|Publication number||US3655853 A|
|Publication date||Apr 11, 1972|
|Filing date||Aug 10, 1970|
|Priority date||Aug 10, 1970|
|Publication number||US 3655853 A, US 3655853A, US-A-3655853, US3655853 A, US3655853A|
|Inventors||Arthur R Gallup|
|Original Assignee||Du Pont|
|Export Citation||BiBTeX, EndNote, RefMan|
|Referenced by (24), Classifications (7)|
|External Links: USPTO, USPTO Assignment, Espacenet|
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.
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US4064214 *||Sep 22, 1975||Dec 20, 1977||E. I. Du Pont De Nemours And Company||Process for making polytetrafluoroethylene yarn|
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|US20050137371 *||Dec 17, 2003||Jun 23, 2005||Paul Smith||Melt-processible poly(tetrafluoroethylene)|
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|U.S. Classification||264/127, 264/210.8, 264/184, 264/44|