WO2015056763A1 - ポリウレタン弾性繊維およびその製造方法 - Google Patents
ポリウレタン弾性繊維およびその製造方法 Download PDFInfo
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- WO2015056763A1 WO2015056763A1 PCT/JP2014/077619 JP2014077619W WO2015056763A1 WO 2015056763 A1 WO2015056763 A1 WO 2015056763A1 JP 2014077619 W JP2014077619 W JP 2014077619W WO 2015056763 A1 WO2015056763 A1 WO 2015056763A1
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/70—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyurethanes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4854—Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4858—Polyethers containing oxyalkylene groups having more than four carbon atoms in the alkylene group
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/487—Polyethers containing cyclic groups
- C08G18/4883—Polyethers containing cyclic groups containing cyclic groups having at least one oxygen atom in the ring
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
- C08G18/7657—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
- C08G18/7664—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
- C08G18/7671—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups containing only one alkylene bisphenyl group
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D175/00—Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
- C09D175/04—Polyurethanes
- C09D175/08—Polyurethanes from polyethers
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- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
- D04H1/54—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving
- D04H1/56—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving in association with fibre formation, e.g. immediately following extrusion of staple fibres
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2190/00—Compositions for sealing or packing joints
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
- C08J2375/04—Polyurethanes
- C08J2375/08—Polyurethanes from polyethers
Definitions
- the present invention relates to a polyurethane elastic fiber obtained by spinning a polyurethane resin and a method for producing the same.
- Polyurethane resin has excellent stretch properties, so it can be widely applied to raw materials for elastomers such as paints, coating agents, sealing materials, adhesives, adhesives, textile processing agents, artificial leather / synthetic leather, rolls, and textile products.
- elastomers such as paints, coating agents, sealing materials, adhesives, adhesives, textile processing agents, artificial leather / synthetic leather, rolls, and textile products.
- the polyurethane resin stretch properties are used to prevent degradation due to thermal history and improve the durability of the final product when producing and processing the final product from polyurethane resin. ) Is maintained while improving its heat resistance.
- Non-Patent Document 1 a method of adjusting the urethane group concentration and / or urea group concentration of a polyurethane resin is disclosed (for example, see Non-Patent Document 1).
- An object of the present invention is to provide a polyurethane elastic fiber having good heat setability, high heat resistance and excellent stretch properties (residual strain rate and elongation), and a method for producing the same.
- the present invention relates to a polyurethane resin comprising as constituent units a diol (a1) having a number average molecular weight of 500 to 10,000, an organic diisocyanate (b), and a chain extender (a2), wherein the urethane group concentration and The total value of the concentration of urea groups is 1.25 to 2.50 mmol / g based on the weight of the polyurethane resin, and the average domain diameter of the hard segment domain of the polyurethane resin measured with an atomic force microscope is 20 to A polyurethane elastic fiber obtained by spinning a polyurethane resin having a thickness of 30 nm; a method for producing the polyurethane elastic fiber, wherein the spinning method is dry spinning.
- the polyurethane elastic fiber of the present invention formed by spinning a polyurethane resin has high heat resistance and high heat resistance and excellent stretch properties.
- FIG. 1 is an image of a hard segment domain in the second embodiment.
- FIG. 2 is an image of the hard segment domain in Comparative Example 1.
- FIG. 3 is an evaluation diagram of elastic fibers in Example 1 and Comparative Example 1.
- the polyurethane resin used as the raw material of the polyurethane elastic fiber of this invention is demonstrated.
- the polyurethane resin has a diol (a1) having a number average molecular weight of 500 to 10,000, an organic diisocyanate (b), and a chain extender (a2) as structural units.
- diol (a1) having a number average molecular weight of 500 to 10,000 examples include polyoxyalkylene diol (a11), polyester diol (a12), polyetherester diol (a13), polybutadiene diol (a14), and 2 A mixture of seeds or more may be mentioned.
- polyoxyalkylene diol (a11) examples include compounds having a structure in which alkylene oxide (hereinafter abbreviated as AO) is added to a dihydric alcohol having 2 to 20 carbon atoms, and mixtures of two or more thereof.
- AO alkylene oxide
- dihydric alcohol having 2 to 20 carbon atoms examples include aliphatic dihydric alcohols having 2 to 12 carbon atoms [ethylene glycol (hereinafter abbreviated as EG), 1,3-propylene glycol, 1,4-butanediol (hereinafter, 1,4-BG), 1,5-pentanediol, 1,6-hexanediol, 1,7-heptanediol, 1,8-octanediol, 1,9-nonanediol, 1,10-dodecanediol
- linear alcohols such as diethylene glycol (hereinafter abbreviated as DEG); 1,2-, 1,3- or 2,3-butanediol, neopentyl glycol, 2,2-diethyl-1,3-propanediol, 2 -Methyl-1,5-pentanediol, 3-methyl-1,5-pentanediol, 2-methyl
- AO added to the dihydric alcohol examples include ethylene oxide (hereinafter abbreviated as EO), propylene oxide (hereinafter abbreviated as PO), 1,2-butylene oxide, 1,3-butylene oxide, and 2,3-butylene oxide.
- EO ethylene oxide
- PO propylene oxide
- 1,2-butylene oxide 1,3-butylene oxide
- 2,3-butylene oxide Tetrahydrofuran
- THF Tetrahydrofuran
- 3M-THF 3-methyltetrahydrofuran
- styrene oxide ⁇ -olefin oxide
- epichlorohydrin and the like.
- AO may be used individually by 1 type, or may use 2 or more types together.
- those having only THF, those using EO and THF, and those using THF and 3M-THF are particularly preferable.
- the coupling type may be random addition, block addition, or a combination of both.
- polyoxyalkylene diol (a11) examples include polyoxyethylene glycol, poly (oxy-1,2-propylene) glycol, polyoxytetramethylene glycol (hereinafter abbreviated as PTMG), polyoxy-3-methyltetramethylene glycol.
- PTMG polyoxytetramethylene glycol
- THF / EO copolymerized diol THF / 3M-THF copolymerized diol, and the like.
- PTMG, THF / EO copolymer diol, and THF / 3M-THF copolymer diol are preferred from the viewpoint of the tensile strength, elongation, and residual strain ratio of the polyurethane resin.
- polyester diol (a12) examples include dehydration condensation type polyester diol (a121), polylactone diol (a122), and polycarbonate diol (a123).
- the dehydration condensation type polyester diol (a121) includes a low molecular diol having a chemical formula weight or a number average molecular weight of less than 500 and a dicarboxylic acid or an ester-forming derivative thereof [an acid anhydride, a lower (1 to 4 carbon atoms) alkyl ester and an acid. And the like obtained by condensation with a halide or the like].
- Examples of the low molecular weight diol having a chemical formula weight or a number average molecular weight of less than 500 include the above dihydric alcohols having 2 to 20 carbon atoms (particularly aliphatic dihydric alcohols having 2 to 12 carbon atoms), bisphenols (bisphenol A, bisphenol S and bisphenol). F) and the like (number average molecular weight less than 500), dihydroxynaphthalene AO adduct (number average molecular weight less than 500) and bis (2-hydroxyethyl) terephthalate.
- the aliphatic dihydric alcohol having 2 to 12 carbon atoms is preferable.
- Low molecular weight diols having a chemical formula weight or number average molecular weight of less than 500 may be used alone or in combination of two or more.
- dicarboxylic acid or an ester-forming derivative thereof examples include aliphatic dicarboxylic acids having 4 to 15 carbon atoms [succinic acid, adipic acid, sebacic acid, glutaric acid, azelaic acid, maleic acid, fumaric acid and the like], and 8 to 12 carbon atoms.
- Aromatic dicarboxylic acids [terephthalic acid, isophthalic acid, etc.] and ester-forming derivatives thereof [acid anhydrides, lower alkyl esters (dimethyl esters, diethyl esters, etc.), acid halides (acid chlorides, etc.)], etc. .
- aliphatic dicarboxylic acids having 4 to 15 carbon atoms and ester-forming derivatives thereof are preferred.
- Dicarboxylic acid may be used individually by 1 type, or may use 2 or more types together.
- a lactone monomer ⁇ -butyrolactone, ⁇ -valerolactone, ⁇ -caprolactone and a mixture of two or more thereof
- dihydric alcohol having 2 to 20 carbon atoms examples thereof include those obtained by ring polymerization.
