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WO2025187710A1 - Artificial leather and method for producing artificial leather - Google Patents

Artificial leather and method for producing artificial leather

Info

Publication number
WO2025187710A1
WO2025187710A1 PCT/JP2025/007810 JP2025007810W WO2025187710A1 WO 2025187710 A1 WO2025187710 A1 WO 2025187710A1 JP 2025007810 W JP2025007810 W JP 2025007810W WO 2025187710 A1 WO2025187710 A1 WO 2025187710A1
Authority
WO
WIPO (PCT)
Prior art keywords
artificial leather
fiber
fibers
ultrafine
less
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
PCT/JP2025/007810
Other languages
French (fr)
Japanese (ja)
Other versions
WO2025187710A8 (en
Inventor
将司 目黒
弘行 菱田
福久 板野
芳明 脇本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kuraray Co Ltd
Original Assignee
Kuraray Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kuraray Co Ltd filed Critical Kuraray Co Ltd
Publication of WO2025187710A1 publication Critical patent/WO2025187710A1/en
Publication of WO2025187710A8 publication Critical patent/WO2025187710A8/en
Pending legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06NWALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
    • D06N3/00Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof

Definitions

  • the present invention relates to artificial leather and a method for manufacturing artificial leather.
  • leather-like sheets such as artificial leather have flexibility and functionality not found in natural leather, and are therefore used in a variety of applications such as clothing and materials.
  • Artificial leathers are also required to satisfy, at a high level, requirements in terms of physical properties such as light resistance, pilling resistance, and abrasion resistance, as well as sensory requirements such as appearance (a surface texture closer to that of natural leather), texture (a soft feel combined with a moderate sense of fullness and fullness), and color development (vividness and depth of color), and various proposals have been made to meet these requirements.
  • Patent Document 1 describes a leather-like sheet comprising an ultrafine fiber entanglement body made of ultrafine fiber bundles and a polymeric elastomer provided inside the ultrafine fiber bundles, wherein the ultrafine fiber bundles are composed of ultrafine individual fibers having an average cross-sectional area of 0.1 to 30 ⁇ m2 , and the average cross-sectional area is 40 to 400 ⁇ m2 , and the ultrafine fiber bundles are present at a density of 600 to 4,000 fibers/ mm2 in any cross section parallel to the thickness direction of the ultrafine fiber entanglement body.
  • the leather-like sheet is also described as having excellent flexibility.
  • thermosol dyeing is a dyeing method that uses less water, but artificial leather dyed by thermosol dyeing has the problem of having a strong rebound feeling and poor flexibility.
  • the present invention aims to solve the above-mentioned problems and provide artificial leather that has a soft feel and little rebound even without softening treatment, as well as a method for manufacturing the same.
  • the present invention encompasses the following inventions:
  • An artificial leather comprising ultrafine fibers containing a polyester-based resin, In the longitudinal cross section of the artificial leather, the area ratio A occupied by the ultrafine fibers oriented in the thickness direction in the range of ⁇ 30° to +30° is 4.5% or less, An artificial leather, wherein an area ratio B occupied by ultrafine fibers oriented at an angle of ⁇ 30° to +30° in the thickness direction in a transverse cross section of the artificial leather and the area ratio A satisfy A/B ⁇ 0.9.
  • a method for producing an artificial leather according to any one of [1] to [8] above Providing a fiber web formed from ultrafine fiber-generating fibers; forming an entangled fiber sheet using the fiber web; a step of shrinking the entangled fiber sheet and removing at least one component from the ultrafine fiber-forming fiber to obtain an artificial leather substrate; and a step of dyeing the artificial leather substrate.
  • a method for producing an artificial leather wherein the ratio (Y/X) of the strength X at the yield point in the transverse direction of the fiber web to the maximum strength Y after the yield point is 4.0 or less.
  • the method for producing an artificial leather according to the above [9] wherein the ultrafine fiber-forming fiber is not impregnated with a polymeric elastomer before one component is extracted from the ultrafine fiber-forming fiber.
  • the present invention provides artificial leather that has a soft feel and little rebound, even without softening treatment, and a method for producing the same.
  • artificial leather according to an embodiment of the present invention and the method for manufacturing the artificial leather according to an embodiment of the present invention (hereinafter, sometimes referred to as “artificial leather according to this embodiment” or “method for manufacturing the artificial leather according to this embodiment”).
  • the artificial leather of this embodiment is an artificial leather containing ultrafine fibers containing a polyester resin, and in a longitudinal cross section of the artificial leather, an area ratio A occupied by ultrafine fibers oriented at an angle of ⁇ 30° to +30° in the thickness direction is 4.5% or less, and an area ratio B occupied by ultrafine fibers oriented at an angle of ⁇ 30° to +30° in the thickness direction in a transverse cross section of the artificial leather and the area ratio A satisfy A/B ⁇ 0.9.
  • the artificial leather of the present embodiment has the above-described configuration, and therefore the crossing of the ultrafine fibers in the artificial leather is moderate, and the artificial leather can have a soft texture with little resilience even without softening treatment.
  • the artificial leather of the present invention means an artificially produced leather having a texture similar to that of natural leather, and includes raised artificial leather with a raised surface, grain-finish artificial leather, etc. Furthermore, raised artificial leather includes suede-like, velour-like, nubuck-like, etc., which are variations depending on the raised surface condition.
  • the direction in which the artificial leather has the smallest extensibility when pulled is referred to as the "longitudinal direction" of the artificial leather, and the direction perpendicular to that direction is referred to as the "lateral direction” of the artificial leather.
  • the flow direction of the artificial leather during production is referred to as the "longitudinal direction” of the artificial leather.
  • area ratio A and “area ratio B” are values calculated from a photograph of the cross section obtained by cutting the artificial leather in the longitudinal thickness direction or the transverse thickness direction and taking the photograph at 150x magnification using a scanning electron microscope (SEM). More specifically, the area ratio A and the area ratio B are measured by the procedures described in the Examples.
  • the area ratio A is 4.5% or less, preferably 4.2% or less, more preferably 4.0% or less, and even more preferably 3.8% or less, and from the viewpoint of mechanical properties such as tensile strength, tensile elongation, and tear strength, the area ratio A is preferably 0.1% or more, more preferably 0.2% or more, and even more preferably 0.3% or more. Suitable ranges include preferably 0.1 to 4.5%, more preferably 0.2 to 4.2%, even more preferably 0.3 to 4.0%, and even more preferably 0.3 to 3.8%, etc.
  • the area ratio A can be adjusted to a desired value by adjusting the number of intersections between fibers in the fiber web.
  • A/B the ratio of area proportion A to area proportion B, is A/B ⁇ 0.9.
  • it is preferably A/B ⁇ 0.8, more preferably A/B ⁇ 0.7, and even more preferably A/B ⁇ 0.6.
  • mechanical properties such as tensile strength, tensile elongation, and tear strength, it is preferably A/B ⁇ 0.1, more preferably A/B ⁇ 0.2, and even more preferably A/B ⁇ 0.3. Suitable ranges include preferably 0.1 ⁇ A/B ⁇ 0.9, more preferably 0.1 ⁇ A/B ⁇ 0.8, even more preferably 0.2 ⁇ A/B ⁇ 0.7, and even more preferably 0.3 ⁇ A/B ⁇ 0.6.
  • the area ratio B is preferably 5.5% or less, more preferably 5.4% or less, and even more preferably 5.3% or less, and from the viewpoint of obtaining an artificial leather having a desired width, the area ratio B is preferably 1.0% or more, more preferably 2.0% or more, and even more preferably 3.0% or more. Suitable ranges include preferably 1.0 to 5.5%, more preferably 2.0 to 5.4%, and even more preferably 3.0 to 5.3%, etc.
  • the area ratio B can be adjusted by the ratio of widening the width of the artificial leather after dyeing, and the higher the ratio of widening the width of the artificial leather, the more it can be reduced, and the smaller the ratio of widening the width of the artificial leather, the more it can be increased.
  • the thickness of the artificial leather of the present embodiment is not particularly limited, but from the viewpoint of obtaining an artificial leather having less repulsion and a softer texture, it is preferably 0.1 to 2.0 mm, more preferably 0.3 to 1.5 mm, and even more preferably 0.5 to 1.2 mm.
  • the "thickness” is a value measured in accordance with JIS L1096 (2010) (Method A).
  • the apparent density of the artificial leather of this embodiment is not particularly limited, but from the viewpoint of obtaining an artificial leather with less resilience and a softer feel, it is preferably 0.10 to 1.00 g/cm 3 , more preferably 0.20 to 0.80 g/cm 3 , even more preferably 0.30 to 0.60 g/cm 3 , and still more preferably 0.35 to 0.48 g/cm 3 .
  • the "apparent density” is a value measured in accordance with JIS K6505 (1995) 5.2.2.
  • the basis weight of the artificial leather of this embodiment is not particularly limited, but from the viewpoint of obtaining an artificial leather with less repulsion and a softer texture, it is preferably 100 to 1000 g/m 2 , more preferably 150 to 800 g/m 2 , and even more preferably 200 to 600 g/m 2 .
  • the "basis weight” is a value measured in accordance with JIS L1096 (2010) (Method A).
  • the artificial leather of this embodiment is not particularly limited, but from the perspective of more easily achieving the effects of the present invention, it is preferable that the artificial leather be an artificial leather with a napped surface, i.e., a napped artificial leather.
  • the ultrafine fibers contained in the artificial leather of this embodiment are ultrafine fibers obtained by removing at least one component from a multicomponent fiber (composite fiber) made of at least two or more spinnable polymers with different chemical or physical properties. Furthermore, the ultrafine fiber bundle is a bundle of a plurality of ultrafine fibers.
  • the ultrafine fibers of the present embodiment are preferably long fibers from the viewpoint of obtaining artificial leather having less repulsion and a softer feel.
  • long fibers means continuous fibers that are not short fibers intentionally cut after spinning. More specifically, it means filaments or continuous fibers that are not short fibers intentionally cut to a fiber length of about 3 to 80 mm, for example.
  • the fiber length of the islands-in-sea type composite fiber before being converted into ultrafine fibers, as described below, is preferably 100 mm or more, and more preferably 200 mm or more.
  • the long fibers may be continuous fibers that are produced, for example, by a spunbonding method and continuously spun, and have a fiber length of several meters, several hundred meters, several kilometers, or even longer. Note that needle punching during entanglement or surface buffing can unavoidably cut some of the long fibers into short fibers during the production process.
  • the ultrafine fibers of this embodiment contain a polyester-based resin.
  • polyester-based resins include modified PET such as polyethylene terephthalate (hereinafter sometimes referred to as "PET"), isophthalic acid-modified PET, sulfoisophthalic acid-modified PET, and cationic dye-dyeable PET; aromatic polyesters such as polybutylene terephthalate and polyhexamethylene terephthalate; and aliphatic polyesters such as polylactic acid, polyethylene succinate, polybutylene succinate, polybutylene succinate adipate, and polyhydroxybutyrate-polyhydroxyvalerate resin.
  • PET polyethylene terephthalate
  • isophthalic acid-modified PET sulfoisophthalic acid-modified PET
  • cationic dye-dyeable PET aromatic polyesters
  • aromatic polyesters such as polybutylene terephthalate and polyhexamethylene terephthalate
  • aliphatic polyesters such as polylactic acid,
  • the polyester-based resin contains dicarboxylic acid-based monomer units and diol-based monomer units
  • modified PET is PET in which at least a portion of the ester-forming dicarboxylic acid-based monomer units or diol-based monomer units of unmodified PET have been replaced with substitutable monomer units.
  • modified monomer unit substituting the dicarboxylic acid monomer unit include units derived from isophthalic acid, sodium sulfoisophthalic acid, sodium sulfonaphthalenedicarboxylic acid, adipic acid, etc., which substitute for the terephthalic acid unit.
  • the polyester resin of the present embodiment is preferably PET from the viewpoint of obtaining artificial leather with less repulsion and a softer feel. Furthermore, from the viewpoint of recyclability and of obtaining artificial leather having less repulsion and a softer texture, the PET preferably contains 94 mol % or more of dicarboxylic acid monomer units as terephthalic acid units, more preferably 95 mol % or more, even more preferably 96 mol % or more, and may even contain 100 mol %.
  • the PET preferably contains 94 mol % or more of diol-based monomer units as ethylene glycol units, more preferably 95 mol % or more, even more preferably 96 mol % or more, and may contain 100 mol %.
  • the polyester resin of the present embodiment is preferably unmodified PET from the viewpoint of sustainability and from the viewpoint of suppressing adhesion of fibers and obtaining artificial leather with less repulsion and a softer texture. Moreover, the polyester resin of the present embodiment is preferably recycled PET from the viewpoint of sustainability.
  • the intrinsic viscosity of the polyester resin of this embodiment is preferably 0.63 dl/g or less, more preferably 0.625 dl/g or less, and even more preferably 0.62 dl/g or less, from the viewpoint of cross-section formability of the ultrafine fiber-forming fiber, and is preferably 0.55 dl/g or more, more preferably 0.56 dl/g or more, and even more preferably 0.57 dl/g or more, from the viewpoint of mechanical properties such as tensile strength, tensile elongation, and tear strength. Suitable ranges include preferably 0.55 to 0.63 dl/g, more preferably 0.56 to 0.625 dl/g, and even more preferably 0.57 to 0.62 dl/g.
  • the "intrinsic viscosity" is a value measured using a phenol/tetrachloroethane (volume ratio 1/1) mixed solvent as a solvent at a measurement temperature of 30°C using an Ubbelohde viscometer, and specifically, is measured by the procedure described in the Examples.
  • the ultrafine fibers of the present embodiment may or may not contain a resin other than the polyester-based resin.
  • resins other than polyester-based resins include nylons such as nylon 6, nylon 66, nylon 10, nylon 11, nylon 12, and nylon 6-12; and fibers such as polypropylene, polyethylene, polybutene, polymethylpentene, and chlorinated polyolefins. From the viewpoint of recyclability, it is preferable that the ultrafine fibers contain no resin other than the polyester-based resin.
  • the resin that constitutes the ultrafine fibers of this embodiment may contain various additives, provided that the effects of the present invention are not impaired.
  • additives include catalysts, colorants, heat resistance agents, flame retardants, lubricants, stain-resistant agents, fluorescent brighteners, matting agents, gloss improvers, antistatic agents, fragrances, deodorizers, antibacterial agents, anti-mite agents, and inorganic fine particles.
  • the average diameter of the ultrafine fibers of this embodiment is preferably 7.5 ⁇ m or less, more preferably 6.0 ⁇ m or less, even more preferably 5.5 ⁇ m or less, and even more preferably 5.0 ⁇ m or less, from the viewpoint of obtaining artificial leather with less resilience and a softer feel.
  • the average fineness of the ultrafine fibers of this embodiment is preferably 0.50 dtex or less, more preferably 0.40 dtex or less, and even more preferably 0.30 dtex or less.
  • the average fineness of the ultrafine fibers of this embodiment is preferably 0.50 dtex or less, more preferably 0.40 dtex or less, and even more preferably 0.30 dtex or less.
  • it may be, for example, 0.01 dtex or more, or 0.02 dtex or more. Suitable ranges include preferably 0.01 to 0.50 dtex, more preferably 0.01 to 0.40 dtex, and even more preferably 0.02 to 0.30 dtex.
  • the "average diameter" and "average fineness" are values calculated based on the cross-sectional areas of a plurality of ultrafine fibers randomly selected from an enlarged photograph of the cross sections of the ultrafine fibers, and are specifically measured by the procedure described in the Examples.
  • the artificial leather of this embodiment may or may not contain a polymeric elastomer. Any polymeric elastomer that has conventionally been used in artificial leathers can be used. Specific examples include polyurethane elastomers, acrylonitrile elastomers, olefin elastomers, polyester elastomers, and acrylic elastomers, with polyurethane elastomers and acrylic elastomers being preferred.
  • polyurethane elastomers include various polyurethane elastomers obtained by combining, as main components, at least one polymer polyol having an average molecular weight of 500 to 3000 selected from polyester diols, polyether diols, polyether ester diols, polycarbonate diols, polycarbonate ether diols, polycarbonate ester diols, and the like, and at least one polyisocyanate selected from aromatic, alicyclic, and aliphatic diisocyanates, such as 4,4'-diphenylmethane diisocyanate, isophorone diisocyanate, and hexamethylene diisocyanate, and further combining with at least one low molecular weight compound having two or more active hydrogen atoms, such as ethylene glycol and ethylenediamine, in a predetermined molar ratio, and polymerizing these in one stage or multiple stages by melt polymerization, bulk polymerization, solution polymerization, or the like.
  • the acrylic elastomer may comprise at least one soft component selected from the group consisting of a monomer whose homopolymer has a glass transition temperature in the range of -90 to -5°C and is preferably non-crosslinkable, such as methyl acrylate, n-butyl acrylate, isobutyl acrylate, isopropyl acrylate, n-hexyl (meth)acrylate, and 2-ethylhexyl (meth)acrylate, and a monomer whose homopolymer has a glass transition temperature in the range of 50 to 250°C and is preferably non-crosslinkable, such as methyl methacrylate, ethyl methacrylate, isopropyl methacrylate, isobutyl methacrylate, or cyclohexyl methacrylate.
  • a monomer whose homopolymer has a glass transition temperature in the range of -90 to -5°C and is preferably non-crosslinkable such
  • acrylic elastomers examples include various acrylic elastomers obtained by polymerizing at least one hard component selected from the group consisting of acrylic acid, acrylic acid, and (meth)acrylic acid with a monofunctional or polyfunctional ethylenically unsaturated monomer unit capable of forming a crosslinked structure, or a compound capable of forming a crosslinked structure by reacting with an ethylenically unsaturated monomer unit introduced into a polymer chain, such as at least one ethylenically unsaturated monomer comprising a crosslinkable component selected from the group consisting of ethylene glycol di(meth)acrylate, triethylene glycol di(meth)acrylate, polyethylene glycol di(meth)acrylate, and 1,4-butanediol di(meth)acrylate.
  • Artificial leathers obtained by using polyurethane elastomers as the main polymeric elastomer are preferred because they have an excellent balance of texture and mechanical properties, and if the type is appropriately selected, they also have an excellent balance, including durability.
  • Artificial leathers obtained by using acrylic elastomers are unsuitable for forming napped artificial leathers because the acrylic elastomers have lower adhesion to ultrafine fiber bundles than polyurethane elastomers and are poor at fixing the nap during nap formation, but are particularly preferred for forming grain-finish artificial leathers because the degree of hardening of the texture relative to the content is suppressed.
  • the polymer elastomer different types may be mixed and contained, or different types may be contained in separate batches.
  • a polymer elastomer such as synthetic rubber may be added as needed to form a polymer elastomer composition.
  • the artificial leather of this embodiment contains a polymeric elastomer
  • its content in the artificial leather is preferably 5 to 45% by mass, more preferably 7 to 40% by mass, and even more preferably 8 to 30% by mass, from the viewpoint of obtaining an artificial leather with an excellent texture.
  • the artificial leather of this embodiment may or may not contain components other than the ultrafine fibers and the polymeric elastomer.
  • Such other components include the other components contained in the ultrafine fibers described above and the various additives that can be added to the polymeric elastomer liquid used to impregnate the ultrafine fibers.
  • the other components may be encapsulated in at least one of the ultrafine fibers and the polymeric elastomer.
  • the content of the other components is preferably 0.5 to 10.0% by mass, more preferably 1.0 to 5.0% by mass, and even more preferably 1.5 to 3.0% by mass, relative to the mass of the artificial leather, from the viewpoints of water absorbency, water repellency, stain resistance, etc., as well as making it easier for the other components to exhibit their intended effects.
  • the artificial leather according to the present embodiment is preferably produced by a production method comprising the following steps (1) to (4), in which the ratio (Y/X) of the strength X at the yield point in the lateral direction of the fiber web prepared in the following step (1) to the maximum strength Y after the yield point is 4.0 or less.
  • Step (1) A step of preparing a fiber web formed from ultrafine fiber-generating fibers.
  • Step (2) A step of forming an entangled fiber sheet using the fiber web.
  • the manufacturing method according to the present embodiment includes a step (step (1)) of preparing a fiber web in which the ratio (Y/X) of the strength X at the yield point in the lateral direction to the maximum strength Y after the yield point is 4.0 or less, thereby making it easier to obtain the artificial leather of the present embodiment.
  • step (1) the ratio (Y/X) of the strength X at the yield point in the lateral direction to the maximum strength Y after the yield point is 4.0 or less, thereby making it easier to obtain the artificial leather of the present embodiment.
  • Step (1) is a step of preparing a fiber web formed from ultrafine fiber-generating fibers.
  • ultrafine fibers are fibers that have been made ultrafine by removing at least one component from a multicomponent fiber (composite fiber) made of at least two or more types of spinnable polymers that differ in chemical or physical properties, and the multicomponent fiber that generates these ultrafine fibers is an ultrafine fiber-generating fiber.
  • Typical examples of ultrafine fiber-generating fibers include islands-in-sea type composite fibers, multilayer laminated composite fibers, and radial laminated composite fibers, which are obtained using methods such as chip blending (mixed spinning) and composite spinning.
  • islands-in-sea type composite fibers are preferred from the viewpoints of increasing productivity through high-speed spinning and of obtaining artificial leather that is excellent in surface abrasion resistance and pilling resistance, and from the same viewpoint, it is preferred to obtain a fiber web by melt spinning islands-in-sea type composite fibers.
  • the ultrafine fiber-generating fiber is an islands-in-sea type composite fiber
  • island components are dispersed in a sea component that serves as a matrix in the fiber cross section, and by removing the sea component, ultrafine fibers in the form of fiber bundles are generated.
  • a method for obtaining a fiber web by melt-spinning islands-in-sea type composite fibers, using islands-in-sea type composite fibers as ultrafine fiber-forming fibers will be described in more detail.
  • Examples of the island component resins contained in the islands-in-sea type composite fibers and later to become the ultrafine fibers include the same resins as those constituting the ultrafine fibers in the above-mentioned "ultrafine fibers.”
  • the sea component resin contained in the islands-in-sea type composite fiber and removed by extraction, decomposition, etc. is preferably a resin that has a solubility or decomposability different from that of the island component resin and has low compatibility with it. Such a resin is preferably selected appropriately depending on the type of island component resin and the production method.
  • the resin for the sea component examples include olefin-based resins such as polyethylene, polypropylene, ethylene-propylene copolymer, and ethylene-vinyl acetate copolymer, as well as resins that are soluble in organic solvents and can be dissolved and removed by organic solvents, such as polystyrene, styrene-acrylic copolymer, and styrene-ethylene copolymer.
  • Other examples include resins that can be removed using only water without using a solvent, such as polyvinyl alcohol-based resins, water-soluble polyester resins, easily alkali-decomposable modified polyester resins, polyacrylamide resins, and carboxymethyl cellulose resins.
  • polyethylene and polyvinyl alcohol-based resins are preferred from the viewpoints of melt spinnability, water solubility, and fiber properties (fiber strength), and more preferred are polyethylene and modified polyvinyl alcohol.
