US2674025A - Polymeric filaments - Google Patents

Polymeric filaments Download PDF

Info

Publication number
US2674025A
US2674025A US110372A US11037249A US2674025A US 2674025 A US2674025 A US 2674025A US 110372 A US110372 A US 110372A US 11037249 A US11037249 A US 11037249A US 2674025 A US2674025 A US 2674025A
Authority
US
United States
Prior art keywords
filaments
core
nozzle
tin
polymeric
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
US110372A
Inventor
Ladisch Rolf Karl
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.)
Texiclon Corp
Original Assignee
Texiclon 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
Application filed by Texiclon Corp filed Critical Texiclon Corp
Priority to US110372A priority Critical patent/US2674025A/en
Application granted granted Critical
Publication of US2674025A publication Critical patent/US2674025A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F8/00Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
    • 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
    • Y10T428/2933Coated or with bond, impregnation or core
    • Y10T428/2935Discontinuous or tubular or cellular core
    • 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
    • Y10T428/2933Coated or with bond, impregnation or core
    • Y10T428/294Coated or with bond, impregnation or core including metal or compound thereof [excluding glass, ceramic and asbestos]
    • 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
    • Y10T428/2973Particular cross section
    • Y10T428/2976Longitudinally varying

Definitions

  • Filaments of this nvention may be matted together to form lightweight polymeric wools having improved characteristics or after twisting to make a yarn may be woven or knitted to make textile-like articles for many different uses.
  • filaments are formed by melt-spraying with the aid of a particular type of nozzle, to form filaments consisting essentially of polymerc tubular envelopes whose walls enclose cores which may be metallic or non-metallic, but which always constitute an important part of the mass of the filamnt, and may constitute a major part thereof.
  • cores may be of substantially uniform diameter throughout the length of the filament or may be of varying diameter, but in all 0bserved cases the walls of the filaments are free from the bulges or swellings which are disclose d in my Patent No. 2,571,457 dated October 16, 1951, and claimed in a divisional application now Patent No. 2612,679 dated October 7, 1952.
  • Patent No. 2,233344; and the Spanagel Patent Filaments made pursuant to the invention may be of increased resilience and flexibility.
  • Fig. 1 is a cross section through the preferred form of nozz1e used in forming the filaments
  • Fig. 2 is a photomcrograph Of, a number of sec. 266) polyvinyl acetate filamerits combined with selenium;
  • Fig. 3 is a similar view of two cellulose propionate and tin fibers.
  • Fig. 4 is a similar view showing in great1y en-" larged cross section two cellulose proponate filaments with so1id cores of metallic tin.
  • the nozzle there shown is similar to the nozzle of German Patent No. 411,948 and corresponding U. S. Patent No. 1,811,637 issued to Carl Ladisch on June 23, 1931. It comprises a straight, central tube through which the hereinafter defined polymeric mixture flows, and a frusto-conical body H with conical internal wal1s 12 and an open end I 3.
  • a coupling I5 connects a gas discharge pipe [6 to the nozzle; usually the gas led to the nozzle will be air (or where a non-oxidizing gas must be used nitrogen, helium, producer gas, steam, etc.
  • the nozzle may be einployed), and such gas will be heated if the polymer is being melts ptayedij
  • the gas enters the nozzle at its 1arger end through a port I'I, flowng under sperat mospheric pressure in a taigential path and then in a, spiral path with constantiy increasing velocity due to the decreasing diameter of the ndzzle, until finally it emerges as a spiral or whirling jet through the narrow annular space between the tube
  • orienng thgas r vapor continues to flow in a contracting spiral pathat constantly increasing veiocity until -it feaches a point (marked Vertex) which is the apex of the cone of the nternal walls 12 of the nozzle.
  • Vertex the apex of the cone of the nternal walls 12 of the nozzle.
  • the formation of the fi1aments takes p1ace at and near this Vertex.
  • polymeric mixture denotes a single polymer or copolymer with or without a plasticizer or a plurality of physically mixed polymers and copolymers. Obviously the polymeric mixture must be such that it will not deeompose under the conditions of heat and. pressure necessary to form the filaments.
  • polystyrene, polydichlorostyrene, polyamides of the nylon type polyacrylonitrile, polymethacrylonitrile, polymethyl methacrylate, polymethyl acrylate, polyvinylidene chloride, polyvinyl chloride, polyvinyl carbazole, polyvinyl alcohol, polymeric glycol terephthalate, cellulose acetate, cellulose propionate, cellulose acetate butyrate, cellulose nitrate, ethyl cellulose, polyethylene, halogenated polyethylenes, polybutene, polyisobutylene, polyvinyl butyral, polyvinyl acetate and silicones.
  • gas as usecl herein includes gaseous mixtures such as air, also vapors such as steam.
  • powdered metal or other powdered solids are added prior to the feeding of said mixture to the nozzle.
  • molten metals of low melting point such as tin, metalloids, such as selenium, and low melting alloys such as soft selder, Roses metal, Newtons metal and Woods metal may be added to the molten polymerio mixture. Due primarily to the descrioed nozzle construction, relatively large amounts, as much as 80%, may be added without running the risk of clogging the nozzle. In other words, the described nozzle makes possible onthe first time the orming of filaments heavily laden with a metallic or metalloidal content, so that the filaments are more pronouncedly metallic (or metalloiclal) than polymeric.
  • Each fiber however consisted of a continuous thin tubular envelope surrounding the metalloidal core.
  • the mixing of polyvinyl acetate with molten selenium in a 5--5O oy volume ratio results in a homogeneous viscous mixture at 240 C. which readily orrns filaments, again with the metalloid orming a core sheathed by the resin.
  • Fig. 3 shows the ends of two cellulose propionate fibers containng tin cores, enlargecl 85 times.
  • Cellulose prcpicnate (Fortcel 28102) wa mixed. with tin powcler passing a. 325 mesh sieve, and the mixture was sprayed with a nozzle pressure of p. s. 1. and 3 p. s. i. pressure in the inner tube 19.
  • Temperatures were 250 C. in the inner tube and. 2'70 C. for the compressed air. While part of the mixture left the Vertex in the form of plan polymeric fibers ancl separate tin pellets,
  • tin cores were not continuous out varied in diameter (as Fig. 3 shows) as well as in length, some being as short as 2 mm., others beng measured as 50 mm. long.
  • Fig. 4 shows in section solid tin cores which are a major part of the fibers, but in some sections the tin cores were so small that they could only be seen under the microscope, after dissolving away the polymeric envelope with methyl acetate. Microscopic examination failed to disclose a single tin fiber ree from a surrounding polymer.
  • Artificial filaments each consisting of a resincus polymeric mixture forming a generally tubular envelope with unbroken walls and nonuniorm thickness, and at least one core within said envelope forming a major fraction of the mass of the filament and being of a material selectedirom the group consisting of all metals, metalloids and alloys which are molten at the temperature of formation of the filaments and which form at least one solid core in the filaments, said core being of irregular but substantially circular cross section which varies non-uniformly in diameter along ts length and which also varies in its position within the envelope.