- the polycarbonate diol (a123) is one or two of the above-mentioned aliphatic dihydric alcohol having 2 to 12 carbon atoms (preferably an aliphatic dihydric alcohol having 3 to 8 carbon atoms, more preferably 4 to 6 carbon atoms).
- a low molecular carbonate compound for example, an alkyl group having 1 to 6 carbon atoms, an alkylene carbonate having 2 to 6 carbon atoms, and a diaryl carbonate having 6 to 9 carbon atoms
- polycarbonate diol produced by condensation while causing a dealcoholization reaction.
- aliphatic dihydric alcohols having 2 to 12 carbon atoms used for the production of the polycarbonate diol (a123) from the viewpoint of the residual strain of the polyurethane resin, 1,4-butanediol, 5-pentanediol, 1,6-hexanediol and 1,9-nonanediol, and in the branched form, 3-methyl-1,5-pentanediol and 2-methyl-1,8-octanediol.
- the polycarbonate diol (a123) includes crystalline polycarbonate diol and amorphous polycarbonate diol, and commercially available crystalline polycarbonate diol includes “Duranol T6002” [manufactured by Asahi Kasei Chemicals Corporation], “ETERRNACOLL UH”.
- the polyether ester diol (a13) is a polycondensation of one or more of the polyoxyalkylene diol (a11) and one or more of the dicarboxylic acids exemplified as the raw material of the dehydration-condensed polyester diol or an ester-forming derivative thereof. Can be obtained.
- polybutadiene diol (a14) examples include those having a 1,2-vinyl structure, those having a 1,4-trans structure, and those having a 1,2-vinyl structure and a 1,4-trans structure.
- (A14) also includes butadiene homopolymers and copolymers (styrene-butadiene copolymers, acrylonitrile-butadiene copolymers, etc.), and hydrogenated products thereof.
- the hydrogenated rate of the hydrogenated products is preferably 20 to 100. %.
- the number average molecular weight of the diol (a1) having a number average molecular weight of 500 to 10,000 is 500 or more, preferably 700 or more, more preferably 1,000 or more, From the viewpoint of the tensile strength of the polyurethane resin, it is 10,000 or less, preferably 5,000 or less, particularly preferably 4,000 or less.
- the number average molecular weight of the diol (a1) having a number average molecular weight of 500 to 10,000 in the present invention is determined from a hydroxyl value measured in accordance with a method defined in JIS K 0070-1992 (potential difference determining method). be able to.
- the organic diisocyanate (b) in the present invention includes an organic diisocyanate (b1) that reacts with a diol (a1) having a number average molecular weight of 500 to 10,000, and an organic diisocyanate (a2) that reacts with a chain extender (a2) described later ( b2) is included.
- the organic diisocyanate (b1) and the organic diisocyanate (b2) may be used alone or in combination of two or more.
- the organic diisocyanate (b1) and the organic diisocyanate (b2) may be the same or different.
- Examples of the organic diisocyanate (b) that can be used as the organic diisocyanate (b1) and the organic diisocyanate (b2) include aromatic diisocyanates having 8 to 26 carbon atoms, chain aliphatic diisocyanates having 4 to 22 carbon atoms, and those having 8 to 18 carbon atoms. Examples thereof include alicyclic diisocyanates, araliphatic diisocyanates having 10 to 18 carbon atoms, and modified products of these diisocyanates (such as carbodiimide modified products, urethane modified products, and uretdione modified products).
- aromatic diisocyanate having 8 to 26 carbon atoms include 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate, 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate, 2,4′- Diphenylmethane diisocyanate, 4,4'-diphenylmethane diisocyanate (hereinafter abbreviated as MDI), 4,4'-diisocyanatobiphenyl, 3,3'-dimethyl-4,4'-diisocyanatobiphenyl, 3,3'- Examples thereof include dimethyl-4,4′-diisocyanatodiphenylmethane and 1,5-naphthylene diisocyanate.
- MDI 4,4'-diphenylmethane diisocyanate
- chain aliphatic diisocyanate having 4 to 22 carbon atoms include ethylene diisocyanate, tetramethylene diisocyanate, hexamethylene diisocyanate, dodecamethylene diisocyanate, 2,2,4-trimethylhexamethylene diisocyanate, lysine diisocyanate, 2,6- Examples include diisocyanatomethyl caproate, bis (2-isocyanatoethyl) carbonate, and 2-isocyanatoethyl-2,6-diisocyanatohexanoate.
- alicyclic diisocyanate having 8 to 18 carbon atoms include isophorone diisocyanate, dicyclohexylmethane-4,4′-diisocyanate, cyclohexylene diisocyanate, methylcyclohexylene diisocyanate, bis (2-isocyanatoethyl) -4-cyclohexyl.
- examples include silene-1,2-dicarboxylate, 2,5-norbornane diisocyanate, and 2,6-norbornane diisocyanate.
- araliphatic diisocyanate having 10 to 18 carbon atoms include m-xylylene diisocyanate, p-xylylene diisocyanate, and ⁇ , ⁇ , ⁇ ', ⁇ '-tetramethylxylylene diisocyanate.
- aromatic diisocyanates having 8 to 26 carbon atoms are preferred from the viewpoint of improving the tensile strength of the polyurethane resin.
- MDI is particularly preferable.
- a diamine having 2 to 10 carbon atoms
- low molecular diols having a chemical formula weight or a number average molecular weight of less than 500 are preferred from the viewpoint of residual strain, tensile strength and elongation of the polyurethane resin, and the aliphatic dihydric alcohol having 2 to 12 carbon atoms is preferred. More preferred. Specific examples include ethylene glycol, diethylene glycol, 1,3-propanediol and 1,4-butanediol. Of these, ethylene glycol, 1,3-propanediol, and 1,4-butanediol are more preferable.
- the amount of the chain extender (a2) used is preferably 0.1 in terms of the number of moles of the diol (a1) having a number average molecular weight of 500 to 10,000 from the viewpoint of heat resistance, tensile strength and residual strain ratio of the polyurethane resin. ⁇ 10 times.
- a chain extender (a2) may be used individually by 1 type, or may use 2 or more types together.
- the total value of the urethane group concentration and the urea group concentration of the polyurethane resin is 1.25 to 2.50 mmol / g based on the weight of the polyurethane resin. If the total value of the urethane group concentration and the urea group concentration is less than 1.25 mmol / g, the tensile strength decreases, and if it exceeds 2.50 mmol / g, the residual strain rate increases and the elongation decreases. From the viewpoint of the residual strain rate of the polyurethane resin, it is preferably 1.55 to 2.30 mmol / g, and more preferably 1.75 to 2.20 mmol / g.
- the total value of the urethane group concentration and urea group concentration of the polyurethane resin is the total molar ratio of the diol (a1) and the chain extender (a2) having a number average molecular weight of 500 to 10,000 and the total mole of the organic diisocyanate (b). Calculated from the theoretical calculation of the ratio.
- the polyurethane resin has an average domain diameter of 20-30 nm of the hard segment domain of the polyurethane resin as measured by an atomic force microscope (hereinafter abbreviated as AFM). Heat resistance falls that the average domain diameter of a hard segment domain is less than 20 nm.
- the average domain diameter of the hard segment domain is preferably 21 to 29 nm, more preferably 21.5 to 28.0 nm, from the viewpoints of heat resistance, tensile strength and elongation of the polyurethane resin.
- the hard segment domain of the polyurethane resin is a domain having a phase shift of 0 to 50% as measured with an atomic force microscope, and includes a chain extender (a2), a chain extender (a2), It is a block (B2) comprised from the organic diisocyanate (b2) to react.
- the average domain diameter of the hard segment domain is the diameter of the block (B2) having a phase shift of 0 to 50% as measured by AFM.
- phase shift measured by AFM is measured by tapping the polyurethane resin surface with a cantilever and measuring the phase shift of the cantilever.
- a phase shift is small in a portion where the resin is hard, and a phase shift is large in a portion where the resin is soft.
- image processing is performed on the measurement result of the phase shift, the hard segment domain defined above is expressed as a constant domain diameter. This domain diameter is calculated using image processing software.
