US2161766A - Synthetic fiber - Google Patents

Synthetic fiber Download PDF

Info

Publication number
US2161766A
US2161766A US16400237A US2161766A US 2161766 A US2161766 A US 2161766A US 16400237 A US16400237 A US 16400237A US 2161766 A US2161766 A US 2161766A
Authority
US
United States
Prior art keywords
yarn
vinyl
resin
fibers
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
Inventor
Edward W Rugeley
Jr Theophilus A Feld
John F Conlon
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Carbide and Carbon Chemicals Corp
Original Assignee
Carbide and Carbon Chemicals Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=35431062&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=US2161766(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Carbide and Carbon Chemicals Corp filed Critical Carbide and Carbon Chemicals Corp
Priority to US16400237 priority Critical patent/US2161766A/en
Priority to FR842532D priority patent/FR842532A/en
Priority to BE429899D priority patent/BE429899A/xx
Priority to GB2519438A priority patent/GB518555A/en
Priority to GB2881139A priority patent/GB518710A/en
Priority to US24047638 priority patent/US2353270A/en
Publication of US2161766A publication Critical patent/US2161766A/en
Application granted granted Critical
Priority to GB3046339A priority patent/GB537583A/en
Priority to FR52401D priority patent/FR52401E/en
Priority to GB1203740A priority patent/GB541261A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02GCRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
    • D02G3/00Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
    • D02G3/02Yarns or threads characterised by the material or by the materials from which they are made
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S264/00Plastic and nonmetallic article shaping or treating: processes
    • Y10S264/73Processes of stretching
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S428/00Stock material or miscellaneous articles
    • Y10S428/907Resistant against plant or animal attack
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S57/00Textiles: spinning, twisting, and twining
    • Y10S57/904Flame retardant
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S8/00Bleaching and dyeing; fluid treatment and chemical modification of textiles and fibers
    • Y10S8/10Polyvinyl halide esters or alcohol fiber modification
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/29Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2913Rod, strand, filament or fiber
    • Y10T428/298Physical dimension
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T442/00Fabric [woven, knitted, or nonwoven textile or cloth, etc.]
    • Y10T442/30Woven fabric [i.e., woven strand or strip material]
    • Y10T442/3976Including strand which is stated to have specific attributes [e.g., heat or fire resistance, chemical or solvent resistance, high absorption for aqueous composition, water solubility, heat shrinkability, etc.]
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T442/00Fabric [woven, knitted, or nonwoven textile or cloth, etc.]
    • Y10T442/40Knit fabric [i.e., knit strand or strip material]
    • Y10T442/413Including an elastic strand
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T442/00Fabric [woven, knitted, or nonwoven textile or cloth, etc.]
    • Y10T442/60Nonwoven fabric [i.e., nonwoven strand or fiber material]
    • Y10T442/696Including strand or fiber material which is stated to have specific attributes [e.g., heat or fire resistance, chemical or solvent resistance, high absorption for aqueous compositions, water solubility, heat shrinkability, etc.]