Description

R. K. LADISCH POLYMERIC F'ILAMENTS F1led Aug 15 1949 pril 6, 1954 Patented Apr. 6, 1954 POLYMERIC FILAMENTS Rolf Karl Ladisch, Drexel Hill, Pa., assignor to Texiclon Corporation, poraton of Delaware Wilmington, Del., a cor- Application August 15, 1949, Serial No. 110,372 5 Claims. 01. 2ss2) (Granted under Title 35, U. S. Code (1952),
and Method of. Making the Same," Ser. No.
89,776 filed April 26, 1949. Filaments of this nvention may be matted together to form lightweight polymeric wools having improved characteristics or after twisting to make a yarn may be woven or knitted to make textile-like articles for many different uses.
In accordance with the present invention, filaments are formed by melt-spraying with the aid of a particular type of nozzle, to form filaments consisting essentially of polymerc tubular envelopes whose walls enclose cores which may be metallic or non-metallic, but which always constitute an important part of the mass of the filamnt, and may constitute a major part thereof. These cores may be of substantially uniform diameter throughout the length of the filament or may be of varying diameter, but in all 0bserved cases the walls of the filaments are free from the bulges or swellings which are disclose d in my Patent No. 2,571,457 dated October 16, 1951, and claimed in a divisional application now Patent No. 2612,679 dated October 7, 1952.
I am aware it is 01d as proposed in the Gardner Patent No. 1692,372, dated November 20, 1928, to
mix a salt oroXide of titanium with artificial silk prior to spinning to delusterize the filaments. Other p'ate'nts suggesting the addition of various salts' and pigments to filaments are the Tay1or Patent No. 2,034,008; the Helm et al.
Patent No. 2,233344; and the Spanagel Patent Filaments made pursuant to the invention may be of increased resilience and flexibility. The electrostatic, electro-conductive, magnetic and insulating qualities and the weight, feel,
curlness and other physical characteristics of filaments may be materially changed by following the invention, to eiect considerable improvements over filaments made from the pure polymer with or without a plasticizer.
In the accompanying drawings forming a part of this specification- Fig. 1 is a cross section through the preferred form of nozz1e used in forming the filaments;
Fig. 2 is a photomcrograph Of, a number of sec. 266) polyvinyl acetate filamerits combined with selenium;
Fig. 3 is a similar view of two cellulose propionate and tin fibers; and
Fig. 4 is a similar view showing in great1y en-" larged cross section two cellulose proponate filaments with so1id cores of metallic tin.
Referrihg to Fig. 1, the nozzle there shown is similar to the nozzle of German Patent No. 411,948 and corresponding U. S. Patent No. 1,811,637 issued to Carl Ladisch on June 23, 1931. It comprises a straight, central tube through which the hereinafter defined polymeric mixture flows, and a frusto-conical body H with conical internal wal1s 12 and an open end I 3. The end of tube |0 projects slght1y beyond the end of the frusto-conical body Il and is beveled as indicated at I4, the arrangement being such that the projecting beveled end of tube !0 does not in any way interfere with or defiect the flow of gas or vapor from the open end !3 of the conical body. A coupling I5 connects a gas discharge pipe [6 to the nozzle; usually the gas led to the nozzle will be air (or where a non-oxidizing gas must be used nitrogen, helium, producer gas, steam, etc. may be einployed), and such gas will be heated if the polymer is being melts ptayedij The gas enters the nozzle at its 1arger end through a port I'I, flowng under sperat mospheric pressure in a taigential path and then in a, spiral path with constantiy increasing velocity due to the decreasing diameter of the ndzzle, until finally it emerges as a spiral or whirling jet through the narrow annular space between the tube |0 and the open end I3 of the 1ozzle. Beyond the discharge orienng thgas r vapor continues to flow in a contracting spiral pathat constantly increasing veiocity until -it feaches a point (marked Vertex) which is the apex of the cone of the nternal walls 12 of the nozzle. At this point theoretically the velocity becomes infinite, but actually, due to air friction and other causes, is a finite figure of supersonic velocity, that is, higher than the velocity of sound in air at sea 1eve1. The formation of the fi1aments takes p1ace at and near this Vertex.
