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
  • D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
  • D01F8/04—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
  • D01F8/12—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyamide as constituent
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10S264/00—Plastic and nonmetallic article shaping or treating: processes
  • Y10S264/26—Composite fibers made of two or more materials
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10S57/00—Textiles: spinning, twisting, and twining
  • Y10S57/905—Bicomponent material
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
  • Y10T428/2913—Rod, strand, filament or fiber
  • Y10T428/2922—Nonlinear [e.g., crimped, coiled, etc.]
  • Y10T428/2924—Composite
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
  • Y10T428/2913—Rod, strand, filament or fiber
  • Y10T428/2929—Bicomponent, conjugate, composite or collateral fibers or filaments [i.e., coextruded sheath-core or side-by-side type]
  • Y10T428/2931—Fibers or filaments nonconcentric [e.g., side-by-side or eccentric, etc.]
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T442/00—Fabric [woven, knitted, or nonwoven textile or cloth, etc.]
  • Y10T442/40—Knit fabric [i.e., knit strand or strip material]
  • Y10T442/444—Strand is a monofilament composed of two or more polymeric materials in physically distinct relationship [e.g., sheath-core, side-by-side, islands-in-sea, fibrils-in-matrix, etc.] or composed of physical blend of chemically different polymeric materials or a physical blend of a polymeric material and a filler material