Definitions

  • This invention makes possible a synthetic fiber ll of many unique and distinctive properties, in-
  • the synthetic fibers of this invention are formed of certain types of vinyl resins, and the invention includes methods of forming, treating and using the new fibers, all as more fully hereinafter described.
  • Vinyl resins have been proposed for use in forming textile fibers by nearly all who have had experience with them, and this was entirely to be expected, since these resins are products which are truly synthetic, as well as readily formable, inherently colorless, odorless, tasteless, and not readily inflammable. Nevertheless, in the twenty years and more since vinyl resins first were suggested for this purpose, useful or practical fibers have never been produced from any vinyl resin of these types...
  • the new fibers of this invention are formed from vinyl resins such as may result from the conjoint polymerization of vinyl halides with vinyl 40 esters of aliphatic acids, and which have an average macromolecular weight of at least about 15,000. (Molecular weights referred to herein are those calculated by means of Staudinger's formula from viscosity determinations of solutions of the resins.)
  • the fibers are formed by spinning a solution or dispersion of the vinyl resin into filaments. These filaments are formed into fibers of the desired size by twisting and doubling operations as desired, and thereafter the fibers are stretched to yield products suitable for use in the customary textile operations.
  • the stretching of the fibers is carried out while they are in their normal state, by which is meant that they are not softened by heat or by the action of a solvent.
  • This stretching operation is a vital feature in the production of useful textile fibers from the vinyl resins, and it serves the dual purpose of greatly increasing the tensile strength, and of conferring on the fibers the unusual and highly 5 desirable property of true elasticity.
  • the two highly imlportant properties of tenacity and elongation may be varied and controlled almost at will.
  • the fibers in finished form are soft and fiexible, and are characterized by their ability to be woven and knitted and formed into a large number of exceptionally useful materials.
  • the new fibers possess a very high strength by comparison with other textile fibers, and they are unusual in that their strength is virtually the same whether they are wet or dry, and, surprisingly enough, the wet strengthof the new fibers is, if anything, slightly greater than the dry strength.
  • the unique resistance to impairment by water, together with the true elasticity, resistance to chemical, bacterial and fungal attack, thermoplasticity, lack of infiammability and great flexibility of the fibers makes possible many uses for these materials which are radically different from those to which ordinary textile fibers are applicable.
  • the vinyl resins from which the new fibers are prepared must have special characteristics.
  • the class of resins use- ,ful in this invention are those such as are described in Patent 1,935,577 to E. W. Reid, and these resins may be made by the processes described by that patent or by other means, such as the process described in Patent 2,064,565 to E. W. Reid. of these conjoint polymers of vinyl halides with vinyl esters of aliphatic acids, the preferred resins are those which contain from to 95% by weight of the halide in the polymer. Within this range, those resins formed from vinyl chloride and vinyl acetate which contain in the polymer about to by weight of the chloride are especially desirable.
  • the resin must have an average macromolecular weight of at least 15,000, and the upper value is limited only by the solubility of the resins in suitable liquids to yield spinnable solutions or dispersions.
  • Vinyl resins, as prepared ordinarily consist of a mixture of polymeric aggregates of different molecular sizes. .
  • those to be used in this invention should be freed from polymers 55 havingexcessively low molecular weightsin orweight of water. It has been found that, when the acetone used contains water in excess of this amount, the quality of the resin dispersion is materially impaired, and solutions made from such solvents can be filtered and spun only with great difiiculty.
  • the concentration of the vinyl resin in the spinning solution is dependent upon and varies inversely with themacromolecular weight of the resin, but theresin content ordinarily employed using acetone as the solvent is 25% or less by weight.
  • the resin is best employed in the form of a dry powder, and the dispersion, or the spinning dope, may be made bycombining the resin with the requisite quantity of dry acetone in a mixing device, such as one of the dough-type mixers or kneaders, provided with means of temperature control, and equipped to eflect reflux of the solvent.
  • the temperature of mixing and subsequent handling is conveniently maintained at about 50 C.
  • the time required for mixing to obtain useful dispersions must be adjusted according to the ease of dispersion or the resin in the solvent, and this ordinarily consumes about 12 hours.
  • the resulting dope is a clear, heavily gelatinous, non-flowing, plastic mass at room temperature, while at a temperature of 50 C. it assumes a very viscous, slowly fiowable state. This viscosity has been determined by experiment to be desirable in the subsequent manipulation of the solution and its formation into filaments.
  • the dispersion may be filtered in high-pressure type plate-and-frame filters, the material being moved by means of high-pressure gear-type pumps.
  • temperature control means such as jackets supplied with heated water or steam, so that an elevated temperature may be maintained to reduce the pressure necessary to handle the viscous mass.
  • Filtration may be carried out in one or more stages, and the filtering medium may be any suitable material capable'of removing the last traces of undispersed or insoluble material from the dope. Filteringv pressures of from about 200 to 500 pounds per square inch, in general, are suitable for this operation.
  • the filtered dope should be thoroughly de-aerated, and this may be efiected by permitting the dispersion to stand for about 24'hours at the operating temperature of 50 C., and this may be assisted, if desired, by creating a partial vacuum over the dispersion.
  • the spinning, or filament extrusion, operation may be carried out in equipment customarily employed for so-called dry-spinning of other types of filaments,
  • a bobbin-type thread takeup may be employed, orthe filaments may be given a twist at the point of spinning by employing a cap-type mechanism.
  • the filaments are dried by heated air or other gas, and the length of the drying cell is determined by the rate of drying so eflected.
  • the length of drying cell required for the formation of these vinyl resin filaments is somewhat greater than is. true of other plastic materials,such as the cellulose esters, because of the tendencies of the material to retain the solvent.
  • this treatment produces delustering oi the fibers which persists in large part throughout their formation into finished yarn.
  • This method of delusterlng the fibers has no efiect on their tensile properties, elasticity, or other qualities, and because of its simplicity and economy it has obvious advantages over delustering methods which involve the addition 0! foreign substances to the filaments themselves.
  • the filaments or thread delivered from the take-up bobbin may be twisted, or doubled and twisted, to form a yarn. It is necessary in most cases to permit the filaments to age for at least 12 hours before the twisting or doubling operations are performed. Ageing of the can be advantageously replaced by a bri ttreatment with heated water. For example, ii! the filaments on the bobbins are immersed in water at 65 C. for a period oi 2 to 5 hours, no ageing is required.
  • the fibers, after twisting or twisting and doubling, are to be stretched, and it is therefore necessary initially to impart greater twist than is intended for the finished yarn, inasmuch as the stretching operation obviously will reduce the twist per unit length oi. the yarn. Allowance for reduction in twist as a result of stretching the yarn is a direct linear function or the degree of stretch to be given the fibers, and can be readily computed.
  • the next step in the yarn processing is that of stretching, and this step is one of paramount importance in the production of the new fibers.
  • the amount of stretch-imparted to the yarn may vary considerably up to about 200%, and in normal procedure a stretch of from about 75% to about 180% is applied.
  • the extent of stretch used is determinedby the polymer size (average macromolecular weight) of the resin, and by the characteristics desired in the finished yarn.
  • the yarn is delustered simultaneously with the stretching operation.
  • the yarn is also delustered, but to a lesser extent than is true when the high degree of stretch is applied in a single stage.
  • the application of heated water to the yarn just prior to stretching apparently does not cause the yarn to be stretched while appreciably softened by heat, since it is likely that most of the heat is dissipated prior to the actual stretching of the yarn.
  • the setting of the stretch in the yarn may be accomplished in several ways; for example, by prolonged ageing of the extended yarn under tension on the stretcher spool, or by subjecting the tensioned stretched yarn to elevated temperatures, which greatly accelerate the rate of setting.
  • the latter treatment may be conveniently carried out by immersing the yarn contained on the stretcher spools in water heated to the desired temperature, or by applying water so heated to the revolving stretcher spool. This latter procedure enables stretching and setting of the yarn to be conducted simultaneously.
  • the temperature of the setting operation depends upon the properties ultimately desired in the yarn, and these effects are more fully described below.
  • the stretched yarn may be set at any temperature below about 75 C. If the yarn is stretched in several stages, the stretch may be set in the yarn between each stage of stretching. Immersion of the stretched yarn in water at about 65 C. for 2 to 3 hours will accomplish this.
  • three rollers of small diameter may be staggered to cause the yarn to change direction abruptly as it passes over each roller.
  • an idler roll of large diameter is used with such an arrangement, the yarn may be sharply flexed in this manner three times, or some multiple of three times, in each pass through the arrangement, depending on the num, ber of turns of yarn over the idler roll.
  • the characteristics of the finished yarn arelargelyoontrolled by,the stretching operation.
  • the properties of filament size, softness, luster, strength, suppleness or flexibility, and extensibility or elongation are of extreme importance. It is desirable to have the proper balance between these properties, particularly those of strength, or tenacity, and elongation.
  • the yarn produced in accordance with this invention before stretching may have, for example, a tenacity of 0.83 gram per denier. and an elongation of 120% or more.
  • the re-' sultant product possessed a tenacity of 2.00 gramsper denier and an elongation of 35%.
  • the product resulting may show a tenacity of 3.40 grams per denier and an eion-- gation of 11%.
  • the foregoing examples will clearly show that, by controlling the degree of stretch imparted to the yarn, the tensile properties of the product can be varied almost at will. As the amount of stretch is increased, the elongation is correspondingly reduced until an impracticaliy low value for the latter is reached.
  • This correlation of the tenacity and elongation with the degree of stretch is illustrated by the accompanying drawing, in which Fig. 2 graphically represents this relation of properties as it exists in one particular sample of yarn.
  • the finished yarn may be packaged according to any of the conventional forms in which yarn is supplied by employing any standard equipment for transferring the yarn from the spools or bobbins containing the stretched and flexed yarn to the final packages.
  • any standard equipment for transferring the yarn from the spools or bobbins containing the stretched and flexed yarn to the final packages.
