Surface exposure degree = 100 × P / (nonwoven fabric constituting fiber composed of short fibers + woven fabric constituting fiber) area The method of obtaining the denominator (nonwoven fabric constituting fibers composed of short fibers + woven fabric constituting fibers) area is as follows: The occupation ratio of the constituent fibers is obtained from the apparent density and the specific gravity of the fiber-entangled constituent fibers, and the value obtained by the calculation is defined as (nonwoven fabric constituent fibers consisting of short fibers + woven / knitted constituent fibers) area. In addition, when the woven or knitted fabric constituting fiber is shown as lying in the horizontal direction instead of as a fiber cross section, the area is obtained by excluding the fiber.
本発明において、繊維積層絡合体へ高分子弾性体を付与する場合、ディップ・ニップ方式などの公知の技術を用いることができるが、環境に優しい点で高分子弾性体水分散液を用いることが好ましい。そして、水溶性高分子成分と水難溶性高分子成分からなる短繊維ウェブから構成された繊維積層絡合体へ高分子弾性体水分散液を含浸する組み合せの場合、ニップ処理した際に水溶性高分子成分が搾り出され、高分子弾性体水分散液が汚染される場合がある。この場合、水溶性高分子成分に対する高分子弾性体水分散液の浸透性と含浸圧力を併用し、高分子弾性体水分散液を大きく加圧すること無く、高分子弾性体水分散液供給量および濃度を制御するだけで所定量の樹脂含浸可能である樹脂含浸方法が好ましい。例えば、含浸装置には、繊維積層絡合体が含浸装置を通過する際の入口と出口にエッジを設け、さらに処理方向と垂直の方向すなわち繊維積層絡合体横断方向(巾方向)両側に側壁を設け、該エッジと該側壁で囲まれた液溜め室が形成されており、該液溜め室内のスリット状吐出口からポンプにより定量の高分子弾性体水分散液を繊維積層絡合体の内部に加圧浸透させて供給するものが好ましい。側壁は液溜め室の液体をシールできれば特に限定されないが、供給される高分子弾性体水分散液が繊維積層絡合体の両端から洩れることなく全て繊維積層絡合体内部へ浸透させるため、繊維積層絡合体横断方向両側に設けている側壁の間隔(高分子弾性体水分散液供給幅)は繊維積層絡合体幅よりも狭めておくことが好ましく、各側壁は各繊維絡合体サイドより5cm以上内側であることがより好ましい。そして該含浸装置は繊維積層絡合体の上方、あるいは下方、あるいは上下両方に設ける場合のいずれでもかまわないが、作業性およびコスト面から下方へ一箇所設置してあることが工業的に有利である。 In the present invention, when a polymer elastic body is imparted to the fiber laminate entangled body, a known technique such as a dip nip method can be used. However, an aqueous dispersion of a polymer elastic body is used in terms of environmental friendliness. preferable. In the case of a combination in which a fiber laminate entangled body composed of a short fiber web composed of a water-soluble polymer component and a poorly water-soluble polymer component is impregnated with an aqueous dispersion of a polymer elastic body, a water-soluble polymer is formed when nip treatment is performed. Ingredients may be squeezed out and the polymer elastic water dispersion may be contaminated. In this case, the permeability of the polymer elastic water dispersion to the water-soluble polymer component and the impregnation pressure are used together, and the polymer elastic water dispersion supply amount and A resin impregnation method capable of impregnating a predetermined amount of resin only by controlling the concentration is preferable. For example, the impregnation device is provided with edges at the inlet and outlet when the fiber laminate entanglement passes through the impregnation device, and further provided with side walls in the direction perpendicular to the processing direction, that is, in the transverse direction of the fiber laminate entanglement (width direction). A liquid reservoir chamber surrounded by the edge and the side wall is formed, and a predetermined amount of the polymer elastic body aqueous dispersion is pressurized into the fiber laminate entangled body by a pump from a slit-like discharge port in the liquid reservoir chamber. What is supplied by infiltration is preferred. The side wall is not particularly limited as long as the liquid in the liquid storage chamber can be sealed. It is preferable that the interval between the side walls provided on both sides in the crossing direction of the coalescence (supply width of the polymer elastic body aqueous dispersion) is narrower than the width of the fiber laminate entanglement, and each side wall is at least 5 cm inside from each fiber entanglement side. More preferably. The impregnation apparatus may be provided above, below, or both above and below the fiber laminate entangled body, but it is industrially advantageous that it is installed at one place downward from the viewpoint of workability and cost. .
前記した含浸方法は、繊維積層絡合体に対する高分子弾性体水分散液の浸透性と含浸圧力を調整することで、煩雑なプロセスを用いること無く、また含浸圧力を高めること無く、繊維積層絡合体の内部に高分子弾性体水分散液を均一な状態でかつ短時間で含浸処理することを可能とするものである。このため、まず高分子弾性体水分散液の浸透性に関しては、繊維積層絡合体への高分子弾性体水分散液の浸透時間は10秒以下であることが好ましく、5秒以下がより好ましく、2秒以下が更に好ましい。10秒を越える場合、繊維積層絡合体へ供給された全ての高分子弾性体水分散液が繊維積層絡合体内部へ均一にかつ十分に含浸しきれず、高分子弾性体水分散液が繊維積層絡合体供給面から溢れ溶液供給部周辺を汚染し、更には繊維積層絡合体内部での含浸樹脂量が不足したものとなり易い。
なお、ここでいう浸透時間とは、高分子弾性体水分散液と繊維積層絡合体の相対的な浸透時間をいい、含浸する高分子弾性体水分散液0.035ccを10cmの高さから繊維絡合体へ滴下し、滴下時より高分子弾性体水分散液が完全に浸透するまでの時間を測定したものである。また、完全に浸透するとは、高分子弾性体水分散液が繊維積層絡合体上に盛り上がった状態でなくなることを目視で確認できた状態をいう。そして、本発明の好適な浸透時間となるように適宜高分子弾性体水分散液の粘度や濃度を調整した後に処理すれば良い。繊維積層絡合体の密度が0.40〜0.90g/m3の場合、高分子弾性体水分散液の粘度は2〜80cpoiseが好ましく、濃度は30〜60%とする組み合せが浸透時間を10秒以下としやすい点で好ましい。また高分子弾性体水分散液濃度は、35〜50質量%であることがより好ましい。30質量%未満では乾燥工程でマイグレーションを生じやすく、また60質量%を越える場合、前記した浸透時間が増加傾向にあり、所定量の含浸樹脂量が低下する傾向がある。
また、繊維積層絡合体と高分子弾性体水分散液の粘度および濃度の組み合せが上記のままの組み合せで浸透時間が10秒を越える場合、浸透性向上のために高分子弾性体水分散液中へ界面活性剤を適宜添加して10秒以下とすることが良い。添加する界面活性剤としては、湿潤剤、浸透剤、レベリング剤など公知のものが使用でき、中でもスルホコハク酸ジー2−エチルヘキシルエステルナトリウム塩、スルホコハク酸ジオクチルエステルナトリウム塩、ドデシルベンゼンスルホン酸ナトリウム等のスルホン酸塩型アニオン界面活性剤:ラウリル硫酸エステルナトリウム、硫酸化オレイン酸ブチルエステルナトリウム塩、ジブチルナフタレンスルホン酸ナトリウム等の硫酸エステル塩型アニオン界面活性剤:ポリエチレングリコールーモノー4―ノニルフエニルエーテル、ポリエチレングリコールーモノーオクチルエーテル、ポリエチレングリコールーモノーデシルエーテル等のHLB価6〜16のポリエチレングリコール型ノニオン界面活性剤:フッ素系界面活性剤、シリコン系界面活性剤から選ばれる1種以上を用いることが好ましい。
