Classifications

• • 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
  • D01F6/88—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
  • D01F6/90—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyamides
• • 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
  • D01F6/60—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides
  • D01F6/605—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides from aromatic polyamides
• • 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
  • D01F1/00—General methods for the manufacture of artificial filaments or the like
  • D01F1/02—Addition of substances to the spinning solution or to the melt
  • D01F1/04—Pigments

Definitions

• This invention relates to colored, high strength, high modulus p-aramid fibers and a process for preparing them.
• High strength, high modulus p-aramid fibers are known from U.S. Patent 3,869,429 (Blades). These fibers are extremely difficult to dye. Some improvement in dyeability can be obtained by mechanically crimping these fibers while wet but dye penetration is limited to the crimp nodes of the individual filaments and the mechanical properties of the fibers are degraded.
• This invention provides colored high strength, high modulus p-aramid fibers having no colorant particles or agglomerates with a diameter of larger than 0.01 microns.
• the fibers are colored with a completely organic pigment.
• the organic pigment is at least one selected from the group consisting of (1) monoazo and disazo pigments, (2) anthanthrone pigments, (3) indanthrone pigments, (4) pyranthrone pigments, (5) vilanthrone pigments, (6) flavanthrone pigments, (7) quinacridone pigments, (8) dioxazine pigments, (9) indigoid and thioindigoid pigments, and (10) isoindolinone pigments.
• Monoazo and disazo pigments have the structure wherein R1, R2 and R3 are chloro, nitro, methyl, methoxy, or hydrogen, R4 is hydroxy, and R7 is wherein R5 and R6 are hydrogen, methyl, or chloro.
• Anthanthrone pigments have the structure wherein R1, R2 and R3 are -H, -Cl, or -Br.
• Indanthrone pigments have the structure wherein R1, R2 and R3 are -H, -OH, -Cl, -Br, -NH2, or fused aromatic groups, R4 and R5 are -H, -CH3, or -C2H5.
• Pyranthrone pigments have the structure wherein R1, R2 and R3 are -H, -Cl, or -Br.
• Vilanthrone pigments have the structure wherein R1, R2, and R3 are -H, -Cl, -Br, -OCH3, -OC2H5, , or a fused aromatic group.
• Flavanthrone pigments having the structure wherein R1, R2 and R3 are -H, -Cl, -Br, -OH, an aromatic group or a fused aromatic group.
• Dioxazine pigments have the structure wherein R1 and R2 are -H or -Cl and R3 and R4 are -CH3 or -C2H5.
• Indigoid pigments have the structure wherein R1, R2, R3, R4, R5 and R6 are -H, -Cl, -Br, -CH3 or -NH2 and thioindigoid pigments have the structure wherein R1, R2, R3, R4, R5 and R6 are -H, -Cl, -NH2, -OC2H5, -SC2H5, -CH3, -OCH3, phenyl or fused aromatic groups.
• Isoindolinone pigments have the structure
• the preferred monoazo pigment is Colour Index Pigment Red 3.
• the preferred disazo pigment is Colour Index Pigment Red 242.
• the preferred anthanthrone pigment is Colour Index Pigment Red 168.
• the preferred indanthrone pigment is Colour Index Pigment Blue 60.
• the preferred pyranthrone pigment is Colour Index Pigment Orange 40.
• the preferred vilanthrone pigment is Colour Index Pigment Blue 65.
• the preferred flavanthrone pigment is Colour Index Yellow 24.
• the preferred quinacridone pigment is Colour Index Pigment Red 122.
• the preferred dioxazine pigment is Colour Index Pigment Violet 23.
• the preferred indigoid and thioindigoid pigments are Colour Index Pigment Red 88 and Colour Index Pigment Red 86, respectively.
• the most preferred isoindolinone pigment is Colour Index Pigment Yellow 173.
• organic pigments of the foregoing structures are those pigments named in the Colour Index published by the Society of Dyers and Colourists.
• the colored high strength, high modulus p-aramid fibers of this invention have no visible colorant particles or agglomerates when viewed under an electron microscope at a magnification of 9000 X. Thus, any particles or agglomerates must be smaller than 0.01 micron in diameter.
• the fibers have a yarn tenacity of at least 18 gpd (15.9 dN/tex) and an initial modulus of at least 400 gpd (354 dN/tex). Filament tenacity is often higher, by as much as 3 gpd (2.6 dN/tex).
• This invention also provides a process for the preparation of the colored, high strength, high modulus p-aramid fibers comprising the steps of (1) agitating a mixture of sulfuric acid soluble organic pigment in an amount sufficient to provide the desired color intensity and sufficient p-aramid polymer having an inherent viscosity of at least 4 to provide a polymer solution having a concentration of at least 18% by weight in cold concentrated sulfuric acid having a concentration of at least 98%, (2) heating the mixture with continued agitation to a temperature of 80 to 105°C whereby a uniform solution is obtained, (3) extruding the solution through a spinneret and then drawing it through a non-coagulating fluid layer wherein the extrudate is stretched 3 to 10 times its original, extruded length, (4) passing the extrudate into an aqueous coagulation bath having a temperature of -5 to 25°C , and (5) washing the newly formed filaments with water and/or dilute alkali.