  • spooling, capping, skeining, and coning may be readily carried out, and in such operations as coning, where lubricants are required, these may be conveniently applied to the yarn by means of a conditioning roll.
  • the staple fiber produced from unstretched filaments of the type shown herein is particularly useful as a binding agent or stlfiener for Example 1
  • a vinyl resin resulting from the conjoint polymerization of vinyl chloride with vinyl acetate in such proportions as to produce a resin confirming 87% of the chloride in the polymer was eated by'fractional extraction according to the method of Patent 1,990,685 to free the polymeric aggregate from the lower average macromolecular weight polymers, and to yield a resin having an average macromolecular weight of about 17,- 000.
  • test piece is conditioned for 4 hours at 25 C.
  • Viscosity (7% solution in methyl isobutyl ketone at 26 C., Ford cup, #4 orifice) not less than 14 seconds.
  • This resin in the form of fine powder was dispersed in acetone having a water content of 0.4% to form a dope containing 23% by weight of resin.
  • the dispersion of resin in the solvent was effected at 50 C. by means of a heated doughtype mixer provided with means for slow solvent reflux. At 25 C., the viscosity of the resin dispersion was not measurable by ordinary means. At 50 0., its viscosity was determined as 200,000 centipoises.
  • This dispersion was] filtered in a plate-and-frame filter press, usinga filter pad consisting of-several layers of cheesecloth and 4 oz. cotton batting, followed by several thicknesses of special filtering cloth.
  • the filament extrusion operation was carried for use.
  • the resin dispersion was fed to the spinning machine by means of metering pumps which discharged to a candle-filter located near the top and within the drying cell proper. Immediately adjacent to the candle-filter was the spinnerette, which was 1.5 inches in diameter, provided with 40 orifices, each having a diameter of 0.06 mm.
  • the drying cell itself was a water-jacketed vertical cylinder 8 inches in inside diameter, provided with a bobbin take-up at its lower end. The effective filament drying space in this cell was about 16 feet in length.
  • the temperature of the water in the drying cell jacket was maintained at C., and heated air, also at 80 C., was admitted to the drying cell at the rate of 5 cubic feet per minute.
  • the air was admitted near the top of the cell at the spinnerette face and directed by means of a cone bailie transverse to the travel of the extruded filaments.
  • the drying air, laden with solvent vapor, was withdrawn from the lower part of the cell by means of a suction pump.
  • the filaments at the bottom of the cell were gathered together through a guide and then wound parallel on a bobbin, the thread crossings and cake build being controlled by the usual equipment.
  • the rate of filament passage through the drying cell was 250 meters per minute, and the filament denier was between 2.5 and 3.0.
  • the yarn was twisted by means of a. standard duplex ring twister.
  • the amount of twist imparted was six turns per inch in the yarn.
  • the thread in this operation was delivered to the twisting device from the spinning bobbins immersed in a water bath. As pointed out before, the water picked up by the thread from this bath served both to lubricate the thread and to eliminate static electrical charges.
  • the twisted yarn was next stretched by immersing the spool on which it was contained in water containing a small amount of the sodium salt of the sulfate ester of a 17 carbon atom branched chain secondary alcohol, which served as a wetting agent.
  • the thread was then guided to a positively driven roll around which it was wrapped a few times to preclude slippage. From this roll the thread was passed upward to a takeup spool, also positively driven, at a sufficiently higher speed to impart a stretch of to the thread. After this operation, the stretch was set in the yarn by immersing it for about 2 hours, while on the take-up spool, in a bath of water heated to about 65 C.
  • the yarn was given a second stage stretching in the same manner as before, and the extent of stretch was 20% of its length.
  • the total stretch imparted by these two stretching operations thus amounted to about based on the original yarn.
  • the stretching operations were carried out with a thread travel of meters per minute. In the stretching operation, the amount of twist in the yarn and its denier were reduced.
  • The may be dyed by incorporating dye- M n th take-up stufls in the resin dispersion prior to filament W W extrusion, or it may be dyed, after its formation, a ,1; 65' c, f pu'lod from baths containing mixtures of solvents and and "ed m at non-solvents for the resin which temporarily themmflngmd swelitheyarn.
  • the yarn M T1118 m be complished by incorpora z Mmwdrlvenron pigmentssuchastitaniumdioxideofsmallparin a m mm heated t 90- c ticie size in the resin dispersion, and the degree The m m mm to the m betmn oi delusterization can be controlled by variation of the particle size of the pigment and the 0 Med 5 The m amount used. It is preferable to achieve the deot the yarn in the stretching operation agm The M m then involve the incorporation of other substances in the filaments.
  • this may be eftectively done by treatment of the filaments with u heated water at their point of formation, coupled with the additional delustering eflected by m the softness, elasticity and tensile strength of the m uniform the 801m and yarn.
  • the application of water heated above 50' C. to the filaments as they leave the spinning cell causes the fibers, when viewed under the microscope, to have a slightly roughened or scaly exterior.
  • This surface modification of the fibers 05 is highly desirable, and is a further instance of the manner in which the properties of the new fibers of this invention resemble those of natural fibers.
  • This yarn lends itself readily to all ordinary 70
  • thisrollandasecondrolldrivenatahigherspeed with previously known yarns In weaving it may be used either as filling, warp or pile. It is desirable to carry out weaving operations with this yarn'under conditions of high relative humidity in order to reduce the development of static electrical charges. Due to the unusual resistance of the yarn to water, it can be' woven while wet without sacrificing strength or risking thread breakage or undue stretching. In weaving, hygroscopic warp sizing should be used which will form a pliable film on the thread.
  • Tempera- Shrinkage, ture, C percent Where this contraction amounts to as much as 10%, a reduction in luster accompanies it.
  • Shrinkage of the yarn also results in reduction in tenacity and an increase in elongation proportional to the extent of the stretch which is lost. After the yarn has shrunk as a result of being subjected to elevated temperatures, it no longer shows any tendency toward contraction when reheated to the same or a lower temperature.
  • This shrinkage of the unset stretched yarn can be utilized in manyapplications of the yarn to tighten the stitch in knitted or woven materials and thereby to prevent "laddering or thread slippage.
  • the yarn can be produced in many filament sizes, and it has been determined that the filament denier which most conveniently lends itself to the processes of textile manufacture is aroun 1.0 to 1.5.
  • the unusual propertiesof the new yarn make possible many applications which take advantage of its remarkable true elasticity, waterresistance and high wet strength, together with its resistance to attack by chemical influences or micro-organisms. For example, it is of value in industrial filtering fabrics; in fishing lines, nets and seines; in forming acidand alkali-resistant clothing; protective pipe coverings; electrical insulation; shower curtains; bathing suits; waterproof clothing; fire-proof awnings and curtains; hosiery; fusible shape-retaining fabrics; and, in admixture with other textile materials, mixed fabrics for obtaining cross-dyeing eiiects and the like.
  • the new yarn is useful in pile fabrics such as velvet, and it can be advantageously employed as either the backing or the pile or both.
  • the staple fibers of this invention in admixture with natural materials such as cotton and wool, make possible the production of fabrics which will retain a pressed fold, and improve mercerlzing and l.
  • Textile fiber composed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which contains from about 80% to 95% by weight of the halide in the polymer and which has an average macromolecular weight of at least 15,000.
  • Textile fiber composed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which has an average macromolecular weight of at least 15,000 and which is substantially free from lower molecular weight polymers.
  • Textile fiber composed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which has an average macromolecular weight of at least 15,000 and which is substantially free from lower molecular weight polymers, said resin being completely dispersible in warm dry acetone and having a heat distortion point above 65 C.
  • Textile fiber composed of a vinyl resin substantially identical with a resin resultingfrom the conjoint polymerization of vinyl chloride with vinyl acetate, which contains from about to by weight of the chloride in the polymer and which has an average macromolecular weight of at least 15,000, said resin having a heat distortion point above 65 C. and being completely dispersible in acetone containing less than 0 0% by weight of water at about 50 C.
  • said fiber being characterized by resistance to deterioration in strength on exposure to ultraviolet light, and by water-resistance, non-inflammability, immunity to attack by bacteria and fungi, and resistance to alkalies and mineral acids,
  • Staple textile fiber formed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which contains from about 85% to about 90% by weight of the halide in the polymer and which has an average macromolecular weight of at least 15,000, said fiber being characterized by resistance to deterioration in strength on exposure to ultra-violet light, and by water-resistance, thermoplasticity, non-infiammability, immunity to attack by bacteria and fungi, and resistance to alkalies and mineral acids.
  • Synthetic textile yarn formed of filaments composed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerall-elongation of from 10% to 35%.
  • Knitted fabrics or articles comprising yarn 'iormedotfilamentsotavinylrminmbstantially identical with a resin resulting from the conjoint polymer-laden oiavinylhalidewithavinylester of an aliphatic acid, which contains from about 00%to05% byweightoi thehaiideinthepo ymet and which has an average macromolecular weight of at least 15,000, saidyarn having been stretchedbetween'fi'ltandmit.
  • Woven iabrlcs or articles comprising yarn iormedoifilammtsotavinylresin identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which contains from about80% to9fi%byweightoithehalideinthe polymer and which has an average macromolecularweightofatleastl5,000,saidyarnhaving been stretched betwem and 200%.
  • Braided articles, lines and cords comprising yarn formed of filaments of a vinyl resin substantially identical with a resin resulting from the conjoint H H ofavinylhalidewitha vinyl ester of an aliphatic acid, which contains from about 50% to 95% by weight of the halide in the polymer and which has an average macromolecular weight 01' at least 15,000, said yarn having been stretched between 75% and 200%.
  • Synthetic textile fibers, fabrics and articles comprising yarn composed of filaments formed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, said resin containing from about 80% to about 95% by weight 01' the vinyl halide in the polymer and having an average macromolecular weight of at least 15,000, said yarn having been stretched to the extent of from 75% to 200% and being characteried by high tensile strength in the wet state, hig true elasticity, controllable shrinkage, w 1 to water, alkalies and mineral acids, to attack by bacteria and fungi, non-bill crease resistance, thermoplasticity, electrical insulating qualities, controllable luster, and high flexibility.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Textile Engineering (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Artificial Filaments (AREA)
  • Ropes Or Cables (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Chemical Treatment Of Fibers During Manufacturing Processes (AREA)
  • Reinforced Plastic Materials (AREA)
  • Inorganic Fibers (AREA)