  • ⁇ -olefins having 4 or less carbon atoms such as ethylene, propylene, 1-butene, and isobutene
  • vinyl ethers such as methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, isopropyl vinyl ether, and n-butyl vinyl ether.
  • the content of copolymerized units in polyvinyl alcohol is preferably from 1 to 20 mol %, more preferably from 4 to 15 mol %, and even more preferably from 6 to 13 mol %. Furthermore, since the copolymerization unit is ethylene, the fiber properties are improved, and therefore ethylene-modified polyvinyl alcohol is more preferred.
  • the ethylene unit content in the ethylene-modified polyvinyl alcohol is preferably 4 to 15 mol %, more preferably 6 to 13 mol %.
  • the mass ratio of the sea component to the island component in the islands-in-sea composite fiber is not particularly limited, but preferably falls within the range of 5:95 to 80:20 (sea component:island component). If the sea component polymer ratio in the islands-in-sea composite fiber is 5% by mass or more, the spinning stability of the islands-in-sea fiber is less likely to decrease, making it easier to ensure industrial productivity. Furthermore, when a polymer elastomer is added, voids of the required size are more likely to form between the ultrafine fiber bundles and the polymer elastomer after the sea component is removed, making it easier to achieve a fluffy, full, dense surface. On the other hand, if the sea component polymer ratio is 80% by mass or less, the shape and distribution of the island component in the cross section of the islands-in-sea fiber are stable, making it easier to prevent a decrease in quality stability.
  • the preferred method for producing a fiber web is to use the so-called spunbond method, in which ultrafine fiber-generating fibers are melt-spun and collected on a conveyor belt without cutting, to form a fiber web of continuous long fibers.
  • a conjugate spinning die having a large number of nozzle holes arranged in a predetermined pattern is used to continuously extrude molten strands of islands-in-sea type composite fibers from a spinning nozzle at a predetermined extrusion speed, and the strands are substantially cooled and solidified by cooling air at any stage between just below the nozzle holes and the suction device described below.
  • a high-velocity air stream is applied using a suction device such as an air jet nozzle, and the islands-in-sea type composite fibers are uniformly drawn and attenuated to a desired diameter or fineness.
  • the high-speed air stream may be applied so that the average spinning speed, which corresponds to the mechanical take-up speed in normal spinning, is any speed in the range of 1,000 to 6,000 m/min.
  • a fiber web can be produced by a spunbonding method in which, depending on the texture of the resulting fiber web, the islands-in-sea type composite fibers are opened by an impingement plate, an air stream, or the like, and then collected and deposited on a collecting surface such as a conveyor belt that moves in the longitudinal direction while being sucked from the opposite side of the conveyor belt to form a long-fiber web.
  • the distance between the air jet nozzle and the collection surface is preferably 10 to 100 cm, more preferably 30 to 80 cm, and even more preferably 40 to 70 cm.
  • the suction speed to the collection surface is preferably 5 to 35 m/sec, more preferably 10 to 25 m/sec.
  • the movement speed of the collection surface is preferably 20 to 150 m/min, more preferably 50 to 120 m/min.
  • the degree of spreading and the number of intersections of the islands-in-sea type composite fibers collected on the collecting surface can be appropriately adjusted by adjusting the average spinning speed, the distance between the air jet nozzle and the collecting surface, the suction speed onto the collecting surface, the movement speed of the collecting surface, etc. As a result, an artificial leather with less repulsion and a softer feel can be obtained.
  • the fiber web may be subjected to a heat press treatment to impart shape stability, and the fiber web may be fused as a result.
  • step (3) such a fiber web shrinks in the transverse direction (width direction), which not only relieves the tension of the fibers in the transverse direction but also allows the fibers to be appropriately passed through in the longitudinal direction, thereby relieving the tension in the longitudinal direction, and thickness collapse is suppressed, making it easy to obtain an artificial leather that is less likely to increase in apparent density and has a soft texture.
  • Y/X is preferably 3.9 or less.
  • Step (2) is a step of forming an entangled fiber sheet using the fiber web.
  • step (2) a plurality of layers of the fiber web obtained in step (1) are superimposed on one another, and then subjected to an entanglement treatment such as needle punching or hydroentanglement treatment to obtain an entangled web in which the long fibers are entangled in the thickness direction.
  • an entanglement treatment such as needle punching or hydroentanglement treatment to obtain an entangled web in which the long fibers are entangled in the thickness direction.
  • the fiber webs may be stacked in the same direction, or the fiber webs may be stacked by changing the conveying direction of the fiber web to a 90° direction and folding it back by a cross-lapping method.
  • the method for stacking a plurality of fiber webs is preferably cross-lapping lamination, from the viewpoints that it is easy to adjust the width of the entangled fiber sheet as desired and it can suppress the occurrence of unevenness in the width direction of the fiber web, i.e., it can suppress unevenness in the basis weight.
  • the number of layers of the web to be superimposed is not particularly limited, but from the viewpoint of mechanical strength, it is preferably 4 layers or more, more preferably 8 layers or more, and from the viewpoint of ease of production, it is preferably 20 layers or less, more preferably 16 layers or less.
  • a fiber web made up of multiple layers is subjected to a mechanical entanglement process using a known method such as a needle punching method or a high-pressure water jet treatment method, thereby three-dimensionally entangling the fibers constituting the fiber web, particularly the fibers between adjacent layers of a wrapped or stacked layered fiber web.
  • various processing conditions are appropriately selected, such as the type of needles (needle shape and count, barb shape and depth, number and position of barbs, etc.), the number of needle punches (needle punch processing density per unit area obtained by multiplying the density of needles implanted in a needle board by the number of strokes at which the board acts on the fiber web per unit area), and the needle punch depth (depth at which the needles act on the fiber web).
  • the punch density for needle punching is preferably 1500 to 5500 punches/cm 2 , more preferably 2000 to 5000 punches/cm 2 , from the viewpoint of easily obtaining high abrasion resistance. If the punch density is within the above range, insufficient entanglement is suppressed, preventing the surface of the artificial leather from becoming rough due to fraying of the fibers, and also preventing fiber breakage from occurring, preventing a decrease in the degree of entanglement.
  • an oil or antistatic agent may be applied to the ultrafine fiber-generating fiber, fiber web, fiber web laminate, entangled fiber sheet, etc.
  • the ultrafine fiber-generating fiber, fiber web, fiber web laminate, entangled fiber sheet, etc. may be immersed in warm water at a temperature of about 70 to 150°C for shrinkage treatment to make the entanglement dense in advance.
  • the basis weight of the entangled fiber sheet obtained by entanglement is preferably in the range of about 100 to 1000 g/ m2 .
  • the entangled fiber sheet may be subjected to a treatment to further increase the fiber density and degree of entanglement by heat shrinking as needed.
  • the entangled fiber sheet densified by the heat shrinking treatment may be further densified, and the fiber density may be further increased by heat pressing as needed for the purposes of fixing the shape of the entangled fiber sheet and smoothing the surface.
  • step (3) the entangled fiber sheet is shrunk and at least one component is removed from the ultrafine fiber-forming fibers to obtain an artificial leather substrate.
  • the one component is preferably a sea component resin contained in the islands-in-sea composite fiber. By removing the sea component, the ultrafine fiber-forming fibers can be converted into a fiber bundle of ultrafine fibers.
  • Methods for shrinking an entangled fiber sheet include heat shrinkage (fiber shrinkage) using steam, hot water, dry heat, etc.
  • heat shrinkage fiber shrinkage
  • an entangled fiber sheet shrinks in the horizontal direction (width direction), relaxing the tension in the horizontal fibers.
  • the process of removing at least one component allows the fibers to be pulled out appropriately in the vertical direction, relaxing the tension in the vertical direction and suppressing an increase in apparent density. As a result, an artificial leather with less resilience and a softer texture can be obtained.
  • the sea component is a water-soluble resin such as a polyvinyl alcohol resin, a water-soluble polyester resin, an easily alkali-decomposable modified polyester resin, a polyacrylamide resin, or a carboxymethyl cellulose resin
  • the sea component can be removed with water.
  • the sea component is insoluble in water but soluble in organic solvents and the island component resin is a polyamide resin or a polyester resin
  • examples of the organic solvent that dissolves and removes the sea component include toluene, trichloroethylene, and tetrachloroethylene.
  • the entangled fiber sheet it is preferable to simultaneously shrink the entangled fiber sheet and remove at least one component from the ultrafine fiber-generating fibers, and when the sea component is a water-soluble resin, it is preferable to use hot water to shrink the entangled fiber sheet and remove the water-soluble resin.
  • a dip-nip treatment may be carried out in parallel.
  • Step (4) is a step of dyeing the artificial leather substrate. Step (4) can be carried out at any stage after the islands-in-the-sea fibers are converted into ultrafine fiber bundles.
  • any dyeing method can be employed using a known dyeing machine that is usually used for dyeing conventional artificial leathers such as padder, jigger, circular, and wince, using a dye mainly composed of a disperse dye, a reactive dye, an acid dye, a metal complex dye, a sulfur dye, or a sulfur vat dye, which is appropriately selected depending on the type of fiber.
  • a dye mainly composed of a disperse dye, a reactive dye, an acid dye, a metal complex dye, a sulfur dye, or a sulfur vat dye which is appropriately selected depending on the type of fiber.
  • conventional artificial leathers dyed by thermosol dyeing have had the problem of having a strong resilience and poor flexibility.
  • thermosol dyeing can significantly reduce the amount of water used compared to dyeing methods used for general artificial leathers, thereby reducing the environmental impact. Therefore, from the perspective of reducing the environmental impact, it is preferable to dye the artificial leather substrate by thermosol dyeing.
  • the method for producing an artificial leather according to this embodiment may further include step (5) of impregnating the entangled fiber sheet with the polymeric elastomer, from the viewpoint of imparting texture and shape stability similar to those of natural leather.
  • Step (5) may be carried out between step (2) and step (3), or between step (3) and step (4).
  • step (5) in order to impart a texture and shape stability similar to those of natural leather as well as flexibility, it is preferable to carry out step (5) between steps (2) and (3). That is, it is preferable to impregnate the artificial leather with a polymeric elastomer before removing the sea component.
  • the ultrafine fibers forming the fiber bundle By impregnating the ultrafine fibers forming the fiber bundle with a polymeric elastomer before removing the sea part in this way, voids are formed between the ultrafine fibers that form the fiber bundle after removing the sea part, which are formed by removing the sea part. As a result, the ultrafine fibers inside the fiber bundle are less likely to be restrained by the polymeric elastomer, i.e., the ultrafine bundle is less likely to be affected by the polymeric elastomer, making it easier to obtain an artificial leather with excellent flexibility.
  • the ultrafine fibers forming the fiber bundle after removing the sea part from the islands-in-sea type composite fiber are impregnated with a polymeric elastomer, the polymeric elastomer penetrates into the voids in the fiber bundle, and the ultrafine fibers forming the fiber bundle are restrained by the polymeric elastomer, making it easier to obtain an artificial leather with a hard texture.
  • a non-aqueous polymeric elastomer liquid in which the polymeric elastomer is dissolved or dispersed in a solvent may be used, or an aqueous polymeric elastomer liquid in which the polymeric elastomer is dispersed in an aqueous medium, optionally together with a dispersant, may be used.
  • a uniform polymeric elastomer liquid is more easily obtained, while in the latter case, it is easier to reduce the amount of organic solvent used.
  • step (5) Details of the polymeric elastomer used in step (5) are as explained above in the "Polymeric elastomer" section.
  • the polymeric elastomer may be fixed within the entangled fiber sheet by impregnating the entangled fiber sheet with the polymeric elastomer and then coagulating the polymeric elastomer using a conventional dry or wet method.
  • the dry method here refers to any method for fixing a polymeric elastomer within a fiber sheet structure by removing solvents, dispersants, etc. by drying or other methods.
  • the wet method here refers to any method for temporarily or completely fixing a polymeric elastomer within the entangled fiber sheet structure prior to removing the dispersant by treating an entangled fiber sheet structure impregnated with a polymeric elastomer liquid with a non-solvent or coagulant for the polymeric elastomer, or by using an aqueous polymeric elastomer liquid containing a heat-sensitive gelling agent or other additive to heat-treat the impregnated entangled fiber sheet.
  • the artificial leather of this embodiment has a texture similar to that of natural leather, even without the polymer elastomer, so it is preferable not to impregnate it with the polymer elastomer. In other words, it is preferable not to include step (5).
  • finishing treatments such as mechanical kneading in a dry state, relaxation treatment in a wet state using a dyeing machine or washing machine, treatment with softeners, functionalization treatments such as flame retardants, antibacterial agents, deodorizers, water and oil repellents, treatments to add texture modifiers such as silicone resins, silk protein-containing treatments, and grip-imparting resins, and design-imparting treatments using resins other than those mentioned above, such as colorants and enamel-like coating resins, may also be performed as needed.
  • the artificial leather of this embodiment can be sliced into multiple pieces in the thickness direction as needed, and the thickness can be adjusted by grinding the back surface, or a solvent capable of dissolving or swelling the polymer elastomer or ultrafine fiber bundles can be applied to the back surface.
  • the artificial leather of this embodiment may have a napped surface.
  • any of the known methods such as buffing with sandpaper or card cloth, or brushing, can be used.
  • a solvent capable of dissolving or swelling the polymeric elastomer or ultrafine fiber bundles such as a treatment liquid containing dimethylformamide (DMF) or a treatment liquid containing a phenolic compound such as resorcinol, may be applied to the surface to be napped.
  • a solvent capable of dissolving or swelling the polymeric elastomer or ultrafine fiber bundles such as a treatment liquid containing dimethylformamide (DMF) or a treatment liquid containing a phenolic compound such as resorcinol, may be applied to the surface to be napped.
  • DMF dimethylformamide
  • a treatment liquid containing a phenolic compound such as resorcinol
  • step (4) allows for fine adjustment of the restraint state of the ultrafine fiber bundles due to adhesion of the polymeric elastomer or ultrafine fiber bundles, the nap length of the ultrafine fibers of the artificial leather, the surface friction durability, etc.
  • the above-mentioned step (4) may be carried out.
  • ⁇ Average diameter> The average diameter of the polyester fibers was measured as follows. A scanning electron microscope (SEM) photograph of the cross section of the artificial leather was taken at 3000x magnification. Ten cross sections of fibers were randomly selected from the SEM photograph, and their cross-sectional areas were measured. The arithmetic mean value of the cross-sectional areas was calculated, and the average diameter of the fibers was calculated based on the following formula (1). Average diameter (average cross-sectional area/ ⁇ ) 1/2 ⁇ 2...Formula (1)
  • the average fineness of the polyester fiber was measured as follows. A scanning electron microscope (SEM) photograph of the cross section of the artificial leather was taken at 3000x magnification. Ten cross sections of fibers were randomly selected from the SEM photograph, and the cross-sectional areas were measured and the arithmetic mean value of the cross-sectional areas was calculated. The mean value of the cross-sectional areas was then converted into an average fineness using the density of the resin.
  • SEM scanning electron microscope
  • ⁇ Measurement of area ratio A and area ratio B> The artificial leather was cut in the longitudinal thickness direction using a single-edged razor, and the resulting cross section was photographed in multiple sections from the front side to the back side using a scanning electron microscope (SEM) at 150x magnification.
  • SEM scanning electron microscope
  • the multiple images were printed on paper and connected so that the cross section of the artificial leather was continuous from the front side to the back side, and a straight line was drawn evenly across the boundary between the artificial leather substrate and the base of the napped fibers on the printed surface. Furthermore, a rectangle equivalent to 400 ⁇ m (depth direction) x 700 ⁇ m (direction perpendicular to the depth direction) was drawn in the center of the cross section of the artificial leather on the printed surface.
  • PET film polyethylene terephthalate film
  • image analysis software "Image-Pro Premier ver. 9.1" (manufactured by Nippon Rover Co., Ltd.), and the area of the longitudinal cross section of the artificial leather was measured.
  • the rectangular portion of the PET film was replaced with a new transparent PET film placed on the printed surface so as to cover the rectangle.
  • the straight line was defined as 0°, and the angle ( ⁇ 90° or less) between the straight line and the ultrafine fibers was defined as the angle in the thickness direction.
  • the surface of the PET film in the portion where the ultrafine fibers were oriented in the thickness direction within a range of -30° to +30° was painted black.
  • the area of the ultrafine fibers oriented in the thickness direction within a range of -30° to +30° was measured using the image analysis software in the same manner as in measuring the area of the longitudinal cross section of the artificial leather. From the area of the obtained longitudinal cross section of the artificial leather and the area of the ultrafine fibers oriented in the thickness direction within a range of -30° to +30°, the area ratio A (%) of the ultrafine fibers oriented in the thickness direction within a range of -30° to +30° was calculated.
  • the artificial leather was cut in the thickness direction in the lateral direction using a single-edged razor, and the area ratio B (%) of the ultrafine fibers oriented in the thickness direction in the lateral cross section of the artificial leather was calculated using the same procedure as in calculating the area ratio A (%).
  • the obtained artificial leather was cut into a size of 16 cm x 16 cm (256 cm 2 ).
  • the mass (g) of the cut artificial leather was measured, and the basis weight (g/m 2 ) of the cut artificial leather was calculated using the following formula (3).
  • Basis weight mass / 256 ⁇ 10000 Formula (3)
  • the thickness (mm) of the cut artificial leather was measured using a thickness gauge (measuring probe diameter: 10 mm) under a constant pressure of 23.5 kPa for 5 seconds, and the apparent density (g/cm 3 ) of the artificial leather was calculated using the following formula (4) in accordance with JIS K6505 (1995) 5.2.2.
  • Apparent density basis weight / thickness / 1000 Formula (4)
  • Texture The texture of the resulting artificial leather after bending was judged visually and by touch according to the following criteria.
  • Example 1 A water-soluble thermoplastic polyvinyl alcohol resin (modified polyvinyl alcohol modified by ethylene copolymerization) was used as the sea component, and recycled polyethylene terephthalate (dicarboxylic acid units, of which constitutional units derived from terephthalic acid account for 100 mol %) having an intrinsic viscosity of 0.60 dl/g was used as the island component. Islands-in-sea type composite fibers were extruded from a melt conjugate spinning nozzle (number of islands: 25/fiber) at 270°C so that the sea component/island component ratio was 25/75 (mass ratio).
  • an air jet nozzle was installed at a position 55 cm above the conveyor belt (the collection surface of the islands-in-sea type composite fibers), and spinning was performed while pulling and attenuating at a spinning speed of 3,279 m/min, and islands-in-sea type composite fibers with an average fineness of 3.05 dtex were collected on the conveyor belt, thereby obtaining an islands-in-sea type composite fiber sheet.
  • the spread (length) of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was measured and found to be 24.5 cm.
  • the resulting islands-in-sea composite fiber sheet was hot-pressed using a calender roll at a roll surface temperature of 58°C and a linear pressure of 36 kg/cm to obtain a fiber web.
  • the fiber webs were then cross-lap laminated to form a laminate web, which was then needle-punched using 6-barb needles to form an entangled fiber sheet having a basis weight of 292 g/ m2 and longitudinal crimping.
  • the entangled fiber sheet was immersed in hot water at 95°C for 10 minutes while undergoing dip-nip treatment and high-pressure water jet treatment to dissolve and remove the water-soluble thermoplastic polyvinyl alcohol resin, which is the sea component of the islands-in-sea type composite fiber, and form polyethylene terephthalate ultrafine fibers with an average diameter of 3.02 ⁇ m and an average fineness of 0.101 dtex.
  • the resulting product was then dried to obtain an artificial leather substrate.
  • the resulting artificial leather substrate was then thermosol dyed with a disperse dye and raised to obtain an artificial leather with a napped surface.
  • the resulting artificial leather had a basis weight of 436 g/ m2 , an apparent density of 0.451 g/ cm3 , and a thickness of 0.97 mm.
  • the resulting artificial leather had a solid feel with little rebound, was bendable without large buckling wrinkles, and had excellent flexibility.
  • Example 2 A dyed artificial leather was obtained in the same manner as in Example 1, except that a sheet of islands-in-sea type composite fibers was obtained by adjusting the air jet nozzle so that the measured spread of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was 26.0 cm. The results are shown in Table 1.
  • Example 3 A dyed artificial leather was obtained in the same manner as in Example 1, except that a sheet of islands-in-sea type composite fibers was obtained by adjusting the air jet nozzle so that the measured spread of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was 27.0 cm. The results are shown in Table 1.
  • Example 4 Dyed artificial leather was obtained in the same manner as in Example 1, except that the artificial leather substrate was dyed by circular dyeing instead of thermosol dyeing. The results are shown in Table 1.
  • Example 5 In Example 3, the artificial leather substrate was impregnated with a mixture of acrylic emulsion Kasesol ARS-2 (manufactured by Nicca Chemical Co., Ltd.) and water in a mass ratio of 30:70 (acrylic emulsion content: approximately 18 mass%), pickled 40%, dried at 140°C for 4 minutes, and then thermosol dyed. Dyed artificial leather was obtained in the same manner as in Example 3. The results are shown in Table 1.
  • Example 1 A dyed artificial leather was obtained in the same manner as in Example 1, except that a sheet of islands-in-sea type composite fibers was obtained by adjusting the air jet nozzle so that the measured spread of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was 23.0 cm. The results are shown in Table 1.
  • Example 2 Dyed artificial leather was obtained in the same manner as in Example 1, except that isophthalic acid-modified polyethylene terephthalate (polyethylene phthalate modified with 6 mol% isophthalic acid) was used instead of the recycled polyethylene terephthalate having an intrinsic viscosity of 0.60 dl/g, and the air jet nozzle was adjusted so that the measured spread of the islands-in-sea type composite fiber on the conveyor belt (collection surface) was 27.0 cm to obtain a sheet of islands-in-sea type composite fiber. The results are shown in Table 1.
  • Example 4 A dyed artificial leather was obtained in the same manner as in Example 1, except that a sheet of islands-in-sea type composite fibers was obtained by adjusting the air jet nozzle so that the measured spread of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was 23.2 cm. The results are shown in Table 1.

