US3774387A - Hydrophilic textile products - Google Patents

Hydrophilic textile products Download PDF

Info

Publication number
US3774387A
US3774387A US00259175A US3774387DA US3774387A US 3774387 A US3774387 A US 3774387A US 00259175 A US00259175 A US 00259175A US 3774387D A US3774387D A US 3774387DA US 3774387 A US3774387 A US 3774387A
Authority
US
United States
Prior art keywords
products
sample
fibrils
water
textile
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
US00259175A
Inventor
R Woodell
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
Application granted granted Critical
Publication of US3774387A publication Critical patent/US3774387A/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
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/11Flash-spinning
    • 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
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S57/00Textiles: spinning, twisting, and twining
    • Y10S57/907Foamed and/or fibrillated
    • 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
    • Y10T428/2904Staple length fiber
    • 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
    • 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
    • Y10T428/2978Surface characteristic

Definitions

  • Woodell HYDROPHILIC TEXTILE PRODUCTS [75] Inventor: Rudolph 'Woodell, Richmond, Va.
  • ABSTRACT Textile products comprising an assembly of fibrils.
  • the assembly can be in the form of a yarn, plexifilament, fabric, or the like, and is of at least staple fiber length.
  • the fibrils are of irregular cross-section and are composed of a non-cellulosic, synthetic organic polymer, and most are interconnected to form a plexus.
  • the products are stable to repeated water exposure, and have a limiting surface tension greater than 72 dynes per centimeter, a specific surface of at least about 0.8 square meter per gram, a fibril concentration of at least about 5 X 10 per quare centimeter, and a wicking parameter greater than 6.
  • the products can be prepared by extruding an aqueous dispersion of the polymer at selected elevated temperature and pressure conditions.
  • Preferred products are plexifilamentary strands of an acrylonitrile polymer.
  • the products are useful in textile applications, particularly in such applications where good water-absorption characteristics are desirable.
  • FIG-5 1' HYDROPI-IILIC TEXTILE PRODUCTS CROSS-REFERENCE To RELATED.
  • This invention relates to textile products, and more particularly to assemblies of fibrils of non-cellulosic synthetic organic polymers.
  • the products possess good water-absorption characteristics.
  • Still other fibrillated products such as plexifilamentary strands, are produced by flashextruding a solution of a crystalline synthetic organicpolymer in an activating liquid under superatmospheric pressure and at a temperature in excess of the boiling point of the activating liquid into a region of lower pressure.
  • the invention is directed to a textile product comprising an assembly of fibrils, said assembly being of at least staple-fiber length; said fibrils being of irregular cross-section and being composed of a non-cellulosic, synthetic, organic polymer, with a majority of said fibrils being interconnected at various points to form a plexus; said product being stable to repeated exposure to water, and having a limiting surface tension ('y greater than 72 dynes per centimeter, and a specific surface (S) of at least about 0.8' square meter per gram, and a fibril concentration (F) of at least about 5X 10 per square centimeter, said numerical values of Y0, S and F also being such that the expression for said product is greater than 6.
  • FIG. 1 illustrates the relationship between the waterabsorption rate and the parameter for-several assemblies of fibrils within the scope of this invention and some conventional yarns outside the scope of this invention;
  • FIG. 2 is a top view of a sample holder employed with the apparatus of FIG. 3;
  • FIG. 3 is a cross-section of an apparatus for determining liquid-absorption rates of textile products
  • FIG. 4- shows the relationship between the surface tension and the absorption rate of liquidi'asmeasured on three textile products of an acrylonitrile terpolymer, each product having a different fibril concentration;
  • FIG. 5 is a drawingof a magnified longitudinal section of an assembly of fibrils of a textile product within .the scope of' this invention.
  • FIG. 6 is a photomicrograph of a greatly magnified longitudinal section of an assembly of fibrils of a textile product within the scope of this invention.
  • FIG. 7 is a drawing of an enlarged cross-section of an assembly of fibrils of a textile product within the scope of this invention.
  • the ability of a fibrillated textile product to absorb water can be determined from the expression S is the specific surface of the product measured as hereinafter described, in square meters per gram.
  • FIG. 1 also depicts the superiority of the plexifilamentary products of this invention over corresponding conventional textile filaments.
  • the wicking parameter used herein to combine the various critical structural features of the products of surface tension is derived from a more generalized equation for the rate of liquid absorption by a textile product comprising an assembly of fibrils of generally irregular cross-section, namely,
  • I is the absorption rate in ml./sec.
  • y is the liquid surface tension in dynes/cm. of the liquid tested
  • 1. is the liquid viscosity in centipoise ofthe liquid tested (usually at 25 C.)
  • y F and S are as previously defined.
  • a textile product of this invention in order to absorb water as well as cotton, a textile product of this invention must have a water-wicking parameter of at least When the wicking parameter exceeds 6, the textile products of this invention absorb water as fast as, or even faster than, the cotton materials tested.
  • the preferred plexifilamentary products of this invention frequently have wicking parameters well in excess of 6, as for example, up to 75 or more.
  • the textile product must also be stable to repeated exposure to water, have a limiting surface tension value (7 of greater than 72 dynes/cm. (and, preferably, at least 74 dynes/cm.), a fibril concentration (F) of at least X l0 /cm. and a specific surface (S) of at least 0.8 m. /gm.
  • limiting surface tension is a characteristic of a synthetic organic polymer and is independent of the shape of the polymer. That is, fibers, filaments, fibrillated materials or films of the same polymer all have the same limiting surface tension characteristic.
  • the limiting surface tension is important in determining whether a liquid will be absorbed by a textile product prepared from any given polymer; liquids with surface tensions (y) greater than the limiting difference (y -y).
  • absorb refers to capillary wicking absorption and not to absorption by swelling or by a chemical mechanism.
  • the textile product to be tested is first washed or treated (e.g., with water, soap solution, dry-cleaning fluid, or aqueous hydrofluoric acid) to remove any additives or contaminants, then rinsed, wrapped on a soft gauze-covered batting, boiled in distilled water for about 30 minutes, dried in a vacuum oven at about 60 C., and cooled.
  • the treated product is then wrapped around a Teflon polytetrafluoroethylene form constructed, as shown in FIG. 2, by cutting a 5.7-cm.- diameter circle from a 0.l6-cm.thick sheet of Teflon and cutting so that dimension 11 is 3.2 cm. and dimen sion 12 is 4.0 cm.
  • the form is mounted on a yarn winder to permit rotation about axis 13.
  • the product is fed to the form through a constant tension device which exerts a load equivalent to 0.05 gram per denier.