The term polymeric mixture, as used above and elsewhere in this specification, denotes a single polymer or copolymer with or without a plasticizer or a plurality of physically mixed polymers and copolymers. Obviously the polymeric mixture must be such that it will not deeompose under the conditions of heat and. pressure necessary to form the filaments. Among the polymers and copolymers which may be used are: polystyrene, polydichlorostyrene, polyamides of the nylon type, polyacrylonitrile, polymethacrylonitrile, polymethyl methacrylate, polymethyl acrylate, polyvinylidene chloride, polyvinyl chloride, polyvinyl carbazole, polyvinyl alcohol, polymeric glycol terephthalate, cellulose acetate, cellulose propionate, cellulose acetate butyrate, cellulose nitrate, ethyl cellulose, polyethylene, halogenated polyethylenes, polybutene, polyisobutylene, polyvinyl butyral, polyvinyl acetate and silicones. 'I'he term gas as usecl herein includes gaseous mixtures such as air, also vapors such as steam.
To mixtures or mixed melts of the selected polymeric mixture, powdered metal or other powdered solids are added prior to the feeding of said mixture to the nozzle. In lieu of powdered metals, molten metals of low melting point such as tin, metalloids, such as selenium, and low melting alloys such as soft selder, Roses metal, Newtons metal and Woods metal may be added to the molten polymerio mixture. Due primarily to the descrioed nozzle construction, relatively large amounts, as much as 80%, may be added without running the risk of clogging the nozzle. In other words, the described nozzle makes possible onthe first time the orming of filaments heavily laden with a metallic or metalloidal content, so that the filaments are more pronouncedly metallic (or metalloiclal) than polymeric.
When selenium (80% by weight) was added to polyvinyl acetate (Mowilith 30), it was in finely dividecl form, passing through a "250 mesh sieve. The nozzle temperature was 240 0., and the air pressure was 20 p. s. i. The. filaments ormed (Fig. 2) had a volume per weight ratio of 23 and. a diameter ranging from 1 to 18 microns. Fig. 2 (magnification 90X) is only an approximation of a few of the fibers forming a curly, tangled mass. The selenium was such a large part of the fiocrs that it impartecl a dark brown appearance and gave a rather harsh feel to them, besides making them quite brittle. Each fiber however consisted of a continuous thin tubular envelope surrounding the metalloidal core. The mixing of polyvinyl acetate with molten selenium in a 5--5O oy volume ratio results in a homogeneous viscous mixture at 240 C. which readily orrns filaments, again with the metalloid orming a core sheathed by the resin.
Fig. 3 shows the ends of two cellulose propionate fibers containng tin cores, enlargecl 85 times. Cellulose prcpicnate (Fortcel 28102) wa mixed. with tin powcler passing a. 325 mesh sieve, and the mixture was sprayed with a nozzle pressure of p. s. 1. and 3 p. s. i. pressure in the inner tube 19. Temperatures were 250 C. in the inner tube and. 2'70 C. for the compressed air. While part of the mixture left the Vertex in the form of plan polymeric fibers ancl separate tin pellets,
a considerable percentage of plastic fibers with tin cores were ormed. These tin cores were not continuous out varied in diameter (as Fig. 3 shows) as well as in length, some being as short as 2 mm., others beng measured as 50 mm. long. Fig. 4 (magnification 625X) shows in section solid tin cores which are a major part of the fibers, but in some sections the tin cores were so small that they could only be seen under the microscope, after dissolving away the polymeric envelope with methyl acetate. Microscopic examination failed to disclose a single tin fiber ree from a surrounding polymer.
Reference should be made to Patent No.
" 2,571,457 for a disclosure of apparatus suitable for practicing the method of the invention.
What I claim is:
1. Artificial filaments each consisting of a resincus polymeric mixture forming a generally tubular envelope with unbroken walls and nonuniorm thickness, and at least one core within said envelope forming a major fraction of the mass of the filament and being of a material selectedirom the group consisting of all metals, metalloids and alloys which are molten at the temperature of formation of the filaments and which form at least one solid core in the filaments, said core being of irregular but substantially circular cross section which varies non-uniformly in diameter along ts length and which also varies in its position within the envelope.
2. The invention according to claim 1 wherein the core is of selenium.
3. The inventon according to claim 1 wherein the core is of selenium which forms not more than about by weight or about 50% by volume of the filament.
4. The invention according to claim 1 wherein the core is composed of metallic tin.
5. The invention according to claim 4 wherein the tin is in dscontinuous cores distributecl along the length of the filament.
References Cited in the file of this patent 995,913 France Aug. 22, 1951