• the para-oriented aromatic polyamides (p-aramids) useful in the present invention are those described in U.S. Patent 3,869,429 in which rigid radicals are linked into polymer chains by amide groups.
• the chain-extending bonds of the rigid radicals are either coaxial or parallel and oppositely directed.
• the rigid radicals may be single-ring radicals, multi-ring radicals in which the chain-extending bonds are para-oriented, fused ring radicals or heterocyclic radicals.
• Preferred rigid radicals are 1,4-phenylene, 2,6-naphthalene, 1,5-naphthalene, 4,4′-biphenylene, trans-1,4-­cyclohexylene, trans-trans-4,4′-bicyclohexylene, 1,4-pyridylene and 1,4-phenylene groups linked by trans-vinylene, ethynylene, azo or azoxy groups.
• the polyamides may be substituted with simple groups such as chloro- and methyl groups. Both homopolymers and copolymers are suitable as long as the rigid radicals are ad defined above. Up to 5 mol percent of non-conforming radicals may be included.
• the polyamides may be prepared by reaction of a suitable aromatic acid halide with a suitable aromatic diamine in a non-reactive amide solvent which may contain solubilizing salts such as LiCl and CaCl2.
• the polyamide should have an inherent viscosity of at least 4.
• high strength is meant a yarn or filament tenacity of at least 18 gpd (15.9 dN/tex).
• high modulus is meant having a yarn or filament initial modulus of at least 400 gpd (354 dN/tex).
• the single fibers of the present invention have a denier of 0.5 to 15.
• the purely organic pigments suitable for use in the present invention are soluble in sulfuric acid having a concentration of at least 98%, but are insoluble in water or organic solvents and do not degrade appreciably in 98% sulfuric acid at 95°C when held at that temperature for three hours. Indications of pigment degradation include change of colour in the final fiber, bleeding of the pigment into the coagulation bath and precipitation of the pigment from the polymer solution.
• the amount of organic pigment will depend on the tint desired and the type of organic pigment used but in general 0.01 to 6% by weight pigment in the fibers provides useful results. Suitable organic pigments may show a change in color when dissolved in concentrated sulfuric acid but will return to the original color on coagulation and washing of the fibers.
• the chemical structures of some preferred organic pigments have been defined above. Organic pigments with an inorganic component are generally unsatisfactory.
• sufficient p-aramid polymer having an inherent viscosity of at least 4.0 is mixed with cold sulfuric acid having a concentration of at least 98% and the desired amount of sulfuric acid soluble organic pigment to provide, when heated, a dope having a p-aramid concentration of at least 18% by weight.
• the dope is heated to 80-105°C with stirring and degassed.
• the hold-up time of the dope may be 1-3 hours in a commercial spinning process.
• the dope is extruded through a spinneret having orifices with a diameter of 0.025 to 0.125 mm through a layer of non-coagulating fluid, usually air, into an aqueous coagulating bath having a temperature of -5 to 25°C.
• the air gap may be from 0.5 to 2.5 cm but preferably is about 0.7 cm.
• the yarn is further washed with dilute alkali and/or water and wound up on bobbins.
• the fibers are of the same color as the original organic pigment added. No color is lost to the aqueous coagulation bath.
• denier This is usually calculated as denier, that is, the weight in grams of a 9000-meter length of yarn. Multiplication of denier by 1.1111 yields linear density in dtex.
• Tenacity is reported as breaking stress divided by linear density. Modulus is reported as the slope of the initial stress/strain curve converted to the same units as tenacity. Elongation is the percent increase in length at break. Both tenacity and modulus are first computed in g/denier units which, when multiplied by 0.8838, yield dN/tex units). Each reported measurement is the average of 10 breaks.
• Tensile properties for yarns are measured at 24°C and 55% relative humidity after conditioning under the test conditions for a minimum of 14 hours. Before testing, each yarn is twisted to a 1.1 twist multiplier (for example, nominal 1500 denier yarn is twisted about 0.8 turns/cm). Each twisted specimen has a test length of 25.4 cm and is elongated 50% per minute (based on the original unstretched length) using a typical recording stress/strain device.
• Tensile properties for filaments are measured at 21°C and 65% relative humidity after conditioning under test conditions for a minimum of 14 hours.