- the detection limit value of the average domain diameter of the hard segment domain that can be measured by the above measurement method is around 5 nm.
- ⁇ Measurement method of average domain diameter of hard segment by AFM The measurement method of the average domain diameter of the hard segment domain by AFM can be measured under the following conditions.
- Sample preparation method Cut the polyurethane resin to a size that fits on the sample table, and fix it to the sample table with double-sided tape.
- Measuring instrument Atomic force microscope SPI4000 Nano Navi Station (made by SII Nanotechnology)
- Cantilever type OMCL-AC240TS-R3
- Measuring unit E-sweep Scanning mode: Phase image (Measuring method of average domain diameter)
- the image measured with the atomic force microscope is analyzed using the following software.
- Measurement software WinROOF (manufactured by MITANI CORPORATION)
- the detection limit value of the average domain diameter of the hard segment domain that can be measured by the above measuring method is around 5 nm.
- the number average molecular weight (M B1 ) calculated using the following formula (1) of B1 ) is preferably 4,000 to 80,000 from the viewpoints of heat resistance, tensile strength and elongation of the polyurethane resin.
- the number average molecular weight calculated using the following formula (2) of the block (B2) composed of the chain extender (a2) and the organic diisocyanate (b2) that reacts with the chain extender (a2) ( M B2 ) is preferably 1,400 to 25,000 from the viewpoints of heat resistance, tensile strength and elongation of the polyurethane resin.
- M a1 represents the number average molecular weight of the diol (a1) having a number average molecular weight of 500 to 10,000
- M b1 represents the number average molecular weight of the organic diisocyanate (b1)
- k is a number This represents the number of moles of the diol (a1) having an average molecular weight of 500 to 10,000
- r represents the number of moles of the organic diisocyanate (b1).
- M a2 represents the number average molecular weight of the chain extender (a2)
- M b2 represents the number average molecular weight of the organic diisocyanate (b2)
- i represents the number of moles of the chain extender (a2).
- J represents the number of moles of the organic diisocyanate (b2).
- the number average molecular weight (M B1 ) of the block (B1) calculated using the above formula (1) is more preferably 4,200 to 70,000. It is particularly preferably 4,500 to 65,000.
- the number average molecular weight (M B2 ) of the block (B2) calculated using the above formula (2) is more preferably 1,450 to 22,000. It is particularly preferably 1,475 to 20,000.
- the polyurethane resin preferably satisfies the following (1) to (3).
- (1) The ratio between the number of moles of the diol (a1) having a number average molecular weight of 500 to 10,000 and the number of moles of the organic diisocyanate (b1) reacting with the diol (a1) having a number average molecular weight of 500 to 10,000 is
- the diol (a1): organic diisocyanate (b1) having a number average molecular weight of 500 to 10,000 is preferably 1: 1.05 to 1: 1.5, and more preferably the number average molecular weight is 500 to 10,000.
- Diol (a1): Organic diisocyanate (b1) 1: 1.05 to 1: 1.4, particularly preferably diol (a1): organic diisocyanate (b1) having a number average molecular weight of 500 to 10,000 1: 1.05 to 1.3.
- the sum of the number of moles of the organic diisocyanate (b1) and the number of moles of the organic diisocyanate (b2) that reacts with the chain extender (a2) is the diol (a1) having a number average molecular weight of 500 to 10,000.
- the number of moles is preferably 1.3 to 4.2 times, more preferably 2.0 to 3.4 times, and particularly preferably 2.4 to 3.0 times.
- the number average molecular weight of the polyurethane resin is preferably 20,000 to 200,000, more preferably 30,000 to 190,000, particularly preferably 40,000 to 180,000, from the viewpoint of tensile strength. is there.
- the number average molecular weight of the polyurethane resin can be measured, for example, under the following conditions by gel permeation chromatography.
- Flow rate 1 ml / min Measurement temperature: 40 ° C
- Detector Refractive index detector
- Reference material Standard polystyrene
- the heat softening point of the polyurethane resin is preferably 180 to 280 ° C., more preferably 185 to 260 ° C., and particularly preferably 190 to 240 ° C. from the viewpoint of heat resistance of the polyurethane resin.
- the heat softening point of the polyurethane resin can be measured according to the following procedure.
- the polyurethane resin is produced by a urethane prepolymer (p) having an isocyanate group obtained by reacting a diol (a1) having a number average molecular weight of 500 to 10,000 with an organic diisocyanate (b1), and an organic diisocyanate (b2). And a process for reacting the chain extender (a2) with a polyurethane resin, which satisfies the following (1) to (3).
- the ratio of the number of moles of the diol (a1) having the number average molecular weight of 500 to 10,000 to the number of moles of the organic diisocyanate (b1) is the diol having the number average molecular weight of 500 to 10,000 (a1 ):
- Organic diisocyanate (b1) 1: 1.05 to 1: 1.5;
- the total value of the number of moles of the organic diisocyanate (b1) and the number of moles of the organic diisocyanate (b2) is 1.3 times the number of moles of the diol (a1) having the number average molecular weight of 500 to 10,000.
- the total value of the number of moles of the diol (a1) having the number average molecular weight of 500 to 10,000 and the number of moles of the chain extender (a2) is the number of moles of the organic diisocyanate (b1) and the organic It is equal to the total value with the number of moles of diisocyanate (b2).
- Conditions such as temperature and time when the diol (a1) having a number average molecular weight of 500 to 10,000 is reacted with the organic diisocyanate (b1) may be the same as those used in the production of a normal urethane prepolymer. it can.
- the polyurethane resin can be produced by performing a step of reacting the urethane prepolymer (p), the organic diisocyanate (b2) and the chain extender (a2). Conditions such as temperature and time in this reaction can be the same as those used in the production of ordinary polyurethane resins.
- the organic diisocyanate (b1) used for producing the urethane prepolymer (p) and the organic diisocyanate (b2) reacted with the urethane prepolymer (p) may be the same or different.
- the total value of the number of moles of the isocyanate group of the organic diisocyanate (b1) and the number of moles of the isocyanate group of the organic diisocyanate (b2) has a number average molecular weight of 500 to 10, from the viewpoint of the tensile strength and residual strain of the polyurethane resin.
- the number of moles of the hydroxyl group of the diol (a1) of 000 is preferably 1.3 to 4.2 times, more preferably 2.0 to 3.4 times, and particularly preferably 2.4 to 3.0 times. It is.
- the total value of the number of moles of hydroxyl groups of the diol (a1) having a number average molecular weight of 500 to 10,000 and the number of moles of hydroxyl groups of the chain extender (a2) is determined from the organic diisocyanate (b1 It is preferable to be equal to the total value of the number of moles of isocyanate groups of) and the number of moles of isocyanate groups of organic diisocyanate (b2).
- a polyurethane resin can be obtained by reacting the urethane prepolymer (p), the organic diisocyanate (b2) and the chain extender (a2), but the urethane prepolymer (p) and the organic diisocyanate (b2). It is preferable to introduce a polymer terminal blocking agent (a3) during the reaction between the polymer and the chain extender (a2) to carry out the polymer terminal blocking stop reaction.
- polymer terminal blocking agent (a3) examples include monoalcohols having 1 to 18 carbon atoms (a31) and monoamines having 2 to 20 carbon atoms (a32).
- a polymer terminal blocker (a3) may be used individually by 1 type, or may use 2 or more types together.
- monoalcohols having 1 to 18 carbon atoms As monoalcohols having 1 to 18 carbon atoms (a31), linear monools (methanol, ethanol, n-propanol, n-butanol, pentanol, hexanol, octanol, nonyl alcohol, decyl alcohol, undecyl alcohol, dodecyl) Alcohol, tridecyl alcohol, tetradecyl alcohol, hexadecyl alcohol, octadecyl alcohol, etc.); branched monools (isopropanol, sec-, iso- or tert-butanol, neopentyl alcohol, 3-methyl-pentanol and 2) A monool having a cyclic group having 6 to 10 carbon atoms [an alicyclic group-containing monool (such as cyclohexanol) and an aromatic ring-containing monool (such as benzy
- Examples of the monoamine (a32) having 2 to 20 carbon atoms include carbons of alkyl groups such as ethylamine, n-propylamine, isopropylamine, n-butylamine, diethylamine, di-n-propylamine, diisopropylamine, and di-n-butylamine.
