EP3816342B1 - Cuir artificiel et son procédé de production - Google Patents

Cuir artificiel et son procédé de production Download PDF

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Publication number
EP3816342B1
EP3816342B1 EP20204538.1A EP20204538A EP3816342B1 EP 3816342 B1 EP3816342 B1 EP 3816342B1 EP 20204538 A EP20204538 A EP 20204538A EP 3816342 B1 EP3816342 B1 EP 3816342B1
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EP
European Patent Office
Prior art keywords
fiber
resin
water
artificial leather
sheet
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EP20204538.1A
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German (de)
English (en)
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EP3816342A1 (fr
Inventor
Daisuke Hironaka
Yoshiyuki Tadokoro
Takuya Teramura
Hisaki Ikebata
Hiroki UMEMOTO
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Asahi Kasei Corp
Asahi Chemical Industry Co Ltd
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Asahi Kasei Corp
Asahi Chemical Industry Co Ltd
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Publication of EP3816342A1 publication Critical patent/EP3816342A1/fr
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Classifications

    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06N—WALL, 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
    • D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
    • D06N3/0002—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by the substrate
    • D06N3/0004—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by the substrate using ultra-fine two-component fibres, e.g. island/sea, or ultra-fine one component fibres (< 1 denier)
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06N—WALL, 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
    • D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
    • D06N3/0043—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by their foraminous structure; Characteristics of the foamed layer or of cellular layers
    • D06N3/0052—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by their foraminous structure; Characteristics of the foamed layer or of cellular layers obtained by leaching out of a compound, e.g. water soluble salts, fibres or fillers; obtained by freezing or sublimation; obtained by eliminating drops of sublimable fluid
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06N—WALL, 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
    • D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
    • D06N3/12—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. gelatine proteins
    • D06N3/14—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. gelatine proteins with polyurethanes
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06N—WALL, 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
    • D06N2211/00—Specially adapted uses
    • D06N2211/12—Decorative or sun protection articles
    • D06N2211/14—Furniture, upholstery
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06N—WALL, 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
    • D06N2211/00—Specially adapted uses
    • D06N2211/12—Decorative or sun protection articles
    • D06N2211/28—Artificial leather

Definitions

  • Artificial leathers which are mainly composed of a fiber sheet (fibrous substrate) such as a nonwoven fabric and polyurethane (hereinafter also referred to as PU) have excellent features such as easy care, functionality, and homogeneity that are difficult to achieve with natural leather, and are suitably used for clothing, shoes, and bags, as well upholstery and interior materials for seats for interior, automobiles, aircraft, trains, and clothing materials such as ribbon and patch base materials.
  • a fiber sheet such as a nonwoven fabric and polyurethane (hereinafter also referred to as PU)
  • PU polyurethane
  • a method for producing such an artificial leather conventionally, a method in which a fiber sheet is impregnated with an organic solvent solution of a PU resin, and thereafter immersing the fiber sheet in a PU nonsolvent (e.g., water or an organic solvent) to wet-coagulate the PU resin is generally used.
  • a PU nonsolvent e.g., water or an organic solvent
  • an organic solvent-based PU resin using N,N-dimethylformamide, which is a PU resin solvent is used as an organic solvent.
  • organic solvents are generally highly harmful to the human body and the environment, there is a strong demand for a method for producing an artificial leather in which an organic solvent is not used.
  • Patent Document 2 there is examined a method in which a water-dispersed PU resin dispersion in which a PU resin is dispersed in water is used instead of a conventional organic solvent type PU resin.
  • a water-dispersed PU resin dispersion in which a PU resin is dispersed in water is used instead of a conventional organic solvent type PU resin.
  • the texture tends to be hard.
  • One of the primary reasons is the difference between the coagulation methods.
  • the coagulation method of the organic solvent-based PU resin dispersion is a "wet-coagulation method" in which PU molecules are precipitated and coagulated by substituting an organic solvent in which PU molecules are dissolved in water, and from the viewpoint of a PU film, a porous film having a low density is formed.
  • a wet-coagulation method in which PU molecules are precipitated and coagulated by substituting an organic solvent in which PU molecules are dissolved in water, and from the viewpoint of a PU film, a porous film having a low density is formed.
  • a sheet-like material in which the porous structure of the PU resin inside the sheet-like material can be expressed regardless of the types of foaming agent and PU, and which has the same uniform nap length as an artificial leather to which an organic solvent-based PU resin is applied, has an elegant surface quality with excellent fiber denseness feeling, has a good texture, and which is flexible and has excellent resilience can be produced by a method for producing a sheet-like material is characterized in that a fiber sheet is impregnated with a PU resin dispersion containing a water-dispersed PU resin, a foaming agent, an anionic surfactant and/or a zwitterionic surfactant.
  • Patent Document 3 discloses an artificial leather consisting of ultrafine fibers and elastomers, wherein in order to provide the artificial leather with inconspicuous color difference between the ultrafine fibers and a PU resin, an elastic and smooth feeling, and uniform and excellent surface qualities, the artificial leather is composed of ultrafine fibers having an average single fiber fineness of 0.01 to 0.50 dtex and a elastomer, the elastomer is contained in a ratio of 10 to 50% by mass, in a cross-section when the artificial leather is cut perpendicularly to the surface direction, the number of a mass of elastomer having a size of 100 ⁇ m or more in the thickness direction of fibers per cross-section length in the surface direction, which is within 200 ⁇ m in the thickness direction from the surface of the artificial leather excluding the napped portion, is 0.1 to 2.5 pieces/mm, and the method for the production thereof includes a step of passing a water stream through a fiber sheet composed of ultrafine fibers to disperse the ultrafine fibers.
  • a vibro-washer is preferable because it can perform a uniform disperse treatment over the entire fiber sheet, but a method such as water jet punching which imparts a mechanical impact by a local high-pressure water stream outside the liquid bath is not preferable because the water jet punching process is difficult to uniformly perform due to the local flow of liquid, and even when the number of nozzles is increased, it tends to cause regular streaky appearance defects in the length direction, which results an artificial leather having an artificial texture.
  • Patent Document 3 describe an ultrafine fiber dispersion treatment in which, after removing the sea component of a sea-island type composite fiber and exposing the ultrafine fibers, the fiber sheet after a sea-component dissolution is treated with a vibro-washer, and in water, the water stream was passed through the inside of the fiber sheet to disperse the ultrafine fibers.
  • the details of the treatment conditions are not described.
  • fiber bundles remain, and the presence of disperse fibers along with the fiber bundles after brushing prevents the dense feeling and uniformity of the dense feeling.
  • Patent Document 3 describes that as long as the obtained artificial leather has "0.1 to 2.5 pieces/mm per cross-section length in the surface direction of a mass of elastomer having a size of 100 ⁇ m or more in the thickness direction within 200 ⁇ m in the thickness direction from the surface", the appearance (color tone) was more uniform. However, the surface PU resin area ratio and the standard deviation thereof have not been examined, and the disperse property of single fibers has not been examined.
  • Patent Document 4 discloses a fiber sheet containing ultrafine fibers having an average single fiber diameter of 0.1 ⁇ m to 8 ⁇ m, wherein at least one surface of the fiber structure has nap, and a discontinuous resin layer is formed on the naps, and wherein 50% to 100% of the total thickness of the resin layer is present in the fiber sheet.
  • suede pig leather surface
  • natural nubuck leather cowhide surface
  • the invention described in Patent Document 4 aims to provide a nubuck-like sheet-like material.
  • Patent Document 4 describes that it is important that a discontinuous resin layer (i.e., a state of a surface layer in which resin portions are scattered in island shapes on the surface of a sheet-like material and napped portions are present between the resin portions) be formed on the brushed surface of the fiber structure, the ratio of the discontinuous resin portion to the surface of the sheet-like material is preferably 10% to 90% in order to obtain excellent abrasion resistance and a nubuck-like surface feeling and texture, and the resin layer is coated by flat screen or gravure coating and dried.
  • a discontinuous resin layer i.e., a state of a surface layer in which resin portions are scattered in island shapes on the surface of a sheet-like material and napped portions are present between the resin portions
  • the surface PU resin area ratio which is an indicator of the dispersion state of the surface PU resin mass, and the standard deviation thereof have not been examined, and the dispersibility of the single fibers has also not been examined.
  • Patent Document 5 proposes a method including a step of imparting crimps having a crimp number of 10 to 30 crimps/2.54 cm and a crimp degree of 15 to 28% to an filaments capable of ultrafine fiber generating prior to exposing the ultrafine fibers, and a step of performing a liquid stream treatment with a vibro-washer at a rotation speed of 300 rpm to 400 rpm after the step of entangling the crimped fibers to form a fibrous base material prior to a step of exposing the ultrafine fibers.
  • Patent Document 5 further describes that regarding the liquid stream treatment, a method of applying water streams in water with a vibro-washer is preferable, and the rotation speed of the vibro-washer is preferably 300 rpm or more and 400 rpm or less, and as a result, the number of long ultrafine fiber bundles having a major axis of 1 mm to 4 mm present on the surface layer of the sheet-like material can be adjusted by entanglement of the ultrafine fiber bundles.
  • the rotation speed of the vibro-washer is less than 300 rpm, the ultrafine fiber bundles are unlikely to entangle with each other, and the number of ultrafine fiber bundles having a major axis of 1 mm to 4 mm on the surface layer of the sheet-like material increases, making it impossible to obtain an elegant appearance, and when the rotation speed of the vibro-washer is 400 rpm or more, the pressure due to the liquid flow of the vibro-washer is strong, whereby the ultrafine fiber bundles can be broken, and linting is likely to occur.