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Abstract

This artificial leather includes ultrafine fibers containing a polyester-based resin. In a longitudinal cross-section of the artificial leather, an area ratio A occupied by ultrafine fibers that are oriented in a range of -30° to +30° in the thickness direction is 4.5% or less. In a lateral cross-section of the artificial leather, the area ratio A and an area ratio B occupied by ultrafine fibers that are oriented in a range of -30° to +30° in the thickness direction satisfy A/B ≤ 0.9.

Description

人工皮革、及び人工皮革の製造方法Artificial leather and method for manufacturing artificial leather

 本発明は、人工皮革、及び人工皮革の製造方法に関する。 The present invention relates to artificial leather and a method for manufacturing artificial leather.

 人工皮革等の皮革様シートは、天然皮革にはない柔軟性や機能性を有していることから、衣料や資材等、種々の用途に使用されている。
 また、人工皮革は、耐光性、耐ピリング性、耐磨耗性等の物性面や、外観(天然皮革により近い表面感)、風合い(柔軟な手触りと適度な膨らみ感や充実感の兼備)、発色性(色の鮮明さや濃度感)等の感性面での要求を全て高いレベルで満足することが求められており、これを解決すべく種々の提案がなされてきた。
BACKGROUND ART Leather-like sheets such as artificial leather have flexibility and functionality not found in natural leather, and are therefore used in a variety of applications such as clothing and materials.
Artificial leathers are also required to satisfy, at a high level, requirements in terms of physical properties such as light resistance, pilling resistance, and abrasion resistance, as well as sensory requirements such as appearance (a surface texture closer to that of natural leather), texture (a soft feel combined with a moderate sense of fullness and fullness), and color development (vividness and depth of color), and various proposals have been made to meet these requirements.

 例えば、特許文献1には、極細繊維束からなる極細繊維絡合体及びその内部に付与された高分子弾性体を含む皮革様シートであって、前記極細繊維束は、平均断面積が0.1~30μmの極細単繊維からなり、その平均断面積が40~400μmであり、前記極細繊維束は、前記極細繊維絡合体の厚み方向と平行な任意の断面において600~4000個/mmの密度で存在する皮革様シートが記載されている。該皮革様シートは柔軟性に優れることが記載されている。 For example, Patent Document 1 describes a leather-like sheet comprising an ultrafine fiber entanglement body made of ultrafine fiber bundles and a polymeric elastomer provided inside the ultrafine fiber bundles, wherein the ultrafine fiber bundles are composed of ultrafine individual fibers having an average cross-sectional area of 0.1 to 30 μm2 , and the average cross-sectional area is 40 to 400 μm2 , and the ultrafine fiber bundles are present at a density of 600 to 4,000 fibers/ mm2 in any cross section parallel to the thickness direction of the ultrafine fiber entanglement body. The leather-like sheet is also described as having excellent flexibility.

国際公開第2007/040144号International Publication No. 2007/040144

 人工皮革は、一般的に、意匠性を付与し、感性面での要求を満足するものとする観点から、染色が施されているが、染色に要する水使用量が非常に多いという問題があった。また、サスティナブルの観点からも、水使用量削減要求が非常に高まっている。
 一方、水使用量が少ない方法として、サーモゾル染色による染色方法が挙げられるが、サーモゾル染色により染色された人工皮革は、反発感が強く、柔軟性に劣るという問題があった。
Artificial leather is generally dyed to impart design and satisfy aesthetic demands, but the dyeing process requires a large amount of water, which is a problem. Also, from the perspective of sustainability, there is a growing demand for reducing water consumption.
On the other hand, thermosol dyeing is a dyeing method that uses less water, but artificial leather dyed by thermosol dyeing has the problem of having a strong rebound feeling and poor flexibility.

 本発明は上述した問題が解決され、柔軟処理を施さなくても、反発感が少なく、柔軟な風合いを有する人工皮革及びその製造方法を提供することを目的とする。 The present invention aims to solve the above-mentioned problems and provide artificial leather that has a soft feel and little rebound even without softening treatment, as well as a method for manufacturing the same.

 本発明者らは種々検討した結果、人工皮革の縦方向断面中及び横方向断面中において、特定の範囲で配向する極細繊維が占める面積割合を、それぞれ特定の値及び比とすることにより、上記課題を解決し得ることを見出し、本発明に至った。すなわち、本発明は以下の発明を包含する。 After extensive investigation, the inventors discovered that the above-mentioned problems could be solved by setting the area proportions of ultrafine fibers oriented within specific ranges in the longitudinal and transverse cross sections of the artificial leather to specific values and ratios, respectively, and arrived at the present invention. In other words, the present invention encompasses the following inventions:

[1] ポリエステル系樹脂を含有する極細繊維を含む人工皮革であって、
 前記人工皮革の縦方向断面中、厚み方向に-30°~+30°の範囲で配向する極細繊維が占める面積割合Aが、4.5%以下であり、
 前記人工皮革の横方向断面中、厚み方向に-30°~+30°の範囲で配向する極細繊維が占める面積割合Bと前記面積割合Aが、A/B≦0.9である、人工皮革。
[2] 前記極細繊維の平均径が、7.5μm以下である、上記[1]に記載の人工皮革。
[3] 前記極細繊維の平均繊度が、0.50dtex以下である、上記[1]又は[2]に記載の人工皮革。
[4] 前記極細繊維が長繊維である、上記[1]~[3]のいずれかに記載の人工皮革。
[5] 前記ポリエステル系樹脂が、ポリエチレンテレフタレートである、上記[1]~[4]のいずれかに記載の人工皮革。
[6] 前記ポリエステル系樹脂の固有粘度が、0.63dl/g以下である、上記[1]~[5]のいずれかに記載の人工皮革。
[7] 前記ポリエチレンテレフタレートは、ジカルボン酸単位及びジオール単位を含み、前記ジカルボン酸単位の94モル%以上がテレフタル酸に由来する構成単位である、上記[5]に記載の人工皮革。
[8] 前記ポリエチレンテレフタレートが、リサイクルポリエチレンテレフタレートである、上記[7]に記載の人工皮革。
[9] 上記[1]~[8]のいずれかに記載の人工皮革の製造方法であって、
 極細繊維発生型繊維から形成された繊維ウェブを準備する工程と、
 前記繊維ウェブを用いて絡合繊維シートを形成する工程と、
 前記絡合繊維シートを収縮させ、前記極細繊維発生型繊維から少なくとも一成分を除去することにより、人工皮革基体を得る工程と、
 前記人工皮革基体を染色する工程とを備え、
 前記繊維ウェブの横方向の降伏点の強度Xと、降伏点以降の最大強度Yとの比(Y/X)が、4.0以下である、人工皮革の製造方法。
[10] 前記極細繊維発生型繊維から一成分を抽出する前に、高分子弾性体を含浸させない、上記[9]に記載の人工皮革の製造方法。
[1] An artificial leather comprising ultrafine fibers containing a polyester-based resin,
In the longitudinal cross section of the artificial leather, the area ratio A occupied by the ultrafine fibers oriented in the thickness direction in the range of −30° to +30° is 4.5% or less,
An artificial leather, wherein an area ratio B occupied by ultrafine fibers oriented at an angle of −30° to +30° in the thickness direction in a transverse cross section of the artificial leather and the area ratio A satisfy A/B≦0.9.
[2] The artificial leather according to the above [1], wherein the average diameter of the ultrafine fibers is 7.5 μm or less.
[3] The artificial leather according to the above [1] or [2], wherein the average fineness of the ultrafine fibers is 0.50 dtex or less.
[4] The artificial leather according to any one of the above [1] to [3], wherein the ultrafine fibers are long fibers.
[5] The artificial leather according to any one of [1] to [4] above, wherein the polyester resin is polyethylene terephthalate.
[6] The artificial leather according to any one of the above [1] to [5], wherein the intrinsic viscosity of the polyester resin is 0.63 dl/g or less.
[7] The artificial leather according to the above [5], wherein the polyethylene terephthalate contains dicarboxylic acid units and diol units, and 94 mol % or more of the dicarboxylic acid units are structural units derived from terephthalic acid.
[8] The artificial leather according to the above [7], wherein the polyethylene terephthalate is recycled polyethylene terephthalate.
[9] A method for producing an artificial leather according to any one of [1] to [8] above,
Providing a fiber web formed from ultrafine fiber-generating fibers;
forming an entangled fiber sheet using the fiber web;
a step of shrinking the entangled fiber sheet and removing at least one component from the ultrafine fiber-forming fiber to obtain an artificial leather substrate;
and a step of dyeing the artificial leather substrate.
A method for producing an artificial leather, wherein the ratio (Y/X) of the strength X at the yield point in the transverse direction of the fiber web to the maximum strength Y after the yield point is 4.0 or less.
[10] The method for producing an artificial leather according to the above [9], wherein the ultrafine fiber-forming fiber is not impregnated with a polymeric elastomer before one component is extracted from the ultrafine fiber-forming fiber.

 本発明によれば、柔軟処理を施さなくても、反発感が少なく、柔軟な風合いを有する人工皮革及びその製造方法を提供することができる。 The present invention provides artificial leather that has a soft feel and little rebound, even without softening treatment, and a method for producing the same.

 以下、本発明の実施形態に係る人工皮革、及び本発明の実施形態に係る人工皮革の製造方法(以下、「本実施形態の人工皮革」、「本実施形態の人工皮革の製造方法」ということがある)について説明する。 The following describes the artificial leather according to an embodiment of the present invention and the method for manufacturing the artificial leather according to an embodiment of the present invention (hereinafter, sometimes referred to as "artificial leather according to this embodiment" or "method for manufacturing the artificial leather according to this embodiment").

[人工皮革]
 本実施形態の人工皮革は、ポリエステル系樹脂を含有する極細繊維を含む人工皮革であって、前記人工皮革の縦方向断面中、厚み方向に-30°~+30°の範囲で配向する極細繊維が占める面積割合Aが、4.5%以下であり、前記人工皮革の横方向断面中、厚み方向に-30°~+30°の範囲で配向する極細繊維が占める面積割合Bと前記面積割合Aが、A/B≦0.9である。
[Artificial leather]
The artificial leather of this embodiment is an artificial leather containing ultrafine fibers containing a polyester resin, and in a longitudinal cross section of the artificial leather, an area ratio A occupied by ultrafine fibers oriented at an angle of −30° to +30° in the thickness direction is 4.5% or less, and an area ratio B occupied by ultrafine fibers oriented at an angle of −30° to +30° in the thickness direction in a transverse cross section of the artificial leather and the area ratio A satisfy A/B≦0.9.

 本実施形態の人工皮革は、上記構成を有することにより、人工皮革中の極細繊維の交差が適度となり、柔軟処理を施さなくても、反発感が少なく、柔軟な風合いを有する人工皮革とすることができる。
 なお、本発明の人工皮革は、人工的に製造された天然皮革に近い風合いを有するものを意味し、表面が起毛された立毛人工皮革、銀付調人工皮革等を含む。さらに、立毛人工皮革は、表面の起毛状態によるバリエーションとしてスエード調、ベロア調、ヌバック調等を含む。
The artificial leather of the present embodiment has the above-described configuration, and therefore the crossing of the ultrafine fibers in the artificial leather is moderate, and the artificial leather can have a soft texture with little resilience even without softening treatment.
The artificial leather of the present invention means an artificially produced leather having a texture similar to that of natural leather, and includes raised artificial leather with a raised surface, grain-finish artificial leather, etc. Furthermore, raised artificial leather includes suede-like, velour-like, nubuck-like, etc., which are variations depending on the raised surface condition.

 本明細書において、人工皮革を引っ張った際に、伸張性が最も小さい方向が人工皮革の「縦方向」を意味し、その方向に直交する方向が人工皮革の「横方向」を意味する。また、人工皮革を製造する際の流れる方向が人工皮革の「縦方向」である。
 本明細書において、「面積割合A」及び「面積割合B」は、人工皮革を縦方向の厚み方向、又は横方向の厚み方向に切断し、得られた断面を、走査型電子顕微鏡(SEM)を用いて150倍で撮影した写真から算出する値である。
 面積割合A及び面積割合Bは、より具体的には、実施例に記載された手順で測定される。
In this specification, the direction in which the artificial leather has the smallest extensibility when pulled is referred to as the "longitudinal direction" of the artificial leather, and the direction perpendicular to that direction is referred to as the "lateral direction" of the artificial leather. Also, the flow direction of the artificial leather during production is referred to as the "longitudinal direction" of the artificial leather.
In this specification, "area ratio A" and "area ratio B" are values calculated from a photograph of the cross section obtained by cutting the artificial leather in the longitudinal thickness direction or the transverse thickness direction and taking the photograph at 150x magnification using a scanning electron microscope (SEM).
More specifically, the area ratio A and the area ratio B are measured by the procedures described in the Examples.

 面積割合Aは、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、4.5%以下、好ましくは4.2%以下、より好ましくは4.0%以下、さらに好ましくは3.8%以下であり、引張強度、引張伸度、引裂強度等の機械物性の観点から、好ましくは0.1%以上、より好ましくは0.2%以上、さらに好ましくは0.3%以上である。好適な範囲としては、好ましくは0.1~4.5%、より好ましくは0.2~4.2%、さらに好ましくは0.3~4.0%、よりさらに好ましくは0.3~3.8%等が挙げられる。
 面積割合Aは、繊維ウェブの繊維同士の交差数等を調整することによって、所望の値に調整することができる。
From the viewpoint of obtaining an artificial leather having less resilience and a softer feel, the area ratio A is 4.5% or less, preferably 4.2% or less, more preferably 4.0% or less, and even more preferably 3.8% or less, and from the viewpoint of mechanical properties such as tensile strength, tensile elongation, and tear strength, the area ratio A is preferably 0.1% or more, more preferably 0.2% or more, and even more preferably 0.3% or more. Suitable ranges include preferably 0.1 to 4.5%, more preferably 0.2 to 4.2%, even more preferably 0.3 to 4.0%, and even more preferably 0.3 to 3.8%, etc.
The area ratio A can be adjusted to a desired value by adjusting the number of intersections between fibers in the fiber web.