  • the winder transverse pitch is adjusted so that with each turn of the winder, product is laid on the form as closely adjacent its neighbor as possible.
  • the textile product should preferably be twistless when wound.
  • the number of turns (Y) i.e., the number of parallel lines of material) per layer and the number of complete layers (N) needed to wind a total of about 0.5 gram of product are recorded.
  • Y i.e., the number of parallel lines of material
  • N number of complete layers
  • the textile product on the form is placed in the absorption-rate testing apparatus shown in FIG. 3.
  • This apparatus comprises a Buchner funnel 20, containing a flat, horizontal, fritted-glass plate 21 measuring 5.8 cm. in diameter by 0.55 cm. in thickness and having a resistance to flow of water of about 0.083 ml./sec./cm. water pressure.
  • the funnel is attached through a flexible coupling tube 22 to a horizontal tube 23 having a 0.3l-cm. inside diameter.
  • tube 23 acts as a reservoir for liquid 24.
  • the top of porous plate 21 is positioned 1.3 cm. above the top inside surface of the horizontal reservoir.
  • porous plate 21, lower portion of funnel 20, flexible coupling tube 22, and part of horizontal tube 23 are filled by adding liquid 24 through the top of plate 21, and applying suction to tube 23. All bubbles are removed from the liquid system. Excess liquid, if any, is removed from the top of plate 21. The system is thus filled with liquid from the meniscus in tube 23 to the top of plate s 21. The sample pad 25 is then placed on top of porous plate 21 and an evenly distributed, load 26 of 500 grams placedon the pad. Theamount of liquid absorbed by pad 25 is measured by the movement of the meniscus in tube 23 with the aid of scale 27.
  • Absorption data are collected as a function of time, starting within about two seconds after the sample pad and weight are placed on the porous plate and finishing when less than about 0.01 ml. of liquid is absorbed during a 60-second period.
  • the textile products of this invention generally display absorption-characteristic curve similar to that of curve c in FIG. 4. As can be seen from the figure, these curves generally have a steep straightline portion of negative slope which levels off as liquid surface tension is reduced. This straightline portion must be defined by several points in order to obtain an accurate measurement (or extrapolation) for 7 To improve the accuracy of the determination, absorption curves for several samples of a given polymer are generated and the intercepts of these curves with the surface-tension axis are averaged to define y to within about :1 dyne/cm. Preferably, 'y,, is determined from samples that yield an absorption rate curve that has a slope steeper than -0.005
  • the results of the first run on a sample pad are always discarded. Additional runs are made until the results from three consecutive runs are substantially constant. Generally, a total of four runs is sufficient. Between runs, the pads are washed and then dried at 60 C. in a vacuum oven. At least three sample pads of the same product should be tested in this manner and the measured absorption rates from each sample averaged to obtain an accurate value for the initial absorption rate for the product under test.
  • liquids of different surface tensions are easily prepared from solutions of ethanol in water, calcium chloride in water or sodium nitrate in water, depending upon the surface tension desired.
  • a correction is made for liquid viscosity by multiplying the absorption rates by the viscosity' of the liquids employed and dividing by the viscosity of water. This procedure gives viscosity-normalized initial absorption rates, -I,,'.
  • Surface tensions for aqueous solutions of ethanol, calcium chloride, and sodium nitrate are given in Lan ges Handbook of Chemistry, 10th Edition, N. A.
  • the viscosity-normalized initial absorption rate, I is plotted on linear coordinates against the surface tension of the liquid used in the test.
  • Such a plot is illustrated in FIG. 4 wherecurve a represents the absorp: tion-rate characteristics of a sample pad made from very fine denier filaments (not fibrillated) of an acrylonitrile terpolymer; curve b, a sample pad made from somewhat fibrillated material of the same terpolymer falling outside the scope of this invention; andc, a sam- 1 ple pad of well-fibrillated material of the same terpolymer falling within the scope of this invention. All three curves intersect the surface-tension axis at the same value of 80.3 dynes/cm. This value, where the curves intersect the axis, is the limiting surface tension (y characteristic of the polymer being tested.
  • Fibril concentration (F) is defined as the number of ends per cm. oftextile product cross-section and can be determined by the following formula which applies to the sample pad used for the absorption-rate test:
  • the number of fibrils or ends per yarn n is determined from photomicrographs of the crosssection of the opened yarn (e.g., an opened plexifilamentary strand). Four representative cross-sectional samples, each microns thick, are taken from the length of the yarn and the photomicrographs of these cross-sections are prepared by standard procedures, well known in the art. Three fibril counts are made on each of the photomicrographs. The 12 counts are then averaged to obtain n.
  • the photomicrograph should provide a linea'l magnification of about SOOX. Each individual fibril appears as an independent particle on the photomicrograph. A representation of such a photomicrograph is shown in FIG. 6 where several types of fibrils are identified, as discussed further below.
  • F must be at least 5 X lO/cm. Below this value of F, the materials are coarse and unsuited for general textile use. In general, F can range up to 15 X l0/cm., or more.
  • Specific surface (S) of a textile product is derived from optical measurements of the light scattering coefficient (s). High specific surface provides good covering power and promotes rapid absorption of liquid. It is known that a light scattering coefficient is a measure of the specific surface of a material (TAPPI, V0. 42, No. 12, December 1959, pages 986-994). Light scattering measurements are used to derive the specific surface of the textile products of this invention by the procedure described below.
  • a sample suitable for light reflectance measurements is prepared by winding a close-packed parallel warp of product, preferably in the form of yarns, on a rectangular frame (e.g., measuring about 10 cm. X 8 cm.).
  • a yarn winder e.g., Suter yarn evenness controller
  • a light tension e.g., at about 2 grams
  • the guide traverse controlling the number of threads per cm. is adjusted to provide a specimen with no gaps between the elements of the parallel warp.
  • a Bausch and Lomb Opacimenter is adjusted to read absolute reflectance by calibration with a standard having an absolute reflectance of about 75 percent. Absolute reflectance is measured at ten points on the sample with the sample backed by a white body; then ten more measurements are made with the sample backed with a black body. The sample is placed over the opening of the instrument so that the yarns run parallel to a line 1961, pp. 322, 323 (namely, equations 48 and 55) are used to determine the scattering power K. The scattering coefficient s is then determined from the equation:
  • C is an instrument calibration constant and N is the fiber surface reflectivity.
  • the calibration constant can be determined by measuring s for a variety of yarns of known specific surface (e.g., smooth round fibers). This calibration constant should not differ much from unity; in the measurements given here it generally is about 0.9.