Claims (1)

1. ARTIFICIAL FILAMENTS EACH CONSISTING OF A RESINOUS POLYMERIC MIXTURE FORMING A GENERALLY TUBULAR ENVELOPE WITH UNBROKEN WALLS AND NONUNIFORM THICKNESS, AND AT LEAST ONE CORE WITHIN SAID ENVELOPE FORMING A MAJOR FRACTION OF THE MASS OF THE FILAMENTS AND BEING OF A MATERIAL SELECTED FROM THE GROUP CONSISTING OF ALL METALS, METALLOIDS AND ALLOYS WHICH ARE MOLTEN AT THE TEMPERATURE OF FORMATION OF THE FILAMENTS AND WHICH FORM AT LEAST ONE SOLID CORE IN THE FILAMENTS, SAID CORE BEING OF IRREGULAR BUT SUBSTANTIALLY CIR-
US110372A 1949-08-15 1949-08-15 Polymeric filaments Expired - Lifetime US2674025A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US110372A US2674025A (en) 1949-08-15 1949-08-15 Polymeric filaments

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US110372A US2674025A (en) 1949-08-15 1949-08-15 Polymeric filaments

Publications (1)

Publication Number Publication Date
US2674025A true US2674025A (en) 1954-04-06

Family

ID=22332658

Family Applications (1)

Application Number Title Priority Date Filing Date
US110372A Expired - Lifetime US2674025A (en) 1949-08-15 1949-08-15 Polymeric filaments

Country Status (1)

Country Link
US (1) US2674025A (en)

Cited By (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2834093A (en) * 1954-05-21 1958-05-13 Du Pont Regenerated cellulose filaments and products therefrom
US2838365A (en) * 1955-12-21 1958-06-10 Eastman Kodak Co Dry spinning process
US2861319A (en) * 1956-12-21 1958-11-25 Du Pont Intermittent core filaments
US2893820A (en) * 1956-07-16 1959-07-07 Du Pont Process for the production of regenerated cellulose filaments
US2906594A (en) * 1955-12-21 1959-09-29 Air Reduction Polyvinyl alcohol filaments of improved dye affinity and method of preparation
US2919258A (en) * 1956-02-17 1959-12-29 Allied Chem Dulled article consisting of a polyamide and a normal metal salt of a saturated aliphatic dicarboxylic acid
US2931091A (en) * 1954-02-26 1960-04-05 Du Pont Crimped textile filament
US2932079A (en) * 1956-03-08 1960-04-12 Schiesser Ag Trikotfabriken Complex artificial filaments
US2957225A (en) * 1956-05-04 1960-10-25 Union Carbide Corp Fiber of poly
US2965925A (en) * 1956-10-30 1960-12-27 Sr Otto Dietzsch Artificial hollow thread and device for making same
US2985503A (en) * 1958-09-24 1961-05-23 Becker Hermann Method for making a plastic thread
US2986446A (en) * 1956-08-01 1961-05-30 Courtaulds Ltd Crimped regenerated cellulose fibres
US2987371A (en) * 1957-12-26 1961-06-06 American Enka Corp Manufacture of rayon
US2987797A (en) * 1956-10-08 1961-06-13 Du Pont Sheath and core textile filament
US2989798A (en) * 1955-06-30 1961-06-27 Du Pont Filaments of improved dye-receptivity
US3001265A (en) * 1957-03-25 1961-09-26 Du Pont Flat low melting point metal filament having an oriented synthetic resin sheath
US3003223A (en) * 1957-03-25 1961-10-10 Du Pont Metal core composite filaments
US3038237A (en) * 1958-11-03 1962-06-12 Du Pont Novel crimped and crimpable filaments and their preparation
US3038235A (en) * 1956-12-06 1962-06-12 Du Pont Textile fibers and their manufacture
US3039524A (en) * 1958-11-03 1962-06-19 Du Pont Filaments having improved crimp characteristics and products containing same
US3039174A (en) * 1958-05-12 1962-06-19 Du Pont Elongated composite structure
US3050823A (en) * 1958-10-30 1962-08-28 Beaunit Mills Inc Crimpable regenerated cellulose fibers and yarn
US3054652A (en) * 1957-08-28 1962-09-18 Exxon Research Engineering Co Isotactic polypropylene melt spinning process
US3057038A (en) * 1957-06-05 1962-10-09 Celanese Corp Wet spun cellulose triacetate
US3057039A (en) * 1958-04-21 1962-10-09 Celanese Corp Wet spun cellulose triacetate
US3057040A (en) * 1959-06-18 1962-10-09 Du Pont Monofilaments
US3059991A (en) * 1959-03-20 1962-10-23 E B & A C Whiting Company Method of making oriented filamentary article of isotactic polypropylene
US3084392A (en) * 1958-04-02 1963-04-09 Johns Manville Fiber Glass Inc Method for producing a gaseous blast and for producing glass fibers
US3088794A (en) * 1960-08-26 1963-05-07 Du Pont Process for spinning and drawing polyalkylene isophthalamides
US3090997A (en) * 1958-11-26 1963-05-28 Du Pont Method of continuous treatment of as-spun birefringent polyamide filaments
US3096144A (en) * 1960-08-12 1963-07-02 Horizons Inc Method of making inorganic fibers
US3095630A (en) * 1959-11-12 1963-07-02 Deering Milliken Res Corp Methods and apparatus for producing intermittently elasticized yarns
US3097414A (en) * 1958-10-30 1963-07-16 Woodell
US3097415A (en) * 1959-02-20 1963-07-16 Acrylonitrile fiber and process for
US3102323A (en) * 1958-08-26 1963-09-03 Du Pont Textile
US3115437A (en) * 1959-05-01 1963-12-24 Du Pont Nubby yarns
US3126435A (en) * 1956-07-25 1964-03-24 Production of regenerated cellulose
US3126699A (en) * 1962-10-09 1964-03-31 Process for preparing
US3214500A (en) * 1960-09-30 1965-10-26 Du Pont Process for making filamentary structures prepared from the polycarbonate of 2, 2-(4, 4'-dihydroxydiphenyl) propane
US3233019A (en) * 1962-08-07 1966-02-01 Du Pont Process of multiple neck drawing while simultaneously infusing modifying agent
US3361616A (en) * 1963-12-20 1968-01-02 Walter G. Scharf Flecked metallized yarn
US3382305A (en) * 1954-10-29 1968-05-07 Du Pont Process for preparing oriented microfibers
US3589793A (en) * 1957-05-06 1971-06-29 Basil I Hirschowitz Glass fiber optical devices
US5679196A (en) * 1995-10-05 1997-10-21 North American Rubber Thread Company, Inc. Process of making rubber thread
US20150031481A1 (en) * 2013-07-29 2015-01-29 Psi 91, Inc. Game ball