  • the vibro-washer treatment is performed not for dispersing the single fibers but for entangling the ultrafine fiber bundles.
  • Patent Document 5 describes the surface qualities such as appearance and texture, and the occurrence of nap has been improved, dyeing unevenness has not been examined.
  • an object of the present invention is to provide an artificial leather which has inconspicuous dyeing unevenness (by dispersing the polyurethane resin which adheres to the fibers more finely than in conventional methods, a color difference between the fibers and the polyurethane resin is inconspicuous), a moist feeling, and a dense feeling (fiber bundle dispersibility) at satisfactory levels.
  • artificial leather means "a material in which a special nonwoven fabric (primarily a fiber layer having a random three-dimensional structure which is impregnated with a PU resin or an elastomer having comparable flexibility) is used as a base material in accordance with the Household Goods Quality Labeling Act.” Furthermore, in the JIS-6601 standard, artificial leathers are classified into those which are “smooth” having a leather grain-like appearance and those which are “nap” having the appearance of suede or velour, depending on appearance. However, the artificial leather of the present embodiment relates to what is classified as "nap” (i.e., a suede-like artificial leather having a brushed appearance).
  • a suede-like appearance can be achieved by subjecting the outer surface of a fiber layer (A) (i.e., a surface serving as a first outer surface of the artificial leather) to a buffing process (brushing) with sandpaper or the like.
  • the first outer surface of the artificial leather is the surface exposed to the outside when the artificial leather is used (e.g., the surface on the side which contacts with a human body in the case of chair applications) (refer to FIGS. 1 and 3 ).
  • the first outer surface is raised or napped by buffing or the like.
  • the phrase “fiber web” means a state before entanglement of cut fibers
  • the phrase “fiber sheet” means a state prior to PU resin filling after entanglement
  • the phrase “sheet-like material” means a state prior to dyeing after PU resin filling
  • the phrase “artificial leather” means a state of a product after dyeing.
  • nonwoven fabric encompasses “fiber web”, “fiber sheet”, “sheet-like material”, and “artificial leather”
  • the phrase “fibrous substrate” encompasses woven fabrics in addition to the phrase “nonwoven fabric.”
  • the PU resin area ratio of the first outer surface of the artificial leather is 8% to 25%, and the standard deviation of the surface PU resin area ratio is 25% or less.
  • the surface PU resin area ratio is 25% or less, the PU resin is moderately present on the surface, whereby a dry texture does not occur, the moist feeling is satisfactory, and dyeing unevenness is suppressed. Furthermore, in this case, since the ratio of the fibers present on the surface is higher than that of the PU resin, the fiber brushing can be successfully performed, whereby a dense feeling can be achieved. Conversely, when the surface PU resin area ratio is 8% or more, since the PU resin is moderately present on the surface, a fabric-like feeling, i.e., a dry texture does not occur, and the moist feeling is satisfactory.
  • the surface PU resin area ratio is preferably 9% to 22%, and more preferably 10% to 20%.
  • the PU resin may be a water-dispersed PU resin.
  • the surface PU resin area ratio is obtained by binarizing the PU resin in the SEM image as a black portion, determining from the obtained binarized image the area ratio of the polyurethane resin to each compartment by the compartment method, and averaging the surface PU resin area ratio (%) for all compartments, and the standard deviation thereof indicates the variation from the average for all compartments. If the standard deviation of the surface PU resin area ratio is 25% or less, since the regions where the PU resin is unevenly distributed are small and the regions where the PU resin and the fiber are adjacent to each other are fine and small, dyeing unevenness is inconspicuous.
  • the standard deviation of the surface PU resin area ratio is preferably 22% or less, and more preferably 20% or less.
  • the lower limit of the standard deviation of the surface PU resin area ratio is not particularly limited, and may be 0% or more.
  • the PU resin may be a water-dispersed PU resin.
  • a fiber web is formed of sea-island type cut fibers, and thereafter subjected to needle-punch processing to obtain a fiber sheet.
  • This fiber sheet is subjected to a sea-component dissolution to obtain a fiber sheet in which single fibers of the island component are exposed, and the obtained fiber sheet is the subjected to the water stream dispersion treatment described below to obtain a fiber sheet in which single fibers are dispersed, whereby the PU resin adhering to the fiber is also dispersed as a result of dispersion of the single fibers, and the standard deviation of the surface PU resin area ratio can be controlled to 25% or less.
  • a step of impregnating a water-dispersed PU resin dispersion containing hot water-soluble resin fine particles (e.g., hot water-soluble fine particle resin fine particles), and thereafter affixing the PU resin by heating to obtain a sheet-like material filled with a PU resin it is possible to control the surface PU resin area ratio to 8% to 25%.
  • the single fibers are present in a state in which the single fibers are appropriately dispersed, and as a result, the PU resin masses of the fiber layer (A) are also present in a moderately dispersed state, and when the artificial leather is touched with the fingertip, the PU resin masses are touched by the fingertip, whereby a moist feeling (a size similar to that of the PU resin masses) can be achieved.
  • the water stream dispersion treatment be carried out by injecting high-pressure water using a plurality of nozzles having a nozzle hole interval of 1.00 mm or less.
  • the nozzle interval is the distance in the nozzle width direction between a nozzle hole and the nozzle hole closest to this nozzle hole in the nozzle width direction (when there are two or more rows of nozzle holes, the same as in the case of one row).
  • the nozzle hole interval is preferably 0.60 mm or less, and more preferably 0.30 mm or less.
  • the number of rows of nozzle hole rows opened in the width direction of the water stream dispersion treatment device may be either one row or two or more rows.
  • a water stream dispersion process it is common to remove the moisture discharged onto the fiber sheet by a water stream dispersion treatment from the viewpoint of uniformity and morphology stability of the fiber sheet, and drying is performed from the surface opposite the water stream dispersion treatment surface by a suction method or the like.
  • the drying capability is insufficient with respect to the amount of input water, and as a result, the uniformity and the morphological stability of the fiber sheet may be deteriorated.
  • the nozzle hole interval (water stream trajectory) is preferably equal because it is easy to disperse the single fibers uniformly, the water stream trajectory is inconspicuous, and the dense feeling and moist feeling are easily improved.
  • the distance between nozzle rows is preferably set to a distance equivalent to, for example, the nozzle hole interval of nozzle holes in one row from the viewpoint of drying.
  • the pore diameters of the high-pressure water injection nozzles of the water stream dispersion treatment are preferably 0.05 mm to 0.30 mm, more preferably 0.05 mm to 0.20 mm, and further preferably 0.08 mm to 0.13 mm from the point of view of achieving a high single fiber dispersion, inconspicuousness of the water stream trajectory, and facilitating balance of the drying ability without excessive water discharge.
  • the pressurized water of the water stream dispersion treatment is injected at 1.0 to 10.0 MPa.
  • the water pressure of the water stream dispersion treatment is set to 1.0 MPa or more, since the single fiber bundles are not excessively dispersed, it is easy to control the k-nearest neighbor ratio value to 10% to 80%.
  • dispersing the single fibers in a single fiber bundle state, and setting the water pressure of the water stream dispersion treatment to 10.0 MPa or less dispersion of the single fibers in single fiber bundle state is facilitated and the water stream trajectory is inconspicuous.
  • the water stream may pass through the fiber sheet, whereby the single fiber bundles may not be dispersed, and the single fiber bundle dispersing effect may be reduced as compared to the case in which the single fiber bundles are treated at a low water pressure. Furthermore, when the water pressure of the water stream dispersion treatment is high, the fiber sheet is densified and the texture (stiffness value) tends to deteriorate.
  • the water pressure of the water stream dispersion treatment is more preferably 1.5 to 7.0 MPa, and further preferably 2.0 to 4.5 MPa.
  • Turbulence is an index of the fluctuation of the diameter of water stream. Since the energy of the water stream can be efficiently converted into the dispersion of the fibers, the turbulence is preferably 12% or more, and more preferably 15% or more.
  • W the average diameter of the water streams in the range of 25 mm to 35 mm from the discharge port of the nozzle hole
  • ⁇ standard deviation of the average diameter
  • the present inventors consider that, when the turbulence is large relative to the case where the turbulence is small, since the water stream energy is easily dispersed in multiple directions toward the horizontal direction in addition to the vertical direction of the fiber sheet, the water stream energy can be efficiently converted into single fiber bundle dispersion energy, whereby the dispersion effect is enhanced. As an example, it is considered that water stream energy, which is wasted when passing the fiber sheet at high water pressure, is easily taken in as dispersion energy.
  • Circular motion or reciprocating motion at right angle to the process progress direction (machine direction) of the high-pressure water injection nozzle is also preferable in order to promote single fiber dispersion and improve dense feeling and moist feeling.
  • the distance from the high pressure water injection surface to the object to be processed is preferably 5 mm to 100 mm, more preferably 10 mm to 60 mm, and further preferably 20 mm to 40 mm from the viewpoint of the passing property of the fabric prior the water stream dispersion treatment and the process at the time of the water stream dispersion treatment, in addition to the single fiber bundle dispersing effect.
  • the adhesion ratio of the PU resin to the fiber sheet is preferably 15% by mass to 50% by mass, more preferably 22% by mass to 45% by mass, and further preferably 26% by mass to 40% by mass.
