US3655853A - Process for producing polytetrafluoroethylene filaments - Google Patents

Process for producing polytetrafluoroethylene filaments Download PDF

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US3655853A
US3655853A US62627A US3655853DA US3655853A US 3655853 A US3655853 A US 3655853A US 62627 A US62627 A US 62627A US 3655853D A US3655853D A US 3655853DA US 3655853 A US3655853 A US 3655853A
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filaments
yarn
viscose
cellulose
polytetrafluoroethylene
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US62627A
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Arthur R Gallup
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EIDP Inc
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EI Du Pont de Nemours and Co
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    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/44—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/48—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds of polymers of halogenated hydrocarbons

Definitions

  • Tolytetrafiuoroethylene filaments of improved strength are produced by extruding a mixture of viscose and PTFE aqueous dispersion having an average particle size of from 0.1 to 0.17 micron into an acidic coagulating and regenerating bath.
  • This invention relates to polytetrafluoroethylene filaments of improved tenacity and to dispersions of polytetrafluoroethylene in viscose, which are used for making the filaments.
  • polytetrafluoroethylene filaments Due to the chemical inertness and heat stability of polytetrafluoroethylene, it cannot be processed into filaments. by conventional solution or melt spinning techniques.
  • One process for making polytetrafluoroethylene filaments is to disperse finely divided tetrafluoroethylene polymer in viscose of the type used for production of viscose rayon fibers; extrude the dispersion into a coagulating, non-regenerating bath or a coagulating and regenerating bath to form filaments consisting of a cellulose matrix containing the polytetrafiuoroethylene particles; heating the filaments to a relatively high temperature to decompose the cellulose and coalesce the polytetrafiuoroethylene particles; and finally drawing the heated polytetrafiuoroethylene filaments.
  • the improved process for the production of polytetrafluoroethylene filaments comprises forming an aqueous mixture of viscose with an aqueous dispersion of tetrafluoroethylene polymer particles having an average particle size of from about 0.1 to about 0.17 micron, extruding the mixture into an acidic coagulating and regenerating bath to form filaments consisting of a cellulosic matrix containing said polymer particles, heating the filaments at a temperature sufficiently high to decompose said cellulosic material and coalesce said polymer particles, and drawing said filaments.
  • the mixture to be extruded comprises an aqueous dispersion of tetrafluoroethylene polymer particles admixed with viscose, said polymer particles constituting from about to about 96% of the combined weight of said polymer particles and the cellulose in said viscose, and having an average particle size of from about 0.1 to about 0.17 micron.
  • a viscose solution containing 4 to 8% cellulose (in the form of cellulose xanthate), 4 to 7% alkali (calculated as sodium hydroxide), and having a total sulfur content of 1.8 to 2.2% may be prepared by methods well known in the art.
  • the viscose solution is then filtered, deaerated and permitted to ripen to increase its coagulability, the salt index at spinning being preferably in the range of 2.5 to 6.0.
  • a preferred method of preparing the dispersion of tetrafluoroethylene polymer particles is to carry out the polymerization of the tetrafluoroethylene in the presence of a surface-active agent which is added in a programmed manner as described by Punderson in US. Pat. 3,391,099.
  • the average particle size is controlled primarily by adjustment of the concentration of surface-active agent during the nucleation phase as taught by Punderson. Increasing the concentration in this phase leads to an increase in the number of nuclei and a lower particle size.
  • Polymer particle dispersions of the critical average particle size of from 0.10 to 0.17 micron may be prepared by this method.
  • the average particle sizes referred to herein are those determined by a relationship based on light-scattering theory, from the percentage of incident light transmitted at 5.16 millimicron wavelength through a unit measure of a dilute dispersion (ca. 0.02 wt. percent solids), using a nominal value of 0.020 cc./g. for the refractive index increment, An/Aa, of said dispersion at 25 C.
  • These values are in theory nearly equal to the weight-average particle diameter, as confirmed by ultracentrifuge analysis, and are further in reasonable agreement with those determined directly by examination of electron micrographs of the particles at 20,000 diameters magnification.