 面積割合Aと面積割合Bの比であるA/Bは、A/B≦0.9であり、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、好ましくはA/B≦0.8、より好ましくはA/B≦0.7、さらに好ましくはA/B≦0.6であり、引張強度、引張伸度、引裂強度等の機械物性の観点から、好ましくはA/B≧0.1、より好ましくはA/B≧0.2、さらに好ましくはA/B≧0.3である。好適な範囲としては、好ましくは0.1≦A/B≦0.9、より好ましくは0.1≦A/B≦0.8、さらに好ましくは0.2≦A/B≦0.7、よりさらに好ましくは0.3≦A/B≦0.6等が挙げられる。 A/B, the ratio of area proportion A to area proportion B, is A/B≦0.9. From the viewpoint of obtaining artificial leather with less resilience and a softer feel, it is preferably A/B≦0.8, more preferably A/B≦0.7, and even more preferably A/B≦0.6. From the viewpoint of mechanical properties such as tensile strength, tensile elongation, and tear strength, it is preferably A/B≧0.1, more preferably A/B≧0.2, and even more preferably A/B≧0.3. Suitable ranges include preferably 0.1≦A/B≦0.9, more preferably 0.1≦A/B≦0.8, even more preferably 0.2≦A/B≦0.7, and even more preferably 0.3≦A/B≦0.6.

 面積割合Bは、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、好ましくは5.5%以下、より好ましくは5.4%以下、さらに好ましくは5.3%以下であり、所望の幅を有する人工皮革を得る観点から、好ましくは1.0%以上、より好ましくは2.0%以上、さらに好ましくは3.0%以上である。好適な範囲としては、好ましくは1.0~5.5%、より好ましくは2.0~5.4%、さらに好ましくは3.0~5.3%等が挙げられる。
 面積割合Bは、染色後に人工皮革の幅を広げる割合によって調整でき、人工皮革の幅を広げる割合が高い程、減少させることができ、人工皮革の幅を広げる割合が小さい程、増加させることができる。
From the viewpoint of obtaining an artificial leather having less repulsion and a softer texture, the area ratio B is preferably 5.5% or less, more preferably 5.4% or less, and even more preferably 5.3% or less, and from the viewpoint of obtaining an artificial leather having a desired width, the area ratio B is preferably 1.0% or more, more preferably 2.0% or more, and even more preferably 3.0% or more. Suitable ranges include preferably 1.0 to 5.5%, more preferably 2.0 to 5.4%, and even more preferably 3.0 to 5.3%, etc.
The area ratio B can be adjusted by the ratio of widening the width of the artificial leather after dyeing, and the higher the ratio of widening the width of the artificial leather, the more it can be reduced, and the smaller the ratio of widening the width of the artificial leather, the more it can be increased.

 本実施形態の人工皮革の厚さは、特に限定されるものではないが、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、好ましくは0.1~2.0mm、より好ましくは0.3~1.5mm、さらに好ましくは0.5~1.2mmである。
 なお、上記「厚さ」は、JIS L1096(2010)(A法)に準じて、測定された値である。
The thickness of the artificial leather of the present embodiment is not particularly limited, but from the viewpoint of obtaining an artificial leather having less repulsion and a softer texture, it is preferably 0.1 to 2.0 mm, more preferably 0.3 to 1.5 mm, and even more preferably 0.5 to 1.2 mm.
The "thickness" is a value measured in accordance with JIS L1096 (2010) (Method A).

 本実施形態の人工皮革の見掛け密度は、特に限定されるものではないが、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、好ましくは0.10~1.00g/cm、より好ましくは0.20~0.80g/cm、さらに好ましくは0.30~0.60g/cm、よりさらに好ましくは0.35~0.48g/cmである。
 なお、上記「見掛け密度」は、JIS K6505(1995) 5.2.2に準じて、測定された値である。
The apparent density of the artificial leather of this embodiment is not particularly limited, but from the viewpoint of obtaining an artificial leather with less resilience and a softer feel, it is preferably 0.10 to 1.00 g/cm 3 , more preferably 0.20 to 0.80 g/cm 3 , even more preferably 0.30 to 0.60 g/cm 3 , and still more preferably 0.35 to 0.48 g/cm 3 .
The "apparent density" is a value measured in accordance with JIS K6505 (1995) 5.2.2.

 本実施形態の人工皮革の目付けは、特に限定されるものではないが、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、好ましくは100~1000g/m、より好ましくは150~800g/m、さらに好ましくは200~600g/mである。
 なお、上記「目付け」は、JIS L1096(2010)(A法)に準じて、測定された値である。
The basis weight of the artificial leather of this embodiment is not particularly limited, but from the viewpoint of obtaining an artificial leather with less repulsion and a softer texture, it is preferably 100 to 1000 g/m 2 , more preferably 150 to 800 g/m 2 , and even more preferably 200 to 600 g/m 2 .
The "basis weight" is a value measured in accordance with JIS L1096 (2010) (Method A).

 本実施形態の人工皮革は、特に限定されるものではないが、本発明の効果をより得られ易い観点から、立毛面を有する人工皮革、すなわち立毛人工皮革であることが好ましい。 The artificial leather of this embodiment is not particularly limited, but from the perspective of more easily achieving the effects of the present invention, it is preferable that the artificial leather be an artificial leather with a napped surface, i.e., a napped artificial leather.

<極細繊維>
 本実施形態の人工皮革に含まれる極細繊維とは、化学的または物理的性質の異なる少なくとも2種類以上の可紡性ポリマーからなる多成分系繊維(複合繊維)から、少なくとも一成分を除去することにより極細化した繊維のことである。また、極細繊維束とは、複数本の極細繊維が集まった束のことである。
<Ultrafine fibers>
The ultrafine fibers contained in the artificial leather of this embodiment are ultrafine fibers obtained by removing at least one component from a multicomponent fiber (composite fiber) made of at least two or more spinnable polymers with different chemical or physical properties. Furthermore, the ultrafine fiber bundle is a bundle of a plurality of ultrafine fibers.

 本実施形態の極細繊維は、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、長繊維であることが好ましい。
 本明細書において、「長繊維」とは、紡糸後に意図的にカットされた短繊維ではない、連続的な繊維であることを意味する。より具体的には、例えば、繊維長が3~80mm程度になるように意図的に切断されたような短繊維ではないフィラメントまたは連続繊維を意味する。後述する、極細繊維化する前の海島型複合繊維の繊維長は、100mm以上であることが好ましく、200mm以上であることがより好ましい。技術的に製造可能であり、かつ、製造工程において不可避的に切断されない限り、上記長繊維は、例えばスパンボンド法により製造され、連続的に紡糸された、数m、数百m、数km、あるいはそれ以上の繊維長の連続繊維であってもよい。なお、絡合時のニードルパンチや、表面のバフィングにより、製造工程において不可避的に長繊維の一部が切断されて短繊維になることもある。
The ultrafine fibers of the present embodiment are preferably long fibers from the viewpoint of obtaining artificial leather having less repulsion and a softer feel.
In this specification, "long fibers" means continuous fibers that are not short fibers intentionally cut after spinning. More specifically, it means filaments or continuous fibers that are not short fibers intentionally cut to a fiber length of about 3 to 80 mm, for example. The fiber length of the islands-in-sea type composite fiber before being converted into ultrafine fibers, as described below, is preferably 100 mm or more, and more preferably 200 mm or more. As long as it is technically possible to produce the long fibers and they are not inevitably cut during the production process, the long fibers may be continuous fibers that are produced, for example, by a spunbonding method and continuously spun, and have a fiber length of several meters, several hundred meters, several kilometers, or even longer. Note that needle punching during entanglement or surface buffing can unavoidably cut some of the long fibers into short fibers during the production process.

 本実施形態の極細繊維は、ポリエステル系樹脂を含有する。ポリエステル系樹脂としては、例えば、ポリエチレンテレフタレート(以下、「PET」と称すことがある。)、イソフタル酸変性PET、スルホイソフタル酸変性PET、カチオン染料可染性PET等の変性PETやポリブチレンテレフタレート、ポリヘキサメチレンテレフタレート等の芳香族ポリエステル;ポリ乳酸、ポリエチレンサクシネート、ポリブチレンサクシネート、ポリブチレンサクシネートアジペート、ポリヒドロキシブチレート-ポリヒドロキシバリレート樹脂等の脂肪族ポリエステルが挙げられる。なお、本明細書において、ポリエステル系樹脂は、ジカルボン酸系単量体単位及びジオール系単量体単位を含み、変性PETは、未変性PETのエステル形成性のジカルボン酸系単量体単位、または、ジオール系単量体単位の少なくとも一部を置換可能な単量体単位で置き換えたPETである。ジカルボン酸系単量体単位を置換する変性単量体単位の具体例としては、例えば、テレフタル酸単位を置換するイソフタル酸、ナトリウムスルホイソフタル酸、ナトリウムスルホナフタレンジカルボン酸、アジピン酸、等に由来する単位が挙げられる。また、ジオール系単量体単位を置換する変性単量体単位の具体例としては、例えば、エチレングリコール単位を置換するブタンジオール、ヘキサンジオール等のジオールに由来する単位が挙げられる。
 本実施形態のポリエステル系樹脂は、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、PETであることが好ましい。
 また、前記PETは、リサイクル性の観点、及びより反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、ジカルボン酸系単量体単位の94モル%以上がテレフタル酸単位であることが好ましく、より好ましくは95モル%以上、さらに好ましくは96モル%以上であり、100モル%であってもよい。
 また、前記PETは、リサイクル性の観点、及びより反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、ジオール系単量体単位の94モル%以上がエチレングリコール単位であることが好ましく、より好ましくは95モル%以上、さらに好ましくは96モル%以上であり、100モル%であってもよい。
The ultrafine fibers of this embodiment contain a polyester-based resin. Examples of polyester-based resins include modified PET such as polyethylene terephthalate (hereinafter sometimes referred to as "PET"), isophthalic acid-modified PET, sulfoisophthalic acid-modified PET, and cationic dye-dyeable PET; aromatic polyesters such as polybutylene terephthalate and polyhexamethylene terephthalate; and aliphatic polyesters such as polylactic acid, polyethylene succinate, polybutylene succinate, polybutylene succinate adipate, and polyhydroxybutyrate-polyhydroxyvalerate resin. In this specification, the polyester-based resin contains dicarboxylic acid-based monomer units and diol-based monomer units, and modified PET is PET in which at least a portion of the ester-forming dicarboxylic acid-based monomer units or diol-based monomer units of unmodified PET have been replaced with substitutable monomer units. Specific examples of the modified monomer unit substituting the dicarboxylic acid monomer unit include units derived from isophthalic acid, sodium sulfoisophthalic acid, sodium sulfonaphthalenedicarboxylic acid, adipic acid, etc., which substitute for the terephthalic acid unit. Specific examples of the modified monomer unit substituting the diol monomer unit include units derived from diols such as butanediol and hexanediol, which substitute for the ethylene glycol unit.
The polyester resin of the present embodiment is preferably PET from the viewpoint of obtaining artificial leather with less repulsion and a softer feel.
Furthermore, from the viewpoint of recyclability and of obtaining artificial leather having less repulsion and a softer texture, the PET preferably contains 94 mol % or more of dicarboxylic acid monomer units as terephthalic acid units, more preferably 95 mol % or more, even more preferably 96 mol % or more, and may even contain 100 mol %.
Furthermore, from the viewpoint of recyclability and of obtaining artificial leather having less repulsion and a softer texture, the PET preferably contains 94 mol % or more of diol-based monomer units as ethylene glycol units, more preferably 95 mol % or more, even more preferably 96 mol % or more, and may contain 100 mol %.

 本実施形態のポリエステル系樹脂は、サスティナブルの観点、及び繊維が膠着することを抑制し、反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、未変性PETであることが好ましい。
 また、本実施形態のポリエステル系樹脂は、サスティナブルの観点からリサイクルPETであることが好ましい。
The polyester resin of the present embodiment is preferably unmodified PET from the viewpoint of sustainability and from the viewpoint of suppressing adhesion of fibers and obtaining artificial leather with less repulsion and a softer texture.
Moreover, the polyester resin of the present embodiment is preferably recycled PET from the viewpoint of sustainability.

 本実施形態のポリエステル系樹脂の固有粘度は、極細繊維発生型繊維の断面形成性の観点から、好ましくは0.63dl/g以下、より好ましくは、0.625dl/g以下、さらに好ましくは0.62dl/g以下であり、引張強度、引張伸度、引裂強度等の機械物性の観点から、好ましくは0.55dl/g以上、より好ましくは0.56dl/g以上、さらに好ましくは0.57dl/g以上である。好適な範囲としては、好ましくは0.55~0.63dl/g、より好ましくは0.56~0.625dl/g、さらに好ましくは0.57~0.62dl/g等が挙げられる。
 なお、上記「固有粘度」は、溶媒としてフェノール/テトラクロロエタン(体積比1/1)混合溶媒を用い、測定温度30℃にて、ウベローデ型粘度計を用いて測定される値であり、具体的には実施例に記載の手順で測定される。
The intrinsic viscosity of the polyester resin of this embodiment is preferably 0.63 dl/g or less, more preferably 0.625 dl/g or less, and even more preferably 0.62 dl/g or less, from the viewpoint of cross-section formability of the ultrafine fiber-forming fiber, and is preferably 0.55 dl/g or more, more preferably 0.56 dl/g or more, and even more preferably 0.57 dl/g or more, from the viewpoint of mechanical properties such as tensile strength, tensile elongation, and tear strength. Suitable ranges include preferably 0.55 to 0.63 dl/g, more preferably 0.56 to 0.625 dl/g, and even more preferably 0.57 to 0.62 dl/g.
The "intrinsic viscosity" is a value measured using a phenol/tetrachloroethane (volume ratio 1/1) mixed solvent as a solvent at a measurement temperature of 30°C using an Ubbelohde viscometer, and specifically, is measured by the procedure described in the Examples.

 本実施形態の極細繊維は、ポリエステル系樹脂以外の樹脂を含有してもよく、含有していなくてもよい。
 ポリエステル系樹脂以外の樹脂としては、例えば、;ナイロン6、ナイロン66、ナイロン10、ナイロン11、ナイロン12、ナイロン6-12等のナイロン;ポリプロピレン、ポリエチレン、ポリブテン、ポリメチルペンテン、塩素系ポリオレフィン等の繊維が挙げられる。
 リサイクル性の観点から、極細繊維は、ポリエステル系樹脂以外の樹脂を含有しないことが好ましい。
The ultrafine fibers of the present embodiment may or may not contain a resin other than the polyester-based resin.
Examples of resins other than polyester-based resins include nylons such as nylon 6, nylon 66, nylon 10, nylon 11, nylon 12, and nylon 6-12; and fibers such as polypropylene, polyethylene, polybutene, polymethylpentene, and chlorinated polyolefins.
From the viewpoint of recyclability, it is preferable that the ultrafine fibers contain no resin other than the polyester-based resin.

 本実施形態の極細繊維を構成する樹脂は、本発明の効果を損なわない範囲で、各種添加剤を含んでもよい。添加剤としては、例えば、触媒、着色剤、耐熱剤、難燃剤、滑剤、防汚剤、蛍光増白剤、艶消剤、光沢改良剤、制電剤、芳香剤、消臭剤、抗菌剤、防ダニ剤、無機微粒子等が挙げられる。 The resin that constitutes the ultrafine fibers of this embodiment may contain various additives, provided that the effects of the present invention are not impaired. Examples of additives include catalysts, colorants, heat resistance agents, flame retardants, lubricants, stain-resistant agents, fluorescent brighteners, matting agents, gloss improvers, antistatic agents, fragrances, deodorizers, antibacterial agents, anti-mite agents, and inorganic fine particles.

 本実施形態の極細繊維の平均径は、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、好ましくは7.5μm以下、より好ましくは6.0μm以下、さらに好ましくは5.5μm以下、よりさらに好ましくは5.0μm以下である。下限に特に制限はないが、製造容易性及び発色性の観点から、1.0μm以上であってもよく、1.5μm以上であってもよい。好適な範囲としては、好ましくは1.0~7.5μm、より好ましくは1.0~6.0μm、さらに好ましくは1.0~5.5μm、よりさらに好ましくは1.5~5.0μm等が挙げられる。 The average diameter of the ultrafine fibers of this embodiment is preferably 7.5 μm or less, more preferably 6.0 μm or less, even more preferably 5.5 μm or less, and even more preferably 5.0 μm or less, from the viewpoint of obtaining artificial leather with less resilience and a softer feel. There is no particular lower limit, but from the viewpoint of ease of production and color development, it may be 1.0 μm or more, or even 1.5 μm or more. Suitable ranges include preferably 1.0 to 7.5 μm, more preferably 1.0 to 6.0 μm, even more preferably 1.0 to 5.5 μm, and even more preferably 1.5 to 5.0 μm.

 本実施形態の極細繊維の平均繊度は、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、好ましくは0.50dtex以下、より好ましくは0.40dtex以下、さらに好ましくは0.30dtex以下である。下限に特に制限はないが、製造容易性及び発色性の観点から、例えば、0.01dtex以上であってもよく、0.02dtex以上であってもよい。好適な範囲としては、好ましくは0.01~0.50dtex、より好ましくは0.01~0.40dtex、さらに好ましくは0.02~0.30dtex等が挙げられる。
 なお、上記「平均径」及び「平均繊度」は、極細繊維の断面の拡大写真において、ランダムに選んだ複数の極細繊維について断面積を測定し、それらに基づいて算出した値であり、具体的には実施例に記載の手順で測定される。
From the viewpoint of obtaining an artificial leather having less resilience and a softer feel, the average fineness of the ultrafine fibers of this embodiment is preferably 0.50 dtex or less, more preferably 0.40 dtex or less, and even more preferably 0.30 dtex or less. There is no particular lower limit, but from the viewpoint of ease of production and color development, it may be, for example, 0.01 dtex or more, or 0.02 dtex or more. Suitable ranges include preferably 0.01 to 0.50 dtex, more preferably 0.01 to 0.40 dtex, and even more preferably 0.02 to 0.30 dtex.
The "average diameter" and "average fineness" are values calculated based on the cross-sectional areas of a plurality of ultrafine fibers randomly selected from an enlarged photograph of the cross sections of the ultrafine fibers, and are specifically measured by the procedure described in the Examples.