The above impregnation method adjusts the permeability and impregnation pressure of the polymer elastomer aqueous dispersion to the fiber laminate entangled body, without using a complicated process, and without increasing the impregnation pressure. It is possible to impregnate the polymer elastic water dispersion in a uniform state in a short time. Therefore, first, with respect to the permeability of the polymer elastic water dispersion, the penetration time of the polymer elastic water dispersion into the fiber laminate entangled body is preferably 10 seconds or less, more preferably 5 seconds or less, More preferably 2 seconds or less. When the time exceeds 10 seconds, all of the polymer elastic water dispersion supplied to the fiber laminate entangled body cannot be uniformly and sufficiently impregnated inside the fiber laminate entangled body, and the polymer elastic body aqueous dispersion does not sufficiently penetrate the fiber laminate entangled body. It overflows from the united supply surface and contaminates the periphery of the solution supply unit, and further, the amount of impregnated resin inside the fiber laminate entangled unit tends to be insufficient.
In addition, the osmosis | permeation time here means the relative osmosis | permeation time of a polymeric elastic body aqueous dispersion and a fiber lamination | entanglement entanglement body. It is dropped into the entangled body, and the time from the time of dropping until the polymer elastic body aqueous dispersion completely penetrates is measured. Moreover, completely penetrating means a state in which it can be visually confirmed that the polymer elastic water dispersion is not raised on the fiber laminate entangled body. Then, the treatment may be carried out after appropriately adjusting the viscosity and concentration of the polymer elastomer aqueous dispersion so as to achieve a suitable infiltration time of the present invention. When the density of the fiber laminated entangled body is 0.40 to 0.90 g / m 3 , the viscosity of the polymer elastic body aqueous dispersion is preferably 2 to 80 cpoise, and the combination with a concentration of 30 to 60% has a penetration time of 10 This is preferable because it can be easily set to less than a second. The concentration of the elastic polymer aqueous dispersion is more preferably 35 to 50% by mass. If it is less than 30% by mass, migration tends to occur in the drying step, and if it exceeds 60% by mass, the above-mentioned permeation time tends to increase, and the amount of the impregnated resin tends to decrease.
In addition, when the combination of the viscosity and concentration of the fiber laminate entangled body and the polymer elastic water dispersion is the same combination as described above, and the penetration time exceeds 10 seconds, the polymer elastic water dispersion is used to improve the permeability. It is preferable to add a surfactant appropriately to 10 seconds or less. As the surfactant to be added, known ones such as a wetting agent, a penetrating agent and a leveling agent can be used. Among them, sulfones such as di-2-ethylhexyl sulfosuccinate sodium salt, dioctyl ester sodium sulfosuccinate and sodium dodecylbenzenesulfonate Acid salt type anionic surfactant: sulfate ester type anionic surfactants such as sodium lauryl sulfate ester, sulfated oleic acid butyl ester sodium salt, sodium dibutylnaphthalenesulfonate: polyethylene glycol mono-4-nonylphenyl ether, polyethylene Polyethylene glycol type nonionic surfactants having an HLB value of 6 to 16, such as glycol-mono-octyl ether and polyethylene glycol-mono-decyl ether: fluorinated surfactant, silicon-based surfactant It is preferred to use at least one member selected from the surface active agent.
前記した含浸方法においては、繊維積層絡合体に対する高分子弾性体水分散液の浸透性が前記の範囲を満足すると共に含浸圧力を調整する必要がある。特に繊維積層絡合体内部に高分子弾性体をより均一に含浸するためには繊維積層絡合体の密度や目付にもよるが、供給する高分子弾性体の含浸圧力は1,000〜100,000Paが好ましく、2,000〜80,000Paがより好ましく、2,000〜50,000Paがさらに好ましい。1,000Pa未満では供給する高分子弾性体水分散液を、人工皮革基体の繊維積層絡合体に対し高分子弾性体供給面から反対側まで充分浸透ができず、さらには得られる人工皮革基体の風合いが低下する。一方100,000Paを越える場合、浸透性は良好であるが供給される高分子弾性体が供給面から洩れを生じ、周囲が汚染され作業性が低下する。前記範囲の高分子弾性体水分散液の含浸圧力で含浸する繊維積層絡合体としては、高分子弾性体水分散液の浸透性が10秒以下である繊維積層絡合体を用いることが必要であり、繊維積層絡合体の密度が0.40〜0.90g/cm3、目付が600〜1500g/m2であることがより好ましい。なお、ここでいう高分子弾性体水分散液の含浸圧力とは、繊維積層絡合体へ接している液溜室内の圧力を指し、該液溜室へ液圧測定装置を設置しておくことで求めることができる。ここでの液圧測定装置は測定できるものであれば特に限定されない。 In the above-described impregnation method, it is necessary to adjust the impregnation pressure while the permeability of the polymer elastomer aqueous dispersion to the fiber laminated entangled body satisfies the above range. In particular, in order to more uniformly impregnate the polymer laminated body with the polymer elastic body, the impregnation pressure of the polymer elastic body to be supplied is 1,000 to 100,000 Pa, depending on the density and basis weight of the fiber laminated entangled body. Is preferable, 2,000-80,000 Pa is more preferable, and 2,000-50,000 Pa is more preferable. If it is less than 1,000 Pa, the polymer elastic water dispersion to be supplied cannot sufficiently permeate the fiber laminate entangled body of the artificial leather substrate from the polymer elastic material supply surface to the opposite side. The texture is reduced. On the other hand, when it exceeds 100,000 Pa, the permeability is good, but the supplied polymer elastic body leaks from the supply surface, the surroundings are contaminated, and the workability is lowered. As the fiber laminate entangled body impregnated with the impregnation pressure of the polymer elastic body aqueous dispersion in the above range, it is necessary to use a fiber laminate entangled body having a permeability of the polymer elastic body aqueous dispersion of 10 seconds or less. More preferably, the density of the fiber laminate entangled body is 0.40 to 0.90 g / cm 3 and the basis weight is 600 to 1500 g / m 2 . The impregnation pressure of the polymer elastic water dispersion here refers to the pressure in the reservoir chamber in contact with the fiber laminate entangled body, and a hydraulic pressure measuring device is installed in the reservoir chamber. Can be sought. The hydraulic pressure measuring device here is not particularly limited as long as it can measure.