• a single filament is mounted to provide a test length of 2.54 cm using 3B Pneumatic Action Clamps with neoprene faces (available from Instron Corp.). Rate of elongation is 10% per min.
• Tensile properties of filaments are normally at least as large as the properties for yarns, and tenacity values often are larger by as much as 3 gpd (2.6 dN/tex).
• the fibers of this invention have no colorant particles or agglomerates with a diameter larger than 0.01 micron. All colorant is present in the fibers as particles having a diameter less than 0.01 micron.
• the fiber is imbedded in an epoxy resin, cut using an ultra-microtome along a direction at 45 degrees to the fiber axis into a 2000 Angstrom thick specimen, and examined on a cut surface using an electron microscope at 9000 x total magnification. Visible particles have diameters of at least 0.01 micron. The absence of visible particles confirms suitability for this invention.
• Sulfuric acid having a concentration of 100.1% (24,235 g) was cooled in a reaction vessel to -5°C by a circulating -25°C glycol jacket.
• Poly(p-phenylene terephthalamide) having an inherent viscosity of 6.3 (5,889 g) and Sandorin Blue RL (Pigment Blue 60) powder (176.7 g) were added to the reaction vessel.
• the mixture was stirred while the temperature was gradually increased to 85°C.
• the mixture was stirred for two hours at 85°C under a reduced pressure of 25 mm (Hg) to eliminate air bubbles.
• the resulting dope was extruded through a filter pack and then through a 267 hole spinneret having spinning capillaries 0.063 mm in diameter, and finally through an air gap of 0.7 cm length into an aqueous coagulating bath at 5°C.
• the extruded dope was stretched 6.3 X in the air gap.
• the resulting fibers were further washed with dilute aqueous alkali and water, dried on a roll at 180°C and wound up at 732 m/min. No colour was lost to the coagulating bath. Pigment level was 3% based on weight of fiber.
• Yarn tenacity/elongation/modulus/filament linear density was 21.0 gpd/2.63%/764 gpd/1.5 den (18.1 dN/tex/2.63%/675 dN/tex/1.7 dtex).
• Corresponding filament properties were 21.0 gpd/3.98%/612 gpd/1.5 den (18.6 dN/tex/3.98%/541 dN/tex/1.7 dtex).
• An identical spin except without added organic pigment resulted in yarns having tenacity/elongation/modulus of 21.5 gpd/2.81%/680 gpd (19.0 dN/tex/2.81%/601 dN/tex).
• a fiber cross-section of the pigment-containing fibers showed no visible particles or agglomerates when viewed under an electron microscope at a magnification of 9000 X. From this it can be concluded that all pigment particles were smaller than 0.01 micron in diameter.
• Example 1 was repeated except for the amounts and kinds of organic pigments used and windup speed and denier changes as noted. The results are summarized in Tables 1 and 2.
• filament properties were also determined on that product after crimping.
• a 0.75 inch (1.9 cm) stuffer box crimper was used with a feed rope of 84,000 denier (93,300 dtex) fed at 175 ypm (160 mpm) using steam in the stuffer box at 12 psig (83 kPa gage) and a clapper-gate pressure of 20 psig (138 kPa gage).
• the T/E/M results were 17.0 gpd/5.19%/270 gpd (15.0 dN/tex/5.19%/239 dN/tex).
• Fiber cross-sections of the colored fibers showed no visible particles or agglomerates when viewed under an electron microscope at a magnification of 9000 X.
• Example 1 was repeated except for the amounts and kinds of pigment used. The results are summarized in the Tables 1 and 2, using C-1 to C-3 for identification/
• Pigment Black 7 is carbon black which is insoluble in concentrated sulfuric acid.
• Pigment White 3 is titanium dioxide which is also insoluble in concentrated sulfuric acid.
• Pigment Green 7 is a copper-phthalocyanine pigment which is degraded by concentrated sulfuric acid with precipitation of copper sulfate. Some vat dyes are soluble in concentrated sulfuric acid but bleed out in the coagulation bath, produce agglomerates of greater than 0.01 micron in diameter and/or provide low tenacity fibers.
• Vat Orange 2 and Vat Black 27 were found to be chemically unstable in sulfuric acid.

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• Engineering & Computer Science (AREA)
• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Textile Engineering (AREA)
• Manufacturing & Machinery (AREA)
• Artificial Filaments (AREA)
• Developing Agents For Electrophotography (AREA)
• Coloring (AREA)
• Compositions Of Macromolecular Compounds (AREA)

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• 1988
  • 1988-06-14 JP JP63144894A patent/JPS6414317A/ja active Pending
  • 1988-06-16 EP EP88109614A patent/EP0295672A3/de not_active Withdrawn
  • 1988-06-16 BR BR8802953A patent/BR8802953A/pt unknown
  • 1988-06-17 AR AR88311154A patent/AR244356A1/es active
  • 1988-06-17 MX MX011962A patent/MX169241B/es unknown
  • 1988-06-17 KR KR1019880007297A patent/KR890000701A/ko not_active Withdrawn
  • 1988-06-17 CN CN88103623A patent/CN1031736A/zh active Pending

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