US2385890A - Spinning process - Google Patents

Spinning process Download PDF

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Publication number
US2385890A
US2385890A US481287A US48128743A US2385890A US 2385890 A US2385890 A US 2385890A US 481287 A US481287 A US 481287A US 48128743 A US48128743 A US 48128743A US 2385890 A US2385890 A US 2385890A
Authority
US
United States
Prior art keywords
yarn
cold
melt
filaments
finely divided
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
US481287A
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English (en)
Inventor
Edgar W Spanagel
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.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
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 EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to US481287A priority Critical patent/US2385890A/en
Priority to GB5775/44A priority patent/GB576647A/en
Application granted granted Critical
Publication of US2385890A publication Critical patent/US2385890A/en
Priority to FR951371D priority patent/FR951371A/fr
Priority to DEP3599A priority patent/DE901332C/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/10Other agents for modifying properties
    • 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
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/60Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides

Definitions

  • This invention relates to the production of fine denier filaments and muitifiiament yarns and threads composed of a synthetic linear polymer. More particularly, this invention relates to the production of such filaments, yarns and threads containing incorporated therein a finely divided, inert material in an amount less than that which will produce a substantially visible delusterins or dulling eilect. whereby the rupturing of the filaments or yarn, during the coid-drawins thereof, will be materially diminished.
  • melt-spinning and cold-drawing that is, drawing under tension in the solid state
  • the U. B. patents to Carothers Nos. 2,071,250, 2,071,201, 2,071,253 and 2,180,048 all disclose the melt-spinning and cold-drawing oi synthetic linear polymers including polyamides, polyesters, polyethers and polyanhydrides as well as mixed polymers or interpolymers, for example polyamide-polyesters.
  • the synthetic linear polyamides more particularly described in the last two above mentioned patents.
  • other synthetic linear polymers for xample vinylidene dichloride polymers, acrylonitrile polymers and interpolymers of vinyl acetate and vinyl chloride can be melt spun and cold-drawn.
  • the present invention in its broad aspects is applicable to the melt spinning and cold-drawing of any fiber-forming synthetic linear polymer.
  • the cold drawing of synthetic linear polymer yarn is usually done by feeding the yarn from one pair oi positively driven rollers to a second pair of positively driven rollers rotating at a suitably higher speed than said first pair.
  • the draw tension is concentrated at a precise point between the pairs of rollers to prevent wandering of the draw-point.
  • the objects of the invention may be accomplished, in general, by producing bright, colddrawable, fine denier filaments and multifilament yarns composed of a synthetic linear polymer containing, homogeneously dispersed throughout the body thereof. a finely divided, inert material in an amount substantially less than that which will produce a visible delustering efiect.
  • the preferred procedure for accomplishing this is to prepare a melt of a synthetic linear polyamlde containing from 0.005% to 0.05% by weight of the finely divided, inert material, for example titanium dioxide, and melt spinning the polyamide in a known manner.
  • Example I to be understood how- The yarn was not visibly delustered.
  • Example I Polyhexamethylene adipamide polymer of relatlve viscosity 34 (determined by the method described below) and containing 0.05% by weight A similar polyhexamethylene adipamide oi relative viscosity 34 (determined by the method described below). but containing no titanium dioxide was melt spun to form a 69-fiiament yarn which was subsequently cold drawn at a draw ratio of 4.40 to produce a 210 denier-68 filament yarn with a tenacity of 6.5 grams per denier and an elongation oi 14%. In the drawing operation here were several complete yarn breaks and a creel mirror test showed seventy broken filaments per 1,000 yards of yarn.
  • a second sample oi the polymer mentioned in the previous paragraph was melt spun to form The yarn was subsequently yards of yarn.
  • the relative Viscosity may be between 15 and 80.
  • the melt and colddrawing of poivhexamethylene adipenude ram is not limited to the use of titanium dioxide. but
  • Quantities of 0.01% to 0.03% of titanium dioxide, based on the weight of the polyamide, are preferred.
  • the quantities of 0.005% to 0.05% weight are effective to produce the desired results while at the same time permitting the production of bright filaments and yarn and the term "bright" is intended to signify filaments and yarn having a brightness not less than that which is incident to the use of said quantities of titanium dioxide.
  • One skilled in the art can quite readily determine the optimum proportion of any other finely divided, inert material which may be used instead 01' the titanium dioxide.
  • finely divided, inert material is meant a material which has no chemical action on said polymer and which is in a state of division of the order of yarn delustering or pismenting material.
  • the invention described herein has importantly advanced the art of producing cold-drawn. bright filaments and yarns composed of a synthetic linear polymer, thereby permitting maximum production of excellent yarn with existing equipment. It has now been found that, by the practice of this invention, the number of yarn and filament breaks during cold-drawing is decreased and a larger percentage of production can now be classified as completely satisfacwry run. It has been found too that bright yarn can be produced having the desired high tenacity (highly drawn yarn) and fine denier per filament.
  • a surprising and unexpected result of the invention is that the yarn produced in accordance 'with this invention is not nearly so wild" on a yarn.
  • An unoriented, cold-drawable, filamentous structure composed of a synthetic linear polyamide containing, homogeneously dispersed throughout the body thereof, a finely divided. inert material in an amount from 0.005% to 0.05%.
  • An unoriented, cold-drawable, filamentous structure composed oi polyhexamethylene adipamide containing, homogeneously dispersed throughout the body thereof. a finely divided. inert material in an amount from 0.005% to 0.05%.
  • I. ran unoriented, cold-drawable, filamentous structure composed of a synthetic linear polyamide containing homogeneously dispersed throughout the body thereof finely divided titanium dioxide in an amount from 0.005% to 0.05%.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Textile Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Artificial Filaments (AREA)
  • Multicomponent Fibers (AREA)
US481287A 1943-03-31 1943-03-31 Spinning process Expired - Lifetime US2385890A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US481287A US2385890A (en) 1943-03-31 1943-03-31 Spinning process
GB5775/44A GB576647A (en) 1943-03-31 1944-03-29 Improvements in or relating to filamentous structures of synthetic linear fibre-forming polymers
FR951371D FR951371A (fr) 1943-03-31 1947-08-06 Procédé de filature de superpolymères linéaires synthétiques
DEP3599A DE901332C (de) 1943-03-31 1950-09-24 Verfahren zur Herstellung von kuenstlichen, nichtmattierten Gebilden aus linearen Polymerisaten, vorzugsweise Polyhexamethylenadipinsaeureamid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US481287A US2385890A (en) 1943-03-31 1943-03-31 Spinning process

