Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.

Patents

  1. Advanced Patent Search
Publication numberUS2846289 A
Publication typeGrant
Publication dateAug 5, 1958
Filing dateDec 17, 1956
Priority dateDec 23, 1955
Publication numberUS 2846289 A, US 2846289A, US-A-2846289, US2846289 A, US2846289A
InventorsGray John
Original AssigneeIci Ltd
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
High luster polyamide filaments and process for producing them
US 2846289 A
Images(2)
Previous page
Next page
Description  (OCR text may contain errors)

United States Patent C HIGH LUSTER POLYAMIDE FILAMENTS AND PROCESS FOR PRODUCING THEM John Gray, Welwyn Garden City, England, assignor to Imperial Chemical Industries Limited, London, England, a corporation of Great Britain Application December 17, 1956 Serial No. 628,509

Claims priority, application Great Britain December 23, 1955 8 Claims. (Cl. 18-54) No Drawing.

This invention relates to a process for the production of filaments from synthetic linear polyamides. These polymers are made by subjecting bifunctional polyamideforming reactants to polymerising conditions until the polyamide formed is capable of being melt-spun into filamerisable amino acid, or a derivative thereof, or a mix-' c ture of one or more diamines and one or more dibasic acids or their amide-forming derivatives.

It is an object of the present invention to provide a process for the production of polyamide filaments having mechanical and surface properties which render them particularly suitable for use in brush tufting and other applications.

This object is achieved by a process for the production of polyamide filaments by extruding a molten synthetic linear polyamide and quenching it by contact with a liquid which has substantially no solvent action on the polymer under the conditions used, characterised in that the quenching liquid is maintained at a temperature below C. The filament is subsequently cold-drawn by any of the known methods. For example, the filament may be passed from one or more rolls rotating at a given speed to one or more draw rolls rotating at a sufficiently greater speed to bring about the required elongation of the filament. Preferred draw ratios are 3:1 to 6:1. My invention also comprises polyamide filaments made by the above processes.

I prefer to quench the extruded filament by means of a liquid at between 2S C. and 60 C. By using a quenching liquid below C. filaments having an optimum combination of mechanical and surface properties are produced. Temperatures below 60 C. are not normally used as little improvement in filament properties is obtained under these conditions compared with the improvement obtained by working within our preferred temperature range and to maintain the liquid at such low I temperatures involves additional cost.

Examples of suitable quenching liquids are alcohols, lzetones, ethers, esters, hydrocarbons, chlorinated hydrocarbons and aqueous solutions of salts which are liquid at the temperature at which it is desired to quench the extruded filament. Particularly good results have been obtained using methyl alcohol and trichloroethylene. The quenching liquid may be used in the form of a bath or a spray although the former is usually more convenient.

To obtain the optimum effect the temperature of the polyamide should not be materially below its melting point when it comes into contact with the quenching liquid. In the preferred method of carrying out the present invention therefore, the molten polymer is extruded directly into the quenching liquid to prevent any preliminary cooling due to the action of air.

The polyamide filaments may, if desired, be coloured by, for example, incorporating a suit-able colourant in the polymer or in an intermediate used in its production or, alternatively, the filaments may be treated with the colourant after extrusion. When making relatively large quantities of filaments in one colour, we prefer to incorporate the colourant-by dispersing it in the molten polymer prior to its extrusion. 0n the other hand, for comparatively small batches, it is preferred to colour the extruded filaments by dyeing.

Excellent results are obtainable in accordance with the present invention using a polyamide derived from hexamethylene diamine and adipic acid. Particularly useful filaments are also obtained by the application of the present invention to an interpolyamide obtained by polymerising together a mixture of hexamethylene diammonium adipate and hexamethylene diammonium sebacate in weight proportions of about 80% of the former to about 20% of the latter. My invention may also be applied to the prduction of filaments of polymerised caprolactam.