  • Fiber surface reflectivity N is calculated by the expression where H is the mean index of refraction of the fiber. If the fiber is birefringent and has two values for the index (n i. for parallel and i for perpendicular), then it should be recognized from the above discussion that some textile products could have large specific surface S principally due to extraneous effects, e.g., the presence of numerous closed-cell internal voids or pigments.
  • closed-cell voids would not generally be available to a liquid and would not contribute to water absorption even though they contribute to light scattering.
  • the scattering coefficient may be measured on a wet specimen. Because water or any common liquid has an index of refraction closer to that of the polymer than does air, the surface reflectivity wet is less than when dry and the scattering coefficient correspondingly lower. In the ideal case where all of the available surface is wetted by liquid, the wet and dry scattering would be proportional to the wet and dry reflectivity. However, in the test procedure summarized below, the sample is not immersed when it is tested. It is only wetted.
  • the sample is (l) soaked for 5 to 10 minutes in a water bath, (2) removed from the bath, (3) has one edge brought briefly into contact with a paper towel to eliminate excess liquid, and (4) then has its scattering coefficient determined as above. Under these test conditions, it is found that the products of this invention generally have a ratio of wet-to-dry scattering coefficient of much less than 0.4.
  • the textile products of this invention generally have a specific surface (dry) of at least 0.8 mF/gm. S can range up to 3 or more, but below 0.8, the covering power of the material is less than desiredIAn accepted 1968, p. 93 as 100 (R /R), and as recorded herein is normalized to a constant basis weight of 34 g. /m
  • the products of this invention are also stable to repeated exposure to water.
  • stable to repeated exposure to water means that the products do not change their structural characteristics (e.g., fibril concentration, specific surface or limiting surface tension) upon such repeated exposure, and that the products remain essentially unswollen, do not become slimy upon being wetted, and upon drying do not become stiff or hardened but rather remain essentially as pliable and soft as before wetting and drying.
  • the products are durable and derive their water-absorption characteristics from their basic structure and not from an additive that may be present only temporarily or that might be effected or removed upon repeated use of solvents or detergents commonly employed in laundering and drycleaning operations.
  • additives which may be present in the products of this invention include the usual textile additives, e.g., dyes, pigments, antioxidants, ,delusterants, antistatic agents, adhesion promoters, ultraviolet stabilizers, and the like.
  • textile products as used herein is defined as including strands, yarns, tapes, fabrics, ribbons, and the like. All these textile products are made of assemblies of fibrils.
  • the non-cellulosic, synthetic organic polymers from which the textile products are prepared are defined herein as polymeric products of at least filmforming molecular weight which are man-made by polymerization or copolymerization of various organic monomer units. Polymers made by chemical modification of naturally occurring products are not included in this definition.
  • the textile products of this invention are made from acrylonitrile or polyamide polymers.
  • polymer as used herein includes both homopolymers and copolymers, including binary and terpolymers, and the like.
  • Preferred polymers are the polyacrylonitriles, especially the acrylonitrile copolymers which contain major amounts of acrylonitrile units, and most preferably at least about 80 percent by weight acrylonitrile units.
  • Comonomers with acrylonitrile include styrene, methyl acrylate, itaconic acid, sodium styrene sulfonate, vinyl acetate, vinyl pyridine, and the like.
  • Useful polyamides include polycaproamide and its homologue polyhexamethylene urea, poly-1,4 benzamide and methylphenylene diamine isophthalic acid/terephthalic acid (70/30).
  • Other polymers which may be used to make textile products capable of absorbing water are those containing large amounts of ionic groups (e.g., sulfonic or carboxylic acids) or hydrogen bonding sites (e.g., amide or hydroxyl groups).
  • the "fibrils" of the fibril assemblies are fine elements which tend to lie roughly parallel to the major axis of the assembly.
  • An-assembly or portion of an assembly of fibrils is shown in.FlG. 5 and in the photomicrograph of FIG. 6.
  • a majority of the fibrils 30 are joined or interconnected to other fibrils to form a continuous structure.
  • Each fibril penetrates the array of adjacent fibrils in a random fashion before terminating at a junction as indicated by points 31.
  • the fibrils may be interconnected in a three-dimensional array.
  • the fibrils may be thought of as an intermingled non-planar matrix of very thin film or ribbon-like elements that are interconnected (joined) at various points to form a web-like three-dimensional network or plexus.
  • the fibrils come in many irregular shapes and sizes as shown in FIG. 7 which is a drawing of an enlarged cross-section of an assembly of fibrils called a plexifilamentary strand.
  • the rather irregular, convoluted, rolled up, or folded shape of most of the fibrils provides bulk to the strand and prevents excessively close packing of fibrils, which could block passages between fibrils thereby deleteriously affecting the wicking and the absorption of water.
  • Film-fibrils are the basic units from which the fibrils are built. Individual film-fibrils may have thicknesses averaging less than one or two microns, as measured with an interference microscope. The individual film-fibrils may occasionally appear as ribbons, such as the one labeled a in FIG. 7. More often, the film-fibrils are folded or rolled or convoluted about their axis, frequently appearing as multilayer laminates or aggregates (labeled b). Sometimes film-fibrils contain voids (labeled c). Any of these configurations, or combinations thereof, may constitute the fibrils defined above. It will be seen that the cross-section of the fibrils is irregular, thus lacking in symmetry and providing a rough fibril surface.
  • the fibril may correspond to a single film-fibril but more usually corresponds to an aggregation of film-fibrils and may be one to several times as thick as the film-fibrils of which it is constituted. Thickness measurements can be made with an interference microscope by the methods discussed in Interference Microscopy, King, Rienitz and Schulz, translated by J. H. Dickson, published by Hilger and Watts, Ltd., 1964.
  • a preferred type of fibril assembly is a plexifilamentary strand.
  • Plexifilamentary strands are a unitary or integral assembly of fibrils which because of their high degree of interconnection among fibrils form a continuous web or strand from one piece of polymer.
  • the term continuous is used herein in the sense that the plexifilament is an integral structure (due to the joining) over lengths many times greater than the length of its individual fibril components (i.e., often many meters or longer).
  • These continuous plexifilaments may, of course, be cut into staple fiber lengths (i.e., lengths suitable for conversion into yarn by established methods, usually 0.6 cm. or greater). They may also be combined intermingled or twisted together, and the like, to obtain higher denier.
  • the textile products of this invention and especially the plexifilamentary strands are prepared by flashextruding a uniform dispersion of the non-cellulosic synthetic organic polymer in water amounting to 25-40 percent by weight of the polymer through an orifice of about 0.02 to 0.75 mm. diameter.