  • the viscose solution and the dispersion of tetrafluoroethylene polymer particles are admixed to form a composition having the unique property of being capable of being spun into filaments of improved strength.
  • This composition is an aqueous mixture and contains about 10% to about 60%, by weight, of said tetrafluoroethylene polymer particles and about 1% to about 8%, by weight, of cellulose.
  • the weight of the tetrafluoroethylene polymer particles is from about 75% to about 96% of the combined weights of the tetrafluoroethylene polymer particles and cellulose in the aqueous mixture.
  • This aqueous mixture is extruded into a combination coagulating and regenerating bath to set the filaments and convert the cellulose xanthate into cellulose.
  • a bath containing sulfuric acid, sodium sulfate and a small amount of zinc sulfate is preferred.
  • the bath contains 5 to 10% sulfuric acid, 10 to 20% sodium sulfate, and 0.5 to 5% zinc sulfate, and the temperature is in the range of 45 to 65% C.
  • the yarn After passing through the coagulating and regenerating bath, the yarn is washed to remove residual acid, salt and other impurities. The yarn is then dried and thereafter passed in contact with a heated surface, at a temperature of 350 to 500 C. and, preferably, between 370 and 390 C. to decompose the cellulose and coalesce the polyeterafluoroethylene particles.
  • the resulting polytetrafluoroethylene filaments are then drawn while maintained at a high temperature as described in US. Pats. 2,776,465 and 2,772,444.
  • a draw ratio of from 4 to 35 times is employed.
  • a drawing of at least 7 times is generally applied.
  • Example I A viscose solution containing 5.5% by weight of cellulose in the form of cellulose xanthate and 5.0% alkali, calculated as sodium hydroxide, is prepared from wood pulp using sufi'icient carbondisulfide based on the Weight of air-dried pulp to provide 2% by Weight total sulfur content in the viscose. The viscose is filtered, deaerated and permitted to ripen to a salt index of 3.25.
  • the viscose is then mixed with an aqueous dispersion containing 60% of finely divided polytetrafluoroethylene having an average particle diameter of 0.16 micron and containing of Triton X-l00, a nonionic octylphenoxyethanol surfactant as a stabilizer.
  • the resulting spinning mixture contains 28.0% polytetrafluoroethylene and 2.8% cellulose.
  • This mixture is filtered and extruded at a temperature of 10 C. through a spinneret having 60 orifices into an aqueous coagulating and regenerating bath maintained at a temperature of 55 C. and containing 7.0% sulfuric acid, 17% sodium sulfate and 1.0% zinc sulfate.
  • the filaments are converged into a yarn and passed for a distance of 72 inches through the bath.
  • the yarn is then passed to an advancing reel Where it is washed with water at a temperature of 95 C. to remove the residual acid and salt.
  • the yarn is then dried by passage over heater rolls followed by passage over a series of sintering rolls ranging in temperature from 370 C. at the inlet to 388 C. at the outlet for 16.5 seconds to decompose the cellulose and coalesce the polytetrafiuoroethylene particles.
  • the resulting polytetrafluoroethylene filaments are then drawn at a temperature of 388 C. to a ratio of 8.6 by means of draw rolls.
  • the polytetrafluoroethylene yarn is then wound into a package in the conventional manner.
  • the denier of the drawn yarn is about 400.
  • Table 1 shows the average tenacity, number of yarn breaks per pound of yarn and percent waste yarn for a spinning machine operated for a period of five months under conditions described above.
  • a process for producing polytetrafiuoroethylene filaments of improved strength comprising forming an aqueous mixture of viscose with an aqueous dispersion of tetrafluoroethylene polymer particles having an average particle size of from about 0.1 to about 0.17 micron,
  • tetrafluoroethylene polymer particles comprise from about 75% to about 96% of the combined weights of the tetrafluoroethylene polymer particles and cellulose in said aqueous mixture.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Artificial Filaments (AREA)

Abstract

POLYTETRAFLUOROETHYLENE FILAMENTS OF IMPROVED STRENGTH ARE PRODUCED BY EXTRUDING A MIXTURE OF VISCOSE AND PTFE AQUEOUS DISPERSION HAVING AN AVERAGE PARTICLE SIZE OF FROM 0.1 TO 0.17 MICRON INTO AN ACIDIC COAGULATING AND REGENERATING BATH.