Description

June 6, 193 E. w. RUGELEY ET AL 2,161,766
SYNTHETIC FIBER Filed Sept. 15, 1937 l SOLVENT VINYL RESIN SPINNING HOT WATER DELUSTERING LUSTROUS FILAMENTS ::l I DOUBLING TWISTING WATER LUBRICATION I COLD STRETCHING HOT ROLL STRETGHING ONE OR MORE STAGES WATE LURICATION SINGLE STAGE HOT WATEI? AGEING WATER LUBRICATION FINAL PACKAGING m 3.40 150 g 3.20 120 Z 300 no 5 Lu Q I- m 2.8 100 g E 260 war monomer: 90 g 240 so A 2 TENACITY H g 2.20 7
. Q |..J I 2.00 so 0 ,2 L60 50 E Q 1.60 40 Z M 7.40 30 1.20 20 0 4O 6O 80 I00 I20 I 760 Z00 INVENTORS EDWARD W. RUGELEY THEOPHILUS A. FEILD, JR.
JOHN FCONLON BY @102 6. J
ATTORNE Patented June 6, 1939 PATENT OFFICE- SYNTHETIC FIBER Edward w. Bugeley,
'l'heophilus John F. Conlon, Charleston. W. Va.,
' A. 1"eild, Jr., and ors to Carbide and Carbon Chemicals Corporation, a corporation of New York Application September 15, 1931, Serial No. 104,002
The quest for a truly synthetic textile fiber has had few rivals in its intensity, and, through the past, in its conspicuous lack of success. It has been-proposed to make textile fibers and filas ments from many synthetically produced materials, but until now none of these has ever yielded acommercially usable product. The only commercially useful textile fibers at present, as in the beginning, are products of nature, supplemented in more recently by those made from chemically modified natural products, such as the esters and ethers of cellulose, and cellulose itself regenerated from its derivatives.
This invention makes possible a synthetic fiber ll of many unique and distinctive properties, in-
cluding high true elasticity, flexibility. high strength and remarkable resistance, and it provides an easily producible product not originating in nature which equals and surpasses in many respects natural fibers and fibers made from modified products of nature. The synthetic fibers of this invention are formed of certain types of vinyl resins, and the invention includes methods of forming, treating and using the new fibers, all as more fully hereinafter described.
Vinyl resins have been proposed for use in forming textile fibers by nearly all who have had experience with them, and this was entirely to be expected, since these resins are products which are truly synthetic, as well as readily formable, inherently colorless, odorless, tasteless, and not readily inflammable. Nevertheless, in the twenty years and more since vinyl resins first were suggested for this purpose, useful or practical fibers have never been produced from any vinyl resin of these types...
The new fibers of this invention are formed from vinyl resins such as may result from the conjoint polymerization of vinyl halides with vinyl 40 esters of aliphatic acids, and which have an average macromolecular weight of at least about 15,000. (Molecular weights referred to herein are those calculated by means of Staudinger's formula from viscosity determinations of solutions of the resins.)
Briefly, the fibers are formed by spinning a solution or dispersion of the vinyl resin into filaments. These filaments are formed into fibers of the desired size by twisting and doubling operations as desired, and thereafter the fibers are stretched to yield products suitable for use in the customary textile operations. The stretching of the fibers is carried out while they are in their normal state, by which is meant that they are not softened by heat or by the action of a solvent.
This stretching operation is a vital feature in the production of useful textile fibers from the vinyl resins, and it serves the dual purpose of greatly increasing the tensile strength, and of conferring on the fibers the unusual and highly 5 desirable property of true elasticity. By means of the stretching operation, the two highly imlportant properties of tenacity and elongation may be varied and controlled almost at will.
The fibers in finished form are soft and fiexible, and are characterized by their ability to be woven and knitted and formed into a large number of exceptionally useful materials. The new fibers possess a very high strength by comparison with other textile fibers, and they are unusual in that their strength is virtually the same whether they are wet or dry, and, surprisingly enough, the wet strengthof the new fibers is, if anything, slightly greater than the dry strength. The unique resistance to impairment by water, together with the true elasticity, resistance to chemical, bacterial and fungal attack, thermoplasticity, lack of infiammability and great flexibility of the fibers, makes possible many uses for these materials which are radically different from those to which ordinary textile fibers are applicable.
The general sequence of operations in the formation of the new textile fibers according to this invention is shown by the fiow sheet appearing as Fig. 1 in the accompanying drawing.
As has been indicated, the vinyl resins from which the new fibers are prepared must have special characteristics. The class of resins use- ,ful in this invention are those such as are described in Patent 1,935,577 to E. W. Reid, and these resins may be made by the processes described by that patent or by other means, such as the process described in Patent 2,064,565 to E. W. Reid. of these conjoint polymers of vinyl halides with vinyl esters of aliphatic acids, the preferred resins are those which contain from to 95% by weight of the halide in the polymer. Within this range, those resins formed from vinyl chloride and vinyl acetate which contain in the polymer about to by weight of the chloride are especially desirable.
The resin must have an average macromolecular weight of at least 15,000, and the upper value is limited only by the solubility of the resins in suitable liquids to yield spinnable solutions or dispersions. Vinyl resins, as prepared, ordinarily consist of a mixture of polymeric aggregates of different molecular sizes. .Those to be used in this invention should be freed from polymers 55 havingexcessively low molecular weightsin orweight of water. It has been found that, when the acetone used contains water in excess of this amount, the quality of the resin dispersion is materially impaired, and solutions made from such solvents can be filtered and spun only with great difiiculty. The concentration of the vinyl resin in the spinning solution is dependent upon and varies inversely with themacromolecular weight of the resin, but theresin content ordinarily employed using acetone as the solvent is 25% or less by weight. In forming the solution, the resin is best employed in the form of a dry powder, and the dispersion, or the spinning dope, may be made bycombining the resin with the requisite quantity of dry acetone in a mixing device, such as one of the dough-type mixers or kneaders, provided with means of temperature control, and equipped to eflect reflux of the solvent. The temperature of mixing and subsequent handling is conveniently maintained at about 50 C. The time required for mixing to obtain useful dispersions must be adjusted according to the ease of dispersion or the resin in the solvent, and this ordinarily consumes about 12 hours. The resulting dope" is a clear, heavily gelatinous, non-flowing, plastic mass at room temperature, while at a temperature of 50 C. it assumes a very viscous, slowly fiowable state. This viscosity has been determined by experiment to be desirable in the subsequent manipulation of the solution and its formation into filaments.
The dispersion, or "dope, may be filtered in high-pressure type plate-and-frame filters, the material being moved by means of high-pressure gear-type pumps. Throughout the handling. of these dispersions, it is highly desirable to provide all storage tanks and conduits with temperature control means, such as jackets supplied with heated water or steam, so that an elevated temperature may be maintained to reduce the pressure necessary to handle the viscous mass.
Filtration may be carried out in one or more stages, and the filtering medium may be any suitable material capable'of removing the last traces of undispersed or insoluble material from the dope. Filteringv pressures of from about 200 to 500 pounds per square inch, in general, are suitable for this operation. The filtered dope should be thoroughly de-aerated, and this may be efiected by permitting the dispersion to stand for about 24'hours at the operating temperature of 50 C., and this may be assisted, if desired, by creating a partial vacuum over the dispersion.
The spinning, or filament extrusion, operation may be carried out in equipment customarily employed for so-called dry-spinning of other types of filaments, A bobbin-type thread takeup may be employed, orthe filaments may be given a twist at the point of spinning by employing a cap-type mechanism. In the spinning device, or drying cell, the filaments are dried by heated air or other gas, and the length of the drying cell is determined by the rate of drying so eflected. In general, the length of drying cell required for the formation of these vinyl resin filaments is somewhat greater than is. true of other plastic materials,such as the cellulose esters, because of the tendencies of the material to retain the solvent. It is desirable to direct astream of water heated to a temperature above 50 C. on the thread at the take-up bobbin. This serves to remove or dilute any solvent retained by the filaments and thereby to prevent sub sequent fusion of the fibers or loss of their identity as individual filaments. At the same time,
this treatment produces delustering oi the fibers which persists in large part throughout their formation into finished yarn. This method of delusterlng the fibers has no efiect on their tensile properties, elasticity, or other qualities, and because of its simplicity and economy it has obvious advantages over delustering methods which involve the addition 0! foreign substances to the filaments themselves.
The filaments or thread delivered from the take-up bobbin may be twisted, or doubled and twisted, to form a yarn. It is necessary in most cases to permit the filaments to age for at least 12 hours before the twisting or doubling operations are performed. Ageing of the can be advantageously replaced by a bri ttreatment with heated water. For example, ii! the filaments on the bobbins are immersed in water at 65 C. for a period oi 2 to 5 hours, no ageing is required. Throughout all handling and transferring of the threads or filaments in such operations as doubling and'twisting, the fibers must be lubricated, and for this purpose water is quite satisfactory, since it serves the dual purpose oi lubrication and reduction or static electrical charges which otherwise would develop on the yarn. The remarkable resistance of these new fibers to impairment in any way by water makes it possible to carry out the twisting, and similar operations, from bobbins of the yarn immersed in water.
The fibers, after twisting or twisting and doubling, are to be stretched, and it is therefore necessary initially to impart greater twist than is intended for the finished yarn, inasmuch as the stretching operation obviously will reduce the twist per unit length oi. the yarn. Allowance for reduction in twist as a result of stretching the yarn is a direct linear function or the degree of stretch to be given the fibers, and can be readily computed.