本発明で繊維積層絡合体へ供給される高分子弾性体水分散液を構成する高分子弾性体としては、人工皮革に用いられる含浸用高分子弾性体であれば特に限定されないが、ウレタン系重合体、アクリル系重合体が好ましく用いられ、該重合体を水などの非溶剤中に分散させて得られる重合体分散液などが挙げられる。そして必要に応じて種々の有機系顔料および無機系顔料などを添加してもよく、その場合の有機顔料としては、例えばフタロシアニン系、アントラキノン系、キナクリドン系、ジオキサジン系、ぺリレン系、チオインジゴ系、アゾ系顔料等が挙げられ、また無機系顔料としては、酸化チタン、カーボンブラック、べんがら、クロムレッド、モリブデンレッド、リサージ、酸化鉄等が挙げられる。
また高分子弾性体水溶液を含浸した後、高分子弾性体を加熱凝固する。凝固する方法としては、公知の方法が挙げられるが、例えば、熱処理して乾式凝固、あるいは熱水処理、スチーム処理して感熱凝固する方法が好ましく挙げられる。
また本発明では、高分子弾性体水分散液に感熱ゲル化性化合物を添加する等の公知の方法で、繊維積層絡合体全体に均一に存在できるように高分子弾性体を凝固する方法を加えることがより好ましい。繊維積層絡合体全体に均一に存在できるように高分子弾性体を凝固する方法がより好ましい。
また、粘度としては高分子弾性体水分散液の浸透性が阻害されない範囲であればよく、上記のように、2〜80cpoiseが好ましく、5〜60cpoiseがより好ましく、10〜50cpoiseが更に好ましい。
The polymer elastic body constituting the polymer elastic body aqueous dispersion supplied to the fiber laminate entangled body in the present invention is not particularly limited as long as it is a polymer elastic body for impregnation used for artificial leather. Polymers and acrylic polymers are preferably used, and examples thereof include polymer dispersions obtained by dispersing the polymers in non-solvents such as water. If necessary, various organic pigments and inorganic pigments may be added. In this case, examples of the organic pigment include phthalocyanine, anthraquinone, quinacridone, dioxazine, perylene, thioindigo, Examples of the inorganic pigment include titanium oxide, carbon black, red pepper, chromium red, molybdenum red, resurge, and iron oxide.
Moreover, after impregnating the polymer elastic body aqueous solution, the polymer elastic body is heated and solidified. Examples of the solidification method include known methods. For example, a dry solidification by heat treatment or a method of heat-sensitive solidification by hot water treatment or steam treatment is preferable.
Further, in the present invention, a method of coagulating the polymer elastic body is added by a known method such as adding a thermosensitive gelling compound to the polymer elastic water dispersion so that it can be uniformly present in the entire fiber laminate entangled body. It is more preferable. A method of solidifying the polymer elastic body so that it can uniformly exist throughout the fiber laminate entangled body is more preferable.
Further, the viscosity may be in a range in which the permeability of the polymer elastic aqueous dispersion is not inhibited, and as described above, 2 to 80 cpoise is preferable, 5 to 60 cpoise is more preferable, and 10 to 50 cpoise is still more preferable.
そして繊維積層絡合体内部で均一な含浸を行うために、高分子弾性体水分散液の供給量が繊維積層絡合体空隙量の60〜100%であることが好ましく、70〜99%がより好ましい。なお、ここでいう繊維積層絡合体空隙量は、以下の計算方法によって求めることができる。
[繊維積層絡合体空隙量]
単位時間あたりに処理する繊維積層絡合体空隙量は以下の計算式より算出した。
A=DEFG×(C/D−1)/B
A(cm3/min) : 繊維積層絡合体空隙量
B(g/cm3) : 高分子弾性体水分散液の密度
C(g/cm3) : 繊維構成樹脂の密度
D(g/cm3) : 繊維積層絡合体の見掛け密度(短繊維密度×短繊維目付/繊維絡合体目付+織編物繊維密度×織編物目付/繊維絡合体目付)
E(cm) : 繊維積層絡合体の厚み
F(cm) : 高分子弾性体水分散液塗布幅
G(cm/min) : 走行速度
高分子弾性体水分散液の供給量が繊維積層絡合体空隙量の60%未満の場合、繊維積層絡合体の高分子弾性体分散液供給側とその反対側での含浸量が異なり、繊維積層絡合体内部での高分子弾性体分散液の分布が不均一となるため、該繊維積層絡合体からなる人工皮革用基体を人工皮革に仕上げた場合、皮革様の風合いとなり難く、さらにスエード調人工皮革に仕上げた場合の表面感が劣ったものとなり易い。一方、100%を越える場合、繊維積層絡合体内部での高分子弾性体分散液の分布は均一であるが、供給過剰のため繊維積層絡合体の高分子弾性体分散液供給面と反対の面から該高分子弾性体水分散液が溢れ、接するローラーなどの含浸設備を汚染するのみならず繊維積層絡合体の不必要な部分にまで高分子弾性体水分散液が付着してしまい、工程通過性や作業性に問題を生じる。
And in order to perform uniform impregnation inside the fiber laminate entangled body, the supply amount of the polymer elastic body aqueous dispersion is preferably 60 to 100%, more preferably 70 to 99% of the fiber laminate entangled body void amount. . The amount of voids in the fiber laminate entangled body here can be determined by the following calculation method.
[Air gap amount of fiber laminate entangled body]
The void amount of the fiber laminate entangled body processed per unit time was calculated from the following calculation formula.