Definitions

• Composite hosiery filaments have been produced as disclosed by Olson in U. S. Pat. No. 3,558,760 which have the ability to crimp under restraint sufficiently to distort the stitches in hosiery fabric, so that the fabric has more stretch than a conventional hosiery fabric. Although those composite filaments have produced good stretch hose, further improvements in crimpability under fabric restraint are desirable, particularly in the production of miniature stretch hose.
• the present invention provides composite polyamide filaments having an improved balance of crimp characteristics and strength.
• the invention also provides composite filaments which develop little or no crimp when removed from the package but which develop a substantial tendency to crimp in a knitting operation and a still greater tendency to crimp on subsequent treatment at elevated temperatures. 7
• the filament of this invention has two or more distinct, continuous, filament components in adherent, eccentric arrangement along the length of the filament.
• the polyamide of one component consists essentially of poly (hexamethylenedodecanedioamide).
• the polyamide of a second component consists essentially of N- alkyl substituted poly (hexamethylenedodecanedioamide) wherein the alkyl substituent has two to four carbon atoms and 25 to 50 percentof polyamide nitrogen atoms have alkyl substituents.
• this latter polyamide is a copolymer wherein to 50 percent of the polymer units are hexamethylenedodecanedioamide and 25 to 50 percent of the polymer units are N,- N'-dialkyl-hexamethylenedodecanedioamide.
• Preferred N-alkyl substituents are ethyl and n-butyl.
• the polyamide components are readily prepared, melt-spun into composite filaments and drawn to provide filaments having a tenacity of at least 6 grams per denier at break.
• the components may be arranged in a side-by-side relationship to provide a helical crimp with a crimp elongation of at least 40 percent when the composite filament is subjected to atmospheric steam while it is under 1.2 milligrams per denier load. Similar results can be obtained with sheathcore arrangements of the components.
• the filaments of this invention are prepared by extruding the homopolyamide and copolyamide in either a side-byside or a sheath-core relationship to form a filament (or two or more filaments as a yarn), quenching and drawing the filament in the conventional manner, passing the drawn filament through a heating zone under low tension to develop crimp and thereafter stretching the filament to remove crimp.
• a temperature in the heating zone of at least 1 15 C. is preferred for the desired crimp characteristics. The temperature required will, of course, depend on the length of the heating zone and the speed of the filament passing through the zone.
• the preferred technique for reducing tension in the heating zone and then removing crimp is by passage of the precrimped filament over a series of snubbing pins in its advance away from the draw roll, a suitable heating means such as an air jet being interposed between the draw roll and snubbing pins, as shown, for example, in FIGS. l and 4 of Olson U. S. Pat. No. 3,558,760.
• a suitable heating means such as an air jet being interposed between the draw roll and snubbing pins, as shown, for example, in FIGS. l and 4 of Olson U. S. Pat. No. 3,558,760.
• the filament passes around a power-driven roll, rotating at a lower peripheral speed than the draw roll to permit the filament to retract between the rolls,
• the degree of retraction permissible will depend on the amount of shrinkage, independent of crimping, which occurs between the two rolls. This, in turn, will depend to a considerable extent on the temperature in the heating zone.
• the two components are usually present in approximately equal amounts by weight of the filaments; however, the ratio may be varied as required to achieve the desired properties.
• sheath-core filaments it may be desirable to employ a somewhat larger percentage of the N-substituted polyamide component in the core.
• the core In producing sheath-core filaments, the core should be highly eccentric in order to develop the required retractive force on crimping. This means that part of the sheath will be very thin, i.e.; the minimum thickness of the sheath will range from 5 percent of the filament diameter to 0.1 percent or less.
• Either or both of the components may contain any of the various additives commonly employed in the production of fibers, such as delusterants, pigments, dyes, antioxidants, antistatic agents and surface-modifying agents.
• hosiery filaments are usually of round cross section, other shapes may be employed and may be particularly useful in certain end uses such as in tricot knit fabrics or certain woven fabrics. For such purposes, cross sections of trilobal shape, shield shape, heart shape, cruciform shape and various multilobal configurations may be employed.
• the filaments of this invention exhibit a surpris-ingly good combination of high crimp elongation, high strength and high crimp recovery. They may be processed to give a desirably low shrinkage level in the hose finishing process. Crimp elongation levels in excess of 40 percent, when crimped in 100 C. steam atmosphere under 1.2 mg./den. load, can readily be achieved at tenacity levels of at least 6 grams per denier at break, i.e., based on the filament denier at the breaking elongation. Crimp recovery is normally at least 85 percent and shrinkages of 3 percent or lower are readily attained.
• the filaments when removed from the package after normal storage and relatively straight (substantially uncrimped) and thus, easily handled, but when stretched slightly and then allowed to relax the filaments develop a considerable amount of crimp.
• This latter characteristic results in a reduction in the size of greige hose knit from the filaments since the filaments are stretched to some extent on knitting and tend to develop crimp when the hose is relaxed.