The next step in the yarn processing is that of stretching, and this step is one of paramount importance in the production of the new fibers, The amount of stretch-imparted to the yarn may vary considerably up to about 200%, and in normal procedure a stretch of from about 75% to about 180% is applied. The extent of stretch used is determinedby the polymer size (average macromolecular weight) of the resin, and by the characteristics desired in the finished yarn. It is important to conduct this operation while the yarn is adequately surface-wetted, and this may be done by immersing, or partly immersing, the spools from which the yarn is to be stretched in water which may contain a wetting agent or surface tension depressant, such as a sodium salt of a higher alkyl sulfate, or another of the materials commonly used for this purpose in textile operations. The actual stretching of the yarn n be eccqmp s ed by any means which will laments eifectthenecusaryextemiomanditcanbeconvenientlycarriedoutbytransferringtheyarn fromtbespooionwbichitiscontainedtoa second spool positively driven at a higher speed thanthatatwhichthefirstspoolisallowedto rotate. Inanothertypicalarrangement, the yarn, astwisted,canbestretchedbyimmersingthe bobbinincoldwaterandbrlng ltheyarnfrom this bobbin once around a roll positively driven subsequent operations given additional stretchingto the extent of 10% or 20% in each stage. If water heated to about to 00 C. is applied to the yarn at the first driven roll, and a stretch in excess of is applied, the yarn is delustered simultaneously with the stretching operation. In the case of stretching in the cold in two or more stages, the yarn is also delustered, but to a lesser extent than is true when the high degree of stretch is applied in a single stage. The application of heated water to the yarn just prior to stretching apparently does not cause the yarn to be stretched while appreciably softened by heat, since it is likely that most of the heat is dissipated prior to the actual stretching of the yarn. This has been demonstrated, in some cases, by the fact that heated water applied to the yarn at points intermediate to the two driven rolls had the apparent effect of restoring some luster to the yarn, and resulting in the production of yarn of lower quality than was otherwise produced by the preferred stretching operation described above.
Throughout all such operations, suitable traverse movements should be employed to provide correct cake-build of the yarn on the several spools and bobbins.
For a period after the yarn has been stretched, it shows a marked tendency to contract. This characteristic may be rudily controlled and modified by a setting" treatment. The setting of the stretch in the yarn may be accomplished in several ways; for example, by prolonged ageing of the extended yarn under tension on the stretcher spool, or by subjecting the tensioned stretched yarn to elevated temperatures, which greatly accelerate the rate of setting. The latter treatment may be conveniently carried out by immersing the yarn contained on the stretcher spools in water heated to the desired temperature, or by applying water so heated to the revolving stretcher spool. This latter procedure enables stretching and setting of the yarn to be conducted simultaneously. The temperature of the setting operation depends upon the properties ultimately desired in the yarn, and these effects are more fully described below. In general, the stretched yarn may be set at any temperature below about 75 C. If the yarn is stretched in several stages, the stretch may be set in the yarn between each stage of stretching. Immersion of the stretched yarn in water at about 65 C. for 2 to 3 hours will accomplish this.
Ithasbeen observedthattheyarnprocessed as described above did not always possess a uniform softness or hand. This was particularly noticeable between portions of the yarn wound nexttothebobbinorspoolascompared with thatneartheoutsideoftheyarncake,thatonthe outside being softer than that first wound on the bobbin. This irregularity can be eliminated, and yarn of lmiformly desirable hand and softness can be produced by subjecting the stretched yarn to abrupt flexing at high speeds while immersed in water. Such flexing can be easily carried out by simply transferring the yarn from one bobbin to another by way of an intermediate roller or set of rollers operating under water and arranged to cause the yarn passing over it to change directionthrough a short radius once or several times. For example, three rollers of small diameter, say 0.125 inch, may be staggered to cause the yarn to change direction abruptly as it passes over each roller. If an idler roll of large diameter is used with such an arrangement, the yarn may be sharply flexed in this manner three times, or some multiple of three times, in each pass through the arrangement, depending on the num, ber of turns of yarn over the idler roll.
As has been stated, the characteristics of the finished yarn arelargelyoontrolled by,the stretching operation. In any textile fiber the properties of filament size, softness, luster, strength, suppleness or flexibility, and extensibility or elongation are of extreme importance. It is desirable to have the proper balance between these properties, particularly those of strength, or tenacity, and elongation. The yarn produced in accordance with this invention before stretching may have, for example, a tenacity of 0.83 gram per denier. and an elongation of 120% or more. When this same yarn had been stretched as described herein to the extent of 90%, the re-' sultant product possessed a tenacity of 2.00 gramsper denier and an elongation of 35%. If, for example, the same, or a similar, yarn were stretched to the extent of (based on the original yarn), the product resulting may show a tenacity of 3.40 grams per denier and an eion-- gation of 11%. The foregoing examples will clearly show that, by controlling the degree of stretch imparted to the yarn, the tensile properties of the product can be varied almost at will. As the amount of stretch is increased, the elongation is correspondingly reduced until an impracticaliy low value for the latter is reached. This correlation of the tenacity and elongation with the degree of stretch is illustrated by the accompanying drawing, in which Fig. 2 graphically represents this relation of properties as it exists in one particular sample of yarn.
.The finished yarn may be packaged according to any of the conventional forms in which yarn is supplied by employing any standard equipment for transferring the yarn from the spools or bobbins containing the stretched and flexed yarn to the final packages. For example, spooling, capping, skeining, and coning may be readily carried out, and in such operations as coning, where lubricants are required, these may be conveniently applied to the yarn by means of a conditioning roll.
All of the foregoing is directed primarily to the production of textile fibers in which continuous filaments are employed. It is also possible to apply these procedures to the formation of staple fibers, or artificial wool-like masses. The filaments of this invention 'may be used in this manner either in the unstretched or stretched condition, and the shorter filaments, or staple fibers, are particularly desirable for use in conjunction with other types of natural or artificial textile fibers.
The staple fiber produced from unstretched filaments of the type shown herein is particularly useful as a binding agent or stlfiener for Example 1 A vinyl resin resulting from the conjoint polymerization of vinyl chloride with vinyl acetate in such proportions as to produce a resin confirming 87% of the chloride in the polymer was eated by'fractional extraction according to the method of Patent 1,990,685 to free the polymeric aggregate from the lower average macromolecular weight polymers, and to yield a resin having an average macromolecular weight of about 17,- 000. This resin conformed to the following specifications, which are, in general, applicable for determining the suitability of vinyl resins for use in the practice of the invention:
1. Complete dispersibility in warm dry acetone.
2. Average macromolecular weight in excess of 3. Impact strength (Izod notched bar method, A. S. T. M!) not less than 0.32 foot pounds/ piece.
A. S. T. M. specification D-256-32'I, modified in that the test piece is conditioned for 4 hours at 25 C.
4. Tensile strength (Olsen method, A. S. 'I. M.) not less than 9500 pounds/square inch.
5. Plasticity in oil at 140 C. (Scott Plastometer) not greater than 10%.
' 6. Heat distortion point not less than 66 C.
7. Water absorption not greater than 0.30%, at
8. Viscosity (7% solution in methyl isobutyl ketone at 26 C., Ford cup, #4 orifice) not less than 14 seconds.
9. Vinyl chloride content 84.5% to 92%.
This resin in the form of fine powder was dispersed in acetone having a water content of 0.4% to form a dope containing 23% by weight of resin. The dispersion of resin in the solvent was effected at 50 C. by means of a heated doughtype mixer provided with means for slow solvent reflux. At 25 C., the viscosity of the resin dispersion was not measurable by ordinary means. At 50 0., its viscosity was determined as 200,000 centipoises. This dispersion was] filtered in a plate-and-frame filter press, usinga filter pad consisting of-several layers of cheesecloth and 4 oz. cotton batting, followed by several thicknesses of special filtering cloth. An operating pressure of between 250 and 350 pounds per square inch was sufiicient to force the dope through this filter. The material was moved and handled by means of high-pressure gear-type pumps. All of the storage tanks and conduits were jacketed to permit them to be maintained at a temperature of about 50 C. by means of hot water. The filtered dope was de-aerated by allowing it to stand for 48 hours at about 50 C.
The filament extrusion operation was carried for use.
out in a device very similar to those commonly used for the dry-spinning" of other materials. The resin dispersion was fed to the spinning machine by means of metering pumps which discharged to a candle-filter located near the top and within the drying cell proper. Immediately adjacent to the candle-filter was the spinnerette, which was 1.5 inches in diameter, provided with 40 orifices, each having a diameter of 0.06 mm. The drying cell itself was a water-jacketed vertical cylinder 8 inches in inside diameter, provided with a bobbin take-up at its lower end. The effective filament drying space in this cell was about 16 feet in length. The temperature of the water in the drying cell jacket was maintained at C., and heated air, also at 80 C., was admitted to the drying cell at the rate of 5 cubic feet per minute. The air was admitted near the top of the cell at the spinnerette face and directed by means of a cone bailie transverse to the travel of the extruded filaments. The drying air, laden with solvent vapor, was withdrawn from the lower part of the cell by means of a suction pump. The filaments at the bottom of the cell were gathered together through a guide and then wound parallel on a bobbin, the thread crossings and cake build being controlled by the usual equipment. The rate of filament passage through the drying cell was 250 meters per minute, and the filament denier was between 2.5 and 3.0.
After the filaments had been allowed to stand for at least 12 hours on the take-up bobbin, the yarn was twisted by means of a. standard duplex ring twister. The amount of twist imparted was six turns per inch in the yarn. The thread in this operation was delivered to the twisting device from the spinning bobbins immersed in a water bath. As pointed out before, the water picked up by the thread from this bath served both to lubricate the thread and to eliminate static electrical charges.
The twisted yarn was next stretched by immersing the spool on which it was contained in water containing a small amount of the sodium salt of the sulfate ester of a 17 carbon atom branched chain secondary alcohol, which served as a wetting agent. The thread was then guided to a positively driven roll around which it was wrapped a few times to preclude slippage. From this roll the thread was passed upward to a takeup spool, also positively driven, at a sufficiently higher speed to impart a stretch of to the thread. After this operation, the stretch was set in the yarn by immersing it for about 2 hours, while on the take-up spool, in a bath of water heated to about 65 C. Following this treatment, the yarn was given a second stage stretching in the same manner as before, and the extent of stretch was 20% of its length. The total stretch imparted by these two stretching operations thus amounted to about based on the original yarn. The stretching operations were carried out with a thread travel of meters per minute. In the stretching operation, the amount of twist in the yarn and its denier were reduced.
For a. period immediately following the final stretching operation the extended yarn shows a marked tendency toward contraction. This characteristic was controlled as indicated by immersing the spools containing the stretched yarn in water heated to 65 C. for a period of 2 to 3 hours. The final yarn was then coned ready It possessed a wet tenacity of 2.75
grams per denier, with an elongation of 15%.