A = DEFG × (C / D−1) / B
A (cm 3 / min): Fiber laminate entangled void volume B (g / cm 3 ): Density C (g / cm 3 ) of polymer elastomer aqueous dispersion: Density D (g / cm 3 ) of fiber constituent resin ): Apparent density of fiber laminate entangled body (short fiber density × short fiber basis weight / fiber entangled basis weight + woven / knitted fiber density × woven / knitted fabric basis / fiber entangled basis weight)
E (cm): Fiber laminate entangled body thickness F (cm): Polymer elastic body aqueous dispersion coating width G (cm / min): Travel speed The amount of polymer elastic body water dispersion supplied is the fiber laminate entangled air gap When the amount is less than 60%, the amount of impregnation on the polymer elastic dispersion dispersion supply side of the fiber laminate entangled body is different from that on the opposite side, and the distribution of the polymer elastic dispersion within the fiber laminate entanglement is uneven. Therefore, when the artificial leather base made of the fiber laminate entangled body is finished into artificial leather, it is difficult to have a leather-like texture, and the surface feeling when finished into suede-like artificial leather tends to be inferior. On the other hand, when it exceeds 100%, the distribution of the elastic polymer dispersion in the fiber laminate entangled body is uniform, but the surface opposite to the polymer elastic dispersion liquid supply surface of the fiber laminate entangled body due to excessive supply. The polymer elastic water dispersion overflows and contaminates the impregnation equipment such as the roller in contact with it, and the polymer elastic water dispersion adheres to unnecessary portions of the fiber laminate entangled body and passes through the process. Cause problems in workability and workability.
そして前記した含浸方法は、繊維積層絡合体が含浸直前に繊維積層絡合体厚みの40〜99%の間隙で圧縮されることが好ましく、70〜98%であることがより好ましい。繊維積層絡合体厚みの40%よりも強く圧縮されている場合、繊維積層絡合体と含浸装置の摩擦抵抗が大きく繊維積層絡合体の走行を阻害し、所定の速度で繊維積層絡合体が走行できないことから、繊維積層絡合体長さ方向における均一で安定な含浸が困難になる。また繊維積層絡合体厚みの99%を越える弱い圧縮では、繊維積層絡合体への高分子弾性体水分散液供給面から液が洩れやすく、含浸装置周囲が汚染されてしまい、また所定量供給された高分子弾性体水分散液が全て浸透できないことから高分子弾性体含浸量が計算による使用予定量より不足してしまう傾向がある。従って圧縮の間隙は広すぎても、狭すぎても均一で安定な含浸が困難な結果となる。なお含浸後に繊維積層絡合体を圧縮する場合、水溶性高分子が溶出することで高分子弾性体水分散液を汚染し、また極細繊維発生型繊維を構成する水溶性高分子成分が過剰に溶出すると水難溶性高分子成分が直接露出し易い傾向にあり、高分子弾性体水分散液中の高分子弾性体が極細繊維を直接把持し、得られる人工皮革の風合いが硬く劣ったものとなることから、含浸直前に繊維積層絡合体を圧縮し圧縮された状態にて含浸することが必要である。なお、供給された高分子弾性体水分散液が繊維積層絡合体内部へ浸透し所定量含浸したものに加え繊維積層絡合体供給面に過剰に付着することで表面層を形成してしまう場合には、繊維積層絡合体の出口にエッジを設けることによって、該表面層を除去することも可能である。
また前記した含浸方法は、高分子弾性体水分散液が浸透する時間を確保できれば生産速度を低下させなくとも処理が可能である。好ましくは2m/min以上であり、より好ましくは2〜10m/minであればよい。2m/min未満では高分子弾性体水分散液の浸透は充分可能であるが、処理速度が遅いことから生産性が低下してしまい、また10m/minを越える場合、浸透時間によっては供給された高分子弾性体水分散液を全て浸透しきれない場合が生じ、所定量の含浸が困難な場合を生じる懸念がある。また、含浸は可能であっても凝固乾燥が不十分となる懸念があり、これらが払拭されれば10m/分以上での処理も可能である。
また含浸される高分子弾性体水分散液は、高分子弾性体:繊維絡合体=5:95〜60:40の質量比となるように付与することが好ましい。人工皮革として仕上げる場合、高分子弾性体は繊維を結束するバインダーとしての効果を得るものであり、5質量%未満の場合、バインダー効果を充分満足できず、また60質量%を越える場合、前述した効果が得られるものの、引裂強力、引張強力などの物性が劣り、また風合いが固く劣ったものとなる。
In the impregnation method described above, the fiber laminate entangled body is preferably compressed at a gap of 40 to 99% of the fiber laminate entangled body thickness just before impregnation, and more preferably 70 to 98%. When compressed more than 40% of the fiber laminate entangled body thickness, the friction resistance between the fiber laminate entangled body and the impregnating device is large, and the fiber laminate entangled body cannot be run at a predetermined speed. Therefore, uniform and stable impregnation in the length direction of the fiber laminate entangled body becomes difficult. In addition, when the compression is weaker than 99% of the fiber laminate entanglement thickness, the liquid is easily leaked from the supply surface of the polymer elastomer aqueous dispersion to the fiber laminate entanglement, the surroundings of the impregnation apparatus are contaminated, and a predetermined amount is supplied. In addition, since all of the polymer elastic water dispersion cannot permeate, there is a tendency that the amount of impregnation of the polymer elastic body is insufficient from the estimated amount of use by calculation. Accordingly, if the compression gap is too wide or too narrow, uniform and stable impregnation is difficult. When compressing the fiber laminate entangled body after impregnation, the water-soluble polymer is eluted to contaminate the polymer elastic water dispersion, and the water-soluble polymer component constituting the ultrafine fiber-generating fiber is excessively eluted. Then, the poorly water-soluble polymer component tends to be directly exposed, the polymer elastic body in the polymer elastic body aqueous dispersion directly grips the ultrafine fibers, and the resulting artificial leather has a hard and inferior texture. Therefore, it is necessary to impregnate the fiber laminate entangled body in a compressed state immediately before impregnation. In addition, in the case where the surface layer is formed by excessively adhering to the fiber laminate entangled body supply surface in addition to the polymer polymer aqueous dispersion dispersed in the fiber laminate entangled body soaked and impregnated with a predetermined amount It is also possible to remove the surface layer by providing an edge at the exit of the fiber laminate entangled body.
Further, the above impregnation method can be processed without reducing the production rate as long as the time for the polymer elastic water dispersion to permeate can be secured. Preferably it is 2 m / min or more, More preferably, it should just be 2-10 m / min. If it is less than 2 m / min, penetration of the polymer elastic water dispersion is sufficiently possible, but the productivity is lowered due to slow processing speed, and if it exceeds 10 m / min, it is supplied depending on the penetration time. There may be a case where the entire polymer elastic body aqueous dispersion cannot be completely penetrated, and there is a concern that a predetermined amount of impregnation is difficult. Moreover, even if impregnation is possible, there is a concern that coagulation and drying will be insufficient, and if these are wiped away, treatment at 10 m / min or more is possible.