- Mono- or dialkylamine having 1 to 8 carbon atoms alicyclic monoamine having 6 to 10 carbon atoms such as cyclohexylamine; aromatic monoamine having 6 to 10 carbon atoms such as aniline; monoethanolamine, monoisopropanolamine, diethanolamine, disopropanol Examples thereof include mono or dialkanol amines having 2 to 4 carbon atoms of alkanol groups such as amines; heterocyclic monoamines such as morpholine; and mixtures of two or more thereof.
- the weight ratio of isocyanate groups in the reaction mixture containing the urethane prepolymer (p), the organic diisocyanate (b2), and the chain extender (a2) is 0.01 to 0.3. It is preferable to introduce the polymer end-capping agent (a3) when the weight percentage is reached. It is more preferable that the ratio of the weight of the isocyanate group when the polymer terminal blocking agent (a3) is added is 0.03 to 0.13% by weight.
- the ratio of the weight of the isocyanate group in the reaction mixture containing a urethane prepolymer (p), organic diisocyanate (b2), and chain extender (a2) is difficult to directly determine the weight of the isocyanate group to the ratio of the total amount of urethane prepolymer (p), organic diisocyanate (b2) and chain extender (a2) to the total amount of reaction mixture.
- the target range of the ratio of the weight of the isocyanate group at the time of charging the polymer end-capping agent (a3) is calculated, and the content of the isocyanate group in the reaction solution containing the organic solvent is measured.
- the target range is reached, the polymer end-capping agent (a3) is charged.
- the conditions such as the temperature and time of the termination reaction can be the same as those for the termination reaction during normal polyurethane resin production.
- an organic solvent can be used in any production process.
- the organic solvent is not particularly limited, and examples thereof include ketone solvents having 3 to 10 carbon atoms (for example, acetone, methyl ethyl ketone and methyl isobutyl ketone), ester solvents having 2 to 10 carbon atoms (for example, ethyl acetate, butyl acetate and ⁇ -butyrolactone).
- C 4-10 ether solvents eg, tetrahydrofuran and diethylene glycol dimethyl ether
- C 3-10 amide solvents eg, N, N-dimethylformamide, N, N-dimethylacetamide (hereinafter abbreviated as DMAC) , N-methyl-2-pyrrolidone and N-methylcaprolactam
- DMAC N-methyl-2-pyrrolidone and N-methylcaprolactam
- a sulfoxide solvent having 2 to 10 carbon atoms for example, dimethyl sulfoxide
- an alcohol solvent having 1 to 8 carbon atoms for example, methanol, ethanol, isopropyl alcohol and octanol
- Hydrocarbon solvents having 4 to 10 carbon atoms (e.g. n- butane, cyclohexane, toluene and xylene), and the like.
- an amide solvent having 3 to 10 carbon atoms and a sulfoxide solvent having 2 to 10 carbon atoms are preferable, and an amide solvent having 3 to 10 carbon atoms is more preferable.
- an amide solvent having 3 to 10 carbon atoms is more preferable.
- N, N-dimethylformamide or DMAC is preferable.
- the amount of the polyurethane resin to be produced is preferably 10 to 90% by weight, more preferably 20 to 80% by weight.
- a catalyst usually used in the production of the polyurethane resin can be contained as necessary for promoting the reaction.
- the catalyst include organic metal compounds [dibutyltin dilaurate, dioctyltin laurate, bismuth carboxylate, bismuth alkoxide, a chelate compound of bismuth with a compound having a dicarbonyl group, etc.], inorganic metal compounds [bismuth oxide, water, etc. Bismuth oxide, bismuth halide, etc.], amines [triethylamine, triethylenediamine, diazabicycloundecene, etc.] and combinations of two or more of these.
- the polyurethane resin composition manufactured by adding an additive is a polyurethane resin composition containing a polyurethane resin and an additive.
- a polyurethane elastic fiber obtained by spinning a polyurethane resin composition containing a polyurethane resin and an additive is also the polyurethane elastic fiber of the present invention.
- the pigment is not particularly limited, and a known organic pigment and / or inorganic pigment can be used, and is usually 0 to 5% by weight, preferably 0.1 to 3% by weight based on the weight of the polyurethane resin to be produced. %.
- organic pigments include insoluble azo pigments, soluble azo pigments, copper phthalocyanine pigments, and quinacridone pigments.
- inorganic pigments include chromates, ferrocyan compounds, metal oxides, selenium sulfide compounds, metal salts. (Sulfates, silicates, carbonates, phosphates, etc.), metal powders, carbon black and the like.
- the stabilizer is not particularly limited, and a known antioxidant and / or ultraviolet absorber can be used, and is usually 0 to 5% by weight, preferably 0.1 to 5% by weight based on the weight of the polyurethane resin to be produced. 3% by weight is blended.
- Antioxidants include phenol-based [2,6-di-t-butyl-p-cresol and butylated hydroxyanisole, etc.]; bisphenol-based [2,2′-methylenebis (4-methyl-6-t-butylphenol) Etc.]; phosphorus-based [triphenyl phosphite and diphenylisodecyl phosphite etc.] and the like.
- ultraviolet absorbers examples include benzophenone series [2,4-dihydroxybenzophenone and 2-hydroxy-4-methoxybenzophenone etc.]; benzotriazole series [2- (2′-hydroxy-5′-methylphenyl) benzotriazole etc.]; Salicylic acid type [phenyl salicylate and the like]; hindered amine type [bis (2,2,6,6-tetramethyl-4-piperidyl) sebacate and the like] and the like.
- the polyurethane elastic fiber of the present invention can be obtained by spinning it.
- the polyurethane elastic fiber of the present invention is produced by spinning a polyurethane resin or a polyurethane resin composition
- the polyurethane resin or polyurethane resin composition is used in a melt spinning method, it is in a molten state, a solvent-free pellet or a solvent-free block. Used in shape.
- the dry spinning method it is usually used as a polyurethane resin solution having a resin concentration of 30 to 80% by weight diluted with a solvent such as DMAC exemplified above.
- a polyurethane elastic fiber formed by spinning a polyurethane resin or a polyurethane resin composition can be obtained by using the polyurethane resin solution configured as described above as a spinning dope, for example, dry spinning, wet spinning, or melt spinning, and winding. it can.
- a spinning dope for example, dry spinning, wet spinning, or melt spinning, and winding.
- the spinning method is preferably dry spinning.
- the fineness, cross-sectional shape, etc. of the polyurethane elastic fiber of the present invention obtained by spinning a polyurethane resin or a polyurethane resin composition are not particularly limited.
- the cross-sectional shape of the polyurethane elastic fiber of the present invention may be circular or flat.
- the dry spinning method is not particularly limited, and spinning may be performed by appropriately selecting a spinning condition or the like suitable for desired characteristics and spinning equipment.
- the permanent set rate and stress relaxation of polyurethane elastic fibers are particularly susceptible to the speed ratio between the godet roller and the winder, and therefore are preferably determined as appropriate according to the intended use of the elastic fibers.
- the speed ratio between the godet roller and the winder is 1.10 to 1.65.
- the speed ratio between the godet roller and the winder is more preferably in the range of 1.15 or more and 1.4 or less, and 1.15 or more. The range of 1.35 or less is more preferable.
- the speed ratio of the godet roller and the winder is wound in the range of 1.25 to 1.65.
- the range of 35 or more and 1.65 or less is more preferable.
- the spinning speed is preferably 450 m / min or more from the viewpoint of improving the strength of the obtained polyurethane elastic fiber.
- the polyurethane elastic fiber of the present invention obtained as described above is used, for example, when producing a fabric together with other fibers.
- Other fibers used together with the polyurethane elastic fiber to produce the fabric include polyamide fiber and polyester fiber.
- other fibers used together with the polyurethane elastic fiber may be long fibers. More preferred.
- the polyamide fiber is a fiber represented by nylon 6 fiber or nylon 66 fiber, but is not limited thereto.
- Polyester fibers include polyethylene terephthalate, polytrimethylene terephthalate, polytetramethylene terephthalate, ester copolymers containing polytetramethylene glycol and ethylene glycol as main components as diol components, and their cationic dye-modified polyesters, etc. It is a fiber composed of polyester.