Polyamide filaments which have been extruded and quenched according to the present invention are highly transparent, smooth and of very attractive appearance. After they have been cold-drawn, the filaments are of high tensile strength and retain their attractive surface lustre. The cold-drawn filaments of our invention, especially those having a diameter within the range of 0.005 to 0.023", are particularly suitable for filling brushes and the like. In order to increase their .ability to recover after deformation, it is normally desirable to condition the cold-drawn filaments by treating them with hot water or steam, preferably under tension. For example, a reel of the filaments may be immersed in boiling water for 30 to 90 minutes. The surface smoothness of these filaments enables them to be handled easily in conventional brushmaking machinery. My invention, therefore, also comprises brushes, e. g. brooms, filled with cold-drawn, preferably conditioned filaments made by the process of my invention.

If it is desired to produce tapered filaments, cyclic variations in the haul-off rate of the extruded and quenched filaments can be applied in the usual manner. It will also 1 be appreciated that, if desired, crimping, tipping or flagging may be carried out by any of the known methods.

My invention is illustrated but in no way limited by the following example.

Example Polyhexamethylene adipamide of number average molecular Weight approximately 11,500, containing 0.05% by weight of a cadmium yellow pigment, was extruded at 300 C. through a circular orifice of 0.030" diameter at a rate of 1.2 lb./hr. The extruded monofilaments were passed at a speed of ft./min. through a bath containing trichloroethylene maintained at 45 C. by the addition of Drikold and thereafter cold-drawn to four times their original length. The cold-drawn filaments were held under tension in boiling water for 45 minutes. Throughout the drawing and subsequent treatment the monofilaments retained their very attractive appearance and smooth surface. The tensile strength of these filaments measured at 100% relative humidity was 53,400 lb./ sq. in. compared with a figure of 51,200 lb./sq. in. shown by filaments made by repeating the above process but using a water bath at 25 C. for quenching.

I claim:

1. A process for the production of polyamide filaments comprising the steps of extruding a molten synthetic linear polyamide, and quenching the extruded polyamide by contact with a liquid having substantially no solvent action on the polymer and maintained at a temperature below 5 C.

2. A process as defined in claim 1, in which the tem- 3 perature of the quenching liquid is maintained at a temperature between -25 C. and 60 C.

3. A process as defined in claim 1, in which the quenching liquid is methyl alcohol.

4. A process as defined in claim 1, in which the quenching liquid is trichloroethylene.

quenching filament is subsequently cold-drawn.

7. A process as defined in claim I, in which the quenching filament is subsequently cold-drawn, and then subjected to high temperature in an aqueous medium under tension.

8. Poiyamide filaments produced by the process at 5 claim 1.

References Cited in the file of this patent UNITED STATES PATENTS Miles May 9, 1939 Hull July 13, 1943

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2157117 *Feb 15, 1937May 9, 1939Du PontSteam treatment of polyamides
US2324397 *Jun 4, 1941Jul 13, 1943Du PontMethod for production of continuous structures
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3005233 *Dec 16, 1958Oct 24, 1961British CelaneseMelt spinning
US3027602 *Dec 16, 1957Apr 3, 1962Du PontProcess for preparing glossy, transparent nylon films by melt extrusion of superpolyamide resins
US3041915 *Jun 4, 1958Jul 3, 1962Inventa A G Fur Forschung & PaProcess for the manufacture of net-like structures from synthetic fibers
US3481685 *Mar 11, 1965Dec 2, 1969Ici LtdProcess for the treatment of textile materials
US3946094 *Aug 22, 1974Mar 23, 1976Agency Of Industrial Science & TechnologyContinuous process, polyamides, polyesters, polyolefins, melt-spinning, stretching
US4119693 *Jun 6, 1977Oct 10, 1978Albany International Corp.Plasticizing, quenching in potassium carbonate, stretching
US4200602 *Dec 22, 1976Apr 29, 1980Phillips Petroleum CompanyExtruding, then cooling a terephthalic acid-5-methyl-nonanediamine polyamide, glass transition temperature
Classifications
U.S. Classification528/335, 264/235, 264/178.00F, 264/28, 264/210.5
International ClassificationD01F6/60
Cooperative ClassificationD01F11/08, D01F6/60
European ClassificationD01F6/60