s m m m u m 5 &3 Wm we mi mw mmwmmmmmm m m m m mm M 37M mmmm wemw mwm wmm mm mm m mmwum m mm mmm m m m m mm mmmwwm mscmmmhmmmmmm a w m.mmmmmm. a%mmmm m mm m mmmmmmmmmxmemia 3 s an E a. w mm mmwwmwmm w WW M MWMM m m mm Ne s M m.mm fi. n wsm mm am mmm mwmmafi mmme N a a M m m W m a w ra h m m m m u mmmwmmmwrmwmmm wwwamm The may be dyed by incorporating dye- M n th take-up stufls in the resin dispersion prior to filament W W extrusion, or it may be dyed, after its formation, a ,1; 65' c, f pu'lod from baths containing mixtures of solvents and and "ed m at non-solvents for the resin which temporarily themmflngmd swelitheyarn. Itcanalsobedyedbymeansof shown in the preceding W of dye-stuiis accordin o s and rd on m; m m given dyeing procedures which are modified slightly as 40 turns per mob from bobbins imto temperature and the us f disp rsine a ents ma th a..- m. for the dye. Some oil-soluble dyes can be applied to the yarn from hydrocarbon baths. pools 0|"III: Asistheusuaipracticewithtextilefiberait m a mm m m istrequently desirable todeluster or dull the fed to the stretching device. The yarn M T1118 m be complished by incorpora z Mmwdrlvenron pigmentssuchastitaniumdioxideofsmallparin a m mm heated t 90- c ticie size in the resin dispersion, and the degree The m m mm to the m betmn oi delusterization can be controlled by variation of the particle size of the pigment and the 0 Med 5 The m amount used. It is preferable to achieve the deot the yarn in the stretching operation agm The M m then involve the incorporation of other substances in the filaments. As shown above, this may be eftectively done by treatment of the filaments with u heated water at their point of formation, coupled with the additional delustering eflected by m the softness, elasticity and tensile strength of the m uniform the 801m and yarn. The application of water heated above 50' C. to the filaments as they leave the spinning cell causes the fibers, when viewed under the microscope, to have a slightly roughened or scaly exterior. This surface modification of the fibers 05 is highly desirable, and is a further instance of the manner in which the properties of the new fibers of this invention resemble those of natural fibers.
This yarn lends itself readily to all ordinary 70 The yarn in the foregoing examples textile processing, and it can be knitted, woven, braided and plaited readily. It is especially well fllemierlotthisinvmflomcneoi'themost adaptedtoknittingoperationaandtestshave ori'whichisthehightrueelasticity shownthatitispossibletoobtainamuchtightottheyarn. 'lhepracticalvalueotthenewfiben 'erstltch without thread rupturethanisthe case 1 WWW thattheyarnwas setintheyarnbylmmersingthespoolscontainu ingitinwaterheatedtoBfa'CJoraperiodot about 3 hours. Theresultingyarn had a wet handotthestretchedyarmitwassubjectedtoa moperationinwhichtheyarniromthe stretchertake-upspoolswasathighspeed 5 aroundaaeriesotsmallrollersoperatingimder waterandarrangedtocuisetheyarntochange direcflmthroughasharpangleninetimeaaiter whichitpassedtotake-upbobbins. Following thisopentimtheyarnwasconedandpackaged toruse.
posaeesedthetypicaipmpm'tiesotthenewtexmentl-waaprecluded. The bobbinswaathenm'eparedfor of hours.
thisrollandasecondrolldrivenatahigherspeed with previously known yarns. In weaving it may be used either as filling, warp or pile. It is desirable to carry out weaving operations with this yarn'under conditions of high relative humidity in order to reduce the development of static electrical charges. Due to the unusual resistance of the yarn to water, it can be' woven while wet without sacrificing strength or risking thread breakage or undue stretching. In weaving, hygroscopic warp sizing should be used which will form a pliable film on the thread.
If the yarn after being stretched is not subjected to a. stretch-setting treatment, it shows a tendency toward shrinkage which is variable in degree according to the temperature to which it is subjected. In general, this tendency towards shrinkage in the unset yarn varies according to the table below:
Tempera- Shrinkage, ture, C, percent Where this contraction amounts to as much as 10%, a reduction in luster accompanies it. Shrinkage of the yarn also results in reduction in tenacity and an increase in elongation proportional to the extent of the stretch which is lost. After the yarn has shrunk as a result of being subjected to elevated temperatures, it no longer shows any tendency toward contraction when reheated to the same or a lower temperature. This shrinkage of the unset stretched yarn can be utilized in manyapplications of the yarn to tighten the stitch in knitted or woven materials and thereby to prevent "laddering or thread slippage.
The yarn can be produced in many filament sizes, and it has been determined that the filament denier which most conveniently lends itself to the processes of textile manufacture is aroun 1.0 to 1.5.
The unusual propertiesof the new yarn make possible many applications which take advantage of its remarkable true elasticity, waterresistance and high wet strength, together with its resistance to attack by chemical influences or micro-organisms. For example, it is of value in industrial filtering fabrics; in fishing lines, nets and seines; in forming acidand alkali-resistant clothing; protective pipe coverings; electrical insulation; shower curtains; bathing suits; waterproof clothing; fire-proof awnings and curtains; hosiery; fusible shape-retaining fabrics; and, in admixture with other textile materials, mixed fabrics for obtaining cross-dyeing eiiects and the like. The new yarn is useful in pile fabrics such as velvet, and it can be advantageously employed as either the backing or the pile or both. The staple fibers of this invention, in admixture with natural materials such as cotton and wool, make possible the production of fabrics which will retain a pressed fold, and improve mercerlzing and l. Textile fiber composed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which contains from about 80% to 95% by weight of the halide in the polymer and which has an average macromolecular weight of at least 15,000.
2. Textile fiber composed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which has an average macromolecular weight of at least 15,000 and which is substantially free from lower molecular weight polymers.
3. Textile fiber composed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which has an average macromolecular weight of at least 15,000 and which is substantially free from lower molecular weight polymers, said resin being completely dispersible in warm dry acetone and having a heat distortion point above 65 C.
4. Textile fiber composed of a vinyl resin substantially identical with a resin resultingfrom the conjoint polymerization of vinyl chloride with vinyl acetate, which contains from about to by weight of the chloride in the polymer and which has an average macromolecular weight of at least 15,000, said resin having a heat distortion point above 65 C. and being completely dispersible in acetone containing less than 0 0% by weight of water at about 50 C.
5. A textile fiber formed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which contains from about 85% to about 90% by weight of the halide in the polymer and which has an average macromolecular weight of at least 15,000,
said fiber being characterized by resistance to deterioration in strength on exposure to ultraviolet light, and by water-resistance, non-inflammability, immunity to attack by bacteria and fungi, and resistance to alkalies and mineral acids,
6. Staple textile fiber formed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which contains from about 85% to about 90% by weight of the halide in the polymer and which has an average macromolecular weight of at least 15,000, said fiber being characterized by resistance to deterioration in strength on exposure to ultra-violet light, and by water-resistance, thermoplasticity, non-infiammability, immunity to attack by bacteria and fungi, and resistance to alkalies and mineral acids.
7. A textile fiber formed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which contains from about 85% to about 90% by weight of the halide in the polymer and which has an average macromolecular weight of at least 15,000, said fiber being characterized by true elasticity, high strength, resistance to deterioration in strength on exposure to ultra-violet light, and by waterresistance, non-infiammability, immunity to attack by bacteriaand fungi, and resistance to alkalies and mineral acids.
8. Synthetic textile yarn formed of filaments composed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerall-elongation of from 10% to 35%.
0.8ynthetictextileyarniormedoifiiaments eunposed ct a'vinylresin identical 10 witharesinresultingtruntheconjdntpolymerimtkmoiavlnyihalidewithavinylesterofan aliphatic acid, which contains fromabcut 80% to%byweightofthehalideinthepolymerand whichhasanaveragemacrcmolecularweightoi ii atleastl5,000,saidyarnhavingatenadty oiat least2.0gramsperdenierandanelongationof from to% and whichhasbeeninitially stretchedtotheextentoibetween'l5%and200%.
4o cous and slowly fiowable at a temperature of 12. Knitted fabrics or articles comprising yarn 'iormedotfilamentsotavinylrminmbstantially identical with a resin resulting from the conjoint polymer-laden oiavinylhalidewithavinylester of an aliphatic acid, which contains from about 00%to05% byweightoi thehaiideinthepo ymet and which has an average macromolecular weight of at least 15,000, saidyarn having been stretchedbetween'fi'ltandmit.
18. Woven iabrlcs or articles comprising yarn iormedoifilammtsotavinylresin identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, which contains from about80% to9fi%byweightoithehalideinthe polymer and which has an average macromolecularweightofatleastl5,000,saidyarnhaving been stretched betwem and 200%.
14. Pile fabrics or articles in which the pile is oiyarniormedotfilamentsoi avinyl resin substantially identical with a resin resulting from the conjoint polymerization 01 a vinyl halide with a vinyl ester 0! an aliphatic acid, which containsiromabout% to% byweightoithe halideinthepolymerandwhichhasanaverage macromolecular weight of at least 15,000, said yaan having been stretched between 75% and l5. Braided articles, lines and cords comprising yarn formed of filaments of a vinyl resin substantially identical with a resin resulting from the conjoint H H ofavinylhalidewitha vinyl ester of an aliphatic acid, which contains from about 50% to 95% by weight of the halide in the polymer and which has an average macromolecular weight 01' at least 15,000, said yarn having been stretched between 75% and 200%.
16. Synthetic textile fibers, fabrics and articles comprising yarn composed of filaments formed of a vinyl resin substantially identical with a resin resulting from the conjoint polymerization of a vinyl halide with a vinyl ester of an aliphatic acid, said resin containing from about 80% to about 95% by weight 01' the vinyl halide in the polymer and having an average macromolecular weight of at least 15,000, said yarn having been stretched to the extent of from 75% to 200% and being characteried by high tensile strength in the wet state, hig true elasticity, controllable shrinkage, w 1 to water, alkalies and mineral acids, to attack by bacteria and fungi, non-bill crease resistance, thermoplasticity, electrical insulating qualities, controllable luster, and high flexibility.
EDWARD w. RUGELEY. THEOPHILUS A. mm), JR. JOHN F. cormon.
D ISCLAI MER 2,161,766.Ed1m'rd W. Bugclcy, flcophilus A. Fel'ld, Jr., and John F. Co'nlo'n, Charleston, W. Va.
hon
Sm-nnmc Fmnn. filed July 22, 1946, by the ac,
Patent dated June 6, 1939. Disclaimer Gdrb'ide and Carbon Chemicals Corpora- Hereby enters this to claims 1 to 6 inclusive, and claim 11 in the said specification.
lofici l Gazette A 20, 1946.]
US16400237 1937-09-15 1937-09-15 Synthetic fiber Expired - Lifetime US2161766A (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
US16400237 US2161766A (en) 1937-09-15 1937-09-15 Synthetic fiber
FR842532D FR842532A (en) 1937-09-15 1938-08-24 Synthetic textile fiber, process for manufacturing it and its applications
BE429899D BE429899A (en) 1937-09-15 1938-08-25
GB2881139A GB518710A (en) 1937-09-15 1938-08-27 Improvements in synthetic filaments, fibres and articles made therefrom
GB2519438A GB518555A (en) 1937-09-15 1938-08-27 Improvements in synthetic filaments, fibres and articles made therefrom
US24047638 US2353270A (en) 1937-09-15 1938-11-15 Process for forming synthetic fibers
GB3046339A GB537583A (en) 1937-09-15 1939-11-21 Improvements in composite materials made from vinyl resins
FR52401D FR52401E (en) 1937-09-15 1939-12-02 Synthetic textile fiber, process for manufacturing it and its applications
GB1203740A GB541261A (en) 1937-09-15 1940-07-23 Improvements in and relating to the production of crimped threads or filaments