<高分子弾性体>
 本実施形態の人工皮革は、高分子弾性体を含んでもよく、含まなくてもよい。
 高分子弾性体は、人工皮革に従来用いられているものであれば何れも採用可能であり、具体例としてはポリウレタンエラストマー、アクリロニトリルエラストマー、オレフィンエラストマー、ポリエステルエラストマー、アクリルエラストマーが挙げられ、好ましくはポリウレタンエラストマー、アクリルエラストマーである。
 ポリウレタンエラストマーとしては、ポリエステルジオール、ポリエーテルジオール、ポリエーテルエステルジオール、ポリカーボネートジオール、ポリカーボネートエーテルジオール、ポリカーボネートエステルジオール等から選ばれた少なくとも1種類の平均分子量500~3000のポリマーポリオールと、4,4’-ジフェニルメタンジイソシアネート、イソホロンジイソシアネート、ヘキサメチレンジイソシアネート等の、芳香族系、脂環族系、脂肪族系のジイソシアネート等から選ばれた少なくとも1種のポリイソシアネートとを主成分として組み合わせ、さらにエチレングリコール、エチレンジアミン等の2個以上の活性水素原子を有する少なくとも1種の低分子化合物を所定のモル比で組み合わせて、これらを1段階、あるいは多段階で溶融重合法、塊状重合法、溶液重合法等により重合反応させて得た各種のポリウレタンエラストマーが挙げられる。
 ポリウレタンエラストマーに占めるポリマーポリオール成分の含有量は15~90質量%が好ましい。
<Polymeric elastomer>
The artificial leather of this embodiment may or may not contain a polymeric elastomer.
Any polymeric elastomer that has conventionally been used in artificial leathers can be used. Specific examples include polyurethane elastomers, acrylonitrile elastomers, olefin elastomers, polyester elastomers, and acrylic elastomers, with polyurethane elastomers and acrylic elastomers being preferred.
Examples of polyurethane elastomers include various polyurethane elastomers obtained by combining, as main components, at least one polymer polyol having an average molecular weight of 500 to 3000 selected from polyester diols, polyether diols, polyether ester diols, polycarbonate diols, polycarbonate ether diols, polycarbonate ester diols, and the like, and at least one polyisocyanate selected from aromatic, alicyclic, and aliphatic diisocyanates, such as 4,4'-diphenylmethane diisocyanate, isophorone diisocyanate, and hexamethylene diisocyanate, and further combining with at least one low molecular weight compound having two or more active hydrogen atoms, such as ethylene glycol and ethylenediamine, in a predetermined molar ratio, and polymerizing these in one stage or multiple stages by melt polymerization, bulk polymerization, solution polymerization, or the like.
The content of the polymer polyol component in the polyurethane elastomer is preferably 15 to 90% by mass.

 また、アクリルエラストマーとしては、その単独重合体のガラス転移温度が-90~-5℃の範囲であり、好ましくは非架橋性であるようなモノマー、例えば、アクリル酸メチル、アクリル酸n-ブチル、アクリル酸イソブチル、アクリル酸イソプロピル、(メタ)アクリル酸n-ヘキシル、及び(メタ)アクリル酸2-エチルヘキシルからなる群から選ばれる少なくとも1種類の軟質成分と、その単独重合体のガラス転移温度が50~250℃の範囲であり、好ましくは非架橋性であるようなモノマー、例えば、メタクリル酸メチル、メタクリル酸エチル、メタクリル酸イソプロピル、メタクリル酸イソブチル、メタクリル酸シクロヘキシル、(メタ)アクリル酸からなる群から選ばれる少なくとも1種類の硬質成分と、架橋構造を形成し得る単官能または多官能エチレン性不飽和モノマー単位、または、ポリマー鎖に導入されたエチレン製不飽和モノマー単位と反応して架橋構造を形成し得るような化合物、例えば、エチレングリコールジ(メタ)アクリレート、トリエチレングリコールジ(メタ)アクリレート、ポリエチレングリコールジ(メタ)アクリレート、1,4-ブタンジオールジ(メタ)アクリレートからなる群から選ばれる少なくとも1種類の架橋形成性成分からなるエチレン性不飽和モノマーを重合反応させて得た各種のアクリルエラストマーが挙げられる。 Furthermore, the acrylic elastomer may comprise at least one soft component selected from the group consisting of a monomer whose homopolymer has a glass transition temperature in the range of -90 to -5°C and is preferably non-crosslinkable, such as methyl acrylate, n-butyl acrylate, isobutyl acrylate, isopropyl acrylate, n-hexyl (meth)acrylate, and 2-ethylhexyl (meth)acrylate, and a monomer whose homopolymer has a glass transition temperature in the range of 50 to 250°C and is preferably non-crosslinkable, such as methyl methacrylate, ethyl methacrylate, isopropyl methacrylate, isobutyl methacrylate, or cyclohexyl methacrylate. Examples of such acrylic elastomers include various acrylic elastomers obtained by polymerizing at least one hard component selected from the group consisting of acrylic acid, acrylic acid, and (meth)acrylic acid with a monofunctional or polyfunctional ethylenically unsaturated monomer unit capable of forming a crosslinked structure, or a compound capable of forming a crosslinked structure by reacting with an ethylenically unsaturated monomer unit introduced into a polymer chain, such as at least one ethylenically unsaturated monomer comprising a crosslinkable component selected from the group consisting of ethylene glycol di(meth)acrylate, triethylene glycol di(meth)acrylate, polyethylene glycol di(meth)acrylate, and 1,4-butanediol di(meth)acrylate.

 主要な高分子弾性体としてポリウレタンエラストマーを採用して得られた人工皮革は、風合いや力学的物性のバランスが優れており、さらには適宜種類を選択すれば耐久性を含めたバランスにも優れている点で好ましい。また、アクリルエラストマーを採用して得られた人工皮革は、アクリルエラストマーがポリウレタンエラストマーに比べて極細繊維束への接着性が低く、立毛形成時の立毛固定効果に乏しいので立毛人工皮革を形成するには不向きだが、含有量に対する風合いの硬化度合いが抑制されるので銀付調人工皮革を形成する場合には特に好ましい。
 高分子弾性体としては、異なる種類を混合して含有させたり、異なる種類を複数回に分けて含有させたりしてもよく、また、上述したポリウレタンエラストマー、アクリロニトリルエラストマー、オレフィンエラストマー、ポリエステルエラストマー、アクリルエラストマー等の主体となる高分子弾性体以外にも、合成ゴム等の高分子弾性体を必要に応じて添加した高分子弾性体組成物として含有させてもよい。
Artificial leathers obtained by using polyurethane elastomers as the main polymeric elastomer are preferred because they have an excellent balance of texture and mechanical properties, and if the type is appropriately selected, they also have an excellent balance, including durability. Artificial leathers obtained by using acrylic elastomers are unsuitable for forming napped artificial leathers because the acrylic elastomers have lower adhesion to ultrafine fiber bundles than polyurethane elastomers and are poor at fixing the nap during nap formation, but are particularly preferred for forming grain-finish artificial leathers because the degree of hardening of the texture relative to the content is suppressed.
As the polymer elastomer, different types may be mixed and contained, or different types may be contained in separate batches. Furthermore, in addition to the above-mentioned polymer elastomers such as polyurethane elastomers, acrylonitrile elastomers, olefin elastomers, polyester elastomers, and acrylic elastomers that serve as the main component, a polymer elastomer such as synthetic rubber may be added as needed to form a polymer elastomer composition.

 本実施形態の人工皮革が高分子弾性体を含む場合、その含有量は、風合いに優れる人工皮革を得る観点から、人工皮革中、好ましくは5~45質量%、より好ましくは7~40質量%、さらに好ましくは8~30質量%である。 When the artificial leather of this embodiment contains a polymeric elastomer, its content in the artificial leather is preferably 5 to 45% by mass, more preferably 7 to 40% by mass, and even more preferably 8 to 30% by mass, from the viewpoint of obtaining an artificial leather with an excellent texture.

<他の成分>
 本実施形態の人工皮革には、極細繊維及び高分子弾性体以外の成分が含まれていてもよいし、含まれていなくてもよい。このような他の成分としては、上述した極細繊維に含まれる他の成分や前述の高分子弾性体を含浸させる際に用いる高分子弾性体液に添加し得る各種添加剤と同様のものが挙げられる。上記他の成分は、極細繊維及び高分子弾性体のうち少なくとも一方に内包されていてもよい。
 上記他の成分の含有量は、上記他の成分による所期の効果を発現させやすくするとともに、吸水性、撥水性、防汚性等の観点から、人工皮革の質量に対して、好ましくは0.5~10.0質量%、より好ましくは1.0~5.0質量%、さらに好ましくは1.5~3.0質量%である。
<Other ingredients>
The artificial leather of this embodiment may or may not contain components other than the ultrafine fibers and the polymeric elastomer. Such other components include the other components contained in the ultrafine fibers described above and the various additives that can be added to the polymeric elastomer liquid used to impregnate the ultrafine fibers. The other components may be encapsulated in at least one of the ultrafine fibers and the polymeric elastomer.
The content of the other components is preferably 0.5 to 10.0% by mass, more preferably 1.0 to 5.0% by mass, and even more preferably 1.5 to 3.0% by mass, relative to the mass of the artificial leather, from the viewpoints of water absorbency, water repellency, stain resistance, etc., as well as making it easier for the other components to exhibit their intended effects.

[人工皮革の製造方法]
 本実施形態に係る人工皮革は、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、以下の工程(1)~(4)を備え、下記工程(1)で準備する繊維ウェブの横方向の降伏点の強度Xと、降伏点以降の最大強度Yとの比(Y/X)が、4.0以下である製造方法により製造することが好ましい。
工程(1):極細繊維発生型繊維から形成された繊維ウェブを準備する工程
工程(2):前記繊維ウェブを用いて絡合繊維シートを形成する工程
工程(3):前記絡合繊維シートを収縮させ、前記極細繊維発生型繊維から少なくとも一成分を除去することにより、人工皮革基体を得る工程
工程(4)前記人工皮革基体を染色する工程
[Manufacturing method of artificial leather]
From the viewpoint of obtaining an artificial leather having less resilience and a softer texture, the artificial leather according to the present embodiment is preferably produced by a production method comprising the following steps (1) to (4), in which the ratio (Y/X) of the strength X at the yield point in the lateral direction of the fiber web prepared in the following step (1) to the maximum strength Y after the yield point is 4.0 or less.
Step (1): A step of preparing a fiber web formed from ultrafine fiber-generating fibers. Step (2): A step of forming an entangled fiber sheet using the fiber web. Step (3): A step of obtaining an artificial leather substrate by shrinking the entangled fiber sheet and removing at least one component from the ultrafine fiber-generating fibers. Step (4): A step of dyeing the artificial leather substrate.

 本実施形態に係る製造方法が、横方向の降伏点の強度Xと、降伏点以降の最大強度Yとの比(Y/X)が、4.0以下である繊維ウェブを準備する工程(工程(1))を有することで、本実施形態の人工皮革が得られやすくなる。
 以下、各工程について説明する。
The manufacturing method according to the present embodiment includes a step (step (1)) of preparing a fiber web in which the ratio (Y/X) of the strength X at the yield point in the lateral direction to the maximum strength Y after the yield point is 4.0 or less, thereby making it easier to obtain the artificial leather of the present embodiment.
Each step will be described below.

<工程(1)>
 工程(1)は、極細繊維発生型繊維から形成された繊維ウェブを準備する工程である。
 上述のとおり、極細繊維とは、化学的または物理的性質の異なる少なくとも2種類以上の可紡性ポリマーからなる多成分系繊維(複合繊維)から、少なくとも一成分を除去することにより極細化した繊維のことであり、この極細繊維を発生させる多成分系繊維が極細繊維発生型繊維である。極細繊維発生型繊維の代表例としては、チップブレンド(混合紡糸)方式や複合紡糸方式等の方法を用いて得られる海島型複合繊維、多層積層型複合繊維、放射型積層型複合繊維等がある。これらの中でも、海島型複合繊維が、高速紡糸により生産性を高められ、さらに表面の耐摩耗性、及び耐ピリング性に優れる人工皮革を得る観点から好ましく、同様の観点から、海島型複合繊維を溶融紡糸して繊維ウェブを得ることが好ましい。
 極細繊維発生型繊維が海島型複合繊維の場合、繊維断面において、マトリクスとなる海成分中に、島成分が分散されており、海成分を除去することにより、繊維束状の極細繊維を発生させる。
 以下、極細繊維発生型繊維として、海島型複合繊維を用い、海島型複合繊維を溶融紡糸して繊維ウェブを得る方法についてより詳しく説明する。
<Step (1)>
Step (1) is a step of preparing a fiber web formed from ultrafine fiber-generating fibers.
As described above, ultrafine fibers are fibers that have been made ultrafine by removing at least one component from a multicomponent fiber (composite fiber) made of at least two or more types of spinnable polymers that differ in chemical or physical properties, and the multicomponent fiber that generates these ultrafine fibers is an ultrafine fiber-generating fiber. Typical examples of ultrafine fiber-generating fibers include islands-in-sea type composite fibers, multilayer laminated composite fibers, and radial laminated composite fibers, which are obtained using methods such as chip blending (mixed spinning) and composite spinning. Among these, islands-in-sea type composite fibers are preferred from the viewpoints of increasing productivity through high-speed spinning and of obtaining artificial leather that is excellent in surface abrasion resistance and pilling resistance, and from the same viewpoint, it is preferred to obtain a fiber web by melt spinning islands-in-sea type composite fibers.
When the ultrafine fiber-generating fiber is an islands-in-sea type composite fiber, island components are dispersed in a sea component that serves as a matrix in the fiber cross section, and by removing the sea component, ultrafine fibers in the form of fiber bundles are generated.
Hereinafter, a method for obtaining a fiber web by melt-spinning islands-in-sea type composite fibers, using islands-in-sea type composite fibers as ultrafine fiber-forming fibers, will be described in more detail.

 海島型複合繊維に含まれ、後に極細繊維となる島成分の樹脂としては、上述の「極細繊維」における極細繊維を構成する樹脂と同様の樹脂が挙げられる。
 海島型複合繊維に含まれ、抽出や分解すること等により除去される海成分の樹脂としては、島成分の樹脂と溶解性または分解性が異なり、かつ、相溶性の低い樹脂を用いることが好ましい。このような樹脂は、島成分の樹脂の種類や製造方法に応じて適宜選択されることが好ましい。
 海成分の樹脂としては、例えば、ポリエチレン、ポリプロピレン、エチレンプロピレン共重合体、エチレン酢ビ共重合体等のオレフィン系樹脂やポリスチレン、スチレンアクリル共重合体、スチレンエチレン共重合体等の有機溶剤に溶解性があり、有機溶剤により溶解除去できる樹脂が挙げられる。また、ポリビニルアルコール系樹脂、水溶性ポリエステル樹脂、易アルカリ分解性の変性ポリエステル樹脂、ポリアクリルアミド樹脂、カルボキシメチルセルロース樹脂等の溶剤を用いず水だけで除去処理可能である樹脂が挙げられる。これらの中でも、溶融紡糸性、水溶性、及び繊維物性(繊維の強度)の観点から、ポリエチレン及びポリビニルアルコール系樹脂を用いることが好ましく、より好ましくはポリエチレン及び変性ポリビニルアルコールである。
Examples of the island component resins contained in the islands-in-sea type composite fibers and later to become the ultrafine fibers include the same resins as those constituting the ultrafine fibers in the above-mentioned "ultrafine fibers."
The sea component resin contained in the islands-in-sea type composite fiber and removed by extraction, decomposition, etc. is preferably a resin that has a solubility or decomposability different from that of the island component resin and has low compatibility with it. Such a resin is preferably selected appropriately depending on the type of island component resin and the production method.
Examples of the resin for the sea component include olefin-based resins such as polyethylene, polypropylene, ethylene-propylene copolymer, and ethylene-vinyl acetate copolymer, as well as resins that are soluble in organic solvents and can be dissolved and removed by organic solvents, such as polystyrene, styrene-acrylic copolymer, and styrene-ethylene copolymer. Other examples include resins that can be removed using only water without using a solvent, such as polyvinyl alcohol-based resins, water-soluble polyester resins, easily alkali-decomposable modified polyester resins, polyacrylamide resins, and carboxymethyl cellulose resins. Among these, polyethylene and polyvinyl alcohol-based resins are preferred from the viewpoints of melt spinnability, water solubility, and fiber properties (fiber strength), and more preferred are polyethylene and modified polyvinyl alcohol.

 変性ポリビニルアルコールで用いる共重合単量体の種類としては、共重合性、溶融紡糸性、及び繊維の水溶性の観点からエチレン、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;及び、メチルビニルエーテル、エチルビニルエーテル、n-プロピルビニルエーテル、イソ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好ましい。
 ポリビニルアルコール中の共重合単位含有量は、1~20モル%が好ましく、4~15モル%がより好ましく、6~13モル%がさらに好ましい。
 さらに、共重合単位がエチレンであると繊維物性が高くなるので、エチレン変性ポリビニルアルコールがより好ましい。エチレン変性ポリビニルアルコール中のエチレン単位含有量は、好ましくは4~15モル%、より好ましくは6~13モル%である。
As the type of copolymerization monomer used in the modified polyvinyl alcohol, from the viewpoints of copolymerizability, melt spinnability, and water solubility of the fibers, preferred are α-olefins having 4 or less carbon atoms, such as ethylene, propylene, 1-butene, and isobutene; and vinyl ethers, such as methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, isopropyl vinyl ether, and n-butyl vinyl ether.
The content of copolymerized units in polyvinyl alcohol is preferably from 1 to 20 mol %, more preferably from 4 to 15 mol %, and even more preferably from 6 to 13 mol %.
Furthermore, since the copolymerization unit is ethylene, the fiber properties are improved, and therefore ethylene-modified polyvinyl alcohol is more preferred. The ethylene unit content in the ethylene-modified polyvinyl alcohol is preferably 4 to 15 mol %, more preferably 6 to 13 mol %.

 海島型複合繊維の海成分と島成分との質量割合は特に限定されないが、例えば、海成分:島成分=5:95~80:20の範囲であることが好ましい。海島型複合繊維中の海成分ポリマー比率が5質量%以上であれば、海島型繊維の紡糸安定性が低下しづらく工業的生産性を確保しやすい。また、高分子弾性体を付与した場合に、海成分を除去した後で極細繊維束と高分子弾性体との間に必要な大きさの空隙が形成されやすくなり、結果的に、膨らみ感や充実感、緻密な表面感等が得られやすくなる。一方、海成分ポリマー比率が80質量%以下であれば、海島型繊維の断面における島成分の形状や分布状態が安定し、品質安定性の低下を防止しやすい。 The mass ratio of the sea component to the island component in the islands-in-sea composite fiber is not particularly limited, but preferably falls within the range of 5:95 to 80:20 (sea component:island component). If the sea component polymer ratio in the islands-in-sea composite fiber is 5% by mass or more, the spinning stability of the islands-in-sea fiber is less likely to decrease, making it easier to ensure industrial productivity. Furthermore, when a polymer elastomer is added, voids of the required size are more likely to form between the ultrafine fiber bundles and the polymer elastomer after the sea component is removed, making it easier to achieve a fluffy, full, dense surface. On the other hand, if the sea component polymer ratio is 80% by mass or less, the shape and distribution of the island component in the cross section of the islands-in-sea fiber are stable, making it easier to prevent a decrease in quality stability.

 繊維ウェブの製造方法としては、いわゆるスパンボンド法を用いて溶融紡糸された極細繊維発生型繊維をカットせずに搬送ベルト上に捕集して、連続繊維である長繊維の繊維ウェブを形成する方法を採用することが好ましい。 The preferred method for producing a fiber web is to use the so-called spunbond method, in which ultrafine fiber-generating fibers are melt-spun and collected on a conveyor belt without cutting, to form a fiber web of continuous long fibers.