  • the ratio of PU resin to fiber sheet affects the surface PU resin area ratio described above. When the ratio of PU resin is low, the surface PU resin area ratio tends to be low. Conversely, when the ratio of PU resin is high, the cross-sectional PU resin area ratio tends to be high. When the ratio of the PU resin to the fiber sheet is 15% by mass or more, the fibers adhere well to the PU resin, and mechanical strength such as abrasion resistance satisfying the market needs is easily obtained. Conversely, when the adhesion ratio of the PU resin to the fiber sheet is 50% by mass or less, an artificial leather having a rich flexible feeling and a dense feeling can easily be obtained.
  • the PU resin may be a water-dispersed PU resin.
  • PU resins obtained by reacting a polymer diol with an organic diisocyanate and a chain extender are preferred.
  • polycarbonate-based, polyester-based, polyether-based, silicone-based, and fluorine-based diols can be used, and a copolymer obtained by combining two or more of these may be used.
  • a polycarbonate-based or polyether-based diol or a combination thereof is preferably used.
  • a polycarbonate-based or polyester-based diol or a combination thereof is preferably used.
  • a polyether-based or polyester-based diol or a combination thereof is preferably used.
  • the polycarbonate-based diol can be produced by transesterification reaction of an alkylene glycol with a carbonic ester or reaction of a phosgene or a chlorformic acid ester with an alkylene glycol.
  • alkylene glycol examples include linear alkylene glycols such as ethylene glycol, propylene glycol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,9-nonanediol, and 1,10-decanediol; branched alkylene glycols such as neopentyl glycol, 3-methyl-1,5-pentanediol, 2,4-diethyl-1,5-pentanediol, and 2-methyl-1,8-octanediol; alicyclic diols such as 1,4-cyclohexanediol; and aromatic diols such as bisphenol A; and combinations of one or two or more of these can be used.
  • linear alkylene glycols such as ethylene glycol, propylene glycol, 1,4-butanediol, 1,5-pentanediol, 1,6
  • polyester-based diol examples include polyester diols obtained by condensing various low molecular weight polyols and polybasic acids.
  • the low molecular weight polyol may be, for example, one or more selected from ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,3-butanediol, 1,4-butanediol, 2,2-dimethyl-1,3-propanediol, 1,6-hexanediol, 3-methyl-1,5-pentanediol, 1,8-octanediol, diethylene glycol, triethylene glycol, dipropylene glycol, tripropylene glycol, cyclohexane-1,4-diol, cyclohexane-1,4-dimethanol.
  • an adduct obtained by adding various alkylene oxides to bisphenol A can be used.
  • polybasic acid includes one or more selected from the group consisting of succinic acid, maleic acid, adipic acid, glutaric acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, dodecanedicarboxylic acid, phthalic acid, isophthalic acid, terephthalic acid, and hexahydroisophthalic acid.
  • polyether-based diol examples include polyethylene glycol, polypropylene glycol, polytetramethylene glycol, or copolymerized diols in which these are combined.
  • the number average molecular weight of the polymer diol is preferably 500 to 4000. By setting the number average molecular weight to 500 or more, more preferably 1500 or more, it is possible to prevent a hard texture. Further, by setting the number average molecular weight to 4000 or less, more preferably 3000 or less, the strength of the PU resin can be maintained.
  • organic diisocyanate examples include aliphatic diisocyanates such as hexamethylene diisocyanate, dicyclohexylmethane diisocyanate, isophorone diisocyanate, and xylylene diisocyanate; and aromatic diisocyanates such as diphenylmethane diisocyanate and tolylene diisocyanate; and these may be used in combination.
  • aromatic diisocyanates such as hexamethylene diisocyanate, dicyclohexylmethane diisocyanate, and isophorone diisocyanate are preferably used from the viewpoint of light resistance.
  • chain extender an amine-based chain extender such as ethylenediamine and methylenebisaniline, or a diol-based chain extender such as ethylene glycol can be used. Further, a polyamine obtained by reacting a polyisocyanate with water can also be used as a chain extender.
  • the PU resin can be used in the form of a solvent type PU resin in which a PU resin is dissolved in an organic solvent such as N,N-dimethylformamide, or a water-dispersed PU resin in which a PU resin is emulsified with an emulsifier and dispersed in water.
  • a water-dispersed PU resin is preferred from the viewpoint that the PU resin can be easily filled into a fiber sheet in a fine form, and the required performance as an artificial leather such as feeling and mechanical properties can be easily obtained even with a small amount of adhesion, and an environmental load can be reduced without the use of an organic solvent.
  • water-dispersed PU resins can be impregnated into the fiber sheet in the form of a dispersion (hereinafter, also referred to as a PU resin dispersion) in which the PU resin is dispersed with a desired particle diameter
  • a PU resin dispersion in which the PU resin is dispersed with a desired particle diameter
  • the filling form of the PU resin in the fiber sheet can be controlled by controlling the particle diameter.
  • water-dispersed PU resin a self-emulsifying PU resin containing a hydrophilic group in the PU molecule or a forced-emulsifying PU resin obtained by emulsifying a PU resin with an external emulsifier can be used.
  • a crosslinking agent in water-dispersed PU resins, can be used in combination for the purpose of improving durability such as wet-heat resistance, abrasion resistance, and hydrolysis resistance. It is preferable to add a crosslinking agent in order to improve durability at the time of liquid flow dyeing processing, to suppress fiber loss, and to obtain excellent surface quality.
  • the crosslinking agent may be an external crosslinking agent added as an additive component to the PU resin, and may be an internal crosslinking agent for introducing a reaction group capable of taking a crosslinked structure in the PU resin structure in advance.
  • water-dispersed PU resins used in artificial leather generally have a crosslinked structure in order to provide dyeing processing resistance, it tends to be poorly soluble in an organic solvent such as N,N-dimethylformamide. Therefore, for example, when the artificial leather is immersed in N,N-dimethylformamide for 12 hours at room temperature, then subjected to a PU resin dissolution treatment, and then its cross-section is observed with an electron microscope or the like, if a resin-like material having no fiber shape remains, it can be determined that the resin-like material is a water-dispersed PU resin.
  • the average primary particle diameter of the PU resin in the dispersion is preferably 0.1 ⁇ m to 0.8 ⁇ m, more preferably 0.1 ⁇ m to 0.6 ⁇ m, and further preferably 0.2 ⁇ m to 0.5 ⁇ m.
  • the average primary particle diameter is a value obtained by measurement of the PU resin dispersion with a laser diffraction particle size distribution measuring device ("LA-920" manufactured by Horiba, Ltd.).
  • an artificial leather having excellent mechanical strength is obtained by improving the adhesion force (i.e., the binding force) of the fibers in the fiber sheet by the PU resin. Further, it is advantageous to set the average primary particle diameter of the PU resin to 0.8 ⁇ m or less from the viewpoint of suppressing aggregation or coarsening of the PU resin and controlling the standard deviation of the surface PU resin area ratio to 20% or less.
  • the average primary particle diameter of the PU resin in the PU resin dispersion 0.1 ⁇ m to 0.8 ⁇ m, a large number of the fibers constituting the artificial leather (particularly, the surface layer thereof) are held each other, whereby a flexible feeling (rigidity value) and an excellent mechanical strength (abrasion resistance, etc.) are obtained.
  • the PU resin is impregnated in the form of an impregnating liquid such as a solution (e.g., in the case of a solvent dissolving type) or a dispersion (e.g., in the case of a water-dispersed).
  • an impregnating liquid such as a solution (e.g., in the case of a solvent dissolving type) or a dispersion (e.g., in the case of a water-dispersed).
  • the solid concentration of the water-dispersed PU resin dispersion may be 10 wt% to 35 wt%, more preferably 15 to 30% by mass, and further preferably 15 to 25% by mass.
  • preparation of the impregnation liquid and impregnation into the fiber sheet are performed so that the adhesion ratio of the PU resin to 100% by mass of the fiber sheet is 15% by mass to 50% by mass.
  • the PU resin may be a water-dispersed PU resin.
  • Additives such as a stabilizer (such as ultraviolet absorber, or antioxidant), a flame retardant, an antistatic agent, or a pigment (such as carbon black) may be added to the impregnation liquid containing the PU resin (e.g., a water-dispersed PU resin) if necessary.
  • the total amount of these additives present in the artificial leather may be, for example, 0.1 to 10.0 parts by mass, or 0.2 to 8.0 parts by mass, or 0.3 to 6.0 parts by mass, per 100 parts by mass of the PU resin. Note that such additives will be distributed in the PU resin of the artificial leather.
  • the value when referring to the size of the PU resin and the mass ratio to the fiber sheet is intended to mean values including the additives (if used).
  • a step of impregnating the fiber sheet with a water-dispersed PU resin dispersion containing hot water-soluble resin fine particles is performed, and then further the PU resin is affixed by heating to obtain a sheet-like material filled with a PU resin.
  • a subsequent step or a dyeing step by removing the hot water-soluble resin fine particles from the obtained fiber sheet using hot water, an effect of partially dividing and aerating a portion of a continuous layer of PU resin and miniaturizing an adhesion state of PU resin is obtained.
  • the hot water-soluble resin fine particles include partially saponified PVA resin fine particles and fully saponified PVA resin fine particles. Since the fully saponified PVA resin fine particles tend to be resistant to elution into water at ambient temperature (20 °C) as compared with partially saponified PVA resin fine particles, it is preferable to use fully saponified PVA resin fine particles as the hot water-soluble resin fine particles. From the viewpoint of resistance to elution into water at ambient temperature (20 °C), the degree of saponification of the fully saponified PVA resin fine particles is preferably 95 mol% or more, and more preferably 98 mol% or more.