  • particulate waterinsoluble stabilizers comprising up to 15 percent (preferably 2 to 12 percent) based on weight of the polymer employed, may be used.
  • Such stabilizers include: inorganic oxides, such as aluminum oxide; silicon compounds, such' as colloidal silica, aluminum silicate, ethyl orthosilicate; cellulose; and cross-linked vinyl polymers, for example, having sulfonic acid groups.
  • the dispersion may also be mechanically stirred to aid in maintaining uniformity.
  • the dispersion is heated and then extruded at temperatures between about 260 C. and about 280 C. and pressures of between about 50 atmospheres and about 110 atmospheres.
  • the pH of the aqueous dispersion is maintained on the acidic side, usually by addition of sulfuric acid, and pHs of between and 6.0, depending on the stabilizer present, are most useful.
  • the dispersion it is generally also useful to hold the dispersion at its extrusion temperature for a short time before extruding, e.g., for about 1 to 5, 10, 15 or even minutes; and it is sometimes convenient to raise the temperature in two discrete and separate levels during the heating. Moreover, it is sometimes advantageous to employ a pressure let-down region immediately adjacent the extrusion orifice.
  • a pressure let-down region immediately adjacent the extrusion orifice.
  • the polymer used is an acrylonitrile polymer
  • a mixture of water and acetonitrile may be employed as the dispersant medium and lower extrusion temperatures (e.g., 220 C.) may be used.
  • the procedure described in greater detail in the examples below, is preferred, particularly for use with the acrylonitrile polymers.
  • the textile products of this invention may also be prepared by flash spinning a solution of the noncellulosic synthetic organic polymer.
  • the solvent employed is one that should have a boiling point below the flow temperature of the polymer and should be able to form a single-phase solution of the polymer at the extrusion temperature but form a twoliquid phase system at the same temperature when the pressure on the solution is reduced in a let-down chamber.
  • the extrusion temperature employed should be within 40 C. of the critical temperature of the solvent; and a pressure of roughly 200-300 p.s.i. above the phase boundary at the extrusion temperature should be employed.
  • a let-down chamber is used and in this chamber the pressure is dropped to a value about 200 p.s.i. below the phase boundary.
  • the polymer concentration in the solution to be flash spun can range from about 10-40 percent by weight of the solution.
  • the yarns obtained are characterized in accordance with the procedures described above after all additives, finishes or contaminants have been removed.
  • siliceous materials are removed from the textile products by washing in dilute aqueous hydrofluoric acid.
  • Measured characteristics and some process conditions for all samples prepared in Examples I through 111 are given in Table II those of Examples IV and V, in Tables III and IV, respectively.
  • L is the length and D is the diameter of a circular orifice or length of tubing or pipe.
  • EXAMPLE I 15 samples of textile products in the form of continuous plexifilamentary strands having interconnected fibrils of irregular shape are prepared in accordance with the details given below from an acrylic terpolymer comprising 94 parts acrylonitrile (AN), 6 parts methyl acrylate (MA) and 0.12 parts sodium styrene sulfonate (SSS).
  • AN acrylonitrile
  • MA methyl acrylate
  • SSS sodium styrene sulfonate
  • Sample 1 A slurry comprising grams of the acrylic terpolymer, 2 grams of Cab-O-Sil colloidal silica and 79 ml. of water is prepared and adjusted to a pH of 4.8. A portion of this slurry is loaded into a cylindrical pressure vessel of about 15-cm. length and 2-cm. inside diameter which is fitted with a closed spinneret at one end and a piston at the other. Nitrogen pressure of 54.4 atm. is applied to the rear of the piston. The contents of the vessel are heated to 230 C., held at temperature for 5 minutes, and heated further to about 245 C. Total time of heating is about 20 minutes. The orifice, which measures 0.64 mm. D X 1.27 mm. L, is then opened and the sample is extruded.
  • Sample 2 A slurry is prepared as for Sample 1 except that 65 ml. of water is used. A lOO-gram portion is concentrated at 60 C. to a weight of 68 grams. A portion of this is extruded as per Sample 1, except that the temperatures are 250 and 270 C. and the orifice measures 0.51 mm. D X 0.64 mm. L.
  • Sample 3 A slurry is prepared as for Sample 1 except that ml. of water is used and a portion processed in the same manner except that a 4-minute hold at 250 C. and extrusion at 250 C. are used.
  • Sample 4 An aqueous slurry containing 29.5 percent of the acrylic terpolymer and 3.7 percent finely divided aluminum silicate is mixed continuously in a 208-1iter tank and pumped with a metering pump through 6.1 m. of steam-jacketed tubing of 6.35 mm. 1.D. (inside diameter) in which it is heated to about 150 to 170 C. The slurry is then raised to 280 C. and 83.3 atm. in an additional 6.1 m. of electrically heated, 7.72-mm. LD. tub- The slurry is passed through a 0.46 mm. D X 0.46 mm. L orifice into a pressure let-down chamber of 3.2-cm. volume, and finally through a 0.38 mm. D X 0.38 mm. L orifice to the atmosphere. In the let-down chamber, the temperature is 280 C. and the pressure is 63.9 atm. Total residence time in the heated zones is approximately 1 minute.
  • Sample 5 A slurry comprising 35 g. of the acrylic terpolymer, 0.14 g. of Cab-O-Sil silica, 6.0 g. of finely divided aluminum silicate, 11 ml. of water and m1. of acetonitrile is prepared. A portion of this slurry is processed in the same manner as for Sample 1 except that extrusion is at 255 C. through a 0.76 mm. D X 1.52 mm. L orifice.
  • Sample 6 An aqueous slurry containing 31 percent of the acrylic terpolymer and 4 percent finely divided aluminum silicate is processed continuously in the same equipment as used for Sample 4 except that (1) the slurry in the final heating stage reaches 279 C. and 85.7 atm., (2) the orifice at the entrance to the letdown chamber is 0.51 mm. D X 0.81 mm. L, and (3) the extrusion orifice, which measures 0.46 mm. D X 0.46 mm. L, is connected to a shroud comprising a cone opening into a cylindrical tube of 3.05 mm. D X 1.78 mm. L.
  • Sample 7 The same materials and apparatus as for Sample 6 are used except that: the slurry contains 31.5 percent acrylic terpolymer, is adjusted to a pH of 4.7, and finally heated to 272 C. and 91.8 atm.; the first orifice measures 0.51 mm. D X 0.51 mm. L, and steel wool is packed in the let-down chamber.