Moreover, it is preferable to provide the polymer elastic body aqueous dispersion to be impregnated so that the mass ratio of polymer elastic body: fiber entangled body = 5: 95 to 60:40. When finished as artificial leather, the polymer elastic body obtains an effect as a binder for binding fibers. When the amount is less than 5% by mass, the binder effect cannot be sufficiently satisfied. Although the effect is obtained, the physical properties such as tear strength and tensile strength are inferior, and the texture is hard and inferior.
本発明では、前記したように、短繊維として極細繊維発生型繊維を用いた場合、該繊維からなる繊維積層絡合体へ高分子弾性体水分散液を含浸した後、極細繊維および高分子弾性体の非溶剤でありかつ抽出除去成分の溶剤である処理液で抽出除去成分を除去し、極細繊維発生型繊維を極細化する。特に抽出除去する場合、環境問題の点から、あるいは水抽出可能な織編物を同時に抽出除去できる点から、熱水、アルカリ液などの水系溶媒で抽出除去成分を除去して極細繊維発生型繊維を極細化する方法が好ましい。特に熱水にて抽出除去する場合は、熱水温度として60〜100℃の温度が好ましく、80〜95℃がより好ましい。60℃未満では水溶性高分子の除去に時間を要することから熱水温度は高いほど好ましい。しかし100℃を越える温度を付与した際、樹脂と繊維の結束がゆるみ易く、樹脂が有する繊維把持性の低下が懸念されるため100℃以下の範囲が好ましい。
なお織編物が繊維積層絡合体の中間付近に存在する場合、織編物を抽出除去することで内部にある程度の空隙ができるが、繊維積層絡合体織編物中の織編物は短繊維と密に絡合していることから高分子弾性体が少なく、わずかに存在する高分子弾性体は大きな連続層を形成しにくい状態となる。従って内部の空隙は適度に潰れ、織編物が存在しない箇所と構造的に変わらないものとなり、外観、風合および物性にほとんど影響を及ぼさない。また織編物が繊維積層絡合体の中間付近に存在する場合、織編物に若干付着した樹脂は上記した通り大きな連続層を形成していないため、織編物を水抽出すると共に若干脱落するものの、短繊維に付着した樹脂は繊維積層絡合体へ残り、短繊維をしっかり把持している。従って織編物が繊維積層絡合体内部、表層いずれに存在している場合も、織編物を水抽出除去後の表面が荒れることはないため、改めてバフ処理などの追加処理は不要である。
In the present invention, as described above, when the ultrafine fiber generating fiber is used as the short fiber, the fiber laminate entangled body made of the fiber is impregnated with the polymer elastic body aqueous dispersion, and then the ultrafine fiber and the polymer elastic body are used. The extraction and removal component is removed with a treatment liquid that is a non-solvent and a solvent of the extraction and removal component, and the ultrafine fiber-generating fiber is made ultrafine. In particular, when extracting and removing, from the point of view of environmental problems or the ability to extract and remove water-extractable knitted fabrics at the same time, the extraction and removal components are removed with an aqueous solvent such as hot water or alkaline liquid to obtain ultrafine fiber-generating fibers. A method of ultra-thinning is preferable. In particular, when extracting and removing with hot water, the hot water temperature is preferably 60 to 100 ° C, more preferably 80 to 95 ° C. When the temperature is lower than 60 ° C., it takes time to remove the water-soluble polymer, so that the hot water temperature is preferably higher. However, when a temperature exceeding 100 ° C. is applied, the binding between the resin and the fiber is easy to loosen, and there is a concern that the fiber gripping property of the resin may be lowered.
If the woven or knitted fabric is present near the middle of the fiber laminate entanglement, a certain amount of voids can be created by extracting and removing the woven or knitted fabric, but the woven or knitted fabric in the fiber laminate entangled fabric is closely entangled with short fibers. Since the polymer elastic bodies are combined, there are few polymer elastic bodies, and the slightly existing polymer elastic bodies are in a state where it is difficult to form a large continuous layer. Accordingly, the internal voids are appropriately crushed and are not structurally different from those where no knitted or knitted fabric exists, and hardly affect the appearance, texture and physical properties. Also, when the woven or knitted fabric is present in the middle of the fiber laminated entangled body, the resin slightly adhered to the woven or knitted fabric does not form a large continuous layer as described above. The resin adhering to the fibers remains on the fiber laminated entangled body, and holds the short fibers firmly. Therefore, even when the woven or knitted fabric is present in the fiber laminate entangled body or on the surface layer, the surface after the water-extraction removal of the woven or knitted fabric is not roughened, so that additional processing such as buffing is unnecessary.
本発明では、必要に応じて所望の厚みに加圧加熱処理や分割処理などで厚みあわせを行う。また、短繊維少なくとも一面をバフィング処理等の起毛処理を施し、極細繊維を主体とした極細繊維立毛面を形成させてスエード調人工皮革としてもよい。なお短繊維が極細繊維発生型繊維である場合、極細繊維発生型繊維を極細化する前あるいは後にバフィング処理等の起毛処理を施せばよい。またその場合、必要により、揉み柔軟化処理、逆シールのブラッシングなどの仕上げ処理を行うことができる。本発明で得られるスエード調人工皮革は、目付斑が少ないため製品の幅方向での繊維量がそろっており、その結果両端部と中央部での色斑が抑制されていることから、収縮による風合いの充実感が得られると同時に発色斑のない良好な品質のものが得られる。 In the present invention, the thickness is adjusted to a desired thickness by pressure heating treatment or division treatment as necessary. Further, at least one surface of the short fiber may be subjected to a raising process such as a buffing process to form an ultrafine fiber raised surface mainly composed of an ultrafine fiber to form a suede-like artificial leather. When the short fiber is an ultrafine fiber generating fiber, a raising process such as a buffing process may be performed before or after the ultrafine fiber generating fiber is ultrafine. In that case, finishing treatment such as stagnation softening and reverse seal brushing can be performed as necessary. Since the suede-like artificial leather obtained in the present invention has less spotted spots, the amount of fibers in the width direction of the product is uniform, and as a result, color spots at both ends and the center are suppressed. A feeling of fullness can be obtained, and at the same time, a good quality without colored spots can be obtained.