Description

United States Patent Olfice 3,655,853 Patented Apr. 11, 1972 ABSTRACT OF THE DISCLOSURE Tolytetrafiuoroethylene filaments of improved strength are produced by extruding a mixture of viscose and PTFE aqueous dispersion having an average particle size of from 0.1 to 0.17 micron into an acidic coagulating and regenerating bath.
This invention relates to polytetrafluoroethylene filaments of improved tenacity and to dispersions of polytetrafluoroethylene in viscose, which are used for making the filaments.
BACKGROUND OF THE INVENTION The outstanding stability of polytetrafluoroethylene to light, heat, solvents, electrical stresses and chemical attack makes it highly desirable for a variety of uses including those in which an inert woven or fibrous material is required. Consequently, polytetrafluoroethylene fibers and filaments have been used in laundry press pads, liquid and gas filters, non-lubricated bearing surfaces, spacesuits, biologically inert sutures, bandages and prosthetic devices. A difliculty with such articles and the production thereof often arises due to the low yarn strength attainable by prior art methods of producing the filaments, however. Accordingly, it is an object of this invention to provide a method for making polytetrafluoroethylene filaments of improved tenacity.
Due to the chemical inertness and heat stability of polytetrafluoroethylene, it cannot be processed into filaments. by conventional solution or melt spinning techniques. One process for making polytetrafluoroethylene filaments, described in US. Pat. 2,772,444, is to disperse finely divided tetrafluoroethylene polymer in viscose of the type used for production of viscose rayon fibers; extrude the dispersion into a coagulating, non-regenerating bath or a coagulating and regenerating bath to form filaments consisting of a cellulose matrix containing the polytetrafiuoroethylene particles; heating the filaments to a relatively high temperature to decompose the cellulose and coalesce the polytetrafiuoroethylene particles; and finally drawing the heated polytetrafiuoroethylene filaments. It has been found that the use of polytetrafluoroethylene particles having a size of from about 0.1 to about 0.17 micron in conjunction wit-h an acidic coagulating and regenerating bath unexpectedly improves the tenacity of filaments produced by the process.
SUMMARY OF THE INVENTION The improved process for the production of polytetrafluoroethylene filaments comprises forming an aqueous mixture of viscose with an aqueous dispersion of tetrafluoroethylene polymer particles having an average particle size of from about 0.1 to about 0.17 micron, extruding the mixture into an acidic coagulating and regenerating bath to form filaments consisting of a cellulosic matrix containing said polymer particles, heating the filaments at a temperature sufficiently high to decompose said cellulosic material and coalesce said polymer particles, and drawing said filaments.
The mixture to be extruded comprises an aqueous dispersion of tetrafluoroethylene polymer particles admixed with viscose, said polymer particles constituting from about to about 96% of the combined weight of said polymer particles and the cellulose in said viscose, and having an average particle size of from about 0.1 to about 0.17 micron.
DETAILED DESCRIPTION OF THE INVENTION The preparation of the viscose, the aqueous dispersion of polytetrafluoroethylene, and the mixture thereof are described in US. Pats. 2,478,229; 2,772,444; and 3,391,099, the disclosures of Which are incorporated herein by reference.
A viscose solution containing 4 to 8% cellulose (in the form of cellulose xanthate), 4 to 7% alkali (calculated as sodium hydroxide), and having a total sulfur content of 1.8 to 2.2% may be prepared by methods well known in the art. The viscose solution is then filtered, deaerated and permitted to ripen to increase its coagulability, the salt index at spinning being preferably in the range of 2.5 to 6.0.
A preferred method of preparing the dispersion of tetrafluoroethylene polymer particles is to carry out the polymerization of the tetrafluoroethylene in the presence of a surface-active agent which is added in a programmed manner as described by Punderson in US. Pat. 3,391,099. The average particle size is controlled primarily by adjustment of the concentration of surface-active agent during the nucleation phase as taught by Punderson. Increasing the concentration in this phase leads to an increase in the number of nuclei and a lower particle size. Polymer particle dispersions of the critical average particle size of from 0.10 to 0.17 micron may be prepared by this method.