  • Sample 8 The same materials and apparatus as for Sample 6 are used except that: the slurry contains 31.5 percent acrylic terpolymer, is adjusted to a pH of 5.2, and is finally heated to 270 C. and 105.4 atm. infinal heating-stage tubing of M 18.3-meter length; and the shroud has a 40 entrance cone.
  • Sample 9 The same materials and apparatus as for Sample 7 are used except that: the slurry contains 31.5 percent acrylic terpolymer and 3 percent aluminum silicate, is adjusted to a pH of 4.8, and is finally heated to Sample 12.
  • the same materialsand apparatus as for Sample 6 are used except that: the slurry contains 31.5 percent acrylic terpolymer and is finally heated to 270 Cfand 90.1 atm.; the entrance orifice to the let-down chamber is 0.38 mm. D X 0.38 mm. L; the extrusion orifice is 0.30 mm. D X 0.30 mm. L; and the tubular section of the shroud is 2.03 mm. D X 1.27 mm. L.
  • Sample 13 An aqueous slurry containing 31.4 percent of the acrylic terpolymer and 4.6 percent Cab-O- Sil colloidal silica is prepared and then processed in the same way as Sample 1, except that the temperature after the final heating is 260 C. and the extrusion orifice measures 0.064 mm. D X 0.127 mm. L.
  • Sample 14 The same materials and apparatus as for Sample 6 are used except that: the slurry contains 32.5 percent acrylic terpolymer and 4.1 percent finely divided aluminum silicate, is adjusted to a pH of 4.0, is finally heated to 275 C. and 97.8 atm., and in the letdown chamber conditions are 273 C. and 91.1 atm.; the orifice at the inlet to the let-down chamber measures 0.76 mm. D X 0.89 mm. L; the extrusion orifice measures 0.33 mm. D X 0.33 mm. L; and the volume of the let-down chamber is 12.1 cm".
  • the extruded plexifilamentary yarn is passed through a 46-cm. long bath containing 95/5 water/ethylene carbonate at 34.3 cm./sec. at room temperature, then wrapped on a bobbin, and finally dried in an oven under vacuum at 80 C.
  • Sample 15 This sample is prepared the same way as Sample 14 except that the post-extrusion treatment bath contains 97.5/2.5 water/ethylene carbonate, the yarn speed in the bath is 10.7 cm./sec. and the yarn is dried by passage through a 60-cm.-long hot-tube oven held at 240 C.
  • Samples 1 through 13 are arranged in order of increasing fibril concentration. With the exception of Samples 1, 2 and 3, all samples of Example l absorbed wateras rapidly as, if not more rapidly than, cotton (see Example V). Samples 1, 2 and 3 each are outside the scope of this invention because of their low fibril concentration (i.e less than 5 X /cm?) Samples 14 and 15 show the general effect of how reducing specific surface, reduces the absorption rate.
  • Samples 4 through 13 and 15 are examples of this invention. 1f such continuous plexifilamentary yarns are to be dyed to a dark hue, one would choose a sample with a small value of specific surface (e.g., Sample 15). 1f whiteness is desired, a plexifilamentary yarn of high specific surface with large light-scattering ability would be preferred.
  • EXAMPLE 11 In this example, four samples of textile products in the form of continuous plexifilament yarns falling within the scope of this invention are prepared from an acrylic copolymer comprising about 96 parts acrylonitrile (AN) and 4 parts sodium styrene sulfonate (SSS).
  • AN acrylonitrile
  • SSS sodium styrene sulfonate
  • Sample 1 A slurry comprising 35 grams of the acrylic copolymer, ml. of water, and 9 grams of ethyl orthosilicate is prepared, and its pH adjusted to 1.4. A portion of this slurry is loaded into the same pressure vessel as used for Example 1, Sample 1. Nitrogen pressure of 54.4 atm. is applied to the piston. The vessel is then heated to 170 C., held at 170 C. for 5 minutes, and finally heated to 260 C. he contents are then passed through a 0.51 mm. D X 0.64 mm. L orifice into a 1.8 cm.- pressure let-down chamber, then through a 0.46 mm. D X 0.46 mm. L extrusion orifice which is attached to the same shroud as that described in Example l, Sample 6.
  • Sample 2 A slurry comprising 35 grams of the acrylic copolymer, 3 grams of Cab-O-Sil silica, and 65 ml. of water is prepared and the pH adjusted to 1.5. A portion of this slurry is processed as in Example 1, Sample 1, except that a 2-minute hold at 230 C. is used, and the extrusion orifice measures 0.46 mm. D X 0.46 mm.
  • Sample 3 A mixture of 4,620 grams of acrylic copolymer, 770 grams of Triton X- isooctyl phenoxy polyoxyethanol surfactant, 6,160 grams of acetonitrile, and 3,850 grams of water is heated in a stirred 18.9-liter autoclave to 222223 C. and 1 18 atm. Total heat-up time is 1 hour. The charge completely fills the vessel at the extrusion temperature and the pressure is internally generated by the confided liquid. The mixture is passed through a 100-mesh filter screen, then through a 0.61 mm. D X 0.64-mm. L orifice into a 1.27 cm. D X 8.4 cm. L pressure let-down chamber and finally through a 0.41 mm.
  • Sample 4 The same materials and apparatus as for Sample 3 are used except that: the temperature and pressure in the autoclave are 221 C. and atm.; the total heating time is 40 min.; the let-down chamber inlet orifice measures 0.86 mm. D X 0.64 mm. L and the extrusion orifice measures 0.58 mm. D X 0.51 mm. L; within the let-down chamber the temperature is 219 C. and the pressure is 102 to 103 atm.; and the extruded'plexifilamentary yarn is drawn 2.4X.
  • Sample 1 A slurry comprising 35 grams of polycaproamide, 5.0 grams of Cab-O-Sil silica, and 65 ml. of water is mixed and a portion is loaded into the same pressure vessel as used for Example I, Sample 1. The pH of the mixture is 6.0. Nitrogen pressure of 54.4 atm. is applied to the piston and the vessel is heated to 230 C., held at 230 C. for minutes, and then heated further to about 260 C. Total heat-up time, including the hold, is about 20 minutes. The material is then extruded through an orifice measuring 0.64 mm. D X 1.27 mm. L.
  • Sample 2 A mixture comprising 35 grams of polycaproamide and 65 grams of 95 percent ethanol is heated to 200 C. in a cylindrical autoclave of about l-liter capacity, which is fitted with a piston which applies a pressure of 170 atm. to the mixture. Total heat-up time is about 35 minutes.
  • the autoclave is connected to a twin autoclave by two square channels, each being about 6.25 mm. X 6.25 mm. X 13 cm. long, each having four 90 bends and the interior of each being connected to the other three times between their common entrances and exits.