本発明において、得られる人工皮革の密度は0.50〜0.85g/cm3であることが好ましい。密度が0.50g/cm3より小さい場合には、引裂強度などの物性が劣ることとなり、また密度が0.85g/cm3より大きい場合には、柔軟性に劣り、風合いが悪化する。好ましくは、0.53〜0.80g/cm3の範囲である。従来の人工皮革の密度は0.3〜0.45g/cm3の範囲であり、本発明の人工皮革は非常に高いと言え、この密度が高いことが本発明の人工皮革に天然皮革に告示した風合いや充実感、ドレープ性、優れた機械的物性をもたらす。 In the present invention, the density of the obtained artificial leather is preferably 0.50 to 0.85 g / cm 3 . When the density is less than 0.50 g / cm 3 , physical properties such as tear strength are inferior. When the density is greater than 0.85 g / cm 3 , the flexibility is inferior and the texture is deteriorated. Preferably, it is the range of 0.53-0.80 g / cm < 3 >. The density of conventional artificial leather is in the range of 0.3 to 0.45 g / cm 3 , and it can be said that the artificial leather of the present invention is very high, and this high density is notified to the artificial leather of the present invention to natural leather. It provides a smooth texture, fullness, drape, and excellent mechanical properties.
本発明の人工皮革は、必要に応じて樹脂層を付与して、銀付き調あるいは半銀付き調の人工皮革とすることもできる。また、表面を加熱し、平滑面に押圧することにより不織布表層部を溶融して樹脂層とすることもできる。表面に付与する樹脂としては、ポリウレタンやアクリルで代表される弾性重合体が好適に用いられる。また、極少量の染料あるいは少量の顔料を用いて着色処理を行っても良い。また、必要に応じて、本発明の人工皮革を上層に使用し、編物あるいは編物を下層となるよう貼り合わせたり、あるいは、本発明の立毛調人工皮革を上層に使用し、該立毛調人工皮革を構成する繊維とは異種の繊維からなる層を下層となるよう貼り合わせたりしても構わない。 The artificial leather of the present invention can be provided with a resin layer as necessary to obtain an artificial leather with a tone with silver or with a semi-silver. Moreover, the nonwoven fabric surface layer part can be melted to form a resin layer by heating the surface and pressing it on a smooth surface. As the resin applied to the surface, an elastic polymer typified by polyurethane or acrylic is preferably used. Further, the coloring treatment may be performed using a very small amount of dye or a small amount of pigment. Further, if necessary, the artificial leather of the present invention is used as an upper layer, and a knitted fabric or a knitted fabric is bonded together as a lower layer, or the raised nail artificial leather of the present invention is used as an upper layer, and the napped-toned artificial leather A layer made of a different kind of fiber from the fibers constituting the layer may be bonded to form a lower layer.
以下、実施例により本発明を具体的に説明するが、本発明はこれらの実施例によってなんら限定されるものではない。なお以下の実施例、比較例中に記載されている性能測定などの評価は以下の方法で行った。 EXAMPLES Hereinafter, although an Example demonstrates this invention concretely, this invention is not limited at all by these Examples. Evaluations such as performance measurement described in the following examples and comparative examples were performed by the following methods.
カーボンブラックを0.5質量%添加したイソフタル酸10モル%共重合ポリエチレンテレフタレート(融点234℃)を島成分とし、エチレン単位10モル%含有し、けん化度98.4モル%、融点210℃のポリビニルアルコール共重合体(株式会社クラレ製 エクセバール)を海成分とし、質量比を海/島=30/70とした64島の海島繊維を複合紡糸した後、延伸することで単糸繊度5.5dtex、密度1.27g/cm3の繊維を得た。この繊維を捲縮処理した後51mmへカットし、カード処理することで目付200g/m2の短繊維ウェブを作成した。 Polyvinyl terephthalate containing 10 mol% of isophthalic acid (melting point 234 ° C) to which 0.5% by mass of carbon black is added is an island component, contains 10 mol% of ethylene units, has a saponification degree of 98.4 mol%, and a melting point of 210 ° C. A single yarn fineness of 5.5 dtex was obtained by subjecting an alcohol copolymer (Exebar, manufactured by Kuraray Co., Ltd.) to sea components and a composite spinning of 64 islands of islands with a mass ratio of sea / island = 30/70, followed by stretching. A fiber with a density of 1.27 g / cm 3 was obtained. The fiber was crimped, cut to 51 mm, and carded to prepare a short fiber web having a basis weight of 200 g / m 2 .
次に、エチレン単位10モル%含有し、けん化度98.4モル%、融点210℃のポリビニルアルコール共重合体(株式会社クラレ製 エクセバール)を紡糸し、ローラープレート方式で通常の条件により延伸することで単糸繊度3.1dtex、密度1.25g/cm3の繊維を得た。この繊維で目付80g/m2の織物を作成した。 Next, a polyvinyl alcohol copolymer containing 10 mol% of ethylene units, having a saponification degree of 98.4 mol% and a melting point of 210 ° C. (Exeval manufactured by Kuraray Co., Ltd.) is spun and stretched under normal conditions by a roller plate method. Thus, a fiber having a single yarn fineness of 3.1 dtex and a density of 1.25 g / cm 3 was obtained. A woven fabric having a weight per unit area of 80 g / m 2 was prepared from this fiber.
上記ウェブ2枚を予め重ね、その下にスクリムを積層した後2500パンチ/cm2の条件でニードルパンチ処理を行った。次に205℃の熱収縮処理により30%面積収縮(面積保持率70%)させ、さらに175℃熱プレスすることで目付け630g/m2、見掛け密度0.75g/cm3、厚み0.84mmの繊維積層絡合体を得た。またこの繊維積層絡合体における織編物繊維の表面露出度は2.0%であった。 The two webs were stacked in advance, and a scrim was stacked thereunder, and then needle punching was performed under the condition of 2500 punch / cm 2 . Next, the film was shrunk by 30% by a heat shrink process at 205 ° C. (area retention rate 70%), and further heat-pressed at 175 ° C. to have a basis weight of 630 g / m 2 , an apparent density of 0.75 g / cm 3 and a thickness of 0.84 mm. A fiber laminate entangled body was obtained. Moreover, the surface exposure degree of the woven or knitted fiber in this fiber laminated entangled body was 2.0%.
次にグレー水分散顔料(大日本インキ化学工業株式会社製 RyudyeWグレー)とエーテル系ポリウレタン水分散エマルジョン (日華化学株式会社製 エバファノールAP−12)を顔料/エマルジョン=1.8/100の固形分質量比に混合し、濃度40質量%、粘度20cpoise、密度1.02g/cm3の高分子弾性体水分散液を得た。 Next, a gray water-dispersed pigment (Ryudye W gray, manufactured by Dainippon Ink & Chemicals, Inc.) and an ether-based polyurethane water-dispersed emulsion (Evaphanol AP-12, manufactured by Nikka Chemical Co., Ltd.) have a solid content of pigment / emulsion = 1.8 / 100. The mixture was mixed in a mass ratio to obtain a polymer elastic water dispersion having a concentration of 40% by mass, a viscosity of 20 cpoise, and a density of 1.02 g / cm 3 .