 具体的には、多数のノズル孔が所定のパターンで配置された複合紡糸用口金を用いて、海島型複合繊維の溶融ストランドを紡糸ノズルから所定の吐出速度で連続的に吐出させ、ノズル孔直下から後述する吸引装置までの間の何れかの段階で冷却風により実質的に冷却固化しながら、エアジェットノズル等の吸引装置を用いて高速気流を作用させ、海島型複合繊維が目的の径または繊度になるよう均一に牽引細化する。
 高速気流は、例えば、通常の紡糸における機械的な引取り速度に相当する平均紡糸速度が、1000~6000m/分の範囲における何れかの速度となるように作用させてもよい。さらに、得られる繊維ウェブの地合い等に応じて、海島型複合繊維を衝突板や気流等により開繊させながら、コンベヤベルト状の縦方向に移動する搬送ベルト等の捕集面上に、搬送ベルトの反対面側から吸引しながら、捕集・堆積させることで長繊維ウェブを形成させるようなスパンボンド法により、繊維ウェブを製造することができる。
 本発明の効果を効率的に得る観点から、エアジェットノズルと捕集面との距離は、10~100cmであることが好ましく、より好ましくは30~80cm、さらに好ましくは40~70cmである。捕集面への吸引速度は5~35m/秒であることが好ましく、より好ましくは10~25m/秒である。また、捕集面の移動速度は20~150m/分であることが好ましく、より好ましくは50~120m/分である。
 平均紡糸速度、エアジェットノズルと捕集面との距離、捕集面への吸引速度、捕集面の移動速度等を調整することで、捕集面上に捕集される海島型複合繊維の広がり具合や交差数を適切に調整することができる。その結果、より反発感が少なく、より柔軟な風合いを有する人工皮革を得ることができる。
Specifically, a conjugate spinning die having a large number of nozzle holes arranged in a predetermined pattern is used to continuously extrude molten strands of islands-in-sea type composite fibers from a spinning nozzle at a predetermined extrusion speed, and the strands are substantially cooled and solidified by cooling air at any stage between just below the nozzle holes and the suction device described below. A high-velocity air stream is applied using a suction device such as an air jet nozzle, and the islands-in-sea type composite fibers are uniformly drawn and attenuated to a desired diameter or fineness.
The high-speed air stream may be applied so that the average spinning speed, which corresponds to the mechanical take-up speed in normal spinning, is any speed in the range of 1,000 to 6,000 m/min. Furthermore, a fiber web can be produced by a spunbonding method in which, depending on the texture of the resulting fiber web, the islands-in-sea type composite fibers are opened by an impingement plate, an air stream, or the like, and then collected and deposited on a collecting surface such as a conveyor belt that moves in the longitudinal direction while being sucked from the opposite side of the conveyor belt to form a long-fiber web.
From the viewpoint of efficiently achieving the effects of the present invention, the distance between the air jet nozzle and the collection surface is preferably 10 to 100 cm, more preferably 30 to 80 cm, and even more preferably 40 to 70 cm. The suction speed to the collection surface is preferably 5 to 35 m/sec, more preferably 10 to 25 m/sec. The movement speed of the collection surface is preferably 20 to 150 m/min, more preferably 50 to 120 m/min.
The degree of spreading and the number of intersections of the islands-in-sea type composite fibers collected on the collecting surface can be appropriately adjusted by adjusting the average spinning speed, the distance between the air jet nozzle and the collecting surface, the suction speed onto the collecting surface, the movement speed of the collecting surface, etc. As a result, an artificial leather with less repulsion and a softer feel can be obtained.

 繊維ウェブを準備する工程において、搬送ベルト等の捕集面上に捕集される海島型複合繊維の広がりが大きい程、繊維同士の交差数が増える。繊維同士の交差数が多い程、絡合繊維シートを収縮させ、極細繊維発生型繊維から少なくとも一成分を除去する際に、縦方向の伸びに伴う残留歪みが高くなり、横方向に伸び難くなることで、面積割合Aは増加する。
 また、ベルトへ着地する時の広がりが小さい程、繊維同士の交差数は減る。繊維同士の交差数が少ない程、極細繊維発生型繊維から少なくとも一成分を除去する際に、縦方向の伸びに伴い繊維が適度に素抜けし易くなり、残留歪みが残り難くなり、横方向に伸び易くなることで、面積割合Aは減少する。
In the step of preparing a fiber web, the greater the spread of the islands-in-sea type composite fibers collected on a collecting surface such as a conveyor belt, the greater the number of intersections between the fibers. The greater the number of intersections between the fibers, the greater the residual strain associated with longitudinal elongation when the entangled fiber sheet is shrunk and at least one component is removed from the ultrafine fiber-generating fibers, making it more difficult to elongate in the transverse direction, and therefore the area ratio A increases.
Furthermore, the smaller the spread when the fibers land on the belt, the fewer the number of intersections between the fibers. The fewer the number of intersections between the fibers, the easier it is for the fibers to be properly pulled out as they stretch in the longitudinal direction when at least one component is removed from the ultrafine fiber-generating fiber, making it less likely that residual strain will remain and making them more likely to stretch in the transverse direction, thereby reducing the area ratio A.

 繊維ウェブは、形態安定性を付与するために熱プレスによる処理がなされてもよく、それに伴い繊維ウェブに融着が施されてもよい。 The fiber web may be subjected to a heat press treatment to impart shape stability, and the fiber web may be fused as a result.

 工程(1)で得られる繊維ウェブの横方向の降伏点の強度Xと、降伏点以降の最大強度Yとの比(Y/X)が、4.0以下であると、繊維の交差数が適度になり、本実施形態の人工皮革が得られやすくなる。このような繊維ウェブは、工程(3)で、横方向(幅方向)が収縮し、横方向の繊維の緊張が緩和することに加え、縦方向に繊維が適度に素抜けて縦方向の緊張も緩和でき、かつ厚みくたりも抑制され、見掛け密度が上昇し難く、柔軟な風合いを有する人工皮革を得られやすくなる。
 Y/Xは、より反発感が少なく、より柔軟な風合いを有する人工皮革を得る観点から、好ましくは3.9以下である。
When the ratio (Y/X) of the strength X at the yield point in the transverse direction of the fiber web obtained in step (1) to the maximum strength Y after the yield point is 4.0 or less, the number of fiber intersections becomes appropriate, and the artificial leather of this embodiment becomes easy to obtain. In step (3), such a fiber web shrinks in the transverse direction (width direction), which not only relieves the tension of the fibers in the transverse direction but also allows the fibers to be appropriately passed through in the longitudinal direction, thereby relieving the tension in the longitudinal direction, and thickness collapse is suppressed, making it easy to obtain an artificial leather that is less likely to increase in apparent density and has a soft texture.
From the viewpoint of obtaining an artificial leather having less repulsion and a softer feel, Y/X is preferably 3.9 or less.

<工程(2)>
 工程(2)は、前記繊維ウェブを用いて絡合繊維シートを形成する工程である。
 工程(2)は、工程(1)で得られた繊維ウェブを、複数層重ね合わせた後、ニードルパンチや水流交絡処理等による絡合処理を施すことにより、厚み方向に長繊維が絡合された絡合ウェブを得る工程である。
 繊維ウェブを複数枚重ねる方法としては、繊維ウェブを全て同方向にして重ねてもよく、クロスラッピング方式により繊維ウェブの搬送方向を90°方向に変えて折り返しながら重ねてもよい。繊維ウェブを複数枚重ねる方法は、絡合繊維シートの幅を任意に調整しやすく、繊維ウェブの幅方向の斑の発生を抑制できる、すなわち目付けの不均一を抑制できる観点から、クロスラップ積層が好ましい。
 重ね合わせるウェブの層数は特に限定されないが、機械的強度の観点から、好ましくは4層以上、より好ましくは8層以上であり、製造容易性の観点から、好ましくは20層以下、より好ましくは16層以下である。
<Step (2)>
Step (2) is a step of forming an entangled fiber sheet using the fiber web.
In step (2), a plurality of layers of the fiber web obtained in step (1) are superimposed on one another, and then subjected to an entanglement treatment such as needle punching or hydroentanglement treatment to obtain an entangled web in which the long fibers are entangled in the thickness direction.
As a method for stacking a plurality of fiber webs, the fiber webs may be stacked in the same direction, or the fiber webs may be stacked by changing the conveying direction of the fiber web to a 90° direction and folding it back by a cross-lapping method. The method for stacking a plurality of fiber webs is preferably cross-lapping lamination, from the viewpoints that it is easy to adjust the width of the entangled fiber sheet as desired and it can suppress the occurrence of unevenness in the width direction of the fiber web, i.e., it can suppress unevenness in the basis weight.
The number of layers of the web to be superimposed is not particularly limited, but from the viewpoint of mechanical strength, it is preferably 4 layers or more, more preferably 8 layers or more, and from the viewpoint of ease of production, it is preferably 20 layers or less, more preferably 16 layers or less.

 複数層重ね合わせた繊維ウェブにニードルパンチ法や高圧水流処理法等の公知の方法により、機械的な絡合処理を施すことで、繊維ウェブを構成する繊維同士、特にラッピングや積重した層状の繊維ウェブの隣接する層間における繊維同士を三次元絡合させる。
 ニードルパンチ法により絡合処理する場合は、ニードルの種類(ニードルの形状や番手、バーブの形状や深さ、バーブの数や位置等)、ニードルのパンチ数(ニードルボードに植針されたニードルの密度と該ボードを繊維ウェブの単位面積当たりに作用させるストローク数を掛け合わせた単位面積当たりのニードルパンチ処理密度)、ニードルのパンチ深さ(繊維ウェブに対してニードルを作用させる深さ)等各種処理条件を適宜選択して実施する。
 人工皮革基体を得る工程において、極細繊維発生型繊維から除去する成分が水溶性高分子の場合、絡合処理時の水溶性高分子の溶出を抑制する観点から、ニードルパンチ法により絡合処理を行うことが好ましい。
A fiber web made up of multiple layers is subjected to a mechanical entanglement process using a known method such as a needle punching method or a high-pressure water jet treatment method, thereby three-dimensionally entangling the fibers constituting the fiber web, particularly the fibers between adjacent layers of a wrapped or stacked layered fiber web.
When entanglement is performed by needle punching, various processing conditions are appropriately selected, such as the type of needles (needle shape and count, barb shape and depth, number and position of barbs, etc.), the number of needle punches (needle punch processing density per unit area obtained by multiplying the density of needles implanted in a needle board by the number of strokes at which the board acts on the fiber web per unit area), and the needle punch depth (depth at which the needles act on the fiber web).
In the step of obtaining an artificial leather substrate, when the component to be removed from the ultrafine fiber-forming fiber is a water-soluble polymer, it is preferable to carry out the entanglement treatment by the needle punch method from the viewpoint of suppressing elution of the water-soluble polymer during the entanglement treatment.

 ニードルパンチ処理のパンチ密度としては、1500~5500パンチ/cm、さらには、2000~5000パンチ/cmであることが、高い耐摩耗性が得られ易い観点から好ましい。パンチ密度が上記範囲内であれば、絡合の不足が抑制されて人工皮革表面の繊維のほつれによってラフな表面となることが防止され、また、繊維の切断が抑制されて絡合度が低下することが防止される。 The punch density for needle punching is preferably 1500 to 5500 punches/cm 2 , more preferably 2000 to 5000 punches/cm 2 , from the viewpoint of easily obtaining high abrasion resistance. If the punch density is within the above range, insufficient entanglement is suppressed, preventing the surface of the artificial leather from becoming rough due to fraying of the fibers, and also preventing fiber breakage from occurring, preventing a decrease in the degree of entanglement.

 また、海島型複合繊維の紡糸から絡合処理までのいずれかの段階において、極細繊維発生型繊維、繊維ウェブ、繊維ウェブの積層体、絡合繊維シート等に、油剤や帯電防止剤を付与してもよい。さらに、必要に応じて、極細繊維発生型繊維、繊維ウェブ、繊維ウェブの積層体、絡合繊維シート等を70~150℃程度の温水に浸漬する収縮処理を行うことにより、絡合状態を予め緻密にしておいてもよい。 Furthermore, at any stage from the spinning of the islands-in-sea composite fiber to the entanglement process, an oil or antistatic agent may be applied to the ultrafine fiber-generating fiber, fiber web, fiber web laminate, entangled fiber sheet, etc. Furthermore, if necessary, the ultrafine fiber-generating fiber, fiber web, fiber web laminate, entangled fiber sheet, etc. may be immersed in warm water at a temperature of about 70 to 150°C for shrinkage treatment to make the entanglement dense in advance.

 絡合して得られる絡合繊維シートの目付けとしては、100~1000g/m程度の範囲であることが好ましい。さらに、絡合繊維シートを必要に応じて熱収縮させることにより繊維密度及び絡合度をさらに高める処理を施してもよい。また、熱収縮処理により緻密化された絡合繊維シートをさらに緻密化するとともに、絡合繊維シートの形態を固定化したり、表面を平滑化したりすること等を目的として、必要に応じて、熱プレス処理を行うことによりさらに、繊維密度を高めてもよい。 The basis weight of the entangled fiber sheet obtained by entanglement is preferably in the range of about 100 to 1000 g/ m2 . Furthermore, the entangled fiber sheet may be subjected to a treatment to further increase the fiber density and degree of entanglement by heat shrinking as needed. Furthermore, the entangled fiber sheet densified by the heat shrinking treatment may be further densified, and the fiber density may be further increased by heat pressing as needed for the purposes of fixing the shape of the entangled fiber sheet and smoothing the surface.

<工程(3)>
 工程(3)は、前記絡合繊維シートを収縮させ、前記極細繊維発生型繊維から少なくとも一成分を除去することにより、人工皮革基体を得る工程である。前記一成分は、海島型複合繊維に含まれる海成分の樹脂であることが好ましい。海成分を除去することにより、極細発生型繊維を極細繊維の繊維束に変換することができる。
<Step (3)>
In step (3), the entangled fiber sheet is shrunk and at least one component is removed from the ultrafine fiber-forming fibers to obtain an artificial leather substrate. The one component is preferably a sea component resin contained in the islands-in-sea composite fiber. By removing the sea component, the ultrafine fiber-forming fibers can be converted into a fiber bundle of ultrafine fibers.

 絡合繊維シートを収縮させる方法としては、水蒸気、熱水、乾熱等、熱収縮処理(繊維収縮処理)を施す方法が挙げられる。絡合繊維シートに熱収縮処理を施すと、横方向(幅方向)に収縮し、横方向の繊維の緊張が緩和することに加え、少なくとも一成分を除去する過程で縦方向に繊維が適度に素抜け、縦方向の緊張も緩和し、見掛け密度の上昇も抑制することができる。その結果、より反発感が少なく、より柔軟な風合いを有する人工皮革を得ることができる。 Methods for shrinking an entangled fiber sheet include heat shrinkage (fiber shrinkage) using steam, hot water, dry heat, etc. When an entangled fiber sheet is heat shrinked, it shrinks in the horizontal direction (width direction), relaxing the tension in the horizontal fibers. In addition, the process of removing at least one component allows the fibers to be pulled out appropriately in the vertical direction, relaxing the tension in the vertical direction and suppressing an increase in apparent density. As a result, an artificial leather with less resilience and a softer texture can be obtained.

 海成分の樹脂を除去する方法としては、例えば、海成分の樹脂のみを選択的に除去し得る溶剤または分解剤を用いて除去する方法が挙げられる。
 海成分が、ポリビニルアルコール系樹脂、水溶性ポリエステル樹脂、易アルカリ分解性の変性ポリエステル樹脂、ポリアクリルアミド樹脂、カルボキシメチルセルロース樹脂等の水溶性樹脂である場合、海成分は水により除去することが可能である。
 海成分が、水に溶解性がなく有機溶剤に溶解性があり、島成分の樹脂がポリアミド系樹脂やポリエステル系樹脂である場合、海成分を溶解除去する有機溶剤としては、トルエン、トリクロロエチレン、テトラクロロエチレン等が挙げられる。
 本実施形態においては、環境対応の観点から、水を使用することが好ましく、水に難溶解性である樹脂に対しては、樹脂の溶解力が高いトルエンを使用することが好ましい。
As a method for removing the sea part resin, for example, a method using a solvent or decomposing agent capable of selectively removing only the sea part resin can be mentioned.
When the sea component is a water-soluble resin such as a polyvinyl alcohol resin, a water-soluble polyester resin, an easily alkali-decomposable modified polyester resin, a polyacrylamide resin, or a carboxymethyl cellulose resin, the sea component can be removed with water.
When the sea component is insoluble in water but soluble in organic solvents and the island component resin is a polyamide resin or a polyester resin, examples of the organic solvent that dissolves and removes the sea component include toluene, trichloroethylene, and tetrachloroethylene.
In this embodiment, from the viewpoint of environmental friendliness, it is preferable to use water, and for resins that are poorly soluble in water, it is preferable to use toluene, which has a high resin dissolving power.

 本願発明の効果を効率的に得る観点から、絡合繊維シートを収縮させることと、前記極細繊維発生型繊維から少なくとも一成分を除去することを同時に行うことが好ましく、海成分が水溶性樹脂である場合は、熱水を用いることにより、絡合繊維シートを収縮させ、水溶性樹脂を除去することが好ましい。
 また、海成分を除去する際、ディップニップ処理を並行して行ってもよい。
From the viewpoint of efficiently obtaining the effects of the present invention, it is preferable to simultaneously shrink the entangled fiber sheet and remove at least one component from the ultrafine fiber-generating fibers, and when the sea component is a water-soluble resin, it is preferable to use hot water to shrink the entangled fiber sheet and remove the water-soluble resin.
When removing the sea component, a dip-nip treatment may be carried out in parallel.

<工程(4)>
 工程(4)は、前記人工皮革基体を染色する工程である。
 工程(4)は、海島型繊維を極細繊維束に変成した後の何れの段階で実行することができる。
<Step (4)>
Step (4) is a step of dyeing the artificial leather substrate.
Step (4) can be carried out at any stage after the islands-in-the-sea fibers are converted into ultrafine fiber bundles.

 工程(4)においては、繊維の種類に応じて適宜選択される分散染料、反応染料、酸性染料、金属錯塩染料、硫化染料、硫化建染染料等を主体とした染料を用いた、パッダー、ジッガー、サーキュラー、ウィンス等の従来の人工皮革の染色に通常用いられる公知の染色機を使用した染色方法が何れも採用可能である。
 一方、従来、サーモゾル染色により染色された人工皮革は、反発感が強く、柔軟性に劣るという問題があった。しかしながら、前記工程(1)~(3)を備え、前記工程(1)で準備する繊維ウェブの横方向の降伏点の強度Xと、降伏点以降の最大強度Yとの比(Y/X)が、4.0以下である製造方法により製造された人工皮革基体を、サーモゾル染色により染色しても、反発感が少なく、柔軟な風合いを有する人工皮革を得ることができる。なお、サーモゾル染色は、一般的な人工皮革に用いられる染色に比べ、水使用量を大幅に低減することができ、環境負荷を低減することができる。よって、環境負荷低減の観点からも、人工皮革基体をサーモゾル染色により染色することが好ましい。
In the step (4), any dyeing method can be employed using a known dyeing machine that is usually used for dyeing conventional artificial leathers such as padder, jigger, circular, and wince, using a dye mainly composed of a disperse dye, a reactive dye, an acid dye, a metal complex dye, a sulfur dye, or a sulfur vat dye, which is appropriately selected depending on the type of fiber.
On the other hand, conventional artificial leathers dyed by thermosol dyeing have had the problem of having a strong resilience and poor flexibility. However, even if an artificial leather substrate manufactured by a manufacturing method comprising the steps (1) to (3) in which the ratio (Y/X) of the strength X at the yield point in the lateral direction of the fiber web prepared in step (1) to the maximum strength Y after the yield point is 4.0 or less is dyed by thermosol dyeing, an artificial leather having a soft texture and a low resilience can be obtained. Furthermore, thermosol dyeing can significantly reduce the amount of water used compared to dyeing methods used for general artificial leathers, thereby reducing the environmental impact. Therefore, from the perspective of reducing the environmental impact, it is preferable to dye the artificial leather substrate by thermosol dyeing.