  • the heated charge is forced back and forth through this tortuous path to ensure good mixing.
  • the charge is finally passed from one of the cylinders through a 0.64 mm. D X 0.64 mm. L orifice into a 1.7-cm. pressure let-down chamber, and then through a 0.46 mm. D X 0.51 mm. L extrusion orifice to atmospheric conditions.
  • F Fibri1 concentration, fibrils/cm.
  • ifilamentary yarns comprising continuous assemblies of fibrils, the fibrils being generally of irregular crosssection.
  • the yarns are stable to repeated exposure to water, have a limiting surface tension (7 of greater than 72 dynes/cm., a specific surface (S) of greater than 0.8 m. /g., a fibril concentration (F) of greater than 5 X 10 /cm3, and an H parameter, ('y,,72)(F/10 (8), of greater than 6.
  • Sample l.'A slurry is prepared containing 13.3 grams of a copolymer comprising 94 parts by weight of acrylonitrile (AN), about 0.1 part sodium styrenesulfonate and 6 parts vinyl acetate (VA), 26 ml. of water, and 1.4 grams of Cab-O-Sil colloidal silica. The pH is adjusted to 4.0.
  • the slurry is loaded into the same pressure vessel as used for Example 1, Sample 1. A pressure of 54.4 atm. is applied.
  • the slurry is heated rapidly to 260 C., then passed through a filter comprising a 1.5- cm. thickness of stainless steel wool and a IOO-mesh screen, and finally extruded through a 0.63-mm.
  • D X 0.63-mm. L orifice which is connected to a shroud having a cone of about 2-mm. length.
  • Sample 2 The same materials, apparatusjand cess as used for Sample 1 are employed for this sample, except that the slurry contains 1.4 g. of finely divided aluminum silicate in place of the Cab-O-Sil and the pH is adjusted t o 4 .5
  • Extrusion conditions are just upstream of the extrusion orifice or spinneret.
  • d Density (reciprocal of bulk) is based on the weight, width, length and thickness of the sample used in the absorption rate test while the pad is under the BOO-gram load.
  • EXAMPLE IV In this example, several other copolymers of acrylonitrile are used to make six samples of textile products of this invention.
  • the products are in the form of plex- .me sq stqilmttPAQ- 1 tum-J1.-.
  • Sample 2 A 23 percent solution of the same acrylic terpolymer-used for Sample-l is dry spun through a 10- hole spinneret having 0.13-mm. diameter holes. Spinning pressure is 4.8 atm. and solution temperature is 45 C. The extrudate is collected at the rate of 272 10- m./min. with a spin-stretch factor of 10. The yarn is plied and steam drawn 13X. The final yarn has 2,000 filaments of 0.2 dpf.
  • Sample 3 This commercial continuous filament nylon yarn manufactured and sold by Allied Chemical Company, Hopewell, Virginia, as 200-l6-l.5Z-BW, is a bright 6-nylon (polycaproamide) yarn having 16 filaments totaling 200 denier.
  • the yam has a Z twist of 1% turns per inch.
  • Sample 6 is a spun yarn removed from a mans cotton T-shirt.
  • Sample 7 is a spun yarn removed from a cotton towel. The yarns are charple. acterized after removal of all additives and finis hes. n
  • Density of the textile product (in the water-absorption sample pad) in gram/cm 1, is the water-absorption rate in ml/sec.
  • Sample 1 A dimethyl formamide solution containing 65 26 percent of the acrylic terpolymer used in Example l is dry spun through a l0-hole spinneret having 0.16 mm.-diameter holes. Solution temperature is 80 C.
  • the textile products of this invention are intended for a wide range of textile uses. Because of the extraordinary ability to absorb large quantities of water rapidly, many can serve in end uses from which synthetic organic polymeric fibers have heretofore been excluded. In many instances, spun cotton yarns may be inferior to the preferred plexifilamentary strands of this invention, because cotton requires high amounts of twist to form a continuous load bearing structure while the preferred plexifilamentary strands are a continuous network as formed and require little or nor twist. High amounts of twist reduce the absorption rate of yarns. However, the
  • strands may be twisted or may be cut into staple lengths and spun into yarns as is cotton or may be converted into paper or processed into other nonwoven materials.
  • the resultant products still provide acceptable water absorption rates along with satisfactory cover and bulk.
  • Fabrication of a terry-cloth towel completely from textile-product yarns of this invention is illustrated as follows: plexifilaments of acrylonitrile terpolymer are spun essentially in the same manner as those of Example 1, Sample 8. The plexifilaments are prepared into yarns and then fabricated into a terry-cloth towel.
  • the towel contains a woven ground having 25.2 ends per cm. (in the warp direction) and 20.5 picks per cm. (in the fill direction); has a pile-to-ground-yarn weight ratio of 5.8/1, weighs 373 grams/m and measures 0.43 cm. in thickness.
  • the ground yarns are of 260 to 265 denier and have a twist of two turns per cm.
  • the yarn for the pile is passed at 15.2 m./sec. through an interlacing jet operating with steam at 9.5 atm. and 275 C.
  • the pile yarn is 223 denier.
  • the towel is very soft and highly effective in absorbing water.
  • a textile product having water-absorbing characteristics comprising an assembly of fibrils, said assembly being of at least staple fiber length; said fibrils being of irregular cross-section and being composed of a noncellulosic, synthetic, organic polymer, with a majority of said fibrils being interconnected at various points to form a plexus; said product being stable to repeated exposure to water, and having a limiting surface tension (y greater than 72 dynes per centimeter, a specific ac o at least ab qu remetetp m”) and a fibril concentration (F) of at least about 5 X 10 per square centimeter. said numerical values of y,,, S and F also being such that the parameter for said product is greater than 6.
  • acrylonitrile polymer is a terpolymer containing a major amount of acrylonitrile and minor amounts of methyl acrylate and sodium styrene sulfonate.
  • acrylonitrile polymer is a copolymer containing a major amount of acrylonitrile and a minor amount of sodium styrene sulfonate.

Abstract

Textile products comprising an assembly of fibrils. The assembly can be in the form of a yarn, plexifilament, fabric, or the like, and is of at least staple fiber length. The fibrils are of irregular cross-section and are composed of a non-cellulosic, synthetic organic polymer, and most are interconnected to form a plexus. The products are stable to repeated water exposure, and have a limiting surface tension greater than 72 dynes per centimeter, a specific surface of at least about 0.8 square meter per gram, a fibril concentration of at least about 5 X 103 per quare centimeter, and a wicking parameter greater than 6. The products can be prepared by extruding an aqueous dispersion of the polymer at selected elevated temperature and pressure conditions. Preferred products are plexifilamentary strands of an acrylonitrile polymer. The products are useful in textile applications, particularly in such applications where good waterabsorption characteristics are desirable.