The average particle sizes referred to herein are those determined by a relationship based on light-scattering theory, from the percentage of incident light transmitted at 5.16 millimicron wavelength through a unit measure of a dilute dispersion (ca. 0.02 wt. percent solids), using a nominal value of 0.020 cc./g. for the refractive index increment, An/Aa, of said dispersion at 25 C. These values are in theory nearly equal to the weight-average particle diameter, as confirmed by ultracentrifuge analysis, and are further in reasonable agreement with those determined directly by examination of electron micrographs of the particles at 20,000 diameters magnification.
The viscose solution and the dispersion of tetrafluoroethylene polymer particles are admixed to form a composition having the unique property of being capable of being spun into filaments of improved strength. This composition is an aqueous mixture and contains about 10% to about 60%, by weight, of said tetrafluoroethylene polymer particles and about 1% to about 8%, by weight, of cellulose. The weight of the tetrafluoroethylene polymer particles is from about 75% to about 96% of the combined weights of the tetrafluoroethylene polymer particles and cellulose in the aqueous mixture.
This aqueous mixture is extruded into a combination coagulating and regenerating bath to set the filaments and convert the cellulose xanthate into cellulose. For this purpose, a bath containing sulfuric acid, sodium sulfate and a small amount of zinc sulfate is preferred. Preferably, the bath contains 5 to 10% sulfuric acid, 10 to 20% sodium sulfate, and 0.5 to 5% zinc sulfate, and the temperature is in the range of 45 to 65% C.
After passing through the coagulating and regenerating bath, the yarn is washed to remove residual acid, salt and other impurities. The yarn is then dried and thereafter passed in contact with a heated surface, at a temperature of 350 to 500 C. and, preferably, between 370 and 390 C. to decompose the cellulose and coalesce the polyeterafluoroethylene particles. The resulting polytetrafluoroethylene filaments are then drawn while maintained at a high temperature as described in US. Pats. 2,776,465 and 2,772,444. Preferably, a draw ratio of from 4 to 35 times is employed. To develop optimum properties, a drawing of at least 7 times is generally applied.
Example I A viscose solution containing 5.5% by weight of cellulose in the form of cellulose xanthate and 5.0% alkali, calculated as sodium hydroxide, is prepared from wood pulp using sufi'icient carbondisulfide based on the Weight of air-dried pulp to provide 2% by Weight total sulfur content in the viscose. The viscose is filtered, deaerated and permitted to ripen to a salt index of 3.25. The viscose is then mixed with an aqueous dispersion containing 60% of finely divided polytetrafluoroethylene having an average particle diameter of 0.16 micron and containing of Triton X-l00, a nonionic octylphenoxyethanol surfactant as a stabilizer. The resulting spinning mixture contains 28.0% polytetrafluoroethylene and 2.8% cellulose. This mixture is filtered and extruded at a temperature of 10 C. through a spinneret having 60 orifices into an aqueous coagulating and regenerating bath maintained at a temperature of 55 C. and containing 7.0% sulfuric acid, 17% sodium sulfate and 1.0% zinc sulfate. The filaments are converged into a yarn and passed for a distance of 72 inches through the bath. The yarn is then passed to an advancing reel Where it is washed with water at a temperature of 95 C. to remove the residual acid and salt. The yarn is then dried by passage over heater rolls followed by passage over a series of sintering rolls ranging in temperature from 370 C. at the inlet to 388 C. at the outlet for 16.5 seconds to decompose the cellulose and coalesce the polytetrafiuoroethylene particles. The resulting polytetrafluoroethylene filaments are then drawn at a temperature of 388 C. to a ratio of 8.6 by means of draw rolls. The polytetrafluoroethylene yarn is then wound into a package in the conventional manner. The denier of the drawn yarn is about 400.