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US16400237 US2161766A (en) 1937-09-15 1937-09-15 Synthetic fiber

Publications (1)

Publication Number Publication Date
US2161766A true US2161766A (en) 1939-06-06

Family

ID=35431062

Family Applications (2)

Application Number Title Priority Date Filing Date
US16400237 Expired - Lifetime US2161766A (en) 1937-09-15 1937-09-15 Synthetic fiber
US24047638 Expired - Lifetime US2353270A (en) 1937-09-15 1938-11-15 Process for forming synthetic fibers

Family Applications After (1)

Application Number Title Priority Date Filing Date
US24047638 Expired - Lifetime US2353270A (en) 1937-09-15 1938-11-15 Process for forming synthetic fibers

Country Status (4)

Country Link
US (2) US2161766A (en)
BE (1) BE429899A (en)
FR (2) FR842532A (en)
GB (4) GB518555A (en)

Cited By (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2418507A (en) * 1944-08-16 1947-04-08 Carbide & Carbon Chem Corp Production of spinnable vinyl resin compositions
US2420565A (en) * 1943-02-20 1947-05-13 Carbide & Carbon Chem Corp Synthetic textile articles
US2433531A (en) * 1940-07-30 1947-12-30 Kendall & Co Milk filter
US2436204A (en) * 1944-02-25 1948-02-17 Pro Phy Lac Tie Brush Company Copolymers comprising acrylonitrile and vinyl ethers and molecularly oriented articles composed thereof
US2438968A (en) * 1943-03-04 1948-04-06 Carbide & Carbon Chem Corp Production of textile filaments, fibers, and yarns
US2440487A (en) * 1943-09-04 1948-04-27 Western Electric Co Corrosion resistant filter
US2445042A (en) * 1943-07-28 1948-07-13 Du Pont Method of treating oriented acrylonitrile structures
US2462927A (en) * 1943-11-06 1949-03-01 Du Pont Artificial filaments and yarn
US2468165A (en) * 1943-10-22 1949-04-26 Bakelite Corp Resin covered wire or cable and method of making
US2489966A (en) * 1945-05-21 1949-11-29 Upjohn Co Infusion device
US2505707A (en) * 1944-12-21 1950-04-25 Wilmington Trust Company Shock absorbing method and apparatus for air pickup systems and the like
US2517581A (en) * 1950-08-08 Method of dehensionaijly stabilizing
US2532991A (en) * 1946-02-08 1950-12-05 Braun William Lewis Carroting brush and method of carroting fur on a skin with said brush
US2539301A (en) * 1949-07-15 1951-01-23 Us Rubber Co Woven glass fabric and method of making same
US2596128A (en) * 1949-10-17 1952-05-13 Chavannes Synthetic Fibres Inc Method and apparatus for producing fine fibers
US2615477A (en) * 1948-03-18 1952-10-28 American Viscose Corp Filter media
US2635942A (en) * 1949-04-27 1953-04-21 Sandoz Ag Dyeing materials made of polyvinyl derivatives
US2636804A (en) * 1950-02-04 1953-04-28 Du Pont Process of treating polyvinyl alcohol fibers
US2636803A (en) * 1950-02-04 1953-04-28 Du Pont Polyvinyl alcohol fibers and process of treating
US2637893A (en) * 1949-03-12 1953-05-12 Shaw Gilbert Artificial filament
US2670267A (en) * 1950-05-02 1954-02-23 Du Pont Heat-treatment of n-alkyl polyamides
US2692875A (en) * 1949-06-17 1954-10-26 Allied Chem & Dye Corp Methacrylonitrile-acrylonitrile copolymers and fibers thereof
US2699593A (en) * 1951-12-07 1955-01-18 Firth Carpet Company Inc Pile fabric and method of making same
US2715763A (en) * 1950-06-27 1955-08-23 American Viscose Corp Synthetic textile fiber
US2754578A (en) * 1951-08-03 1956-07-17 Magee Carpet Co Pile fabric and method of making same
US2795888A (en) * 1953-10-01 1957-06-18 Garland Ventilator Corp Receptacle for live fish
US2821457A (en) * 1958-01-28 Method of heat stabilizing polyethyl-
US2821771A (en) * 1957-04-05 1958-02-04 F C Huyck & Sons Method of making a papermaker's felt
US2836509A (en) * 1954-10-08 1958-05-27 Berry Kenneth Ollerenshaw Stretchable plastic-coated fabric and method of making the same
US2870454A (en) * 1954-10-04 1959-01-27 Florence J Schippert Swimming pool cover
US2877084A (en) * 1955-10-14 1959-03-10 Dow Chemical Co Method for heat treating oriented fibers of blended polyvinyl chloride polymers and cellulose acetate and products produced thereby
US2895171A (en) * 1957-03-22 1959-07-21 Ici Ltd Production of films from polymeric materials
US2916038A (en) * 1954-02-23 1959-12-08 American Viscose Corp Tobacco smoke filter
US2999413A (en) * 1959-02-26 1961-09-12 Momoi Kazuo Process of making a fishing net
US3036026A (en) * 1957-02-28 1962-05-22 Montedison Spa Spinning solutions of polyvinyl chloride in mixtures of trichloroethylene and nitromethane
US3092891A (en) * 1958-08-01 1963-06-11 Montedison Spa Production of monofilaments obtained from highly viscous alpha-olefin polymers
US4529768A (en) * 1982-04-01 1985-07-16 Rhovyl Solutions based on polyvinyl chloride, the process for their preparation and yarns and fibres thus obtained
US20090151214A1 (en) * 2007-12-12 2009-06-18 The Otis Patent Trust Gun cleaning tool kit