  • the average particle diameter (size) of the hot water-soluble resin fine particles is 1 ⁇ m to 8 ⁇ m, preferably 2 ⁇ m to 6 ⁇ m, and more preferably 2 ⁇ m to 4 ⁇ m.
  • the average particle diameter is 1 ⁇ m or more, the hot water-soluble resin fine particles are unlikely to aggregate, and by setting the average particle diameter to 8 ⁇ m or less, the hot water-soluble resin fine particles can easily impregnate the fiber sheet.
  • NL-05 manufactured by Mitsubishi Chemical Co., Ltd. can be used as the fine particles, or the fine particles can be obtained by the method described in Japanese Unexamined Patent Publication (Kokai) No. 07-82384 .
  • the content of the hot water-soluble resin fine particles in the water-dispersed PU resin dispersion is preferably 1 wt% to 20 wt%, more preferably 2 wt% to 15 wt%, and further preferably 3 wt% to 10 wt%.
  • 1% by mass or more of the hot water-soluble resin fine particles are contained in the water-dispersed PU resin dispersion, dispersion of the PU resin mass is easily accelerated.
  • the hot water-soluble resin fine particles are contained in the water-dispersed PU resin dispersion in a quantity of 20 wt% or less, the fine particles do not aggregate and the stability of the dispersion is easily maintained.
  • hot water-soluble resin refers to a resin which is resistant to dissolution in ambient temperature water, and specifically has a loss rate of 25% or less with respect to ambient temperature water at a temperature of 20 ⁇ 2 °C.
  • a step of adhering the hot water-soluble resin to the fiber sheet before impregnating the fiber sheet with the water-dispersed PU resin dispersion containing hot water-soluble resin fine particles can also be performed.
  • a hot water-soluble resin aqueous solution can be prepared, and the aqueous solution can be adhered by a method such as impregnation into the fiber sheet and then drying.
  • a subsequent step or a dyeing step by removing the hot water-soluble resin together with the hot water-soluble resin fine particles from the obtained fiber sheet using hot water, adhesion between the fibers and the PU resin is suppressed, and a portion of the continuous layer of the PU resin is fragmented and aerated, whereby the effect of miniaturizing the adhesion state of the PU resin is obtained, so that the feeling of the artificial leather is easily improved.
  • the hot water-soluble resin examples include partially saponified PVA resins and fully saponified PVA resins. Since fully saponified PVA resins tend to be resistant to elution into water at ambient temperature (20 °C) as compared with partially saponified PVA resins, it is preferable to use a fully saponified PVA resin as the hot water-soluble resin. From the viewpoint of resistance to elution into water at ambient temperature (20 °C), the degree of saponification of the fully saponified PVA resin is preferably 95 mol% or more, more preferably 98 mol% or more. Furthermore, in order to enhance the permeability of the hot water-soluble resin aqueous solution at the time of impregnation, the degree of polymerization is preferably 1000 or less, and more preferably 700 or less.
  • the fiber sheet 1 includes at least a fiber layer (A) 12, and the scrim 11 and the fiber layer (B) 13 are optional and not indispensable elements. Therefore, the artificial leather of the present embodiment includes the case of a single layer of the fiber layer (A), the case of two layers including the fiber layer (A) and scrim or the fiber layer (B), the case of three layers including the fiber layer (A), scrim, and the fiber layer (B).
  • the fiber layer (A) may be a single layer fiber sheet which is sliced in half horizontally and filled with PU resin, as will be described later.
  • the fiber sheet is a scrim-free single layer structure. This is because the productivity is increased by slicing in half horizontally.
  • the fiber sheet has a three-layer structure and the scrim is an intermediate layer.
  • the scrim 11 as a woven or knit fabric is interposed between the fiber layer (A) 12 constituting a first outer surface of the artificial leather and the fiber layer (B) 13 constituting the second outer surface of the artificial leather, and fibers are entangled between these layers is preferable in terms of dimensional stability, tensile strength, and tear strength.
  • the fiber layer (A), the fiber layer (B), and the scrim interposed therebetween since the fiber layer (A) and the fiber layer (B) can be individually designed, it is preferable that the diameter, the type, and the sort of the fibers constituting these layers be freely customized according to the function and the application required for the artificial leather. For example, when ultrafine fibers are used for the fiber layer (A) and flame-retardant fibers are used for the fiber layer (B), respectively, compatibility between excellent surface quality and high flame retardancy can be achieved.
  • the scrim which is a woven or knit fabric
  • the scrim is constituted of the same type of polymer as the fibers constituting the fiber layer (A) from the viewpoint of color unification by dyeing.
  • the fibers constituting the fiber layer (A) are polyester-based
  • the fibers constituting the scrim are also preferably polyester-based
  • the fibers constituting the fiber layer (A) are polyamide-based
  • the fibers constituting the scrim are also preferably polyamide-based.
  • the scrim is preferably a single knit knitted at 22 gauge to 28 gauge.
  • the textile structure may be plain weave, twill weave, or satin weave, and plain weave is preferred from the viewpoint of cost, entanglement, etc.
  • the yarn constituting the fabric may be a monofilament or a multifilament.
  • the single fiber fineness of the yarn is preferably 5.5 dtex or less from the viewpoint wherein a flexible artificial leather can be easily obtained.
  • a yarn obtained by twisting a raw yarn of a multifilament such as polyester or polyamide or a machining yarn subjected to a false twisting treatment at a twist number of 0 to 3000 T/m is preferred.
  • the multifilament may be conventional, and, for example, a 33dtex/6f, 55dtex/24f, 83dtex/36f, 83dtex/72f, 110dtex/36f, 110dtex/48f, 167dtex/36f, 166dtex/48f polyester or polyamide is preferably used.
  • the yarn constituting the fabric may be a long fiber of a multifilament.
  • the woven density of yarns in the fabric is preferably 30 to 150 yarns per inch, and more preferably 40 to 100 yarns per inch, in terms of obtaining an artificial leather which is flexible and excellent in mechanical strength. In order to impart suitable mechanical strength and a moderate texture, a basis weight of 20 to 150 g/m 2 is preferred.
  • the presence or absence of false twisting machining in the fabric, the number of twists, the single fiber fineness of the multifilament, and the weave density contribute to mechanical properties such as stitch strength, tear strength, tensile strength, stretchability, and elasticity in addition to entanglement of the fibers constituting the fiber layer (A) and the fibers constituting the fiber layer (B), which is an optional layer, and the flexibility of the artificial leather, and may be appropriately selected according to the desired physical properties and application.
  • the fiber layer (A) is preferably composed of fibers having an average diameter of 1 ⁇ m to 8 ⁇ m, more preferably 2 ⁇ m to 6 ⁇ m, and further preferably 2 ⁇ m to 5 ⁇ m.
  • the average diameter of the fibers is 1 ⁇ m or more, the abrasion resistance, color developability after dyeing, and light fastness are suitable.
  • the average diameter of the fibers is 8 ⁇ m or less, since the number density of the fibers is large, an artificial leather having a dense feeling, a smooth surface texture, and superior surface qualities can be obtained.
  • synthetic fibers including polyester-based fibers such as polyethylene terephthalate, polybutylene terephthalate, and polytrimethylene terephthalate; polyamide-based fibers such as nylon 6, nylon 66, and nylon 12 are suitable.
  • polyester-based fibers such as polyethylene terephthalate, polybutylene terephthalate, and polytrimethylene terephthalate
  • polyamide-based fibers such as nylon 6, nylon 66, and nylon 12 are suitable.
  • polyethylene terephthalate is preferred from the viewpoint that the fibers themselves do not yellow even when exposed to direct sunlight for long periods of time, and the dyeing fastness thereof is excellent, and in consideration of applications requiring durability, such as in the application of automobile seats.
  • polyethylene terephthalate which has been chemically recycled or material recycled, or polyethylene terephthalate using plant-derived raw materials is further preferred.
  • the phrase "dispersed single fiber” means that the fibers do not form a fiber bundle, for example, an island component in the sea-island composite fibers described below.
  • a fiber obtained by using an filaments capable of ultrafine fiber generating such as a sea-island type composite fiber e.g., a copolymerized polyester is used as the sea component and a conventional polyester is used as the island component
  • subjecting it to a three-dimensional entanglement with scrim subjecting it to a three-dimensional entanglement with scrim, and subsequently subjecting it to a sea-component dissolution (removing the sea component of the sea-island type composite fiber by dissolution or decomposition) is present as a fiber bundle in the fiber layer (A), and is not a dispersed single fiber.
  • an ultrafine fiber having a single fiber fineness of 0.2 dtex is obtained by producing a sea-island type composite cut fiber in which an island component is 24 islands/If corresponding to a single fiber fineness of 0.2 dtex, thereafter forming a fiber layer (A) with the sea-island type composite cut fiber, forming a three dimensional entangled body with a scrim by needle-punch processing, filling the three dimensional entangled body with PU resin, and then dissolving or decomposing the sea component.
  • the single fibers are present in the fiber layer (A) in a state of 24 convergent fibers (corresponding to 4.8 dtex in a convergent state)
  • the fiber layer (A) is composed of dispersed single fibers, it is excellent in surface smoothness, and, for example, uniform nap can be easily obtained when the outer surface of the fiber layer (A) is raised by buffing, and even when the adhesion ratio of the PU resin is relatively small, a lint-like appearance called pilling is not readily generated by friction, whereby an artificial leather having superior surface quality and abrasion resistance is obtained. Furthermore, when the fibers are dispersed single fibers, since the fiber interval tends to be narrow and uniform, good abrasion resistance can be obtained even if the PU resin is adhered in a fine state.