- the polyurethane elastic fiber of the present invention formed by spinning a polyurethane resin or a polyurethane resin composition is preferably a fabric composed of these polyamide fibers or polyester fibers from the viewpoint of processability and durability of the fabric.
- Synthetic fibers made of polyacrylic, polyvinyl chloride, etc., regenerated cellulose fibers made of copper ammonia rayon, viscose rayon, refined cellulose, natural fiber materials such as regenerated protein fibers, semi-synthetic fibers, cotton, silk, wool May be used in combination.
- the polyurethane elastic fiber in the fabric may be used in a bare yarn state, a core spun yarn covered with another fiber, an air covering yarn, a twisted yarn with another fiber, a twisted yarn, an interlaced yarn, etc. It may be used in the state of composite yarn.
- the fabric composed of polyurethane elastic fibers and other fibers may be a knitted fabric composed of the above-mentioned composite yarn, or in other knitting such as warp knitting, circular knitting, and weft knitting, It may be knitted.
- the fabric When the fabric is knitted fabric, it may be warp knitted or weft knitted, and examples thereof include tricot, russell, and circular knitting.
- the knitting structure may be any knitting structure such as half knitting, reverse half knitting, double atlas knitting, double denby knitting, etc., but the knitted fabric surface is composed of natural fibers other than polyurethane elastic fibers, chemical fibers, and synthetic fibers. It is preferable in terms of texture.
- the polymer end-capping agent (a3) was added to conduct an end-stop reaction for 1 hour, and the polyurethane resin solutions (P-1) to (P-9) of Examples 1 to 9 and Comparative Examples 3 and 4 Polyurethane resin solutions (R-3) and (R-4) were obtained.
- the composition of the diol (a1) having a number average molecular weight of 500 to 10,000 in Table 1 is as follows.
- PTMG1500 polyoxytetramethylene glycol having a number average molecular weight of 1,500 [“PTMG1500” manufactured by Mitsubishi Chemical Corporation]
- PTMG2000 polyoxytetramethylene glycol having a number average molecular weight of 2,000 ["PTMG2000” manufactured by Mitsubishi Chemical Corporation]
- PTMG3000 Polyoxytetramethylene glycol having a number average molecular weight of 3,000 ["PTMG3000” manufactured by Mitsubishi Chemical Corporation]
- THF / EO copolymer a copolymer diol of tetrahydrofuran and ethylene oxide having a number-average molecular weight of 2,000 THF / EO in a molar ratio of 70:30.
- THF / 3M-THF copolymer number average Copolymerized diol of tetrahydrofuran and 3-methyltetrahydrofuran having a molecular weight of 2,000 [“PTGL2000” manufactured by Hodogaya Chemical Co., Ltd.]
- -Sun Ester 24625 Dehydration condensation type polyester diol having a number average molecular weight of 2,500 [manufactured by Sanyo Chemical Industries, Ltd .: “San Ester 24625”]
- FIGS. 1 is an image of a hard segment domain in the second embodiment.
- the band represented by the color shading indicates the degree of phase shift of the cantilever, and the dark color portion in the left half corresponds to 0-50% of phase shift.
- the domain shown in this dark color is the hard segment domain of Example 2.
- FIG. 2 is an image of the hard segment domain in Comparative Example 1. The way of viewing the figure is the same as in FIG.
- the average domain diameter of the hard segment domain is shown together with the urethane group concentration and urea group concentration in the polyurethane resin, the number average molecular weight of the block (B1), the number average molecular weight of the block (B2), and the number average molecular weight of the polyurethane resin. It was shown in 2.
- the number-average molecular weight of the block (B1), the calculation method number average molecular weight of the number average molecular weight of the block (B2) and (M B1) has a number average molecular weight of 500 to 10,000 diol (a1), the number-average molecular weight was calculated using the following formula (1) of a block (B1) composed of an organic diisocyanate (b1) that reacts with a diol (a1) of 500 to 10,000.
- M a1 represents the number average molecular weight of the diol (a1) having a number average molecular weight of 500 to 10,000
- M b1 represents the number average molecular weight of the organic diisocyanate (b1)
- k is a number This represents the number of moles of the diol (a1) having an average molecular weight of 500 to 10,000
- r represents the number of moles of the organic diisocyanate (b1).
- the number average molecular weight (M B2 ) is calculated using the following formula (2) of the block (B2) composed of the chain extender (a2) and the organic diisocyanate (b2) that reacts with the chain extender (a2). Calculated.
- M a2 represents the number average molecular weight of the chain extender (a2)
- M b2 represents the number average molecular weight of the organic diisocyanate (b2)
- i represents the number of moles of the chain extender (a2).
- J represents the number of moles of the organic diisocyanate (b2).
- polyurethane elastic fibers (L-1) to (L-9) and (L′-1) to (L′-1) to (L Table 3 shows the values of the breaking elongation, breaking strength, permanent strain rate, stress relaxation, thermal softening point, heat set, chemical resistance, and fineness variation coefficient of L′-4).
- the agent solution was uniformly mixed at 3% by weight to obtain a solution. This was dry-spun at a speed ratio of 490 m / min with a speed ratio of 1.4 between the godet roller and the winder to obtain 300 g of a polyurethane elastic fiber of 33 dtex and 3 filaments.
- the tension when the polyurethane elastic fiber was fed through the roll was measured with a tensiometer. Since the fineness is directly proportional to the tension, the coefficient of variation is obtained by dividing the standard deviation of the tension by the average tension. The fineness variation coefficient is independent of the fineness, and a small fineness variation coefficient indicates that the fiber has high homogeneity.
- stretch fabrics were produced by the following method, and the appearance quality was evaluated.
- the obtained polyurethane elastic fiber was covered.
- warping and weaving were performed.
- Films (urethane sheets) obtained from the polyurethane resin solutions of Examples 1 to 9 had high heat resistance and excellent stretch properties.
- the films (urethane sheets) obtained from the polyurethane resin solutions of Comparative Examples 1 to 3 had a low heat softening point, and the films (urethane sheets) obtained from the polyurethane resin solutions of Comparative Example 4 had poor stretch properties. .
- the stretch fabric obtained from the polyurethane elastic fibers of Examples 1 to 9 had no defects and was excellent in appearance quality.
- the stretch fabrics obtained from the polyurethane elastic fibers of Comparative Examples 1 to 3 had warp-direction streaks and poor appearance quality.
- yarn breakage occurred frequently when creating the covering yarn, and it was particularly difficult to obtain the covering yarn for warp yarn.
- the polyurethane elastic fiber of the present invention is excellent in heat set property, heat resistance and stretchability, it is possible to obtain an excellent stretch fabric by combining with various fibers as well as use alone, knitting, weaving, Suitable for string processing.
- Specific applications that can be used include socks, stockings, circular knitting, tricots, swimwear, ski pants, work clothes, smoke fire clothes, golf trousers, wet suits, bras, girdles, various textile products such as gloves, fastening materials, Further examples include fastening materials for preventing sanitary items such as paper diapers, waterproofing materials, imitation baits, artificial flowers, electrical insulation materials, wiping cloths, copy cleaners, and gaskets.