<工程(5)>
 本実施形態に係る人工皮革の製造方法は、天然皮革に近い風合いや形態安定性等を付与する観点から、前記絡合繊維シートへ前記高分子弾性体を含浸させる工程である工程(5)をさらに備えてもよい。
 工程(5)は、工程(2)と工程(3)の間に実施してもよく、工程(3)と工程(4)の間に実施してもよい。
 本実施形態の人工皮革の製造においては、天然皮革に近い風合いや形態安定性を付与すると共に柔軟性を付与するために、工程(2)と工程(3)の間に工程(5)を実施することが好ましい。すなわち、海成分を除去する前に高分子弾性体を含浸付与することが好ましい。
 このように、海成分を除去する前に高分子弾性体を含浸付与することにより、海成分の除去後に繊維束を形成する極細繊維の間に、海成分を除去して形成される空隙が形成される。その結果、繊維束内部の極細繊維が高分子弾性体に拘束され難くなり、すなわち極細繊束が高分子弾性体の影響を受け難くなり、柔軟性に優れる人工皮革が得られ易くなる。なお、海島型複合繊維から海成分を除去した後の、繊維束を形成している極細繊維に高分子弾性体を含浸付与した場合には、繊維束の空隙に高分子弾性体が侵入することにより、繊維束を形成する極細繊維が高分子弾性体で拘束されて硬い風合いの人工皮革が得られやすくなる。
<Step (5)>
The method for producing an artificial leather according to this embodiment may further include step (5) of impregnating the entangled fiber sheet with the polymeric elastomer, from the viewpoint of imparting texture and shape stability similar to those of natural leather.
Step (5) may be carried out between step (2) and step (3), or between step (3) and step (4).
In the production of the artificial leather of this embodiment, in order to impart a texture and shape stability similar to those of natural leather as well as flexibility, it is preferable to carry out step (5) between steps (2) and (3). That is, it is preferable to impregnate the artificial leather with a polymeric elastomer before removing the sea component.
By impregnating the ultrafine fibers forming the fiber bundle with a polymeric elastomer before removing the sea part in this way, voids are formed between the ultrafine fibers that form the fiber bundle after removing the sea part, which are formed by removing the sea part. As a result, the ultrafine fibers inside the fiber bundle are less likely to be restrained by the polymeric elastomer, i.e., the ultrafine bundle is less likely to be affected by the polymeric elastomer, making it easier to obtain an artificial leather with excellent flexibility. Note that when the ultrafine fibers forming the fiber bundle after removing the sea part from the islands-in-sea type composite fiber are impregnated with a polymeric elastomer, the polymeric elastomer penetrates into the voids in the fiber bundle, and the ultrafine fibers forming the fiber bundle are restrained by the polymeric elastomer, making it easier to obtain an artificial leather with a hard texture.

 上記高分子弾性体を上記絡合繊維シートに付与するに当たっては、高分子弾性体を溶剤中に溶解または分散させた非水系の高分子弾性体液を用いてもよいし、高分子弾性体を必要に応じて分散剤とともに水系媒体に分散させた水系の高分子弾性体液を用いてもよい。前者の場合、均一な高分子弾性体液が得られ易く、後者の場合は有機溶剤の使用量を低下させ易くなる。 When applying the polymeric elastomer to the entangled fiber sheet, a non-aqueous polymeric elastomer liquid in which the polymeric elastomer is dissolved or dispersed in a solvent may be used, or an aqueous polymeric elastomer liquid in which the polymeric elastomer is dispersed in an aqueous medium, optionally together with a dispersant, may be used. In the former case, a uniform polymeric elastomer liquid is more easily obtained, while in the latter case, it is easier to reduce the amount of organic solvent used.

 高分子弾性体液の濃度、すなわち高分子弾性体液中の高分子弾性体の含有量は、0.1~60質量%が好ましい。
 高分子弾性体液には、最終的に得られる人工皮革の性質を損なわない範囲で、染料や顔料等の着色剤、凝固調節剤、酸化防止剤、紫外線吸収剤、蛍光剤、防黴剤、浸透剤、消泡剤、滑剤、撥水剤、撥油剤、増粘剤、増量剤、硬化促進剤、発泡剤、ポリビニルアルコールやカルボキシルメチルセルロース等の水溶性高分子化合物等、各種添加剤を適宜配合してもよい。
The concentration of the polymeric elastomer body fluid, that is, the content of the polymeric elastomer in the polymeric elastomer body fluid, is preferably 0.1 to 60% by mass.
The polymer elastic body fluid may contain various additives, such as colorants such as dyes and pigments, coagulation regulators, antioxidants, ultraviolet absorbers, fluorescent agents, antifungal agents, penetrating agents, antifoaming agents, lubricants, water repellents, oil repellents, thickeners, bulking agents, hardening accelerators, foaming agents, and water-soluble polymer compounds such as polyvinyl alcohol and carboxymethyl cellulose, within the range that does not impair the properties of the artificial leather that is finally obtained.

 工程(5)で使用する高分子弾性体の詳細は、上述の「高分子弾性体」の欄で説明したとおりである。 Details of the polymeric elastomer used in step (5) are as explained above in the "Polymeric elastomer" section.

 高分子弾性体を絡合繊維シートに含浸させ、次いで高分子弾性体を従来公知の乾式法または湿式法により凝固させることで、高分子弾性体を絡合繊維シート内に固定してもよい。ここでいう乾式法とは、溶剤や分散剤等を乾燥等により除去することで、高分子弾性体を繊維シート構造体内に固定させる方法全般を指す。また、ここでいう湿式法とは、高分子弾性体液を含浸した絡合繊維シート構造体を、高分子弾性体の非溶剤や凝固剤で処理したり、感熱ゲル化剤等を添加した水系高分子弾性体液を用いて、含浸後の絡合繊維シートに加熱処理等を施すことにより、分散剤を除去するに先立って絡合繊維シート構造体内に高分子弾性体を仮に固定するか完全に固定させる方法全般を指す。 The polymeric elastomer may be fixed within the entangled fiber sheet by impregnating the entangled fiber sheet with the polymeric elastomer and then coagulating the polymeric elastomer using a conventional dry or wet method. The dry method here refers to any method for fixing a polymeric elastomer within a fiber sheet structure by removing solvents, dispersants, etc. by drying or other methods. The wet method here refers to any method for temporarily or completely fixing a polymeric elastomer within the entangled fiber sheet structure prior to removing the dispersant by treating an entangled fiber sheet structure impregnated with a polymeric elastomer liquid with a non-solvent or coagulant for the polymeric elastomer, or by using an aqueous polymeric elastomer liquid containing a heat-sensitive gelling agent or other additive to heat-treat the impregnated entangled fiber sheet.

 本実施形態に係る人工皮革は、高分子弾性体を有していなくても、天然皮革に近い風合いを有していることから、高分子弾性体を含浸させないことが好ましい。すなわち、工程(5)を備えていないことが好ましい。 The artificial leather of this embodiment has a texture similar to that of natural leather, even without the polymer elastomer, so it is preferable not to impregnate it with the polymer elastomer. In other words, it is preferable not to include step (5).

 前記工程(1)~(5)以外にも、必要に応じて、ドライ状態での機械的もみ処理、染色機や洗濯機等を使用したウェット状態でのリラックス処理、柔軟剤処理、防燃剤や抗菌剤、消臭剤、撥水撥油剤等の機能性付与処理、シリコーン系樹脂やシルクプロテイン含有処理剤、グリップ性付与樹脂等の触感改質剤付与処理、着色剤やエナメル調用コーティング樹脂等の、上述した樹脂以外の樹脂を塗布する意匠性付与処理等の仕上げ処理を行ってもよい。 In addition to the above steps (1) to (5), finishing treatments such as mechanical kneading in a dry state, relaxation treatment in a wet state using a dyeing machine or washing machine, treatment with softeners, functionalization treatments such as flame retardants, antibacterial agents, deodorizers, water and oil repellents, treatments to add texture modifiers such as silicone resins, silk protein-containing treatments, and grip-imparting resins, and design-imparting treatments using resins other than those mentioned above, such as colorants and enamel-like coating resins, may also be performed as needed.

 本実施形態の人工皮革は、従来の人工皮革製造と同様に、必要により、厚み方向に複数枚にスライスし、裏面となる面を研削する等して厚さを調節したり、裏面となる面に、高分子弾性体または極細繊維束を溶解または膨潤させることのできる溶剤を塗布してもよい。 As with conventional artificial leather manufacturing, the artificial leather of this embodiment can be sliced into multiple pieces in the thickness direction as needed, and the thickness can be adjusted by grinding the back surface, or a solvent capable of dissolving or swelling the polymer elastomer or ultrafine fiber bundles can be applied to the back surface.

 本実施形態の人工皮革は、立毛面を有していてもよい。
 立毛面の形成には、サンドペーパーや針布等によるバフィング処理や、ブラッシング処理等の公知の方法を何れも用いることができる。また、このような起毛処理の前あるいは後に、高分子弾性体または極細繊維束を溶解または膨潤させることのできる溶剤、例えば、高分子弾性体がポリウレタンエラストマーであればジメチルホルムアミド(DMF)等を含む処理液や、レゾルシン等のフェノール系化合物を含む処理液等を起毛処理する表面に塗布してもよい。これにより、高分子弾性体や極細繊維束の接着による極細繊維束の拘束状態、人工皮革の極細繊維立毛長、表面摩擦耐久性等を微調節することができる。
 また、上記起毛処理を行なった後に、上述した工程(4)を行ってもよい。
The artificial leather of this embodiment may have a napped surface.
To form a napped surface, any of the known methods, such as buffing with sandpaper or card cloth, or brushing, can be used. Furthermore, before or after such nap-raising treatment, a solvent capable of dissolving or swelling the polymeric elastomer or ultrafine fiber bundles, such as a treatment liquid containing dimethylformamide (DMF) or a treatment liquid containing a phenolic compound such as resorcinol, may be applied to the surface to be napped. This allows for fine adjustment of the restraint state of the ultrafine fiber bundles due to adhesion of the polymeric elastomer or ultrafine fiber bundles, the nap length of the ultrafine fibers of the artificial leather, the surface friction durability, etc.
After the raising treatment, the above-mentioned step (4) may be carried out.

 以下、本発明を実施例によりさらに具体的に説明する。なお、本発明の範囲は実施例の内容により何ら限定されるものではない。 The present invention will be explained in more detail below using examples. Note that the scope of the present invention is not limited in any way by the contents of the examples.

 はじめに、後述する実施例及び比較例で用いた評価方法を以下にまとめて説明する。 First, the evaluation methods used in the examples and comparative examples described below will be summarized below.

〈固有粘度〉
 溶媒としてフェノール/テトラクロロエタン(体積比1/1)混合溶媒を用い、測定温度30℃にて、ウベローデ型粘度計「HRK-3型」(林製作所製)を用いて測定した。
<Intrinsic viscosity>
A phenol/tetrachloroethane (volume ratio 1/1) mixed solvent was used as the solvent, and the measurement was carried out at a measurement temperature of 30° C. using an Ubbelohde viscometer "HRK-3" (manufactured by Hayashi Seisakusho).

〈搬送ベルト上(捕集面)での海島型複合繊維の広がり〉
 エアジェットノズルから停止した搬送ベルト上へ、海島型複合繊維を2秒間吐出し、搬送ベルトが駆動する方向への海島型複合繊維の広がり(長さ)を測定した。
<Spreading of islands-in-the-sea composite fiber on the conveyor belt (collection surface)>
The islands-in-sea type composite fiber was discharged from the air jet nozzle onto the stationary conveyor belt for 2 seconds, and the spread (length) of the islands-in-sea type composite fiber in the direction in which the conveyor belt was moving was measured.

〈繊維ウェブ横方向の降伏点の強度X及び降伏点以降の最大強度Y〉
 繊維ウェブを16cm×16cmの大きさに切り出した後、縦方向に四つ折り(最初に2分の1の面積になるように重ねて折り、さらに4分の1の面積になるように重ねて折る)にして、試験片の幅を4cmとし、精密万能試験機(株式会社島津製作所製オートグラフ AG-X plus)を用いてつかみ間隔10cm、定速伸長型引張試験器により200mm/minの引張速度で伸長させ、強度(kg)と伸度(%)の関係をプロットしたSSカーブを測定した。得られたSSカーブから、降伏点の強度X(kg)と、降伏点以降の最大強度Y(kg)(降伏点以降の強度の最大値)を読み取った。
<Yield strength X in the fiber web transverse direction and maximum strength Y after the yield point>
The fiber web was cut into a size of 16 cm x 16 cm, and then folded in quarters lengthwise (first folded in half to reduce the area, and then folded again to reduce the area to a quarter) to give a test specimen width of 4 cm. Using a precision universal testing machine (Shimadzu Corporation, Autograph AG-X plus), the specimens were elongated at a gripping distance of 10 cm and a constant-rate extension tensile tester at a tension rate of 200 mm/min, and an SS curve plotting the relationship between strength (kg) and elongation (%) was measured. From the obtained SS curve, the yield point strength X (kg) and the maximum strength Y (kg) after the yield point (maximum value of strength after the yield point) were read.

〈高分子弾性体の含有量〉
 1g以上の質量となる大きさに切り出した人工皮革の重量Cを測定した。次に、上記人工皮革をヘキサフルオロ-2-プロパノール(HFIP)に常温(25℃)で12時間浸漬してポリエステル繊維を溶解し、残った固形分を濾過してHFIPで洗浄した後、乾燥してHFIPを除去し、得られた固体の重量Dを測定した。そして、以下の式(2)に基づいて、人工皮革中の高分子弾性体の含有量を求めた。
高分子弾性体の含有量(質量%)=D/C×100・・・式(2)
 なお、「固形分」とは、溶剤または分散剤を除く成分を意味する。
<Content of polymer elastomer>
The weight C of the artificial leather cut into a size having a mass of 1 g or more was measured. Next, the artificial leather was immersed in hexafluoro-2-propanol (HFIP) at room temperature (25°C) for 12 hours to dissolve the polyester fibers, and the remaining solid content was filtered and washed with HFIP, and then dried to remove the HFIP. The weight D of the resulting solid was measured. The content of the polymer elastomer in the artificial leather was then calculated based on the following formula (2).
Content of polymer elastomer (mass%)=D/C×100 Equation (2)
The term "solid content" refers to components excluding solvents and dispersants.

〈平均径〉
 ポリエステル繊維の平均径は、以下のように測定した。
 人工皮革の断面の走査型電子顕微鏡(SEM)写真を3000倍で撮影した。そのSEM写真から繊維の断面をランダムに10個選んで断面積を測定した。その断面積の算術平均値を算出して、以下の式(1)を元に算出したものを繊維の平均径とした。
平均径=(平均断面積/π)1/2×2・・・式(1)
<Average diameter>
The average diameter of the polyester fibers was measured as follows.
A scanning electron microscope (SEM) photograph of the cross section of the artificial leather was taken at 3000x magnification. Ten cross sections of fibers were randomly selected from the SEM photograph, and their cross-sectional areas were measured. The arithmetic mean value of the cross-sectional areas was calculated, and the average diameter of the fibers was calculated based on the following formula (1).
Average diameter = (average cross-sectional area/π) 1/2 ×2...Formula (1)

〈平均繊度〉
 ポリエステル繊維の平均繊度は以下のように測定した。
 人工皮革の断面の走査型電子顕微鏡(SEM)写真を3000倍で撮影した。そのSEM写真から繊維の断面をランダムに10個選んで断面積を測定し、その断面積の算術平均値を算出した。そして、断面積の平均値を樹脂の密度を用いて平均繊度に換算した。
<Average fineness>
The average fineness of the polyester fiber was measured as follows.
A scanning electron microscope (SEM) photograph of the cross section of the artificial leather was taken at 3000x magnification. Ten cross sections of fibers were randomly selected from the SEM photograph, and the cross-sectional areas were measured and the arithmetic mean value of the cross-sectional areas was calculated. The mean value of the cross-sectional areas was then converted into an average fineness using the density of the resin.

〈面積割合A及び面積割合Bの測定〉
 人工皮革を縦方向の厚み方向に片刃カミソリを用いて切断し、得られた断面を、走査型電子顕微鏡(SEM)を用いて150倍で、表面側から裏面側にかけて複数枚に分けて撮影した。その複数枚の画像を紙に印刷して人工皮革の断面が表面側から裏面側にかけて連続するように繋ぎ、印刷面上の人工皮革基材と立毛繊維の根元部分の境界部分を平均的に横切るように直線を引いた。さらに、印刷面上の人工皮革の断面の中央部分に400μm(深さ方向)×700μm(深さ方向に直交する方向)相当の長方形を描画した。前記長方形を覆うように印刷面上に透明なポリエチレンテレフタレートフィルム(PETフィルム)を置き、前記長方形の部分のPETフィルム表面を黒く塗った。このPETフィルムの黒く塗った部分の面積を画像解析ソフト「Image-Pro Premier ver.9.1」(株式会社日本ローバー製)を用いて解析し、人工皮革の縦方向断面の面積を測定した。次に、前記長方形の部分を黒く塗ったPETフィルムに替えて新たに透明なPETフィルムを、前記長方形を覆うように印刷面上に置き、前記直線を0°として直線と極細繊維の成す角度(±90°以下)を厚み方向の角度とした時、厚み方向に-30°~+30°の範囲で配向した極細繊維の部分のPETフィルム表面を黒く塗り、人工皮革の縦方向断面の面積測定と同様に前記画像解析ソフトを用いて、人工皮革の縦方向断面中、厚み方向に-30°~+30°の範囲で配向した極細繊維の面積を測定した。得られた人工皮革の縦方向断面の面積と厚み方向に-30°~+30°の範囲で配向した極細繊維の面積から、人工皮革の縦方向断面中、厚み方向に-30°~+30°の範囲で配向した極細繊維が占める面積割合A(%)を算出した。次に、人工皮革の横方向の厚み方向に片刃カミソリを用いて切断し、得られた断面について、前記面積割合A(%)を算出した際と同様の操作により、人工皮革の横方向断面中、厚み方向に-30°~+30°の範囲で配向する極細繊維が占める面積割合B(%)を算出した。
<Measurement of area ratio A and area ratio B>
The artificial leather was cut in the longitudinal thickness direction using a single-edged razor, and the resulting cross section was photographed in multiple sections from the front side to the back side using a scanning electron microscope (SEM) at 150x magnification. The multiple images were printed on paper and connected so that the cross section of the artificial leather was continuous from the front side to the back side, and a straight line was drawn evenly across the boundary between the artificial leather substrate and the base of the napped fibers on the printed surface. Furthermore, a rectangle equivalent to 400 μm (depth direction) x 700 μm (direction perpendicular to the depth direction) was drawn in the center of the cross section of the artificial leather on the printed surface. A transparent polyethylene terephthalate film (PET film) was placed on the printed surface to cover the rectangle, and the surface of the PET film in the rectangular area was painted black. The area of the blackened portion of the PET film was analyzed using image analysis software "Image-Pro Premier ver. 9.1" (manufactured by Nippon Rover Co., Ltd.), and the area of the longitudinal cross section of the artificial leather was measured. Next, the rectangular portion of the PET film was replaced with a new transparent PET film placed on the printed surface so as to cover the rectangle. The straight line was defined as 0°, and the angle (±90° or less) between the straight line and the ultrafine fibers was defined as the angle in the thickness direction. The surface of the PET film in the portion where the ultrafine fibers were oriented in the thickness direction within a range of -30° to +30° was painted black. The area of the ultrafine fibers oriented in the thickness direction within a range of -30° to +30° was measured using the image analysis software in the same manner as in measuring the area of the longitudinal cross section of the artificial leather. From the area of the obtained longitudinal cross section of the artificial leather and the area of the ultrafine fibers oriented in the thickness direction within a range of -30° to +30°, the area ratio A (%) of the ultrafine fibers oriented in the thickness direction within a range of -30° to +30° was calculated. Next, the artificial leather was cut in the thickness direction in the lateral direction using a single-edged razor, and the area ratio B (%) of the ultrafine fibers oriented in the thickness direction in the lateral cross section of the artificial leather was calculated using the same procedure as in calculating the area ratio A (%).