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1665230A (en) * 1926-01-19 1928-04-10 Albert T Otto & Sons Lace web and process of making the same
US2237315A (en) * 1938-08-24 1941-04-08 Dow Chemical Co Coating filamentous articles with vinylidene chloride compositions
US2267597A (en) * 1939-09-13 1941-12-23 Devoe & Raynolds Co Inc Method and apparatus for making artificial bristles
US2285552A (en) * 1940-07-25 1942-06-09 Du Pont Production of filaments
US2307470A (en) * 1941-06-07 1943-01-05 Jack P Tidbail Gut string with wear resisting coating
US2323333A (en) * 1939-06-22 1943-07-06 Gen Cable Corp Insulating enamel for electric conductors
US2328998A (en) * 1939-12-27 1943-09-07 George S Radford Attrition product and method for making same
US2406319A (en) * 1943-11-19 1946-08-27 Sprague Electric Co Insulated electrical conductor
US2421652A (en) * 1943-08-02 1947-06-03 Sprague Electric Co Electrical conductor
US2445768A (en) * 1944-05-05 1948-07-27 Standard Telephones Cables Ltd Manufacture of selenium products
US2571457A (en) * 1950-10-23 1951-10-16 Ladisch Rolf Karl Method of spinning filaments
FR995913A (en) * 1949-09-22 1951-12-11 Textile metallic thread