  • Examples of the method for dispersing a fibers in single fibers include a method of converting a fiber produced by a direct spinning method into a fiber sheet by a papermaking method, a method of promoting a single fiber conversion of an ultrafine fiber bundle by dissolving or decomposing the sea component of a fiber sheet composed of a sea-island type composite fiber to generate an ultrafine fiber bundle, and thereafter subjecting the ultrafine fiber bundle surface to the aforementioned water stream dispersion treatment.
  • the fibers may or may not be dispersed single fibers.
  • the layers other than the fiber layer (A) are also composed of dispersed single fibers. Since the fibers constituting the layers other than the fiber layer (A) are dispersed single fibers, it is preferable from the viewpoint that the thickness of the artificial leather becomes homogeneous, the processing accuracy is improved, and quality is stabilized. Furthermore, it is also preferable from the viewpoint of homogenizing the appearances of the front and back surfaces of the artificial leather.
  • the basis weight of the fibers constituting the fiber layer (A) is preferably 40 g/m 2 to 500 g/m 2 , more preferably 50 g/m 2 to 370 g/m 2 , and further preferably 60 g/m 2 to 320 g/m 2 , from the viewpoint of mechanical strength such as abrasion resistance.
  • the basis weight of the fibers constituting the fiber layer (A) is preferably 10 g/m 2 to 200 g/m 2 , more preferably 30 g/m 2 to 170g/m 2 , and further preferably 60 g/m 2 to 170 g/m 2 , from the viewpoint of mechanical strength such as abrasion resistance.
  • the basis weight of the fibers constituting the fiber layer (B) is preferably 10 g/m 2 to 200 g/m 2 , and more preferably 20 g/m 2 to 170 g/m 2 .
  • the basis weight of the scrim is preferably 20 g/m 2 to 150 g/m 2 , more preferably 20 g/m 2 to 130 g/m 2 , and further preferably 30 g/m 2 to 110 g/m 2 , from the viewpoint of mechanical strength and entanglement between the fiber layer and the scrim.
  • the basis weight of artificial leather filled with PU is preferably 50 g/m 2 to 550 g/m 2 , more preferably 60 g/m 2 to 400 g/m 2 , and further preferably 70 g/m 2 to 350 g/m 2 .
  • the dyeing unevenness inconspicuousness of the artificial leather is preferably grade 4.0 or higher, and more preferably grade 5.0 class or higher.
  • the dyeing unevenness inconspicuousness is a value obtained by judging the difficulty in discriminating the color differences between the fiber and the PU resin in seven grades by visual evaluation.
  • the moist feeling of the artificial leather is preferably grade 4.0 or higher, and more preferably grade 5.0 or higher.
  • the moist feeling is a value obtained by judging the moist feeling when the first outer surface of the fiber layer (A) is touched in seven grades by sensory evaluation according to texture.
  • the dense feeling (dispersibility of the fiber bundle) of the artificial leather is preferably grade 4.0 or higher, and more preferably grade 5.0 or higher.
  • the dense feeling (dispersibility of the fiber bundle) is a value obtained by judging the denseness of nap in seven grades by visual and tactile sensory evaluation. By setting the dense feeling to grade 3.0 or higher, the quality as upholstery or an interior material of seats such as in interior, automobiles, aircraft, and railway vehicles is improved.
  • Examples of the method for producing each fiber layer (fiber layer (A) and optional fiber layer (B)) constituting a fiber sheet of the artificial leather include spinning direct coupling methods (e.g., the spunbond method and melt blowing method), and a method of forming a fiber sheet using cut fibers (e.g., dry methods such as carding or the airlaid method, and wet methods such as a papermaking method), and any of these can be suitably used.
  • cut fibers e.g., dry methods such as carding or the airlaid method, and wet methods such as a papermaking method
  • sea-island (SIF) cut fibers are used as the raw material.
  • a fiber sheet produced using cut fibers is suitable in terms of improving the surface quality of the artificial leather because it has small basis weight and is excellent in uniformity, whereby uniform nap is easily obtained.
  • an ultrafine fiber expression type fiber As the means for forming the ultrafine fibers of the fiber sheet, an ultrafine fiber expression type fiber can be used. By using an ultrafine fiber expression type fiber, a state in which ultrafine fiber bundles are entangled can be stably obtained.
  • a sea-island type fiber in which two thermoplastic resins having different solvent solubilities are used as the sea component and island component, and the island component is formed into ultrafine fibers by dissolving and removing the sea component with a solvent or a peelable composite fiber in which a thermoplastic resin having two components which alternately arranged in a fiber cross-section in a radial or multi-layered manner, and each component is peeled and divided into ultrafine fibers can be used.
  • sea-island type fibers are preferably used from the viewpoint of flexibility and texture of the sheet-like material because suitable voids can be imparted between the island components, i.e., between the ultrafine fibers, by removing the sea component.
  • sea-island type fibers examples include sea-island type composite fibers which are spun by arranging two components including the sea component and the island component using a sea-island type composite spinneret, and sea-island type composite fibers which are spun by mixing the two components including the sea component and the island component.
  • a sea-island type composite fiber is preferably used.
  • Polyethylene, polypropylene, polystyrene, a copolymerized polyester obtained by copolymerizing sodium sulfoisophthalic acid or polyethylene glycol, and polylactic acid can be used as the sea component of the sea-island fiber.
  • a copolymerized polyester or a polylactic acid obtained by copolymerizing an alkali-decomposable sodium sulfoisophthalic acid or polyethylene glycol which can be decomposed without the use of an organic solvent is preferred.
  • the sea-component dissolution is performed prior to the application of the PU resin onto the fiber sheet when a sea-island fiber is used. If the sea-component dissolution is performed prior to the application of the PU resin, the PU resin is adhered directly with the ultrafine fibers, whereby the ultrafine fibers can be strongly adhered, improving the abrasion resistance of the sheet-like material.
  • the method for entangling the fibers or fiber bundles of the fiber web a method in which the sea-island fibers are cut into predetermined fiber lengths to form staple fibers, a fiber web is formed with a card and a cross-lapper, and the fiber web is entangled by a needle punching process or a water stream entanglement process referred to as the spunlace method can be used.
  • the number of barbs of a needle used is preferably one to nine.
  • the number of barbs of a needle By setting the number of barbs of a needle to one or more, the entangling effect can be obtained and damage to fibers can be suppressed.
  • the number of barbs of a needle By setting the number of barbs of a needle to nine or fewer, damage to the fibers can be reduced, and additionally, needle marks remaining in the artificial leather can be reduced, whereby the appearance of the product can be improved.
  • the total depth (length from the tips of the barb to the bottom of the barb) of the barbs be 0.05 mm to 0.10 mm. If the total depth of the needle is 0.05 mm or more, efficient fiber entanglement is facilitated because good hooking of the fibers is obtained. Furthermore, when the total depth of the barb is 0.10 mm or less, needle marks remaining in the artificial leather are reduced and the quality is improved. In consideration of the balance between the strength of the needles and fiber entanglement, the total depth of the barb is more preferably 0.06 mm to 0.08 mm.
  • the range of the punch density is preferably 300 needles/cm 2 to 6000 needles/cm 2 , and more preferably 1000 needles/cm 2 to 6000 needles/cm 2 .
  • the fiber sheet obtained by the needle punch processing may be, for example, immersed in water at a temperature of 98 °C for 2 minutes for shrinkage, and dried at a temperature of 100 °C for 5 minutes to obtain a fiber sheet prior to a sea-component dissolution.
  • the sea-component dissolution can be performed by immersing the sea-island fibers in a solvent to constrict.
  • a solvent for dissolving the sea component an aqueous alkali solution such as sodium hydroxide can be used when the sea component is a copolymerized polyester or a polylactic acid. From the viewpoint of environmental considerations of the treatment, a sea-component dissolution with an aqueous alkali solution such as sodium hydroxide is preferred.
  • the cut fiber length in the case in which a method using cut fibers (staple fibers) is selected, is preferably 13 mm to 102 mm, more preferably 25 mm to 76 mm, and further preferably 38 mm to 76 mm in dry methods (carding, airlaid method, etc.), and is preferably 1 mm to 30 mm, more preferably 2 mm to 25 mm, and further preferably 3 mm to 20 mm in wet methods (papermaking method, etc.).
  • the aspect ratio (L/D) which is a ratio of the length (L) and the diameter (D), of the cut fibers used in wet methods (such as a papermaking method) is preferably 500 to 2000, and more preferably 700 to 1500.
  • the fiber length of cut fibers having a diameter of 4 ⁇ m is preferably 2 mm to 8mm, and more preferably 3 mm to 6 mm.
  • the obtained fiber sheet By subjecting the obtained fiber sheet to the aforementioned water stream dispersion treatment, a fiber sheet in which the single fibers are dispersed can be obtained.
  • the fiber sheet is impregnated with a water-dispersed PU resin dispersion containing hot water-soluble resin fine particles, and the PU resin is then affixed by heating to fill the PU resin.
  • the PU resin is impregnated in the form of an impregnating liquid such as a dispersion (e.g., in the case of water-dispersed PU resin).
  • the concentration of PU resin in the impregnating liquid may be, for example, 10 to 35% by mass.
  • the impregnation solution is prepared and impregnated into the fiber sheet so that the ratio of PU resin to 100% by mass of the fiber sheet is 15 to 50% by mass.