〈厚さ、目付け及び見掛け密度〉
 得られた人工皮革を16cm×16cmの大きさ(256cm)にカットした。カットした人工皮革の質量(g)を測定し、以下の式(3)によりカットした人工皮革の目付け(g/m)を算出した。
目付け=質量/256×10000・・・式(3)
 JIS L1096(2010)(A法)に準じて、厚さ測定器(測定子直径:10mm)を用いて、5秒間、23.5kPaの一定圧力の下、カットした人工皮革の厚さ(mm)を測定し、JIS K6505(1995) 5.2.2に準じて、以下の式(4)により人工皮革の見掛け密度(g/cm)を算出した。
見掛け密度=目付け/厚さ/1000・・・式(4)
<Thickness, basis weight and apparent density>
The obtained artificial leather was cut into a size of 16 cm x 16 cm (256 cm 2 ). The mass (g) of the cut artificial leather was measured, and the basis weight (g/m 2 ) of the cut artificial leather was calculated using the following formula (3).
Basis weight = mass / 256 × 10000 Formula (3)
In accordance with JIS L1096 (2010) (Method A), the thickness (mm) of the cut artificial leather was measured using a thickness gauge (measuring probe diameter: 10 mm) under a constant pressure of 23.5 kPa for 5 seconds, and the apparent density (g/cm 3 ) of the artificial leather was calculated using the following formula (4) in accordance with JIS K6505 (1995) 5.2.2.
Apparent density = basis weight / thickness / 1000 Formula (4)

〈ヤング率〉
 YAWASA(YWS-5N-1-SL)(株式会社テック技販製)を用い、実施例及び比較例で得られた人工皮革を3枚に重ねて、押圧1mm径の先端を用い速度0.2m/secで最大押圧0.2Nとなるまで厚み方向に圧縮し、ヤング率測定を行った。
<Young's modulus>
Three sheets of the artificial leathers obtained in the Examples and Comparative Examples were stacked together and compressed in the thickness direction using a YAWASA (YWS-5N-1-SL) (manufactured by Tech Gihan Co., Ltd.) with a pressing tool having a diameter of 1 mm at a speed of 0.2 m/sec up to a maximum pressing force of 0.2 N, and Young's modulus was measured.

〈風合い〉
 得られた人工皮革を折り曲げた後の風合いを、目視及び触感にて以下の基準で判定した。
 A:充実感があり、反発感が少なく、大きな座屈シワが無く折れ曲がり、柔軟性に優れた風合いであった。
 B:充実感に欠ける、反発感がある、大きな座屈シワがある、及び硬いのいずれか1つ以上に該当する風合いであった。
Texture
The texture of the resulting artificial leather after bending was judged visually and by touch according to the following criteria.
A: The texture was solid, had little resilience, was bendable without large buckling wrinkles, and had excellent flexibility.
B: The texture fell into one or more of the following categories: lacking in a sense of fullness, having a sense of resilience, having large buckling wrinkles, and being hard.

[実施例1]
 海成分として水溶性熱可塑性ポリビニルアルコール系樹脂(エチレン共重合により変性した変性ポリビニルアルコール)、島成分として固有粘度が0.60dl/gのリサイクルポリエチレンテレフタレート(ジカルボン酸単位中、テレフタル酸に由来する構成単位が100モル%)とを、海成分/島成分が25/75(質量比)となるように270℃で溶融複合紡糸用口金(島数:25島/繊維)より海島型複合繊維を吐出した。
 次に、搬送ベルト(海島型複合繊維の捕集面)から55cm上方の位置にエアジェットノズルを設け、紡糸速度3279m/分で牽引細化しながら紡糸を行い、搬送ベルト上に、平均繊度3.05dtexの海島型複合繊維を捕集し、海島型複合繊維シートを得た。上記捕集条件で、搬送ベルト上(捕集面)での海島型複合繊維の広がり(長さ)を測定した結果、24.5cmであった。
 得られた海島型複合繊維シートを、カレンダーロールを用いて、ロール表面温度58℃、線圧36kg/cmの条件で熱プレスし、繊維ウェブを得た。得られた繊維ウェブの横方向の降伏点における強度Xは0.6kg、伸度は6%であり、降伏点以降の最大強度Yは1.73kg、最大強度Yの時の伸度は190%であり、Y/X=2.9であった。
 次に、繊維ウェブをクロスラップ積層して積層ウェブを形成した。そして、積層ウェブに対して6バーブのニードルを用いてニードルパンチ処理を行うことにより、目付け292g/mの縦方向捲縮の絡合繊維シートを形成した。
 次に、絡合繊維シートを、ディップニップ処理、及び高圧水流処理しながら95℃の熱水中に10分間浸漬することにより、海島型複合繊維の海成分である水溶性熱可塑性ポリビニルアルコール系樹脂を溶解除去し、平均径3.02μm、平均繊度0.101dtexのポリエチレンテレフタレートの極細繊維を形成させた。そして、乾燥することにより人工皮革基体を得た。
 次に、得られた人工皮革基体を、分散染料を用いて、サーモゾル染色を行い、起毛処理をすることにより立毛面を有する人工皮革を得た。得られた人工皮革は、目付け436g/m、見掛け密度0.451g/cm、厚さ0.97mmであった。得られた人工皮革は、充実感があり反発感が少なく、大きな座屈シワが無く折れ曲がり、柔軟性に優れた風合いであった。
[Example 1]
A water-soluble thermoplastic polyvinyl alcohol resin (modified polyvinyl alcohol modified by ethylene copolymerization) was used as the sea component, and recycled polyethylene terephthalate (dicarboxylic acid units, of which constitutional units derived from terephthalic acid account for 100 mol %) having an intrinsic viscosity of 0.60 dl/g was used as the island component. Islands-in-sea type composite fibers were extruded from a melt conjugate spinning nozzle (number of islands: 25/fiber) at 270°C so that the sea component/island component ratio was 25/75 (mass ratio).
Next, an air jet nozzle was installed at a position 55 cm above the conveyor belt (the collection surface of the islands-in-sea type composite fibers), and spinning was performed while pulling and attenuating at a spinning speed of 3,279 m/min, and islands-in-sea type composite fibers with an average fineness of 3.05 dtex were collected on the conveyor belt, thereby obtaining an islands-in-sea type composite fiber sheet. Under the above collection conditions, the spread (length) of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was measured and found to be 24.5 cm.
The resulting islands-in-sea composite fiber sheet was hot-pressed using a calender roll at a roll surface temperature of 58°C and a linear pressure of 36 kg/cm to obtain a fiber web. The resulting fiber web had a strength X of 0.6 kg at the yield point in the transverse direction, an elongation of 6%, a maximum strength Y after the yield point of 1.73 kg, and an elongation at the maximum strength Y of 190%, so that Y/X = 2.9.
The fiber webs were then cross-lap laminated to form a laminate web, which was then needle-punched using 6-barb needles to form an entangled fiber sheet having a basis weight of 292 g/ m2 and longitudinal crimping.
Next, the entangled fiber sheet was immersed in hot water at 95°C for 10 minutes while undergoing dip-nip treatment and high-pressure water jet treatment to dissolve and remove the water-soluble thermoplastic polyvinyl alcohol resin, which is the sea component of the islands-in-sea type composite fiber, and form polyethylene terephthalate ultrafine fibers with an average diameter of 3.02 µm and an average fineness of 0.101 dtex. The resulting product was then dried to obtain an artificial leather substrate.
The resulting artificial leather substrate was then thermosol dyed with a disperse dye and raised to obtain an artificial leather with a napped surface. The resulting artificial leather had a basis weight of 436 g/ m2 , an apparent density of 0.451 g/ cm3 , and a thickness of 0.97 mm. The resulting artificial leather had a solid feel with little rebound, was bendable without large buckling wrinkles, and had excellent flexibility.

[実施例2]
 実施例1において、海島型複合繊維の搬送ベルト上(捕集面)での広がり測定結果が26.0cmとなるようにエアジェットノズルを調整して、海島型複合繊維のシートを得たこと以外は同様にして、染色された人工皮革を得た。結果を表1に示す。
[Example 2]
A dyed artificial leather was obtained in the same manner as in Example 1, except that a sheet of islands-in-sea type composite fibers was obtained by adjusting the air jet nozzle so that the measured spread of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was 26.0 cm. The results are shown in Table 1.

[実施例3]
 実施例1において、海島型複合繊維の搬送ベルト上(捕集面)での広がり測定結果が27.0cmとなるようにエアジェットノズルを調整して、海島型複合繊維のシートを得たこと以外は同様にして、染色された人工皮革を得た。結果を表1に示す。
[Example 3]
A dyed artificial leather was obtained in the same manner as in Example 1, except that a sheet of islands-in-sea type composite fibers was obtained by adjusting the air jet nozzle so that the measured spread of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was 27.0 cm. The results are shown in Table 1.

[実施例4]
 実施例1において、サーモゾル染色の代わりにサーキュラー染色により人工皮革基体を染色したこと以外は同様にして、染色された人工皮革を得た。結果を表1に示す。
[Example 4]
Dyed artificial leather was obtained in the same manner as in Example 1, except that the artificial leather substrate was dyed by circular dyeing instead of thermosol dyeing. The results are shown in Table 1.

[実施例5]
 実施例3において、人工皮革基体へ、アクリルエマルジョンであるカセゾールARS-2(日華化学株式会社製)と水を質量比で30:70の割合で混合(アクリルエマルジョン含有量:約18質量%)し、pick up40%で含浸させた後、140℃で4分間乾燥を行い、その後サーモゾル染色を行ったこと以外は同様にして、染色された人工皮革を得た。結果を表1に示す。
[Example 5]
In Example 3, the artificial leather substrate was impregnated with a mixture of acrylic emulsion Kasesol ARS-2 (manufactured by Nicca Chemical Co., Ltd.) and water in a mass ratio of 30:70 (acrylic emulsion content: approximately 18 mass%), pickled 40%, dried at 140°C for 4 minutes, and then thermosol dyed. Dyed artificial leather was obtained in the same manner as in Example 3. The results are shown in Table 1.

[比較例1]
 実施例1において、海島型複合繊維の搬送ベルト上(捕集面)での広がり測定結果が23.0cmとなるようにエアジェットノズルを調整して、海島型複合繊維のシートを得たこと以外は同様にして、染色された人工皮革を得た。結果を表1に示す。
[Comparative Example 1]
A dyed artificial leather was obtained in the same manner as in Example 1, except that a sheet of islands-in-sea type composite fibers was obtained by adjusting the air jet nozzle so that the measured spread of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was 23.0 cm. The results are shown in Table 1.

[比較例2]
 実施例1において、固有粘度が0.60dl/gのリサイクルポリエチレンテレフタレートの代わりにイソフタル酸変性ポリエチレンテレフタレート(イソフタル酸で6mol%変性させたポリエチレンフタレート)を用い、海島型複合繊維の搬送ベルト上(捕集面)での広がり測定結果が27.0cmとなるようにエアジェットノズルを調整して、海島型複合繊維のシートを得たこと以外は同様にして、染色された人工皮革を得た。結果を表1に示す。
[Comparative Example 2]
Dyed artificial leather was obtained in the same manner as in Example 1, except that isophthalic acid-modified polyethylene terephthalate (polyethylene phthalate modified with 6 mol% isophthalic acid) was used instead of the recycled polyethylene terephthalate having an intrinsic viscosity of 0.60 dl/g, and the air jet nozzle was adjusted so that the measured spread of the islands-in-sea type composite fiber on the conveyor belt (collection surface) was 27.0 cm to obtain a sheet of islands-in-sea type composite fiber. The results are shown in Table 1.

[比較例3]
 比較例2において、サーモゾル染色の代わりにサーキュラー染色により染色したこと以外は同様にして、染色された人工皮革を得た。結果を表1に示す。
[Comparative Example 3]
Dyed artificial leather was obtained in the same manner as in Comparative Example 2, except that circular dyeing was used instead of thermosol dyeing. The results are shown in Table 1.

[比較例4]
 実施例1において、海島型複合繊維の搬送ベルト上(捕集面)での広がり測定結果が23.2cmとなるようにエアジェットノズルを調整して、海島型複合繊維のシートを得たこと以外は同様にして、染色された人工皮革を得た。結果を表1に示す。
[Comparative Example 4]
A dyed artificial leather was obtained in the same manner as in Example 1, except that a sheet of islands-in-sea type composite fibers was obtained by adjusting the air jet nozzle so that the measured spread of the islands-in-sea type composite fibers on the conveyor belt (collection surface) was 23.2 cm. The results are shown in Table 1.

 表1から、実施例1~5で得られた人工皮革は、反発感が少なく、柔軟な風合いを有することが分かる。
 一方、本願発明の構成を有さない比較例1、2及び4で得られた人工皮革は、反発感が強く、風合いに劣るものであり、本願発明の構成を有さない比較例3で得られた人工皮革は、反発感が強いものであることが分かる。

 
It can be seen from Table 1 that the artificial leathers obtained in Examples 1 to 5 have a soft feel with little rebound.
On the other hand, the artificial leathers obtained in Comparative Examples 1, 2, and 4, which do not have the configuration of the present invention, have a strong resilience and are inferior in texture, and the artificial leather obtained in Comparative Example 3, which does not have the configuration of the present invention, has a strong resilience.

Claims (10)

 ポリエステル系樹脂を含有する極細繊維を含む人工皮革であって、
 前記人工皮革の縦方向断面中、厚み方向に-30°~+30°の範囲で配向する極細繊維が占める面積割合Aが、4.5%以下であり、
 前記人工皮革の横方向断面中、厚み方向に-30°~+30°の範囲で配向する極細繊維が占める面積割合Bと前記面積割合Aが、A/B≦0.9である、人工皮革。
An artificial leather including ultrafine fibers containing a polyester resin,
In the longitudinal cross section of the artificial leather, the area ratio A occupied by the ultrafine fibers oriented in the thickness direction in the range of −30° to +30° is 4.5% or less,
An artificial leather, wherein an area ratio B occupied by ultrafine fibers oriented at an angle of −30° to +30° in the thickness direction in a transverse cross section of the artificial leather and the area ratio A satisfy A/B≦0.9.
 前記極細繊維の平均径が、7.5μm以下である、請求項1に記載の人工皮革。 The artificial leather described in claim 1, wherein the average diameter of the ultrafine fibers is 7.5 μm or less.  前記極細繊維の平均繊度が、0.50dtex以下である、請求項1又は2に記載の人工皮革。 The artificial leather according to claim 1 or 2, wherein the average fineness of the ultrafine fibers is 0.50 dtex or less.  前記極細繊維が長繊維である、請求項1又は2に記載の人工皮革。 The artificial leather according to claim 1 or 2, wherein the ultrafine fibers are long fibers.  前記ポリエステル系樹脂が、ポリエチレンテレフタレートである、請求項1又は2に記載の人工皮革。 The artificial leather according to claim 1 or 2, wherein the polyester resin is polyethylene terephthalate.  前記ポリエステル系樹脂の固有粘度が、0.63dl/g以下である、請求項1又は2に記載の人工皮革。 The artificial leather according to claim 1 or 2, wherein the intrinsic viscosity of the polyester resin is 0.63 dl/g or less.  前記ポリエチレンテレフタレートは、ジカルボン酸単位及びジオール単位を含み、前記ジカルボン酸単位の94モル%以上がテレフタル酸に由来する構成単位である、請求項5に記載の人工皮革。 The artificial leather described in claim 5, wherein the polyethylene terephthalate contains dicarboxylic acid units and diol units, and 94 mol % or more of the dicarboxylic acid units are structural units derived from terephthalic acid.  前記ポリエチレンテレフタレートが、リサイクルポリエチレンテレフタレートである、請求項7に記載の人工皮革。 The artificial leather described in claim 7, wherein the polyethylene terephthalate is recycled polyethylene terephthalate.  請求項1又は2に記載の人工皮革の製造方法であって、
 極細繊維発生型繊維から形成された繊維ウェブを準備する工程と、
 前記繊維ウェブを用いて絡合繊維シートを形成する工程と、
 前記絡合繊維シートを収縮させ、前記極細繊維発生型繊維から少なくとも一成分を除去することにより、人工皮革基体を得る工程と、
 前記人工皮革基体を染色する工程とを備え、
 前記繊維ウェブの横方向の降伏点の強度Xと、降伏点以降の最大強度Yとの比(Y/X)が、4.0以下である、人工皮革の製造方法。
A method for producing the artificial leather according to claim 1 or 2,
Providing a fiber web formed from ultrafine fiber-generating fibers;
forming an entangled fiber sheet using the fiber web;
a step of shrinking the entangled fiber sheet and removing at least one component from the ultrafine fiber-forming fiber to obtain an artificial leather substrate;
and a step of dyeing the artificial leather substrate.
A method for producing an artificial leather, wherein the ratio (Y/X) of the strength X at the yield point in the transverse direction of the fiber web to the maximum strength Y after the yield point is 4.0 or less.
 前記極細繊維発生型繊維から一成分を抽出する前に、高分子弾性体を含浸させない、請求項9に記載の人工皮革の製造方法。

 
The method for producing an artificial leather according to claim 9, wherein the ultrafine fiber-forming fibers are not impregnated with a polymeric elastomer before one component is extracted from the ultrafine fiber-forming fibers.

PCT/JP2025/007810 2024-03-08 2025-03-05 Artificial leather and method for producing artificial leather Pending WO2025187710A1 (en)

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Citations (5)

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Publication number Priority date Publication date Assignee Title
WO2010098364A1 (en) * 2009-02-27 2010-09-02 株式会社クラレ Artificial leather, entangled web of long fibers, and processes for producing these
JP2011214206A (en) * 2010-03-18 2011-10-27 Kuraray Co Ltd Method for producing long fiber nonwoven fabric and artificial leather substrate
JP2020070518A (en) * 2018-10-31 2020-05-07 株式会社クラレ Entangled non-woven fabric and artificial leather
WO2021049413A1 (en) * 2019-09-10 2021-03-18 株式会社クラレ Napped artificial leather
JP2021070904A (en) * 2019-10-30 2021-05-06 旭化成株式会社 Artificial leather and method for producing the same

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010098364A1 (en) * 2009-02-27 2010-09-02 株式会社クラレ Artificial leather, entangled web of long fibers, and processes for producing these
JP2011214206A (en) * 2010-03-18 2011-10-27 Kuraray Co Ltd Method for producing long fiber nonwoven fabric and artificial leather substrate
JP2020070518A (en) * 2018-10-31 2020-05-07 株式会社クラレ Entangled non-woven fabric and artificial leather
WO2021049413A1 (en) * 2019-09-10 2021-03-18 株式会社クラレ Napped artificial leather
JP2021070904A (en) * 2019-10-30 2021-05-06 旭化成株式会社 Artificial leather and method for producing the same

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