Description

United States Patent [191 Woodell HYDROPHILIC TEXTILE PRODUCTS [75] Inventor: Rudolph 'Woodell, Richmond, Va.
[73] Assignee: E. I. du Pont de Nemours and Company, Wilmington, Del.
[ Notice: The portion of the term of this patent subsequent to Apr. 1 1, 1989,
has been disclaimed.
[22] Filed: June 2, 1972 21 App]. No.: 259,175
Related US. Application Data [63] Continuation-in-part of Ser. No. 86,438, Nov. 3, 1970, abandoned, which is a continuation-in-part of Ser. No. 71,582, Sept. 11, 1970, Pat. No. 3,659,498, which is a continuation-in-part of Ser. No. 677,949, Oct. 25, 1967, abandoned.
[52] US. Cl. 57/140 R, 57/140 J, 161/172, 161/177 [51] Int. Cl D02g 3/02, D02g 3/22 [58] Field of Search 161/172, 178, 169, 161/177, 165; 264/176; 57/140 R, 140 J [56] References Cited UNITED STATES PATENTS 3,081,519 3/1963 Blades et a]. 161/173 X 3,227,784 1/1966 Blades et a]. 264/176 X 3,290,207 12/1966 Magat et al 161/178 3,169,899 2/1965 Steuben 161/172 FOREIGN PATENTS OR APPLICATIONS 891,943 3/ 1962 Great Britain 891,945 3/1962 Great Britain 1,090,478 1 l/1967 Great Britain 1,114,151 5/1968 Great Britain 1,129,831 10/ 1 968 Great Britain Primary ExaminerGeorge F. Lesmes Assistant ExaminerLorraine T. Kendell AttorneyGary A. Samuels [5 7] ABSTRACT Textile products comprising an assembly of fibrils. The assembly can be in the form of a yarn, plexifilament, fabric, or the like, and is of at least staple fiber length. The fibrils are of irregular cross-section and are composed of a non-cellulosic, synthetic organic polymer, and most are interconnected to form a plexus. The products are stable to repeated water exposure, and have a limiting surface tension greater than 72 dynes per centimeter, a specific surface of at least about 0.8 square meter per gram, a fibril concentration of at least about 5 X 10 per quare centimeter, and a wicking parameter greater than 6. The products can be prepared by extruding an aqueous dispersion of the polymer at selected elevated temperature and pressure conditions. Preferred products are plexifilamentary strands of an acrylonitrile polymer. The products are useful in textile applications, particularly in such applications where good water-absorption characteristics are desirable.
12 Claims, 7 Drawing Figures Patented Nov 27, 1913 3,774,387
4 Sheets-Sheet l FIG-Z Patented Nov. 27, 1973 4 Sheets-Sheet 3 FIG-4 O 0 86:2 MEE zofiniom @503 LIQUID SURFACE TENSION,
DYNES/ CM Patented Nov. 27, 1973 4 Sheets-Sheet 4 FIG-5 1' HYDROPI-IILIC TEXTILE PRODUCTS CROSS-REFERENCE To RELATED.
APPLICATIONS BACKGROUND OF THE INVENTION FIELD OF THE INVENTION This invention relates to textile products, and more particularly to assemblies of fibrils of non-cellulosic synthetic organic polymers. The products possess good water-absorption characteristics.
BACKGROUND OF THE INVENTION properties that enable them to be employed in such end uses.
Several types of textile products containing fibrils of synthetic organic polymers are found in the prior art. Some are produced by mechanically working or fibrillating sheets, bands, films, foils, ribbons or filaments of highly oriented organic polymers. Others are produced by melt-extruding blends of two or more incompatible polymers into filaments or sheets, followed by drawing the extrudate and then either mechanically working to cause fibrillation or extracting ordissolving one of the polymers to leave a coarsely fibrillated product. Other such fibrillated products are prepared by stretching or mechanically working foamed polymeric sheets or filaments. Still other fibrillated products, such as plexifilamentary strands, are produced by flashextruding a solution of a crystalline synthetic organicpolymer in an activating liquid under superatmospheric pressure and at a temperature in excess of the boiling point of the activating liquid into a region of lower pressure.
None of the prior art products described above possess all the structural features that provide the good water-absorption characteristics of the textile products of this invention.
SUMMARY OF THE INVENTION The invention is directed to a textile product comprising an assembly of fibrils, said assembly being of at least staple-fiber length; said fibrils being of irregular cross-section and being composed of a non-cellulosic, synthetic, organic polymer, with a majority of said fibrils being interconnected at various points to form a plexus; said product being stable to repeated exposure to water, and having a limiting surface tension ('y greater than 72 dynes per centimeter, and a specific surface (S) of at least about 0.8' square meter per gram, and a fibril concentration (F) of at least about 5X 10 per square centimeter, said numerical values of Y0, S and F also being such that the expression for said product is greater than 6.
The products defined above have high surface area, high coveringpower and absorb water as well as, or even better, than cotton, thus renden'ng'them useful in textile applications from which wholly synthetic organic fibers have generally been excludedheretofore:
Because of the fewer process steps needed compared to alternative processes, and because of better control of product quality, it is preferred to obtain the product of this invention in the form of continuous plexifilamentary'strands;
DESCRIPTION OF THE DRAWINGS The invention may be more easily understood by reference to the figures where FIG. 1 illustrates the relationship between the waterabsorption rate and the parameter for-several assemblies of fibrils within the scope of this invention and some conventional yarns outside the scope of this invention;
FIG. 2 is a top view of a sample holder employed with the apparatus of FIG. 3;
FIG. 3 is a cross-section of an apparatus for determining liquid-absorption rates of textile products;
FIG. 4-shows the relationship between the surface tension and the absorption rate of liquidi'asmeasured on three textile products of an acrylonitrile terpolymer, each product having a different fibril concentration;
FIG. 5 is a drawingof a magnified longitudinal section of an assembly of fibrils of a textile product within .the scope of' this invention;
FIG. 6 is a photomicrograph of a greatly magnified longitudinal section of an assembly of fibrils of a textile product within the scope of this invention; and
FIG. 7 is a drawing of an enlarged cross-section of an assembly of fibrils of a textile product within the scope of this invention.