  • Water-dispersed PU resins are classified into forced-emulsification type PU resins which are forcibly dispersed and stabilized using a surfactant and self-emulsification type PU resins which have a hydrophilic structure in the PU molecular structure and which disperses and stabilizes in water even in the absence of a surfactant. Though any of these may be used in the present embodiment, it is preferable to use a forced-emulsification type PU resin from the viewpoint of imparting a thermal coagulation property, which is described later.
  • the water-dispersed PU resin dispersion containing hot water-soluble resin fine particles is impregnated into the fiber sheet, it is not preferable that the hot water-soluble resin fine particles be dissolved in the water-dispersed PU resin dispersion.
  • a forced-emulsification type PU resin dispersion containing a surfactant is preferred over a self-emulsification type PU resin dispersion containing no surfactant.
  • the concentration of the water-dispersed PU resin (the content of the PU resin relative to the water-dispersed PU resin dispersion) is preferably 10 to 35% by mass, more preferably 15 to 30% by mass, and further preferably 15 to 25% by mass, from the viewpoint of controlling the quantity of the water-dispersed PU resin to be adhered, and from the viewpoint of promoting adhesion of the PU resin when the concentration is high and reduction of the stability of the impregnation liquid.
  • water-dispersed PU resin dispersions having thermal coagulation properties are preferred.
  • the PU resin can be uniformly distributed in the thickness direction of the fiber sheet.
  • Thermal coagulation properties refers to the property in which when the PU resin dispersion is heated, the fluidity of the PU resin dispersion decreases and it solidifies when a certain temperature (thermal coagulation temperature) is reached.
  • the fiber sheet is impregnated with the PU resin dispersion, and the PU resin is the coagulated by dry heat coagulation, wet heat coagulation, hot water coagulation, or a combination thereof, and dried to impart the fiber sheet with the PU resin.
  • dry coagulation is conventional in industrial production, but in this case, a migration phenomenon in which PU resin is concentrated on a surface layer of the sheet-like material occurs, whereby the texture of sheet-like material filled with PU resin tends to become hard.
  • the thermal coagulation temperature of the water-dispersed PU resin dispersion is preferably 40 to 90 °C.
  • the thermal coagulation temperature is preferably 40 to 90 °C.
  • thermal coagulation agent In order to set the thermal coagulation temperature as described above, a thermal coagulation agent may be added as needed.
  • thermal coagulation agents include inorganic salts such as sodium sulfate, magnesium sulfate, calcium sulfate, and calcium chloride, and radical reaction initiators such as sodium persulfate, potassium persulfate, ammonium persulfate, azobisisobutyronitrile, and benzoyl peroxide.
  • the fiber sheet is impregnated or coated with the water-dispersed PU resin dispersion, and the PU resin can be coagulated by dry heat coagulation, wet heat coagulation, hot water coagulation, or a combination thereof.
  • the temperature of the wet heat coagulation is set to be equal to or higher than the thermal coagulation temperature of the PU resin, and is preferably 40 to 200 °C. By setting the temperature of the wet heat coagulation to 40 °C or higher, more preferably 80 °C or higher, it is possible to further suppress the migration phenomenon by shortening the time to coagulation of the PU resin.
  • the temperature of the wet heat coagulation is set to be equal to or higher than the thermal coagulation temperature of the PU resin, and is preferably set to 40 to 100 °C.
  • the dry coagulation temperature and the drying temperature are preferably 80 to 180 °C.
  • the content of the hot water-soluble resin fine particles in the water-dispersed PU resin dispersion is preferably 1 wt% to 20 wt%, preferably 2 wt% to 15 wt%, and more preferably 3 wt% to 10 wt%.
  • Examples of the means for removing the hot water-soluble resin from the sheet-like material include a method of immersion in hot water at 60 °C or higher, preferably 80 °C or higher, and a method of removing the hot water-soluble resin fine particles while circulating hot water at 80 °C or higher prior to performing dyeing processing in a j et dyeing machine.
  • a method of removing hot water-soluble resin fine particles in a jet dyeing machine is preferred since a step of drying and winding of the sheet-like material after removing the hot water-soluble resin fine particles can be omitted, whereby production efficiency can be increased.
  • a flexible sheet-like material is obtained by removing the hot water-soluble resin fine particles from the sheet-like material after the PU resin has been applied.
  • the method for removing the hot water-soluble resin fine particles is not particularly limited, for example, dissolving and removing the particles by immersing the sheet in hot water at 60 to 100 °C, and if necessary, wringing the sheet with a wringer is preferred.
  • the sheet-like material filled with the PU resin can be sliced in half horizontally. As a result, production efficiency can be improved.
  • the sheet-like material filled with a PU resin may be imparted with a lubricant such as a silicone dispersion before brushing, which is described later. Furthermore, applying an antistatic agent before brushing is preferable in order to prevent the grindings generated from the sheet-like material by grinding from accumulating on the sandpaper.
  • Brushing can be performed to form naps on the surface of the sheet-like material.
  • Brushing can be performed by a method of grinding or the like using a sandpaper, a roll sander, or the like. Furthermore, applying silicone or the like as a lubricant prior to brushing easily enables brushing by surface grinding, whereby surface quality becomes very good.
  • the artificial leather be subjected to a dyeing treatment for the purpose of enhancing the surface appearance value (i.e., visual effect).
  • the dye may be selected in accordance with the type of fiber constituting the fiber sheet, and, for example, a disperse dye may be used for polyester-based fibers, and an acid dye or a metal-complexed dye may be used for polyamide-based fibers, and a combination thereof may be used.
  • a disperse dye When dyeing is performed with a disperse dye, reduction cleaning may be performed after dyeing.
  • the dyeing method a conventional method well known to dyeing processors can be used.
  • the dyeing temperature is preferably 80 to 150 °C, depending on the type of fiber. By setting the dyeing temperature to 80 °C or higher, more preferably 110 °C or higher, dyeing of the fibers can be efficiently performed. Conversely, by setting the dyeing temperature to 150 °C or lower, more preferably 130 °C or lower, it is possible to prevent the deterioration of the PU resin.
  • the artificial leather dyed in this manner is preferably subjected to soaping and, if necessary, reduction cleaning (i.e., washing in the presence of a chemical reducing agent) to remove excess dye. It is also preferable to use a dyeing aid at the time of dyeing. By using a dyeing auxiliary, uniformity and reproducibility of dyeing can be improved. Further, in the same bath as used in dyeing or after dyeing, finishing using a softener such as silicone, an antistatic agent, a water repellent, a flame retardant, a light resistant agent, or an antibacterial agent can be applied.
  • a softener such as silicone, an antistatic agent, a water repellent, a flame retardant, a light resistant agent, or an antibacterial agent can be applied.
  • the artificial leather of the present embodiment can also be suitably used as an upholstery or interior material requiring an elegant appearance, for example, a surface material of furniture, chairs, and walls, seats, ceilings, and interiors of vehicles such as automobiles, trains, and aircrafts, a clothing material of a part of shirts and jackets, the uppers of shoes such as casual shoes, sports shoes, men's shoes, women's shoes, various trims, bags, belts, wallets, etc., or an industrial material of wiping cloths, abrasive cloths, and CD curtains.
  • FIG. 3 shows the sample collection sites.
  • the fiber layer (A) or the artificial leather comprising the fiber layer (A) was cut at ten substantially evenly positions (sampling areas 1, 2, ...) in the machine direction (MD) into bands (indicated by dotted lines).
  • the thickness (t) cross-section was made electroconductive by coating it with osmium atom in 1nm thick.
  • k-nearest neighbor ratio value (%) in these cross-sections ten substantially uniform SEM images were captured in the CD direction perpendicular to the MD direction.
  • the surface PU resin area ratio (%) in each sampling region ten substantially uniform SEM images of the first outer surface of the fiber layer (A) were made electroconductive by coating it with osmium atom in 1nm thick, and then were captured in the CD direction. Specifically, 100 images were prepared for each of the images used for obtaining the single fiber cross-section k-nearest neighbor ratio value (%), and the surface PU resin area ratio (%). In this case, the average and standard deviation of each value is for 100 images.
  • the napped direction is the MD direction.
  • one direction can be defined in arbitrary as MD direction, and another direction perpendicular to the defined MD direction can be defined as CD direction.
  • the obtained SEM-reflected electron images were binarized by the following method using image analysis software "ImageJ (version: 1.51j8), National Institutes of Health", and the average sizes of the PU-resin was obtained.
  • the value obtained by dividing the sum of the areas of the respective PU resins distributed within each compartment by the area of each compartment was defined as the surface PU resin area ratio (%) of each compartment.
  • the number of pixels of the x and y axes of the target image were counted, the size of the compartment was designated by the pixel size, the number of divisions of the x and y axes was determined, and the PU resin area% within each divided area was calculated.
  • the PU resin area ratio calculated with one SEM image was obtained by averaging the surface PU resin area ratio (%) for all compartments of the one SEM image, and the standard deviation thereof is calculated by the formula shown in FIG. 6 .
  • the surface PU resin area ratio (%) and the standard deviation thereof were obtained by averaging the PU resin area ratio and the standard deviation thereof calculated with one SEM image. That is, as shown in FIG. 6 , the standard deviation was first calculated for all compartments obtained by dividing one SEM image into compartments, and second obtained by averaging the standard deviations calculated for each of 100 SEM images.
  • the k-nearest neighbor method is a method in which k number single fiber cross-sections are taken to any one single fiber cross-section, and the kth nearest radius in the Euclidean distance is set as the determination boundary.