Table 1 below shows the average tenacity, number of yarn breaks per pound of yarn and percent waste yarn for a spinning machine operated for a period of five months under conditions described above. These results show that there is not only a marked increase in tenacity using the smaller particle size dispersion, but that the number of yarn breaks and the amount of waste yarn are reduced. The results of spinning with the 0.20 micron dispersion on another machine were improved but still inferior to the 0.16 dispersion.
In addition to the improved strength attained with 400 denier yarns, it has been found possible to draw 1200 denier yarn at a higher ratio than heretofore practicable, e.g., increasing the ratio from 5.0 to 6.5, thus obtaining a yarn tenacity of about 1.6 g./den. as compared to 0.8 g./den. usually obtained with 1200 denier yarn using the larger particle dispersions. This results in a tenacity of 1.0 g./den. in bleached yarn, i.e., yarn treated with strong oxidizing agents or hot air to remove residual cellulose decomposition products, as compared to 0.5 g./den. preciously obtained.
I claim: 1. A process for producing polytetrafiuoroethylene filaments of improved strength comprising forming an aqueous mixture of viscose with an aqueous dispersion of tetrafluoroethylene polymer particles having an average particle size of from about 0.1 to about 0.17 micron,
extruding said mixture into an acidic coagulating and regenerating bath to form filaments consisting of a cellulosic matrix containing said polymer particles,
heating the filaments at a temperature sufi'iciently high to decompose said cellulosic material and coalesce said polymer particles, and
drawing said filaments.
2. The process of claim 1 wherein said tetrafluoroethylene polymer particles comprise from about 75% to about 96% of the combined weights of the tetrafluoroethylene polymer particles and cellulose in said aqueous mixture.
3. The process of claim 2 wherein said aqueous mixture contains about 10% to about by weight, of said tetrafluoroethylene polymer particles and about 1% to about 8% by weight, of cellulose.
4. The process of claim 1 wherein said heating is conducted at a temperature between 370 C. and 390 C.
References Cited UNITED STATES PATENTS 2,478,229 8/1949 Berry 161-Tefion 2,559,750 7/1951 Berry 260-296 T 2,559,752 7/1951 Berry 260-296 T 2,772,444 12/ 1956 Burrows 260-17.4 CL 2,776,465 1/1957 Smith 264-191 3,051,545 8/1962 Steuber 264-182 3,301,807 1/1967 Hoashi 260-296 T 3,303,154 2/1967 Hirose et a1 260-296 T 3,372,082 3/1968 Komethani et al 161-178 3,391,099 7/ 1968 Punderson 260-296 T 3,513,144 5/1970 Kometani et a1 161-169 JAY H. WOO, Primary Examiner US. Cl. X.R.
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Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4064214A (en) * 1975-09-22 1977-12-20 E. I. Du Pont De Nemours And Company Process for making polytetrafluoroethylene yarn
US4565663A (en) * 1981-06-26 1986-01-21 Minnesota Mining And Manufacturing Company Method for making water-swellable composite sheet
US5470655A (en) * 1993-09-16 1995-11-28 Japan Gore-Tex, Inc. Polytetrafluoroethylene filamentary material
US5723081A (en) * 1996-12-20 1998-03-03 E. I. Du Pont De Nemours And Company Dispersion spinning process for polytetrafluoroethylene and related polymers
US5762846A (en) * 1996-12-20 1998-06-09 E. I. Du Pont De Nemours And Company Dispersion spinning process for polytetrafluoroethylene and related polymers