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1665230A (en) * 1926-01-19 1928-04-10 Albert T Otto & Sons Lace web and process of making the same
US2237315A (en) * 1938-08-24 1941-04-08 Dow Chemical Co Coating filamentous articles with vinylidene chloride compositions
US2323333A (en) * 1939-06-22 1943-07-06 Gen Cable Corp Insulating enamel for electric conductors
US2267597A (en) * 1939-09-13 1941-12-23 Devoe & Raynolds Co Inc Method and apparatus for making artificial bristles
US2328998A (en) * 1939-12-27 1943-09-07 George S Radford Attrition product and method for making same
US2285552A (en) * 1940-07-25 1942-06-09 Du Pont Production of filaments
US2307470A (en) * 1941-06-07 1943-01-05 Jack P Tidbail Gut string with wear resisting coating
US2421652A (en) * 1943-08-02 1947-06-03 Sprague Electric Co Electrical conductor
US2406319A (en) * 1943-11-19 1946-08-27 Sprague Electric Co Insulated electrical conductor
US2445768A (en) * 1944-05-05 1948-07-27 Standard Telephones Cables Ltd Manufacture of selenium products
FR995913A (en) * 1949-09-22 1951-12-11 Textile metallic thread
US2571457A (en) * 1950-10-23 1951-10-16 Ladisch Rolf Karl Method of spinning filaments

Cited By (50)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2931091A (en) * 1954-02-26 1960-04-05 Du Pont Crimped textile filament
US3038236A (en) * 1954-02-26 1962-06-12 Du Pont Crimped textile products
US2834093A (en) * 1954-05-21 1958-05-13 Du Pont Regenerated cellulose filaments and products therefrom
US3382305A (en) * 1954-10-29 1968-05-07 Du Pont Process for preparing oriented microfibers
US3546063A (en) * 1954-10-29 1970-12-08 Du Pont Microfibers and shaped structures containing microfibers
US2989798A (en) * 1955-06-30 1961-06-27 Du Pont Filaments of improved dye-receptivity
US2906594A (en) * 1955-12-21 1959-09-29 Air Reduction Polyvinyl alcohol filaments of improved dye affinity and method of preparation
US2838365A (en) * 1955-12-21 1958-06-10 Eastman Kodak Co Dry spinning process
US2919258A (en) * 1956-02-17 1959-12-29 Allied Chem Dulled article consisting of a polyamide and a normal metal salt of a saturated aliphatic dicarboxylic acid
US2932079A (en) * 1956-03-08 1960-04-12 Schiesser Ag Trikotfabriken Complex artificial filaments
US2957225A (en) * 1956-05-04 1960-10-25 Union Carbide Corp Fiber of poly
US2893820A (en) * 1956-07-16 1959-07-07 Du Pont Process for the production of regenerated cellulose filaments
US3126435A (en) * 1956-07-25 1964-03-24 Production of regenerated cellulose
US2986446A (en) * 1956-08-01 1961-05-30 Courtaulds Ltd Crimped regenerated cellulose fibres
US2987797A (en) * 1956-10-08 1961-06-13 Du Pont Sheath and core textile filament
US2965925A (en) * 1956-10-30 1960-12-27 Sr Otto Dietzsch Artificial hollow thread and device for making same
US3038235A (en) * 1956-12-06 1962-06-12 Du Pont Textile fibers and their manufacture
US2861319A (en) * 1956-12-21 1958-11-25 Du Pont Intermittent core filaments