  • the deepest portion of the fiber layer (A) on the cut surface of the sample subjected to the conductive process i.e., the most scrim-side portion
  • the observation region i.e., the observation region
  • the fibers constituting the scrim were not observed, and observation was carried out with a scanning electron microscope (SEM, "JSM-5610" manufactured by JEOL).
  • SEM scanning electron microscope
  • Presence of the single-fiber cross-sections within SEM images can be identified regarding presence by performing markings by a person, as shown in FIG. 4 .
  • the specific procedures are as follows:
  • the Euclidean distance (k-nearest neighbor distance: matrix distance) to the kth nearest fiber cross-section was calculated for all fiber cross-sections.
  • the number of cross-sections with a k-nearest neighbor distance less than or equal to R was divided by the total number of fiber cross-sections, and set as the k-nearest neighbor ratio value in the SEM image.
  • the positions of the fiber cross-sections may be specified by machine learning (deep learning) which classifies at the pixel level by semantic segmentation using a network FCN (Fully Convolutional Networks) technique (Jonathan Long, Evan Shelhamer, and Trevor Darrel (2015): Fully Convolutional Networks for Semantic Segmentation; In The IEEE Conference on Computer Vision and Pattern Recognition (CVPR)).
  • FCN Full Convolutional Networks
  • the average diameter of the fibers constituting the fiber layer (A) was obtained by capturing a thickness direction cross-section of the artificial leather using a scanning electron microscope (SEM, "JSM-5610" made of JEOL) at a magnification of 1500-fold to obtain 10 SEM images, randomly selecting 100 fibers in a thickness direction cross-section of the artificial leather, measuring the diameters of the cross-sections of the single fibers, and determining the arithmetic average value of the 100 measured values.
  • SEM scanning electron microscope
  • the distance between the outer circumferences on a straight line perpendicular to the middle point of the longest diameter of the single fiber cross section was taken as the fiber diameter.
  • FIG. 2 is a conceptual diagram detailing the method for determining fiber diameter.
  • the outer peripheral distance c on the straight line b orthogonal to the midpoint p of the longest diameter a of the cross-section A in the observation image is defined as the fiber diameter.
  • Grade 4 It was judged that the color difference between fiber and PU resin was inconspicuous for 8 or more evaluators, and colored spots were unrecognizable.
  • Grade 1 It was judged that the color difference between fiber and PU resin was inconspicuous for 2 or fewer evaluators, and colored spots were unrecognizable.
  • evaluation scores of dyeing unevenness is the average value for 10 samples.
  • a total of 20 evaluators including 10 adult males and 10 adult females each in good health performed visual and sensory evaluation across seven grades according to the following criteria, and the most common evaluation was moist feeling.
  • a moist feeling of grade 4.0 to 7 was considered suitable (pass).
  • Grade 7 The feeling is very smooth (feels moist) and the appearance is very good.
  • Grade 6 Evaluation between Grade 7 and Grade 5.
  • Grade 5 The feel is smooth (feels moist) and the appearance is good.
  • Grade 4 Evaluation between the Grade 5 and Grade 3.
  • Grade 2 Evaluation between Grade 3 and Grade 1.
  • a total of 20 evaluators including 10 adult males and 10 adult females each in good health performed visual and sensory evaluation across seven grades according to the following criteria, and the most common evaluation was dense feeling.
  • a dense feeling (dispersibility of fiber bundles) of grade 4.0 to 7.0 was considered suitable (pass).
  • Grade 6 Evaluation between Grade 7 and Grade 5.
  • Grade 4 Evaluation between the Grade 5 and Grade 3.
  • Grade 2 Evaluation between Grade 3 and Grade 1.
  • the adhesion ratio of the PU resin to the fiber sheet was measured by the following method.
  • the mass of the fiber sheet before PU resin impregnation was defined as A (g).
  • the fiber sheet was impregnated with a PU resin dispersion and then heated and dried using a pin tenter dryer at 130 °C, subsequently submerged in hot water heated to 90 °C and then dried to obtain a fiber sheet filled with PU resin (hereinafter, also referred to as a "resin filled fiber sheet").
  • the mass of the resin filled fiber sheet was defined as B1 (g).
  • the adhesion ratio (C1) of the PU resin was calculated by the following formula.
  • C 1 B 1 ⁇ A / A ⁇ 100 wt %
  • Average primary particle size was measured with a laser diffraction particle size distribution measuring device ("LA-920", manufactured by HORIBA, Ltd.) according to the measuring manual of the device, and the average diameter was taken as the average primary particle diameter.
  • the degree of saponification was measured in accordance with the JIS K6726 (1994) 3.5 standard.
  • the degree of polymerization was measured in accordance with the JIS K6726 (1994) 3.7 standard.
  • the turbulence of the water streams discharged from the nozzles in the water stream dispersion treatment was measured by the following method.
  • the water streams discharged from the nozzles were captured with a single-lens camera ("D600” manufactured by Nikon Corporation) fitted with a telecentric lens ("S5LPJ007/212" manufactured by Sill Optics GmbH & Co.KG) to obtain image data.
  • the image data was output to a PC, water streams in the range of 25 mm to 35 mm from the nozzle discharge port were removed, and the water stream diameter was measured for each single pixel row (approximately 6 ⁇ m) in the width direction of the water streams.
  • turbulence is the average value of the values obtained from five sets of image data.
  • Polyethylene terephthalate obtained by copolymerizing 8 mol% of 5-sulfoisophthalic acid sodium was used as the sea component, and polyethylene terephthalate was used as the island component, and a sea-island type conjugate fiber having an island number of 16 islands/If and an average fiber diameter of 18 ⁇ m was obtained at a composite ratio of 20% by mass of sea component and 80% by mass of island component.
  • the obtained sea-island composite fibers were cut to a fiber length of 51 mm to form a staple, and a fiber web was formed through a card and a cross-lapper, and a fiber sheet was obtained by needle-punch processing.
  • the obtained fiber sheet was immersed in hot water at 95 °C to shrink, and dried using a pin tenter dryer at 100 °C for 5 minutes to obtain a single layer of fiber sheet having a basis weight of 600 g/m 2 .
  • the obtained fiber sheet was immersed in an aqueous sodium hydroxide solution having a concentration of 10 g/L heated to a temperature of 95 °C, subjected to treatment for 25 minutes, and subjected to a sea-component dissolution to remove the sea component of the sea-island composite fibers.
  • the average diameter of the single fibers of the fibers constituting the fiber sheet after sea-component dissolution was 4 ⁇ m.
  • high-speed water streams were discharged from the upper layer side at 4 MPa and 3 MPa pressures from the lower layer side using straight stream injection nozzles having a nozzle hole interval of 0.25 mm, a turbulence of 7%, a hole diameter of 0.10 mm, and three rows of holes to promote the formation of single fibers of the fibers constituting the fiber bundle.
  • the above fiber sheet was impregnated with an impregnation solution containing 9.0 wt%, as a quantity (% by mass of solid content) in the impregnation solution, of a polyether-based aqueous dispersion PU dispersion "AE-12" (manufactured by Nikka Chemical Co., Ltd.) (solid concentration: 35% by mass) having an average primary particle diameter of 0.3 ⁇ m, 3.0 wt%, as a quantity (% by mass of solid content) of an anhydrous sodium sulfate as an impregnation aid, and PVA resin fine particles "NL-05” (manufactured by Mitsubishi Chemical Co., Ltd.) having an average particle diameter of 3 ⁇ m, and thereafter, the impregnated sheet wet-hot coagulated at 100 °C for 5 minutes and hot air dried at 130 °C for 5 minutes using a hot air dryer.
  • an impregnation solution containing 9.0 wt%, as a quantity (% by mass
  • the dried sheet was then immersed in hot water heated to 95 °C, thereby extracting and removing the impregnated anhydrous sodium sulfate and PVA resin fine particles to obtain a sheet-like material filled with a water-dispersed PU resin.
  • the ratio of the water-dispersed PU resin to the total mass of fibers of this sheet was 30% by mass.
  • the sheet-like material was sliced in half horizontally, and the surface which was not half-cut was subjected to brushing using a #400 emery paper, and then dyed with a blue disperse dye having a dye density of 5.0% owf ("BlueFBL" manufactured by Sumitomo Chemical Co., Ltd.) for 15 minutes using a jet dyeing machine at 130 °C, followed by reduction cleaning. Thereafter, it was dried using a hot air dryer at 100 °C for 5 minutes to obtain a single layer of artificial leather.
  • a blue disperse dye having a dye density of 5.0% owf
  • An artificial leather was obtained in the same manner as in Example 1, except that the water pressure from the upper layer side in the water stream dispersion treatment was changed to 4.0 MPa
  • An artificial leather was obtained in the same manner as in Example 2, except that the ratio of PU resin to fiber sheet was 44% by mass.
  • An artificial leather was obtained in the same manner as in Example 2, except that the ratio of PU resin to fiber sheet was 47% by mass.
  • An artificial leather was obtained in the same manner as in Example 2, except that the ratio of PU resin to fiber sheet was 17% by mass.
  • An artificial leather was obtained in the same manner as in Example 2, except that the nozzle hole interval in the water stream dispersion treatment was changed to 0.50 mm and the number of nozzle rows was changed to two.
  • An artificial leather was obtained in the same manner as in Example 2, except that the nozzle hole interval in the water stream dispersion treatment was changed to 0.50 mm and the number of nozzle rows was changed to one.