• the filaments tend to develop additional crimp when subjected to hot aqueous treatment as in a dye bath and require no separate or special treatment to develop the necessary crimping tendency.
• these filaments have the ability to generate very small coils and this provides a high compressive force in the hose at a given fabric density. This, in turn, leads to a more comfortable fit over a wide range of leg sizes.
• the coil diameter of a given filament may be varied considerably by varying the hose finishing temperature. For instance, a filament having a crimp diameter of 0.19 mm. with 100 C. steam treatment has been found to give a crimp diameter of 0.11 mm. at 150 C. This permits the hosiery manufacture to vary the characteristics of the hose substantially by appropriate selection of finishing conditions.
• inherent viscosity signifies the natural logarithm of the ratio of flow time in a viscometer of a polymer solution containing approximately 0.5 percent by weight of polymer, relative to the flow time of the solvent by itself, divided by the concentration. Measurements of inherent viscosity are made with 0.25 gram of polyamide in 50 milliliters of meta cresol at 25 C.
• Shrinkage and crimp elongation of the filament are determined as follows:
• a 750 denier skein of monofil or multifilament yarn is prepared by winding the requisite number of turns on a reel to give a skein of about 55 centimeters length when suspended with a weight attached.
• the denier of the filament bundle representing the collapsed skein will, of course, be twice that of the original skein, i.e., l500-denier.
• the skein is hungon a hook with a 500 gm. weight suspended from its other end. After 1 minute, the length (a) of the skein is measured. The 500 gm. load is removed and a 1.8 gm. load is applied in its place so that the skein is under a tensile load of 1.2 mg./den.
• the skein with the weight attached is subjected to 100 C. steam at atmospheric pressure (hereinafter referred to as atmospheric steam") for 1 minute, after which the skein is allowed to dry in air for 10 minutes.
• the skein length (b) is then measured.
• the 1.8 gm. load is then removed, the 500 gm. load is again applied for 1 minute, and the length (c) of the skein determined.
• the 500 gm. load is then replaced by the 1.8 gm. load. After the 1.8 gm. load has been applied for 2 minutes, the length (d) of the skein is measured.
• the crimp elongation, shrinkage, and crimp recovery of the filament are calculated from the following equations:
• Crimp Elongation percent 100 (c-b/b) Shrinkage, percent 100 X (a-c/a) Crimp Recovery, percent 100 X (c-d/c-b)
• the crimp diameter of the filament under a tension of 1.2 mgd is determined by taping l-inch lengths of the crimped tensioned skein on a microscope slide and projecting the magnified image on a grid covered screen by means of a projection microscope.
• the strength of the filaments or yarns is usually expressed in terms of tenacity and may be measured by conventional means. Values given herein were measured on yarn conditioned at 72 F. (22.2 C.) and 65 percent RH using an lnstron tester. The tenacity after boil-off is measured on yarn which has been boiled in water for 30 minutes under no load, dried at 72 F. (222 C.) and conditioned as above. The tenacity of a conventional yarn is calculated on a basis of the denier of the yarn as measured before testing. However, since the yarn of this invention elongates considerably before breaking, the actual denier at the breaking point is substantially lower than the measured denier. Therefore, tenacity based on the breaking denier is a more useful value for comparing different fibers. Tenacity in grams per denier at break (T may be calculated from the usual tenacity value (T) and the percent elongation at the breaking point (E) as follows:
• EXAMPLE 1 The salt of hexamethylenediamine and dodecanedioic acid is prepared as follows: 9,080 gm. of dodecanedioic acid are dissolved in 46 liters of anhydrous methanol with stirring and heating until solution is complete. To this solution is added 5,500 gm. of an 84.9 percent aqueous solution of hexamethylenediamine, the diamine solution being added rapidly with rapid mixing. The resulting solution is cooled to l0-l5 C. to precipitate the salt, with continued agitation for 2 hours. The salt is then filtered off, washed with 7.6 liters of cold methanol, dried in a vacuum oven at 80 C. under 75-125 mm. Hg. pressure for 16 hours. A solution of 10 gm. of the resulting salt in milliliters of water is found to have a pH value of 7.7.
• the salt of N,N'-diethylhexamethylenediamine and dodecanedioic acid is prepared as follows: 5,000 g. of N,N'-diethylhexamethylenediamine are added to 4.3 liters of isopropyl alcohol. The diamine solution is added with stirring to a 50-60 C. solution of 6,510 gm. of dodecanedioic acid in 44 liters of isopropyl alcohol, the solution being kept under a nitrogen atmosphere. The warm solution is stirred until a clear solution is obtained. 44 liters of isopropyl alcohol are then added to the mixture which is cooled to 0l0 C. to precipitate the salt. If the salt fails to precipitate on cooling, 2 gallons of ethylacetate are added to bring about precipitation. The salt is then filtered off and dried at 50 C. for 24 hours.
• a copolymer is prepared by combining equal weights of the above salts in an autoclave under a nitrogen atmosphere.
• Other additives are 1.5 percent by weight of hexamethylenediamine, 0.6 percent formic acid, 0.2 percent boric acid, 0.03 percent potassium phenyl' phosphinate and 8.6 percent water.
• the salts and the additives are heated in the closed autoclave with agitation to a temperature of 215 C. over a period of 120 minutes.
• the pressure in the autoclave is then reduced to atmospheric and the temperature increased to 295 C. over a period of 90 minutes. This temperature is maintained for 30 minutes while the autoclave is flushed with dry nitrogen.