US3001265A (en) * 1957-03-25 1961-09-26 Du Pont Flat low melting point metal filament having an oriented synthetic resin sheath
US3003223A (en) * 1957-03-25 1961-10-10 Du Pont Metal core composite filaments
US3589793A (en) * 1957-05-06 1971-06-29 Basil I Hirschowitz Glass fiber optical devices
US3057038A (en) * 1957-06-05 1962-10-09 Celanese Corp Wet spun cellulose triacetate
US3054652A (en) * 1957-08-28 1962-09-18 Exxon Research Engineering Co Isotactic polypropylene melt spinning process
US2987371A (en) * 1957-12-26 1961-06-06 American Enka Corp Manufacture of rayon
US3084392A (en) * 1958-04-02 1963-04-09 Johns Manville Fiber Glass Inc Method for producing a gaseous blast and for producing glass fibers
US3057039A (en) * 1958-04-21 1962-10-09 Celanese Corp Wet spun cellulose triacetate
US3039174A (en) * 1958-05-12 1962-06-19 Du Pont Elongated composite structure
US3102323A (en) * 1958-08-26 1963-09-03 Du Pont Textile
US2985503A (en) * 1958-09-24 1961-05-23 Becker Hermann Method for making a plastic thread
US3050823A (en) * 1958-10-30 1962-08-28 Beaunit Mills Inc Crimpable regenerated cellulose fibers and yarn
US3097414A (en) * 1958-10-30 1963-07-16 Woodell
US3038237A (en) * 1958-11-03 1962-06-12 Du Pont Novel crimped and crimpable filaments and their preparation
US3039524A (en) * 1958-11-03 1962-06-19 Du Pont Filaments having improved crimp characteristics and products containing same
US3090997A (en) * 1958-11-26 1963-05-28 Du Pont Method of continuous treatment of as-spun birefringent polyamide filaments
US3097415A (en) * 1959-02-20 1963-07-16 Acrylonitrile fiber and process for
US3059991A (en) * 1959-03-20 1962-10-23 E B & A C Whiting Company Method of making oriented filamentary article of isotactic polypropylene
US3115437A (en) * 1959-05-01 1963-12-24 Du Pont Nubby yarns
US3057040A (en) * 1959-06-18 1962-10-09 Du Pont Monofilaments
US3095630A (en) * 1959-11-12 1963-07-02 Deering Milliken Res Corp Methods and apparatus for producing intermittently elasticized yarns
US3096144A (en) * 1960-08-12 1963-07-02 Horizons Inc Method of making inorganic fibers
US3088794A (en) * 1960-08-26 1963-05-07 Du Pont Process for spinning and drawing polyalkylene isophthalamides
US3214500A (en) * 1960-09-30 1965-10-26 Du Pont Process for making filamentary structures prepared from the polycarbonate of 2, 2-(4, 4'-dihydroxydiphenyl) propane
US3233019A (en) * 1962-08-07 1966-02-01 Du Pont Process of multiple neck drawing while simultaneously infusing modifying agent
US3126699A (en) * 1962-10-09 1964-03-31 Process for preparing
US3361616A (en) * 1963-12-20 1968-01-02 Walter G. Scharf Flecked metallized yarn
US5679196A (en) * 1995-10-05 1997-10-21 North American Rubber Thread Company, Inc. Process of making rubber thread
US5804307A (en) * 1995-10-05 1998-09-08 North American Rubber Thread Co., Inc. Rubber thread
US20150031481A1 (en) * 2013-07-29 2015-01-29 Psi 91, Inc. Game ball
US9089740B2 (en) * 2013-07-29 2015-07-28 Psi 91, Inc. Game ball
US9956458B2 (en) 2013-07-29 2018-05-01 Psi 91, Inc. Game ball