Publications (1)

Publication Number Publication Date
US2385890A true US2385890A (en) 1945-10-02

Family

ID=23911366

Family Applications (1)

Application Number Title Priority Date Filing Date
US481287A Expired - Lifetime US2385890A (en) 1943-03-31 1943-03-31 Spinning process

Country Status (4)

Country Link
US (1) US2385890A (de)
DE (1) DE901332C (de)
FR (1) FR951371A (de)
GB (1) GB576647A (de)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2612679A (en) * 1950-10-23 1952-10-07 Ladisch Rolf Karl Filaments containing fillers
US2679450A (en) * 1951-04-11 1954-05-25 British Celanese Manufacture of textile materials
US2907096A (en) * 1952-06-28 1959-10-06 Halbig Paul Shaped polyacrylonitrile structures
US2924503A (en) * 1957-07-30 1960-02-09 Du Pont Process for melt spinning polyesters containing an alkaline earth sulfate filler
US2927841A (en) * 1958-04-25 1960-03-08 Du Pont Process for spinning polyamides which contain a phenylphosphinate and product
US3088932A (en) * 1960-12-02 1963-05-07 Monsanto Chemicals Acrylonitrile polymer composition and stabilized with zinc oxalate, zinc acetate, or chromium acetate
US3164947A (en) * 1963-02-28 1965-01-12 Wall Rope Works Inc Cordage and methods of manufacture thereof
US3314919A (en) * 1962-05-22 1967-04-18 Du Pont Process of melt spinning roughsurfaced fibers
US3378514A (en) * 1965-02-09 1968-04-16 Du Pont Process for making polycarbonamide yarns
US3397171A (en) * 1963-04-18 1968-08-13 Du Pont Polyamide fibers containing kaolinite and process of preparation
US3408251A (en) * 1964-01-10 1968-10-29 Davies Stanley Tows of synthetic filaments and method for making the same
US4900496A (en) * 1986-09-26 1990-02-13 E. I. Du Pont De Nemours And Company Process for making a tire cord using yarns containing a dip penetration regulator
US5096778A (en) * 1986-09-26 1992-03-17 E. I. Du Pont De Nemours And Company Dip penetration regulators for tire yarns
US5238637A (en) * 1991-06-07 1993-08-24 Rhone-Poulenc Fibres Process for obtaining polyamide yarns with better output efficiency

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2612679A (en) * 1950-10-23 1952-10-07 Ladisch Rolf Karl Filaments containing fillers
US2679450A (en) * 1951-04-11 1954-05-25 British Celanese Manufacture of textile materials
US2907096A (en) * 1952-06-28 1959-10-06 Halbig Paul Shaped polyacrylonitrile structures
US2924503A (en) * 1957-07-30 1960-02-09 Du Pont Process for melt spinning polyesters containing an alkaline earth sulfate filler
US2927841A (en) * 1958-04-25 1960-03-08 Du Pont Process for spinning polyamides which contain a phenylphosphinate and product
US3088932A (en) * 1960-12-02 1963-05-07 Monsanto Chemicals Acrylonitrile polymer composition and stabilized with zinc oxalate, zinc acetate, or chromium acetate
US3314919A (en) * 1962-05-22 1967-04-18 Du Pont Process of melt spinning roughsurfaced fibers
US3164947A (en) * 1963-02-28 1965-01-12 Wall Rope Works Inc Cordage and methods of manufacture thereof
US3397171A (en) * 1963-04-18 1968-08-13 Du Pont Polyamide fibers containing kaolinite and process of preparation
US3408251A (en) * 1964-01-10 1968-10-29 Davies Stanley Tows of synthetic filaments and method for making the same
US3378514A (en) * 1965-02-09 1968-04-16 Du Pont Process for making polycarbonamide yarns
US4900496A (en) * 1986-09-26 1990-02-13 E. I. Du Pont De Nemours And Company Process for making a tire cord using yarns containing a dip penetration regulator
US5096778A (en) * 1986-09-26 1992-03-17 E. I. Du Pont De Nemours And Company Dip penetration regulators for tire yarns
US5238637A (en) * 1991-06-07 1993-08-24 Rhone-Poulenc Fibres Process for obtaining polyamide yarns with better output efficiency
US5405697A (en) * 1991-06-07 1995-04-11 Rhone-Poulenc Fibres Process for obtaining polyamide yarns with better output efficiency

Also Published As

Publication number Publication date
GB576647A (en) 1946-04-12
DE901332C (de) 1954-01-11
FR951371A (fr) 1949-10-24

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