• the pressure in the autoclave is reduced to millimeters of mercury or less and held for 60 minutes.
• the polymer is then cooled to 250 C., extruded and cut to flake in the conventional manner.
• the flake is then dried in a vacuum oven at 120 C. for 24 hours.
• the final polymer has an inherent viscosity of 1.75.
• a polymer is prepared from the salt of hexamethylenediamine and dodecanedioic acid in the conventional manner, cut into flake and dried.
• the final poly mer has an inherent viscosity of 1.40.
• the two above prepared polymers are melted and pumped to a spinneret assembly of the type illustrated in FIG. 2 of U. S. Pat. No. 3,558,760 to Olson, with holes arranged to spin three filament yarns.
• the polymers are extruded in side-by-side relation to produce filaments containing about 50 percent of each of the two polymers.
• the filaments are quenched in air at 25 C. and then converged into a three-filament yarn.
• the yarn is given 4 passes around a feed roll rotating at 330 yds. (302 meters/min.) peripheral speed and its associated separator roll and then is given 7 passes around a feed roll having a peripheral speed of 1,300 yds./min.
• the yarn is then passed to another roll operating at 1,300 yds./min. (1,189 meters/min.) and then to a roll operating at 1,250 yds./min. (1,143 meters/min.) and is finally wound into a package in the conventional manner at 1,200 yds./min. (1,097 meters/min). Subsequently, the yarn is withdrawn from the package and given an additional 1.3X draw in order to reduce the elongation to the desired range of 25-30 percent. The yarn is then passed from the draw roll through a tubular air jet device of the type illustrated in U. S. Pat. No. 3,558,760, FIG.
• the yarn is passed through the jet device at 420 yds./min. (384 meters/min.) then around a series of four snubbing pins of 3/16 inch (4.8 mm.) diameter where the yarn is passed in contact with the pins for a total cumulative angle of 1,100.
• the yarn is then passed around a power driven roll rotating with a peripheral speed which is 28 percent less than the speed of the draw roll. From the snubbing pins the yarn is passed to a conventional winding device and wound into a package.
• the denier of the final yarn is 22.
• Table 1 below gives properties of the yarn prepared as above, designated yarn A, in comparison with properties obtained on a commercial bicomponent yarn, yarn B, of the same denier-filament count, which is used in the manufacture of stretch hosiery.
• Yarn A has better tenacity and elongation at break, both before boil-off (BBO) and after boil-off (ABO) and has greatly improved crimp elongation.
• greige hose When the above yarn is knitted into miniature style stretch hose, it is found that greige hose, immediately after knitting, are relatively small in size due to the tendency of the yarn to crimp at this point.
• Table l-A shows a comparison of the hose, designated hose A, with hose knit from yarn B above. The relative reduction in hose size after various treatments is shown with the commercial greige hose, hose B, taken as 100.
• the yarn A of this invention gives a greige hose of greatly reduced size, and treatment of this hose with boiling water is sufficient to reduce the size below that obtained by treatment of the commercial hose, B,
• the two polymers are mixed in a 50/50 weight ratio in a homogenizer at 305 C. and then pumped to a spinneret assembly of the type used in Example 1.
• the total elapsed time from mixing to extrusion of the polymer is about 90 min.
• Analysis of the polymer indicates about 12 percent of amide interchange between the two polymers.
• the block copolymer is extruded in sideby-side relationship with poly(hexamethylenedodecanedioamide) of 0.96 inherent viscosity and processed in the yarn as described in Example 1. Properties of the yarn (D) in comparison with yarn (B) of Example 1 and of hose knitted from the yarn are given below.
• Example 3 is repeated except that poly(N,N'-di-nbutyl-hexamethylenedodecanedioamide) is substituted for poly (N,N-diethylhexamethylenedodecanedioamide). Properties of the yarn (d) in comparison with yarn B of Ex. 1 and hose prepared from the yarn are shown below.
• Crimp recovery 85 The greige hose resulting from yarn E had a relative area of 42 compared to 100 units for hose made from yarn B. Additional area contraction occurred after boil-off and treatment with 1 18 C. steam.
• a composite polyamide filament having a tenacity of at least 6 grams per denier at break comprising distinct, continuous, filament components in adherent, eccentric arrangement along the length of the filament to provide a helical crimp with a crimp elongation of at least 40 percent when the filament is subjected to atmospheric steam while the filament is under 1.2 milligrams per denier load,
• the polyamide of one component consisting essentially of poly(hexamethylenedodecanedioamide) and the polyamide of a second component is a copolymer consisting of to 50 percent hexamethylenedodecanedioamide polymer units and 25 to 50 percent N,N'-dialkyl-hexamethylene-dodecanedioamide polymer units.

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• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Textile Engineering (AREA)
• Multicomponent Fibers (AREA)
• Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
• Artificial Filaments (AREA)

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Cited By (8)

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Citations (4)

• 1972
  • 1972-01-05 US US00215625A patent/US3779853A/en not_active Expired - Lifetime
• 1973
  • 1973-01-04 GB GB62173A patent/GB1416231A/en not_active Expired
  • 1973-01-04 FR FR7300226A patent/FR2167678B1/fr not_active Expired
  • 1973-01-05 JP JP48000072A patent/JPS4873509A/ja active Pending

Patent Citations (4)

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