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Abstract
Description
本発明の目的は、ヒートセット性が良好でありながら、耐熱性が高く、伸縮特性(残留歪率及び伸び)に優れるポリウレタン弾性繊維及びその製造方法を提供することである。
ポリウレタン樹脂は、数平均分子量が500~10,000のジオール(a1)と有機ジイソシアネート(b)と鎖伸長剤(a2)とを構成単位とする。
有機ジイソシアネート(b1)及び有機ジイソシアネート(b2)はそれぞれ1種を単独で用いても2種以上を併用してもよい。
また、有機ジイソシアネート(b1)及び有機ジイソシアネート(b2)は、同種であっても、異種であってもよい。
有機ジイソシアネート(b1)及び有機ジイソシアネート(b2)として使用できる有機ジイソシアネート(b)としては、炭素数8~26の芳香族ジイソシアネート、炭素数4~22の鎖状脂肪族ジイソシアネート、炭素数8~18の脂環式ジイソシアネート、炭素数10~18の芳香脂肪族ジイソシアネート及びこれらのジイソシアネートの変性体(カーボジイミド変性体、ウレタン変性体及びウレトジオン変性体等)等が挙げられる。
ポリウレタン樹脂の残留歪率の観点から、好ましくは1.55~2.30mmol/gであり、更に好ましくは1.75~2.20mmol/gである。
ハードセグメントドメインの平均ドメイン径が20nm未満であると耐熱性が低下する。ハードセグメントドメインの平均ドメイン径は、ポリウレタン樹脂の耐熱性と引張強度及び伸びの観点から好ましくは21~29nmであり、さらに好ましくは21.5~28.0nmである。
本発明において、ポリウレタン樹脂のハードセグメントドメインとは原子間力顕微鏡で測定される位相のズレが0~50%であるドメインであって、鎖伸長剤(a2)と、鎖伸長剤(a2)と反応する有機ジイソシアネート(b2)とから構成されるブロック(B2)である。
また、ハードセグメントドメインの平均ドメイン径とは、AFMで測定される位相のズレが0~50%であるブロック(B2)の径の大きさである。
AFMで測定される位相のズレは、ポリウレタン樹脂表面をカンチレバーでタップさせ、カンチレバーの位相のズレを測定することで測定する。樹脂が硬い部分では位相のズレが小さく、軟らかい部分では位相のズレが大きくなる。位相のズレの測定結果を画像処理すると、上記で定義されるハードセグメントドメインが一定のドメイン径として表される。このドメイン径は画像処理ソフトを使用して算出する。
上記測定方法で測定できるハードセグメントドメインの平均ドメイン径の検出限界値は5nm付近である。
AFMによるハードセグメントドメインの平均ドメイン径の測定方法は以下の条件で測定することができる。
(試料調整方法)
サンプル台に乗る大きさに、ポリウレタン樹脂をカットし、両面テープでサンプル台に固定する。
(測定条件)
測定機器:原子間力顕微鏡SPI4000 Nano Navi Station(エスアイアイ・ナノテクノロジー社製)
カンチレバー種類:OMCL-AC240TS-R3
測定ユニット:E-sweep
走査モード:位相像
(平均ドメイン径の測定方法)
原子間力顕微鏡で測定した画像を以下のソフトを使用して、画像解析する。
測定ソフト:WinROOF(MITANI CORPORATION社製)
ただし、上記測定方法で測定できるハードセグメントドメインの平均ドメイン径の検出限界値は5nm付近である。
また、鎖伸長剤(a2)と、鎖伸長剤(a2)と反応する有機ジイソシアネート(b2)とから構成されるブロック(B2)の下記計算式(2)を用いて算出される数平均分子量(MB2)が、ポリウレタン樹脂の耐熱性と引張強度及び伸びの観点から、好ましくは1,400~25,000である。
(1)数平均分子量が500~10,000のジオール(a1)のモル数と数平均分子量が500~10,000のジオール(a1)と反応する有機ジイソシアネート(b1)のモル数との比が、好ましくは数平均分子量が500~10,000のジオール(a1):有機ジイソシアネート(b1)=1:1.05~1:1.5であり、更に好ましくは数平均分子量が500~10,000のジオール(a1):有機ジイソシアネート(b1)=1:1.05~1:1.4であり、特に好ましくは数平均分子量が500~10,000のジオール(a1):有機ジイソシアネート(b1)=1:1.05~1.3である。
(2)有機ジイソシアネート(b1)のモル数と鎖伸長剤(a2)と反応する有機ジイソシアネート(b2)のモル数との合計値が、数平均分子量が500~10,000のジオール(a1)のモル数の好ましくは1.3~4.2倍であり、更に好ましくは2.0~3.4倍であり、特に好ましくは2.4~3.0倍である。
(3)数平均分子量が500~10,000のジオール(a1)のモル数と鎖伸長剤(a2)のモル数との合計値が、有機ジイソシアネート(b1)のモル数と有機ジイソシアネート(b2)のモル数との合計値と等しい。
装置:「HLC-8220GPC」[東ソー(株)製]
カラム:「Guardcolumn α」(1本)、「TSKgel α-M」(1本)[いずれも東ソー(株)製]
試料溶液:0.125重量%のジメチルホルムアミド溶液
溶液注入量:100μl
流量:1ml/分
測定温度:40℃
検出装置:屈折率検出器
基準物質:標準ポリスチレン
[1]フィルムの作製方法
ポリウレタン樹脂溶液を、離型処理したガラス板上に1.0mmの厚みに塗布し、70℃の循風乾燥機で3時間乾燥した後、ガラス板から剥がすことにより、厚さが約0.2mmのフィルムを作製する。
[2]測定方法
前記で得られたフィルムから、縦10mm×横10mmの試験片を切り出し、JIS K 7196に準じて、サンプルを室温から300℃まで5℃/分のスピードで昇温し、熱軟化点を測定する。測定にはTMA/SS6100(SII製)を使用することができる。
(1)前記数平均分子量が500~10,000のジオール(a1)のモル数と前記有機ジイソシアネート(b1)のモル数との比が、前記数平均分子量が500~10,000のジオール(a1):有機ジイソシアネート(b1)=1:1.05~1:1.5である;
(2)前記有機ジイソシアネート(b1)のモル数と前記有機ジイソシアネート(b2)のモル数との合計値が、前記数平均分子量が500~10,000のジオール(a1)のモル数の1.3~4.2倍である;
(3)前記数平均分子量が500~10,000のジオール(a1)のモル数と前記鎖伸長剤(a2)のモル数との合計値が、前記有機ジイソシアネート(b1)のモル数と前記有機ジイソシアネート(b2)のモル数との合計値と等しい。
これらのうちでは、直鎖モノオールが好ましい。具体的に、メタノール、エタノール、n-プロパノール、n-ブタノール等である。
このような、ポリウレタン樹脂と添加剤とを含有するポリウレタン樹脂組成物を紡糸してなるポリウレタン弾性繊維も、本発明のポリウレタン弾性繊維である。
酸化防止剤としては、フェノール系[2,6-ジ-t-ブチル-p-クレゾール及びブチル化ヒドロキシアニソール等];ビスフェノール系[2,2’-メチレンビス(4-メチル-6-t-ブチルフェノール)等];リン系[トリフェニルフォスファイト及びジフェニルイソデシルフォスファイト等]等が挙げられる。
ポリウレタン樹脂又はポリウレタン樹脂組成物を紡糸して本発明のポリウレタン弾性繊維を製造する際、ポリウレタン樹脂又はポリウレタン樹脂組成物が溶融紡糸法で使用される場合は溶融状態、無溶剤ペレット又は無溶剤ブロックの形状で使用される。一方、乾式紡糸法で使用される場合は先に例示したDMAC等の溶剤で希釈した通常30~80重量%の樹脂濃度のポリウレタン樹脂溶液として使用される。
そして、乾式紡糸方式についても特に限定されるものではなく、所望する特性や紡糸設備に見合った紡糸条件等を適宜選択して紡糸すればよい。
たとえば、ポリウレタン弾性繊維の永久歪率と応力緩和は、特にゴデローラーと巻取機の速度比の影響を受けやすいので、弾性繊維の使用目的に応じて適宜決定されるのが好ましい。すなわち、所望の永久歪率と応力緩和を有するポリウレタン弾性繊維を得る観点から、ゴデローラーと巻取機の速度比は1.10以上1.65以下の範囲として巻き取ることが好ましい。そして、特に高い永久歪率と、低い応力緩和を有するポリウレタン弾性繊維を得る際には、ゴデローラーと巻取機の速度比は1.15以上1.4以下の範囲がより好ましく、1.15以上1.35以下の範囲がさらに好ましい。