US6531559B1 (en) 1998-08-06 2003-03-11 Eidgenössische Technische Hochschule Zürich Melt-processible poly (tetrafluoroethylene)
US6737165B1 (en) 1998-08-06 2004-05-18 Omlidon Technologies Llc Melt-processible poly(tetrafluoroethylene)
US20050137371A1 (en) * 2003-12-17 2005-06-23 Paul Smith Melt-processible poly(tetrafluoroethylene)
US20050143494A1 (en) * 2003-12-31 2005-06-30 Jones Clay W. Dispersion spinning core-shell fluoropolymers
US20060057925A1 (en) * 2001-07-24 2006-03-16 Auza Jaime A A Nonwoven material for low friction bearing surfaces
US20060134414A1 (en) * 2002-10-01 2006-06-22 William Neuberg Process of making cellulosic fibers including ptfe
US20070029697A1 (en) * 2005-08-05 2007-02-08 Devin Flowers Spinning low fluorosurfactant fluoropolymer dispersions
US20070173159A1 (en) * 2006-01-24 2007-07-26 Kishio Miwa Blend of polytetrafluoroethylene, glass and polyphenylene sulfide fibers and filter felt made from same
US20100224710A1 (en) * 2009-03-03 2010-09-09 Donckers Ii J Michael Method of making hydrophilic fluoropolymer material
US20100227110A1 (en) * 2009-03-03 2010-09-09 Donckers Ii J Michael Hydrophilic Fluoropolymer Material
US20100224712A1 (en) * 2009-03-03 2010-09-09 Donckers Ii J Michael Method of making hydrophilic fluoropolymer material
WO2011015485A1 (en) 2009-08-04 2011-02-10 Dsm Ip Assets B.V. Coated high strength fibers
US20150031801A1 (en) * 2013-07-29 2015-01-29 Toray Fluorofibers (America), Inc. Wear Polytetrafluoroethylene (PTFE) Fiber and Method of Making Same
US20160108557A1 (en) * 2013-07-29 2016-04-21 Toray Fluorofibers (America), Inc. Wear Polytetrafluoroethylene (PTFE) Fiber and Method of Making Same

Cited By (42)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4064214A (en) * 1975-09-22 1977-12-20 E. I. Du Pont De Nemours And Company Process for making polytetrafluoroethylene yarn
US4565663A (en) * 1981-06-26 1986-01-21 Minnesota Mining And Manufacturing Company Method for making water-swellable composite sheet
US5470655A (en) * 1993-09-16 1995-11-28 Japan Gore-Tex, Inc. Polytetrafluoroethylene filamentary material
US5723081A (en) * 1996-12-20 1998-03-03 E. I. Du Pont De Nemours And Company Dispersion spinning process for polytetrafluoroethylene and related polymers
US5762846A (en) * 1996-12-20 1998-06-09 E. I. Du Pont De Nemours And Company Dispersion spinning process for polytetrafluoroethylene and related polymers
RU2186889C2 (en) * 1996-12-20 2002-08-10 Е.И. Дюпон Де Немур Энд Компани Method of spinning fibers from dispersion of polytetrafluoroethylene and relative polymers
US20040019167A1 (en) * 1998-08-06 2004-01-29 Paul Smith Melt-processible poly(tetrafluoroethylene)
US6548612B2 (en) 1998-08-06 2003-04-15 Eidgenossische Technische Hochschule Zürich Melt-processible poly(tetrafluoroethylene)
US6737165B1 (en) 1998-08-06 2004-05-18 Omlidon Technologies Llc Melt-processible poly(tetrafluoroethylene)
US6531559B1 (en) 1998-08-06 2003-03-11 Eidgenössische Technische Hochschule Zürich Melt-processible poly (tetrafluoroethylene)
US7872081B2 (en) 1998-08-06 2011-01-18 Omlidon Technologies Llc Melt-processible poly(tetrafluoroethylene)
US7160623B2 (en) 1998-08-06 2007-01-09 Eidgenossische Technische Hochschule Zurich Melt-processible poly(tetrafluoroethylene)
US20070255012A1 (en) * 1998-08-06 2007-11-01 Omlidon Technologies Llc Melt-processible poly(tetrafluoroehtylene)
US7247587B2 (en) 2001-07-24 2007-07-24 E. I. Du Pont De Nemours And Company Nonwoven material for low friction bearing surfaces