次に含浸設備としてリップコーター設備(株式会社ヒラノテクシード製 リップダイレト方式)を用い、B(高分子弾性体水分散液の密度):1.02g/cm3、C(繊維構成樹脂の密度):1.26g/cm3、D(繊維絡合体の見掛け密度)0.75g/cm3、E(繊維絡合体の厚み):0.84mm、F(高分子弾性体水分散液塗布幅):170cm、G(走行速度):2.5m/minより算出されたA(繊維絡合体空隙量)1733cm3/minの80%に相当する量の高分子弾性体水分散液を極細繊維化された繊維絡合体/高分子弾性体=74/26の質量比となるように含浸した。その直後160℃の熱風乾燥機で3分30秒間加熱凝固乾燥した。その後、両サイド5cmの未含浸個所をカットし、90℃の熱水でポリビニルアルコール共重合体成分を抽出することで人工皮革用基体を得た。得られた人工皮革用基体はシワ、伸びの発生が無く良好な外観であり、皮革様の均一な風合いや優れた物性を有する人工皮革用基体であった。得られた人工皮革要基体の表面をバフィングにより起毛処理を行って、スエード調の人工皮革を得た。 Next, a lip coater equipment (a lip direct system manufactured by Hirano Techseed Co., Ltd.) was used as the impregnation equipment, B (density of the polymer elastic body aqueous dispersion): 1.02 g / cm 3 , C (density of the fiber constituent resin): 1. 26 g / cm 3 , D (apparent density of fiber entangled body) 0.75 g / cm 3 , E (thickness of fiber entangled body): 0.84 mm, F (polymer elastic body aqueous dispersion coating width): 170 cm, G (Running speed): Fiber entangled body obtained by ultrafine fiber formation of a polymer elastic body aqueous dispersion in an amount corresponding to 80% of A (fiber entangled void amount) 1733 cm 3 / min calculated from 2.5 m / min / Polymer elastic body = impregnated so as to have a mass ratio of 74/26. Immediately after that, the mixture was heated and solidified and dried in a hot air dryer at 160 ° C. for 3 minutes 30 seconds. Thereafter, unimpregnated portions of 5 cm on both sides were cut, and a polyvinyl alcohol copolymer component was extracted with hot water at 90 ° C. to obtain a base for artificial leather. The obtained substrate for artificial leather had a good appearance with no wrinkles or elongation, and was a substrate for artificial leather having a uniform leather-like texture and excellent physical properties. The surface of the obtained artificial leather essential substrate was subjected to raising treatment by buffing to obtain a suede-like artificial leather.
次に分散染料としてSumikaron UL染料(住友化学株式会社製)のYellow 3RF 0.24owf%、Red GF 0.34owf%、Blue GF 0.70owf%、アンチフェードMC−500(明成化学株式会社製)、2owf%、ディスパーTL(明成化学株式会社製)1g/Lを用い130℃高圧染色を行った。人工皮革製造にあたり、繊維積層絡合体熱収縮後から染色処理後までの形態変化が縦×横=102%×98%と少ないものであった。得られたスエード調人工皮革は充実感があり、中央部と両端部との目付差は20g/m2と少ないものであった。そして、両端部と中央部で色斑が無く灰色の発色性に優れ、かつスエード感、ドレープ性などの風合いに優れたものであった。 Next, Sumikaron UL dye (manufactured by Sumitomo Chemical Co., Ltd.) Yellow 3RF 0.24 owf%, Red GF 0.34 owf%, Blue GF 0.70 owf%, Antifade MC-500 (manufactured by Meisei Chemical Co., Ltd.), High pressure dyeing was performed at 130 ° C. using 2 ow% and Disper TL (manufactured by Meisei Chemical Co., Ltd.) 1 g / L. In the production of artificial leather, the change in form from the heat shrinkage of the fiber laminate entangled body to after the dyeing treatment was as small as length × width = 102% × 98%. The obtained suede-like artificial leather had a sense of fulfillment, and the basis weight difference between the center and both ends was as small as 20 g / m 2 . In addition, there was no color unevenness at both ends and the center, and the color development of gray was excellent, and the texture such as suede feeling and drape was excellent.
(織編物成分変更)
目付け100g/m2の織物を用いる以外は実施例1と同様の操作を行った。その結果、得られたスエード調人工皮革は充実感があり、該スエード調人工皮革の中央部と両端部との目付差は15g/m2と少ないものであった。そして、両端部と中央部で色斑が無く灰色の発色性に優れ、かつスエード感、ドレープ性などの風合いに優れたものであった。
(Weaving and knitting composition change)
The same operation as in Example 1 was performed except that a fabric with a basis weight of 100 g / m 2 was used. As a result, the obtained suede-like artificial leather had a sense of fulfillment, and the basis weight difference between the central portion and both ends of the suede-like artificial leather was as small as 15 g / m 2 . In addition, there was no color unevenness at both ends and the center, and the color development of gray was excellent, and the texture such as suede feeling and drape was excellent.
(短繊維構成海成分変更)
短繊維の海成分をポリエチレンとする以外は実施例1と同様にして繊維積層絡合体を製造した。次に90℃で熱水収縮処理を行った後、高分子弾性体としてポリウレタンDMF溶液をディップ・ニップ方式にて含浸し、その後トルエンでポリエチレンを抽出した以外は実施例1と同様の操作を行った。その結果、得られたスエード調人工皮革は充実感があり、該スエード調人工皮革の中央部と両端部との目付差は19g/m2と少ないものであった。そして、両端部と中央部で色斑が無く灰色の発色性に優れ、かつスエード感、ドレープ性などの風合いに優れたものであった。
(Short fiber component sea component change)
A fiber laminate entangled body was produced in the same manner as in Example 1 except that the short fiber sea component was polyethylene. Next, after performing a hot water shrinkage treatment at 90 ° C., the same operation as in Example 1 was performed except that a polyurethane DMF solution was impregnated as a polymer elastic body by a dip-nip method, and then polyethylene was extracted with toluene. It was. As a result, the obtained suede-like artificial leather had a sense of fulfillment, and the difference in basis weight between the center and both ends of the suede-like artificial leather was as small as 19 g / m 2 . In addition, there was no color unevenness at both ends and the center, and the color development of gray was excellent, and the texture such as suede feeling and drape was excellent.
(収縮率変更)
熱収縮処理を190℃で実施し、25%面積収縮(面積保持率70%)させた以外は実施例1と同様の操作を行った。得られたスエード調人工皮革は充実感があり、両端部と中央部で色斑が無く灰色の発色性に優れ、かつスエード感、ドレープ性などの風合いに優れたものであった。
(Shrinkage rate change)
The same operation as in Example 1 was performed except that the heat shrink treatment was performed at 190 ° C. and the area was shrunk by 25% (area retention rate: 70%). The obtained suede-like artificial leather had a feeling of solidity, had no color spots at both ends and the center, and was excellent in gray color development, and was excellent in texture such as suede and drape.