また、紡糸速度は、得られるポリウレタン弾性繊維の強度を向上させる観点から、450m/分以上であることが好ましい。
以上のようにして得られた本発明のポリウレタン弾性繊維は、たとえば他の繊維とともに布帛を製造する際に用いられる。布帛を製造するために、ポリウレタン弾性繊維とともに用いられる他の繊維としては、ポリアミド繊維やポリエステル繊維等が挙げられる。
さらには、本発明のポリウレタン弾性繊維の高いヒートセット性と低い繊度変動係数を反映した外観品位に優れた布帛を製造する観点から、ポリウレタン弾性繊維とともに用いられる他の繊維は長繊維であることがより好ましい。
また、布帛中のポリウレタン弾性繊維は、裸糸の状態で用いてもよいし、他の繊維によってカバーリングしたコアスパンヤーン、エアーカバリングヤーン、他の繊維との合撚糸、交撚糸、インターレース糸等の複合糸の状態で用いてもよい。また、ポリウレタン弾性繊維と他の繊維とから構成される布帛は、上記複合糸から構成される編織物でもよいし、もしくは、経編み、丸編み、緯編み等の製編において、他の繊維と交編することでもよい。
表1に記載の処方に基づいて、撹拌装置及び温度制御装置付きの反応容器に数平均分子量が500~10,000のジオール(a1)、有機ジイソシアネート(b1)及び有機溶剤を投入し、窒素雰囲気下、70℃で7時間反応させてウレタンプレポリマー(p)を得た。続いて、鎖伸長剤(a2)及び有機ジイソシアネート(b2)を投入、窒素雰囲気下、70℃で反応させて反応混合物中のイソシアネート基の重量の割合が表2又は表3に記載の値になった時点でポリマー末端封止剤(a3)を加えて1時間末端停止反応を行い、実施例1~9のポリウレタン樹脂溶液(P-1)~(P-9)、及び比較例3、4のポリウレタン樹脂溶液(R-3)、(R-4)を得た。
表1に記載の処方に基づいて、撹拌装置及び温度制御装置付きの反応容器に数平均分子量が500~10,000のジオール(a1)、鎖伸長剤(a2)、有機ジイソシアネート(b1)及び有機ジイソシアネート(b2)(表1には投入量の合計値を記載)及び有機溶剤を投入し、乾燥窒素雰囲気下、70℃で反応させて反応混合物中のイソシアネート基の重量の割合が表3に記載の値になった時点でポリマー末端封止剤(a3)を加えて1時間末端停止反応を行い、比較例1及び比較例2のポリウレタン樹脂溶液(R-1)及び(R-2)を得た。
・PTMG1500:数平均分子量が1,500のポリオキシテトラメチレングリコール[三菱化学(株)製「PTMG1500」]
・PTMG2000:数平均分子量が2,000のポリオキシテトラメチレングリコール[三菱化学(株)製「PTMG2000」]
・PTMG3000:数平均分子量が3,000のポリオキシテトラメチレングリコール[三菱化学(株)製「PTMG3000」]
・THF/EO共重合体:数平均分子量が2,000のTHFとEOのモル比が70:30である、テトラヒドロフランとエチレンオキサイドとの共重合ジオール
・THF/3M-THF共重合体:数平均分子量が2,000である、テトラヒドロフランと3-メチルテトラヒドロフランとの共重合ジオール[保土谷化学(株)製「PTGL2000」]
・サンエスター 24625:数平均分子量が2,500の脱水縮合型ポリエステルジオール[三洋化成工業(株)製:「サンエスター24625」]
ポリウレタン樹脂溶液を、離型処理したガラス板上に1.0mmの厚みに塗布し、70℃の循風乾燥機で3時間乾燥した後、ガラス板から剥がすことにより、厚さが約0.2mmのフィルムを作製した。
前記で得られたフィルムを温度25℃、湿度65%RHに調整した室内に1日間静置した後、JIS K 6251に準じて、切断時引張強さ及び切断時伸びを測定した。これらの値が大きい程、弾性繊維としての性質に優れている。尚、ダンベル状試験片の平行部分の厚さは200μm、平行部分の幅は5mm、初期の標線間距離は20mmである。
前記で得られたフィルムから、縦100mm×横5mmの短冊状の試験片を切り出して標線間距離が50mmとなるように標線をつけた。この試験片をインストロン型引張り試験機(島津製作所製オートグラフ)のチャックにセットして、25℃の雰囲気下、500mm/分の一定速度で標線間の距離が300%になるまで伸長後、直ちに同じ速度で伸長前のチャック間の距離まで戻す操作を行った。
前記操作後の標線間の距離(D1)を測定してこの値と試験前の標線間の距離(D0=50mm)を用いて下式から残留歪率(%)を求めた。
残留歪率(%)={(D1-D0)/D0}×100
前記で得られたフィルムから、縦10mm×横10mmの試験片を切り出し、JIS K 7196に準じて、サンプルを室温から300℃まで5℃/分のスピードで昇温し、熱軟化点を測定した。測定にはTMA/SS6100(SII製)を使用した。
熱軟化点が高い程、ポリウレタン樹脂の耐熱性が良好である。
(試料調整方法)
サンプル台に乗る大きさに、ポリウレタン樹脂をカットし、両面テープでサンプル台に固定した。
(測定条件)
測定機器:原子間力顕微鏡SPI4000 Nano Navi Station(エスアイアイ・ナノテクノロジー社製)
カンチレバー種類:OMCL-AC240TS-R3
測定ユニット:E-sweep
走査モード:位相像
(平均ドメイン径の測定方法)
原子間力顕微鏡で測定した画像を以下のソフトを使用して、画像解析した。
測定ソフト:WinROOF(MITANI CORPORATION社製)
実施例2及び比較例1のハードセグメントドメインの画像を図1及び図2に示す。
図1は、実施例2におけるハードセグメントドメインの画像である。
図1の下部、色の濃淡で表された帯はカンチレバーの位相のずれの程度を示し、左半分の濃い色の部分が位相のずれ0~50%に対応する。この濃い色で示されたドメインが実施例2のハードセグメントドメインである。
図2は、比較例1におけるハードセグメントドメインの画像である。図の見方は図1と同じである。
数平均分子量が500~10,000のジオール(a1)及び鎖伸長剤(a2)の合計モル比と有機ジイソシアネート(b)の合計モル比の理論計算から算出した。
ウレタン基の濃度とウレア基の濃度の合計値を表2に示した。
数平均分子量(MB1)は数平均分子量が500~10,000のジオール(a1)と、数平均分子量が500~10,000のジオール(a1)と反応する有機ジイソシアネート(b1)とから構成されるブロック(B1)の下記計算式(1)を用いて算出した。
数平均分子量(MB2)は、鎖伸長剤(a2)と、鎖伸長剤(a2)と反応する有機ジイソシアネート(b2)とから構成されるブロック(B2)の下記計算式(2)を用いて算出した。
ブロック(B1)の数平均分子量、ブロック(B2)の数平均分子量を表2に示した。
ポリウレタン樹脂の数平均分子量は、ゲルパーミエーションクロマトグラフィーにより、以下の条件で測定した。
装置:「HLC-8220GPC」[東ソー(株)製]
カラム:「Guardcolumn α」(1本)、「TSKgel α-M」(1本)[いずれも東ソー(株)製]
試料溶液:0.125重量%のジメチルホルムアミド溶液
溶液注入量:100μl
流量:1ml/分
測定温度:40℃
検出装置:屈折率検出器
基準物質:標準ポリスチレン
ポリウレタン樹脂の数平均分子量を表2に示した。
米国特許第3555115号明細書に記載されているt-ブチルジエタノールアミンとメチレン-ビス-(4-シクロヘキシルイソシアネ-ト)の反応によって生成せしめたポリウレタンと米国特許第3553290号に記載されているp-クレゾ-ルとジビニルベンゼンの縮合重合体の2対1重量比の混合物のDMAC溶液(35重量%)を調製し、酸化防止剤溶液(35重量%)とした。実施例1~9及び比較例1~4で得られたポリウレタン樹脂溶液[(P-1)~(P-9)及び(R-1)~(R-4)]を97重量%、酸化防止剤溶液を3重量%で均一に混合し、溶液とした。これをゴデローラーと巻取機の速度比1.4として490m/分のスピードで乾式紡糸することにより、33デシテックス、3フィラメントであるポリウレタン弾性繊維の300g巻糸体を得た。
破断強度、応力緩和、永久歪率、破断伸度は、試料糸をインストロン4502型引張試験機にて、引張テストをすることにより測定した。