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR913924A (en) * 1942-08-24 1946-09-24 Rhodiaceta Process for the manufacture of superchlorinated polyvinyl chloride yarns or filaments
US2423182A (en) * 1943-04-29 1947-07-01 Du Pont Method of cold-drawing tapered filaments
DE962633C (en) * 1947-09-04 1957-04-25 American Cyanamid Co Process for the production of shaped structures from thermoplastic polymerization products
BE493893A (en) * 1947-09-04
US2558731A (en) * 1947-09-04 1951-07-03 American Cyanamid Co Method of producing synthetic fibers from polymers and copolymers of acrylonitrile
US2712490A (en) * 1950-06-22 1955-07-05 Rhodiaceta Process for spinning swollen polyvinyl chloride
US2677591A (en) * 1950-07-07 1954-05-04 Du Pont Removal of porosity in wet-spun acrylonitrile filaments by pressing against a hot surface
US2677590A (en) * 1950-07-07 1954-05-04 Du Pont Removal of porosity in wet-spun acrylonitrile filaments by treatment with heated fluids
US2679450A (en) * 1951-04-11 1954-05-25 British Celanese Manufacture of textile materials
US2713547A (en) * 1952-08-08 1955-07-19 Edward R Frederick Simulated down filler and method of making the same
US2970124A (en) * 1953-10-14 1961-01-31 Folsom E Drummond Plastic cement composition for lightweight ceramic tile
GB1092321A (en) * 1963-07-30 1967-11-22 British Ropes Ltd Improvements in or relating to strands, ropes or cores of plastic monofilaments
CA2122548A1 (en) * 1993-05-25 1994-11-26 George M. Kent Reinforcing composite items with composite thermoplastic staple fibers

Cited By (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2517581A (en) * 1950-08-08 Method of dehensionaijly stabilizing
US2821457A (en) * 1958-01-28 Method of heat stabilizing polyethyl-
US2433531A (en) * 1940-07-30 1947-12-30 Kendall & Co Milk filter
US2420565A (en) * 1943-02-20 1947-05-13 Carbide & Carbon Chem Corp Synthetic textile articles
US2438968A (en) * 1943-03-04 1948-04-06 Carbide & Carbon Chem Corp Production of textile filaments, fibers, and yarns
US2445042A (en) * 1943-07-28 1948-07-13 Du Pont Method of treating oriented acrylonitrile structures
US2440487A (en) * 1943-09-04 1948-04-27 Western Electric Co Corrosion resistant filter
US2468165A (en) * 1943-10-22 1949-04-26 Bakelite Corp Resin covered wire or cable and method of making
US2462927A (en) * 1943-11-06 1949-03-01 Du Pont Artificial filaments and yarn
US2436204A (en) * 1944-02-25 1948-02-17 Pro Phy Lac Tie Brush Company Copolymers comprising acrylonitrile and vinyl ethers and molecularly oriented articles composed thereof
US2418507A (en) * 1944-08-16 1947-04-08 Carbide & Carbon Chem Corp Production of spinnable vinyl resin compositions
US2505707A (en) * 1944-12-21 1950-04-25 Wilmington Trust Company Shock absorbing method and apparatus for air pickup systems and the like
US2489966A (en) * 1945-05-21 1949-11-29 Upjohn Co Infusion device
US2532991A (en) * 1946-02-08 1950-12-05 Braun William Lewis Carroting brush and method of carroting fur on a skin with said brush
US2615477A (en) * 1948-03-18 1952-10-28 American Viscose Corp Filter media
US2637893A (en) * 1949-03-12 1953-05-12 Shaw Gilbert Artificial filament
US2635942A (en) * 1949-04-27 1953-04-21 Sandoz Ag Dyeing materials made of polyvinyl derivatives
US2692875A (en) * 1949-06-17 1954-10-26 Allied Chem & Dye Corp Methacrylonitrile-acrylonitrile copolymers and fibers thereof
US2539301A (en) * 1949-07-15 1951-01-23 Us Rubber Co Woven glass fabric and method of making same
US2596128A (en) * 1949-10-17 1952-05-13 Chavannes Synthetic Fibres Inc Method and apparatus for producing fine fibers
US2636803A (en) * 1950-02-04 1953-04-28 Du Pont Polyvinyl alcohol fibers and process of treating
US2636804A (en) * 1950-02-04 1953-04-28 Du Pont Process of treating polyvinyl alcohol fibers
US2670267A (en) * 1950-05-02 1954-02-23 Du Pont Heat-treatment of n-alkyl polyamides
US2715763A (en) * 1950-06-27 1955-08-23 American Viscose Corp Synthetic textile fiber
US2754578A (en) * 1951-08-03 1956-07-17 Magee Carpet Co Pile fabric and method of making same
US2699593A (en) * 1951-12-07 1955-01-18 Firth Carpet Company Inc Pile fabric and method of making same
US2795888A (en) * 1953-10-01 1957-06-18 Garland Ventilator Corp Receptacle for live fish
US2916038A (en) * 1954-02-23 1959-12-08 American Viscose Corp Tobacco smoke filter
US2870454A (en) * 1954-10-04 1959-01-27 Florence J Schippert Swimming pool cover
US2836509A (en) * 1954-10-08 1958-05-27 Berry Kenneth Ollerenshaw Stretchable plastic-coated fabric and method of making the same
US2877084A (en) * 1955-10-14 1959-03-10 Dow Chemical Co Method for heat treating oriented fibers of blended polyvinyl chloride polymers and cellulose acetate and products produced thereby
US3036026A (en) * 1957-02-28 1962-05-22 Montedison Spa Spinning solutions of polyvinyl chloride in mixtures of trichloroethylene and nitromethane
US2895171A (en) * 1957-03-22 1959-07-21 Ici Ltd Production of films from polymeric materials
US2821771A (en) * 1957-04-05 1958-02-04 F C Huyck & Sons Method of making a papermaker's felt
US3092891A (en) * 1958-08-01 1963-06-11 Montedison Spa Production of monofilaments obtained from highly viscous alpha-olefin polymers
US2999413A (en) * 1959-02-26 1961-09-12 Momoi Kazuo Process of making a fishing net
US4529768A (en) * 1982-04-01 1985-07-16 Rhovyl Solutions based on polyvinyl chloride, the process for their preparation and yarns and fibres thus obtained
US20090151214A1 (en) * 2007-12-12 2009-06-18 The Otis Patent Trust Gun cleaning tool kit
WO2009076257A1 (en) * 2007-12-12 2009-06-18 The Otis Patent Trust Gun cleaning tool kit

Also Published As

Publication number Publication date
GB518555A (en) 1940-02-29
FR52401E (en) 1944-04-13
US2353270A (en) 1944-07-11
BE429899A (en) 1938-09-30
GB537583A (en) 1941-06-27
FR842532A (en) 1939-06-14
GB518710A (en) 1940-03-05
GB541261A (en) 1941-11-19

Similar Documents

Publication Publication Date Title
US2161766A (en) Synthetic fiber
US2420565A (en) Synthetic textile articles
US2715763A (en) Synthetic textile fiber
US4153660A (en) Process for producing a mixed-shrinkage heat-bulkable polyester yarn
US2852333A (en) Viscose spinning process
US2663989A (en) Coated articles and textiles and emulsions for producing them
DE2510361C2 (en) Process for making a polyamide yarn
US2277782A (en) Crimping materials containing synthetic textile fibers
US2312152A (en) Rayon and method of manufacturing same
US2558735A (en) Method of forming dyed shaped articles from acrylonitrile polymerization products
US3214899A (en) Cordage product
US2666038A (en) Textile-finishing compositions, finished articles, and methods of producing them
DE2534234A1 (en) MANUFACTURING TEXTURED POLYESTER YARN
US2249745A (en) Cellulosic structures and method of producing same
EP0529506B1 (en) Paper-machine felt and method of making the same
US3057038A (en) Wet spun cellulose triacetate
US2436978A (en) Reinforcing cord and process of manufacture
US2438968A (en) Production of textile filaments, fibers, and yarns
US3846532A (en) Continuous spinning and stretching process of the production of polyamide-6 filaments
DE3508955C2 (en) Process for high-speed spinning and drawing of synthetic yarns
US3120095A (en) Method of making high bulk yarns
EP0173200B2 (en) High-strength filaments for a sewng-yarn, and process for manufacturing those filaments
US2202031A (en) Method of treating yarn
US3549741A (en) Process for preparing improved carpet yarn
US2339408A (en) Manufacture of artificial materials