US20060057925A1 (en) * 2001-07-24 2006-03-16 Auza Jaime A A Nonwoven material for low friction bearing surfaces
US7015159B2 (en) 2001-07-24 2006-03-21 E. I. Du Pont De Nemours And Company Nonwoven material for low friction bearing surfaces
US20060134414A1 (en) * 2002-10-01 2006-06-22 William Neuberg Process of making cellulosic fibers including ptfe
US20050137371A1 (en) * 2003-12-17 2005-06-23 Paul Smith Melt-processible poly(tetrafluoroethylene)
US7276287B2 (en) 2003-12-17 2007-10-02 Eidgenössische Technische Hochschule Zürich Melt-processible poly(tetrafluoroethylene)
US20050143494A1 (en) * 2003-12-31 2005-06-30 Jones Clay W. Dispersion spinning core-shell fluoropolymers
US7347960B2 (en) * 2003-12-31 2008-03-25 E. I. Du Pont De Nemours And Company Dispersion spinning core-shell fluoropolymers
US20080119608A1 (en) * 2003-12-31 2008-05-22 E. I. Du Pont De Nemours And Company Dispersion Spinning Core-Shell Fluoropolymers
US7872073B2 (en) * 2003-12-31 2011-01-18 E.I. Du Pont De Nemours And Company Dispersion spinning core-shell fluoropolymers
US20070029697A1 (en) * 2005-08-05 2007-02-08 Devin Flowers Spinning low fluorosurfactant fluoropolymer dispersions
US7390448B2 (en) * 2005-08-05 2008-06-24 E.I. Du Pont De Nemours And Company Spinning low fluorosurfactant fluoropolymer dispersions
US20080221250A1 (en) * 2005-08-05 2008-09-11 E. I. Du Pont De Nemours And Company Spinning Low Fluorosurfactant Fluoropolymer Dispersions
US7985361B2 (en) * 2005-08-05 2011-07-26 E. I. Du Pont De Nemours And Company Spinning low fluorosurfactant fluoropolymer dispersions
US20070173159A1 (en) * 2006-01-24 2007-07-26 Kishio Miwa Blend of polytetrafluoroethylene, glass and polyphenylene sulfide fibers and filter felt made from same
US8459579B2 (en) * 2009-03-03 2013-06-11 II J. Michael Donckers Method of making hydrophilic fluoropolymer material
US20120128979A1 (en) * 2009-03-03 2012-05-24 Toray Fluorofibers (America), Inc. Method of Making Hydrophilic Fluoropolymer Material
US20100224710A1 (en) * 2009-03-03 2010-09-09 Donckers Ii J Michael Method of making hydrophilic fluoropolymer material
US20100227110A1 (en) * 2009-03-03 2010-09-09 Donckers Ii J Michael Hydrophilic Fluoropolymer Material
US8003208B2 (en) 2009-03-03 2011-08-23 Toray Fluorofibers (America), Inc. Hydrophilic fluoropolymer material
US8132748B2 (en) 2009-03-03 2012-03-13 Toray Fluorofibers (America), Inc. Method of making hydrophilic fluoropolymer material
US8132747B2 (en) 2009-03-03 2012-03-13 Toray Fluorofibers (America), Inc. Method of making hydrophilic fluoropolymer material
US20100224712A1 (en) * 2009-03-03 2010-09-09 Donckers Ii J Michael Method of making hydrophilic fluoropolymer material
WO2011015485A1 (en) 2009-08-04 2011-02-10 Dsm Ip Assets B.V. Coated high strength fibers
US20150031801A1 (en) * 2013-07-29 2015-01-29 Toray Fluorofibers (America), Inc. Wear Polytetrafluoroethylene (PTFE) Fiber and Method of Making Same
WO2015017272A1 (en) 2013-07-29 2015-02-05 Toray Fluorofibers (America), Inc. Improved wear polytetrafluoroethylene(ptfe) fiber and method of making same
US20160108557A1 (en) * 2013-07-29 2016-04-21 Toray Fluorofibers (America), Inc. Wear Polytetrafluoroethylene (PTFE) Fiber and Method of Making Same
US9422642B2 (en) * 2013-07-29 2016-08-23 Toray Fluorofibers (America), Inc. Wear polytetrafluoroethylene (PTFE) fiber and method of making same
US10106916B2 (en) * 2013-07-29 2018-10-23 Toray Fluorofibers (America), Inc. Wear polytetrafluoroethylene (PTFE) fiber and method of making same

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