これらは下記により定義される。5cm(L1)の試料を50cm/分の引張速度で300%伸長を5回繰返した。このときの応力を(G1)とした。
次に300%伸長を30秒間保持した。30秒間保持後の応力を(G2)とした。次に伸長を回復せしめ応力が0になった際の試料糸の長さを(L2)とした。さらに6回目に試料糸が切断するまで伸長した。この破断時の応力を(G3)、破断時の試料糸の長さを(L3)とした。
以下、前記特性は下記式により与えられる。
破断強度 =(G3)
応力緩和=100×((G1)-(G2))/(G1)
永久歪率=100×((L2)-(L1))/(L1)
破断伸度 =100×((L3)-(L1))/(L1)
レオメトリック社製動的弾性率測定機RSAIIを用い、昇温速度10℃/分で、動的貯蔵弾性率E’の温度分散を測定した。熱軟化点は、E’曲線が80℃以上130℃以下のプラト領域での接線と、160℃以上にてE’が熱軟化により降下するE’曲線の接線との交点から求めた。なお、E’は対数軸、温度は線形軸を用いた。
図3には、実施例1及び比較例1における弾性繊維の熱軟化点の測定曲線を、弾性繊維の評価図として示した。
試料糸(長さ=L5)を100%伸長した(長さ=2×(L5))。この長さのまま160℃で1分間処理した。さらに同じ長さで、1日室温で放置した。次に、試料糸の伸長状態をはずし、その長さ(L6)を測定した。
ヒートセット性=100×((L6)-(L5))/(L5)
ヒートセット性は値が高いほうが良好であることを示している。
糸を100%伸長状態で固定し、次の3種の暴露処理を実施した。まず、オレイン酸のヘキサン溶液(5重量%)に1時間浸積処理し、次に調製した次亜塩素酸溶液(塩素濃度500ppm)に2時間浸積処理し、次に2時間UV暴露を行った。UV暴露処理は、機器としてスガ試験機社製のカーボンアーク型フェードメーターを用い、63℃、60%RHの温湿度で実施した。この暴露処理を合計2回実施した後、糸をフリーで24時間、室温で放置し、前記と同じ方法で破断強度(G4)を測定した。未処理糸の破断強度(G3)に対する、処理後の破断強度(G4)の割合(保持率)を耐薬品性とした。
耐薬品性(%)=100×(G4)/(G3)
ポリウレタン弾性繊維を巻き上げたパッケージ(巻糸体)の表面で、最初の50メートルのポリウレタン弾性繊維を除去することで、ハンドリングから生ずる損傷が原因の不正確さが入らないようにする。次いで、その巻糸体から回転引取装置を用いて、ポリウレタン弾性繊維を130秒間引き出して、圧電セラミックピンを備えた張力計を通過させる。次に、引取りロールの円周を供給ロールの円周よりも50%大きくして、供給ロールと引取りロールの回転速度を同じにした結果、そのポリウレタン弾性繊維は、張力計を通過する際に50%の伸びに延伸される。張力計により、ポリウレタン弾性繊維がロールを通って供給される際の張力を測定した。繊度は張力と直接的な比例関係にあるので、張力の標準偏差を平均張力で割り算して変動係数を得る。繊度変動係数は、繊度とは無関係であって、繊度変動係数が小さいということは、繊維の均質性が高いということを示している。
得られたポリウレタン弾性繊維のカバーリング加工を行った。カバーリング用糸としてナイロン長繊維168dtex-24filを使用し、カバーリング機を用いてヨリ数=450t/m、ドラフト=3.0の条件で加工してヨコ糸用カバーリング糸を作製した。また、同様に、カバーリング用糸として同ナイロン長繊維を使用し、カバーリング機を用いてヨリ数700t/m、ドラフト=3.5の条件で加工してタテ糸用カバーリング糸を作製した。
次に、整経・製織を行った。タテ糸の5100本(荒巻き整経1100本)を糊付け整経し、レピアー織機を用いて2/1綾組織で製織した。
次に、染色加工を行った。製織で得た生機を、常法に従い精練加工、中間セット(175℃)、エンボス加工(180℃)、染色加工(98℃)、乾燥、仕上げ剤処理、仕上げセット(175℃、布速20m/min、セットゾーン24m)を順次行った。
そして外観品位の評価を目視により行った。評価基準は以下の通りである。
○:ストレッチ織物は欠点がない。
△:ストレッチ織物は経方向のスジが発生した。
×:カバーリング糸作成時に糸切れが多発した。
その使用可能な具体的用途としては、ソックス、ストッキング、丸編、トリコット、水着、スキーズボン、作業服、煙火服、ゴルフズボン、ウエットスーツ、ブラジャー、ガードル、手袋等の各種繊維製品、締め付け材料、さらには、紙おしめなどサニタリー品の漏れ防止用締め付け材料、防水資材の締め付け材料、似せ餌、造花、電気絶縁材、ワイピングクロス、コピークリーナー、ガスケットなどが挙げられる。
Claims (10)
- 数平均分子量が500~10,000のジオール(a1)と有機ジイソシアネート(b)と鎖伸長剤(a2)とを構成単位とするポリウレタン樹脂であって、ウレタン基の濃度とウレア基の濃度の合計値が、ポリウレタン樹脂の重量に基づいて、1.25~2.50mmol/gであり、原子間力顕微鏡で測定されるポリウレタン樹脂のハードセグメントドメインの平均ドメイン径が20~30nmであるポリウレタン樹脂を紡糸してなるポリウレタン弾性繊維。
- 前記数平均分子量が500~10,000のジオール(a1)と、前記数平均分子量が500~10,000のジオール(a1)と反応する有機ジイソシアネート(b1)とから構成されるブロック(B1)の下記計算式(1)を用いて算出される数平均分子量(MB1)が4,000~80,000であり、
前記鎖伸長剤(a2)と、前記鎖伸長剤(a2)と反応する有機ジイソシアネート(b2)とから構成されるブロック(B2)の下記計算式(2)を用いて算出される数平均分子量(MB2)が1,400~25,000であるポリウレタン樹脂を紡糸してなる請求項1に記載のポリウレタン弾性繊維。
- 以下の(1)~(3)を満たすポリウレタン樹脂を紡糸してなる請求項1又は2に記載のポリウレタン弾性繊維:
(1)前記数平均分子量が500~10,000のジオール(a1)のモル数と前記数平均分子量が500~10,000のジオール(a1)と反応する有機ジイソシアネート(b1)のモル数との比が、数平均分子量が500~10,000のジオール(a1):有機ジイソシアネート(b1)=1:1.05~1:1.5である;
(2)前記有機ジイソシアネート(b1)のモル数と前記鎖伸長剤(a2)と反応する有機ジイソシアネート(b2)のモル数との合計値が、前記数平均分子量が500~10,000のジオール(a1)のモル数の1.3~4.2倍である;
(3)前記数平均分子量が500~10,000のジオール(a1)のモル数と前記鎖伸長剤(a2)のモル数との合計値が、前記有機ジイソシアネート(b1)のモル数と前記有機ジイソシアネート(b2)のモル数との合計値と等しい。 - 前記数平均分子量が500~10,000のジオール(a1)が、ポリオキシエチレングリコール、ポリ(オキシ-1,2-プロピレン)グリコール、ポリオキシテトラメチレングリコール、テトラヒドロフランとエチレンオキサイドとの共重合ジオール及びテトラヒドロフランと3-メチルテトラヒドロフランとの共重合ジオールからなる群から選ばれる少なくとも1種のジオールであるポリウレタン樹脂を紡糸してなる請求項1~3のいずれかに記載のポリウレタン弾性繊維。
- 前記有機ジイソシアネート(b)が、炭素数8~26の芳香族ジイソシアネートであるポリウレタン樹脂を紡糸してなる請求項1~4のいずれかに記載のポリウレタン弾性繊維。
- 前記鎖伸長剤(a2)が、化学式量又は数平均分子量が500未満の低分子ジオールであるポリウレタン樹脂を紡糸してなる請求項1~5のいずれかに記載のポリウレタン弾性繊維。
- 数平均分子量が20,000~200,000であるポリウレタン樹脂を紡糸してなる請求項1~6のいずれかに記載のポリウレタン弾性繊維。
- 熱軟化点が180~280℃であるポリウレタン樹脂を紡糸してなる請求項1~7のいずれかに記載のポリウレタン弾性繊維。
- 請求項1~8のいずれかに記載のポリウレタン樹脂と添加剤とを含有するポリウレタン樹脂組成物を紡糸してなるポリウレタン弾性繊維。
- 請求項1~9のいずれかに記載のポリウレタン弾性繊維の製造方法であって、
紡糸方法が乾式紡糸であることを特徴とするポリウレタン弾性繊維の製造方法。
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