Similar Documents

Publication Publication Date Title
US2674025A (en) Polymeric filaments
US2612679A (en) Filaments containing fillers
US2571457A (en) Method of spinning filaments
US4071594A (en) Production of continuous ceramic fibers
US4376743A (en) Melt spinning process
US2957747A (en) Process for producing crimpable polyamide filaments
US3348445A (en) Method of making solid propellants in textile form
CN1039040C (en) Spinning nozzle
US4357379A (en) Melt blown product
US4267002A (en) Melt blowing process
BG62408B1 (en) Method for the production of cellulose fibres and device for its materialization
US20050106391A1 (en) Centrifugal spinning process
US3497585A (en) Self-crimping filament process
US2399260A (en) Filamentous product
JP5000840B2 (en) Composite yarn manufacturing method and apparatus
JPS6158566B2 (en)
US3758373A (en) Spray-spun continuous tubular structure
JPH07501588A (en) Fine denier staple fiber
US3615998A (en) Method of biaxially oriented nonwoven tubular material
US3304867A (en) Solid propellants in textile form
US2588583A (en) Process for spinning
US3164949A (en) Trilobal filamentary yarns
US3608041A (en) Spinning process
US2351090A (en) Process of preparing rubber-coated artificial filaments
KR950000941A (en) Polyfilament yarns of polyethylene naphthalate and preparation method thereof