(繊維積層体密度変更)
熱収縮処理後に185℃で熱プレスを行い、繊維積層絡合体の密度を0.87g/cm3とする以外は実施例1と同様の操作を行った。その結果、スエード調人工皮革製造工程においてしわ、折れなどが無く、繊維積層絡合体熱収縮後から染色処理後までの形態変化が縦×横=101%×99%と少ないものであった。得られたスエード調人工皮革は両端部と中央部で色斑が無く灰色の発色性に優れ、かつスエード感、ドレープ性などの風合いに優れたものであった。
(Fiber laminate density change)
A heat press was performed at 185 ° C. after the heat shrink treatment, and the same operation as in Example 1 was performed except that the density of the fiber laminate entangled body was 0.87 g / cm 3 . As a result, there was no wrinkle or crease in the suede-like artificial leather manufacturing process, and the shape change from after the heat shrinkage of the fiber laminate entangled body to after the dyeing treatment was as small as vertical × horizontal = 101% × 99%. The obtained suede-like artificial leather had no gray spots at both ends and the central part, was excellent in gray color development, and was excellent in texture such as suede feeling and drape.
比較例1(織編物変更)
ポリエチレンからなる目付80g/m2の織物を用い、該織物の除去方法を熱トルエン抽出法で行った以外は実施例1と同様の操作を行った。その結果、スエード調人工皮革製造工程において、しわ、折れなどなく、形態安定性にも優れていた。しかしこの織編物を除去する際、トルエン抽出したところ、ポリエチレン抽出のため繰り返しディップ・ニップ処理が必要であり、処理時間が多くかかるばかりかディップ・ニップ処理で人工皮革用基体が大きく圧縮され、得られたスエード調人工皮革は中央部と両端部との目付差は15g/m2と差が少ないものであったが、膨らみ感に欠け風合いの劣ったものであった。
Comparative example 1 (weaving / knitting change)
Using fabric having a basis weight of 80 g / m 2 made of polyethylene, except that the method for removing fabric was carried out with hot toluene extraction method were carried out in the same manner as in Example 1. As a result, in the suede-like artificial leather manufacturing process, there was no wrinkle or crease, and the form stability was excellent. However, when this woven or knitted fabric is removed, extraction with toluene requires repeated dip / nip treatment for polyethylene extraction, which not only takes a lot of processing time, but also the substrate for artificial leather is greatly compressed by dip / nip treatment. The obtained suede-like artificial leather had a difference in basis weight of 15 g / m 2 between the central portion and both ends, but the difference was small, but the feeling of swelling was lacking and the texture was inferior.
比較例2(織物除去方法変更)
バフィング処理で実施例1の織物の除去を行う以外は、実施例1と同様の操作を行った。その結果、スエード調人工皮革製造工程において、しわ、折れなどなく、繊維積層絡合体熱収縮後〜染色までの形態変化が縦×横=102%×98%と少ないものであった。また、得られたスエード調人工皮革の中央部と両端部との目付差は20g/m2と差が少ないものであった。しかし織物を除去する際のバフィング処理によって短繊維部分も一部研削除去され、得られた人工皮革は薄っぺらなものとなり、風合いに劣ったものであった。
Comparative example 2 (textile removal method change)
The same operation as in Example 1 was performed except that the fabric of Example 1 was removed by buffing treatment. As a result, in the suede-like artificial leather manufacturing process, there was no wrinkle or breakage, and the change in shape from the heat shrinkage of the fiber laminate entangled body to the dyeing was as small as vertical x horizontal = 102% x 98%. Further, the difference in basis weight between the center portion and both end portions of the obtained suede-like artificial leather was as small as 20 g / m 2 . However, the short fiber portion was partly ground and removed by the buffing treatment when removing the fabric, and the resulting artificial leather was thin and inferior in texture.
比較例3(熱収縮処理無し)
熱収縮処理を除いた以外は実施例1と同様の操作を行なった。その結果、スエード調人工皮革製造工程においてしわ、折れなどなく、繊維積層絡合体熱収縮後〜染色までの形態変化が少ないものであった。また、得られたスエード調人工皮革は繊維積層絡合体の中央部と両端部との目付差は20g/m2と差が少ないものであった。しかしながら、該人工皮革の表面の毛羽密度が低く、風合いに劣ったものであった。
Comparative Example 3 (no heat shrink treatment)
The same operation as in Example 1 was performed except that the heat shrink treatment was omitted. As a result, there was no wrinkle or crease in the suede-like artificial leather production process, and there was little change in form from heat shrinkage to dyeing of the fiber laminate entangled body. Moreover, the obtained suede-like artificial leather had a small difference in basis weight of 20 g / m 2 between the center and both ends of the fiber laminate entangled body. However, the fluff density on the surface of the artificial leather was low and the texture was inferior.
Claims (5)
(1)短繊維ウェブと実質的に水抽出除去可能な繊維からなる織編物を積層した後、絡合一体化処理することで繊維積層絡合体を製造する工程、
(2)繊維積層絡合体を熱収縮する工程、
(3)繊維積層絡合体の内部に高分子弾性体を付与する工程、
(4)織編物を水抽出除去する工程、 A method for producing artificial leather, comprising sequentially performing the following steps (1) to (4) when producing an artificial leather in which a polymer elastic body is provided inside a fiber entangled body.
(1) The process of manufacturing a fiber lamination entangled body by carrying out an entanglement integration process, after laminating | knitting the woven / knitted fabric which consists of a fiber which can be substantially extracted by water extraction with a short fiber web,
(2) a step of thermally shrinking the fiber laminate entangled body,
(3) A step of providing a polymer elastic body inside the fiber laminate entangled body,
(4) a step of extracting and removing the woven or knitted fabric with water,
A suede-like artificial leather obtained by raising the artificial leather according to claim 4.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2007099951A1 (en) * | 2006-02-28 | 2009-07-16 | 株式会社クラレ | Artificial leather and method for producing the same |
CN113338046A (en) * | 2020-02-18 | 2021-09-03 | 世联株式会社 | Synthetic leather |
-
2004
- 2004-08-09 JP JP2004231816A patent/JP2006045737A/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2007099951A1 (en) * | 2006-02-28 | 2009-07-16 | 株式会社クラレ | Artificial leather and method for producing the same |
CN113338046A (en) * | 2020-02-18 | 2021-09-03 | 世联株式会社 | Synthetic leather |
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