  • An artificial leather was obtained in the same manner as in Example 2, except that the nozzle hole interval in the water stream dispersion treatment was changed to 0.90 mm and the number of nozzle rows was changed to one.
  • An artificial leather was obtained in the same manner as in Example 2, except that the nozzle hole interval in the water stream dispersion treatment was changed to 0.50 mm, the nozzle hole diameter was changed to 0.15 mm, and the number of nozzle rows was changed to two.
  • An artificial leather was obtained in the same manner as in Example 2, except that the nozzle hole interval in the water stream dispersion treatment was changed to 0.50 mm, the nozzle hole diameter was changed to 0.22 mm, and the number of nozzle rows was changed to two.
  • An artificial leather was obtained in the same manner as in Example 2, except that the turbulence of the water stream dispersion treatment was set to 13%.
  • An artificial leather was obtained in the same manner as in Example 2, except that the turbulence of the water stream dispersion treatment was set to 11%.
  • An artificial leather was obtained in the same manner as in Example 2, except that the turbulence of the water stream dispersion treatment was set to 16%.
  • An artificial leather was obtained in the same manner as in Example 2, except that the average primary particle diameter of PVA particles in PU resin impregnation was set to 5 ⁇ m and the turbulence of the water stream dispersion treatment was set to 13%.
  • An artificial leather was obtained in the same manner as in Example 2, except that the average primary particle diameter of PVA particles in PU resin impregnation was set to 7 ⁇ m and the turbulence of the water stream dispersion treatment was set to 13%.
  • An artificial leather was obtained in the same manner as in Example 2, except that PVA resin fine particles were not added to the PU resin impregnation liquid.
  • An artificial leather was obtained in the same manner as in Example 2, except that the PVA resin fine particles were not added to the PU resin impregnation liquid and the turbulence of the water stream dispersion treatment was set to 13%.
  • An artificial leather was obtained in the same manner as in Example 2, except that the water stream dispersion treatment was not performed.
  • An artificial leather was obtained in the same manner as in Example 2, except that the water pressure from the upper layer side in the water stream dispersion treatment was changed to 12.0 MPa.
  • An artificial leather was obtained in the same manner as in Example 2, except that the water pressure from the upper layer side in the water stream dispersion treatment was changed to 0.7 MPa.
  • An artificial leather was obtained in the same manner as in Example 2, except that the ratio of PU resin to fiber sheet was 58% by mass.
  • An artificial leather was obtained in the same manner as in Example 2, except that the ratio of PU resin to fiber sheet was 13% by mass.
  • An artificial leather was obtained in the same manner as in Example 2, except that the average primary particle diameter of PVA particles in PU resin impregnation was set to 10 ⁇ m and the turbulence of the water stream dispersion treatment was set to 13%.
  • the surface PU resin area ratio in the thickness direction cross section was 8% to 25%
  • the standard deviation of the surface PU resin area ratio was 25% or less
  • the PU resin and the single fibers are distributed in a specific structure, whereby an artificial leather having excellent dyeing unevenness inconspicuousness, dense feeling, and moist feeling was obtained.
  • the artificial leather according to the present invention is excellent in dyeing unevenness inconspicuousness, dense feeling, and moist feeling, it can be suitably used for the upholstery or interior material of seats for interior, automobiles, aircrafts, railway vehicles, etc., garment products, or the like.
  • the artificial leather of the present embodiment can also be suitably used as an upholstery or interior material requiring an elegant appearance, for example, a surface material of furniture, chairs, and walls, seats, ceilings, and interiors of vehicles such as automobiles, trains, and aircrafts, a clothing material of a part of shirts and jackets, the uppers of shoes such as casual shoes, sports shoes, men's shoes, women's shoes, various trims, bags, belts, wallets, etc., or an industrial material of wiping cloths, abrasive cloths, and CD curtains.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Synthetic Leather, Interior Materials Or Flexible Sheet Materials (AREA)

Claims (15)

  1. Cuir artificiel comprenant une feuille de fibres et une résine de polyuréthane, dans lequel la feuille de fibres inclut au moins une couche de fibres (A) constituant une première surface externe du cuir artificiel et présente une valeur du rapport de k-plus proche voisin (k = 9, rayon r = 20 µm) entre des sections transversales à fibre unique constituant la couche de fibres (A), déterminée comme décrit dans la description, de 10 % à 80 %, un rapport de surface de résine de polyuréthane en surface de la couche de fibres (A), déterminé comme décrit dans la description, est de 8 % à 25 %, et un écart-type du rapport de surface de résine de polyuréthane en surface de la couche de fibres (A) est de 25 % ou inférieur.
  2. Cuir artificiel selon la revendication 1, dans lequel la feuille de fibres présente une structure à deux couches ou plus constituée de la couche de fibres (A) constituant la première surface externe et d'un canevas et/ou une couche de fibres (B) en contact avec la couche de fibres (A).
  3. Cuir artificiel selon la revendication 1 ou 2, dans lequel le diamètre moyen de fibres uniques constituant la couche de fibres (A) est de 1,0 µm à 8,0 µm.
  4. Cuir artificiel selon l'une quelconque des revendications 1 à 3, dans lequel la résine de polyuréthane est une résine de polyuréthane dispersée dans l'eau.
  5. Cuir artificiel selon l'une quelconque des revendications 1 à 4, dans lequel un taux d'adhérence de la résine de polyuréthane à la feuille de fibres est de 15 % en masse à 50 % en masse.
  6. Cuir artificiel selon l'une quelconque des revendications 1 à 5, dans lequel une irrégularité de coloration de celui-ci est de degré 4,0 ou supérieure.
  7. Cuir artificiel selon l'une quelconque des revendications 1 à 6, dans lequel la feuille de fibres est constituée de fibres de polyester.
  8. Cuir artificiel selon l'une quelconque des revendications 1 à 7, dans lequel une sensation d'humidité de celui-ci est de degré 4,0 ou supérieure.
  9. Cuir artificiel selon l'une quelconque des revendications 1 à 8, dans lequel une sensation dense de celui-ci est de degré 4,0 ou supérieure.
  10. Procédé de production du cuir artificiel selon l'une quelconque des revendications 1 à 9, le procédé comprenant les étapes consistant à :
    former une bande de fibres à partir de fibres de coupe mer-île, réaliser après cela un procédé d'aiguilletage pour obtenir une feuille de fibres et réaliser une dissolution du constituant mer de la feuille de fibres pour obtenir une feuille de fibres dans laquelle des fibres uniques de constituant île sont exposées,
    soumettre la feuille de fibres obtenue à un traitement de dispersion dans un courant d'eau pour obtenir une feuille de fibres dans laquelle les fibres uniques sont dispersées, dans lequel l'eau pressurisée du traitement de dispersion de courant d'eau est injectée à de 1,0 à 10,0 MPa,
    imprégner la feuille de fibres dans laquelle les fibres uniques sont dispersées avec une dispersion de résine de polyuréthane dispersée dans l'eau contenant de fines particules de résine soluble dans l'eau chaude, dans lequel le diamètre moyen de particule des fines particules de résine soluble dans l'eau chaude est de 1 µm à 8 µm, et fixer après cela la résine de polyuréthane par chauffage pour obtenir un matériau en forme de feuille dans lequel la résine de polyuréthane est chargée, et
    éliminer les fines particules de résine soluble dans l'eau chaude du matériau en forme de feuille en utilisant de l'eau chaude.
  11. Procédé de production selon la revendication 10, dans lequel les fines particules de résine soluble dans l'eau chaude sont une résine de poly(alcool vinylique).
  12. Procédé de production selon l'une quelconque des revendications 10 à 11, dans lequel le traitement de dispersion dans un courant d'eau est réalisé en utilisant plusieurs buses ayant un intervalle de perforation de buse de 1,0 mm ou inférieur et un diamètre de perforation de buse de 0,05 mm à 0,30 mm.
  13. Procédé de production selon l'une quelconque des revendications 10 à 12, dans lequel le traitement de dispersion dans un courant d'eau est réalisé en utilisant une pluralité de buses qui déchargent des courants d'eau ayant une turbulence de 10 % ou supérieure.
  14. Procédé de production selon l'une quelconque des revendications 11 à 13, dans lequel une concentration de teneur solide de la dispersion de résine de polyuréthane dispersée dans l'eau est de 10 % en masse à 35 % en masse.
  15. Procédé selon l'une quelconque des revendications 11 à 14, dans lequel la teneur des fines particules de résine soluble dans l'eau chaude dans la dispersion de résine de polyuréthane dispersée dans l'eau est de 1 % en masse à 20 % en masse.
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FR2339697A1 (fr) * 1976-01-30 1977-08-26 Asahi Chemical Ind Etoffe composite et son procede de fabrication
JPH0782384A (ja) 1993-09-20 1995-03-28 Kuraray Co Ltd ポリビニルアルコール微粒子の製造方法
JP4089324B2 (ja) 2002-07-16 2008-05-28 東レ株式会社 スエード調人工皮革およびその製造方法
JP2014025165A (ja) 2012-07-26 2014-02-06 Toray Ind Inc シート状物の製造方法
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TWI666359B (zh) 2014-03-31 2019-07-21 日商東麗股份有限公司 染色人工皮革及其製造方法
JP6613764B2 (ja) 2014-09-30 2019-12-04 東レ株式会社 人工皮革およびその製造方法
JP6364383B2 (ja) 2015-06-30 2018-07-25 アオイ電子株式会社 配線基板、およびサーマルヘッド
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