DESCRIPTION OF THE INVENTION It has been found that when fibril assemblies of noncellulosic synthetic organic textile products have the specific surface, fibril concentration and limiting surface tension recited above, the products have an increased propensity for absorbing water.
The ability of a fibrillated textile product to absorb water can be determined from the expression S is the specific surface of the product measured as hereinafter described, in square meters per gram.
As is shown in FIG. 1, the above-described waterwicking parameter H is directly proportional to waterabsorption rates. Thus, as the water-wicking parameter of a textile product increases, the water-absorption rate of the product also increases at roughly the same percentage increments. FIG. 1 also depicts the superiority of the plexifilamentary products of this invention over corresponding conventional textile filaments.
The wicking parameter used herein to combine the various critical structural features of the products of surface tension (y characteristic of the polymer will not be absorbed by a textile product made from the polymer, whereas liquids with 7 less than the 7,, of the polymer will be absorbed at a rate proportional to the this invention is derived from a more generalized equation for the rate of liquid absorption by a textile product comprising an assembly of fibrils of generally irregular cross-section, namely,
where I is the absorption rate in ml./sec., y is the liquid surface tension in dynes/cm. of the liquid tested, 1. is the liquid viscosity in centipoise ofthe liquid tested (usually at 25 C.), and y F and S are as previously defined. This generalized equation was developed from a large series of tests on products both within the scope of, and outside the scope of, this invention. To reduce the generalized equation to one applicable to water only, values for the viscosity and surface tension of water are substituted, constants rearranged, and exponents rounded off, to give the equation where I is the water-absorption rate.
Tests with various samples of cotton by procedures described below show that cotton absorbs water at rates equal to or above 0.086 ml./sec. Thus, in order to absorb water as well as cotton, a textile product of this invention must have a water-wicking parameter of at least When the wicking parameter exceeds 6, the textile products of this invention absorb water as fast as, or even faster than, the cotton materials tested. The preferred plexifilamentary products of this invention, however, frequently have wicking parameters well in excess of 6, as for example, up to 75 or more.
Of course, to fall within the scope of this invention, the textile product must also be stable to repeated exposure to water, have a limiting surface tension value (7 of greater than 72 dynes/cm. (and, preferably, at least 74 dynes/cm.), a fibril concentration (F) of at least X l0 /cm. and a specific surface (S) of at least 0.8 m. /gm. These characteristics and the tests used to measure them are described below.
DETERMINATION OF LIMITING SURFACE TENSION The term limiting surface tension ('y,,) as defined herein is a characteristic of a synthetic organic polymer and is independent of the shape of the polymer. That is, fibers, filaments, fibrillated materials or films of the same polymer all have the same limiting surface tension characteristic. The limiting surface tension is important in determining whether a liquid will be absorbed by a textile product prepared from any given polymer; liquids with surface tensions (y) greater than the limiting difference (y -y). The term absorb as used herein refers to capillary wicking absorption and not to absorption by swelling or by a chemical mechanism.
To measure the limiting surface tension characteristic of a textile product, a series of absorption-rate tests are carried out with liquids of different surface tension, and the viscosity-normalized initial absorption rates, I,,, so obtained are plotted on linear coordinates against the surface tension of the liquid used in the tests.
To measure the absorption rate, the procedure described generally by E. M. Buras, Jr., et al., Measurement and Theory of Absorbency of Cotton Fabrics, Textile Research Journal, Vol. 20, April, 1950, pp. 239-248, is followed.
The textile product to be tested is first washed or treated (e.g., with water, soap solution, dry-cleaning fluid, or aqueous hydrofluoric acid) to remove any additives or contaminants, then rinsed, wrapped on a soft gauze-covered batting, boiled in distilled water for about 30 minutes, dried in a vacuum oven at about 60 C., and cooled. The treated product is then wrapped around a Teflon polytetrafluoroethylene form constructed, as shown in FIG. 2, by cutting a 5.7-cm.- diameter circle from a 0.l6-cm.thick sheet of Teflon and cutting so that dimension 11 is 3.2 cm. and dimen sion 12 is 4.0 cm. The form is mounted on a yarn winder to permit rotation about axis 13. The product is fed to the form through a constant tension device which exerts a load equivalent to 0.05 gram per denier. The winder transverse pitch is adjusted so that with each turn of the winder, product is laid on the form as closely adjacent its neighbor as possible. The textile product should preferably be twistless when wound. The number of turns (Y) (i.e., the number of parallel lines of material) per layer and the number of complete layers (N) needed to wind a total of about 0.5 gram of product are recorded. A minimum of at least two layers of product is required, and in those cases where very large denier yarns are used, the 0.5-gram limit may be exceeded in order to obtain the required two-layer minimum.
The textile product on the form, prepared as described above and referred to hereinafter as a sample pad, is placed in the absorption-rate testing apparatus shown in FIG. 3. This apparatus comprises a Buchner funnel 20, containing a flat, horizontal, fritted-glass plate 21 measuring 5.8 cm. in diameter by 0.55 cm. in thickness and having a resistance to flow of water of about 0.083 ml./sec./cm. water pressure. The funnel is attached through a flexible coupling tube 22 to a horizontal tube 23 having a 0.3l-cm. inside diameter. When the apparatus is filled with liquid, tube 23 acts as a reservoir for liquid 24. The top of porous plate 21 is positioned 1.3 cm. above the top inside surface of the horizontal reservoir.
To carry out an absorption-rate determination, porous plate 21, lower portion of funnel 20, flexible coupling tube 22, and part of horizontal tube 23 are filled by adding liquid 24 through the top of plate 21, and applying suction to tube 23. All bubbles are removed from the liquid system. Excess liquid, if any, is removed from the top of plate 21. The system is thus filled with liquid from the meniscus in tube 23 to the top of plate s 21. The sample pad 25 is then placed on top of porous plate 21 and an evenly distributed, load 26 of 500 grams placedon the pad. Theamount of liquid absorbed by pad 25 is measured by the movement of the meniscus in tube 23 with the aid of scale 27. Absorption data are collected as a function of time, starting within about two seconds after the sample pad and weight are placed on the porous plate and finishing when less than about 0.01 ml. of liquid is absorbed during a 60-second period. The cumulative volume of liquid absorbed q, in
ml., is plotted against time t, in seconds. The initial ab made with twistless yarns, even though the determination of limiting surface tension does not require that the yarns of the sample pad be twistless.
The textile products of this invention generally display absorption-characteristic curve similar to that of curve c in FIG. 4. As can be seen from the figure, these curves generally have a steep straightline portion of negative slope which levels off as liquid surface tension is reduced. This straightline portion must be defined by several points in order to obtain an accurate measurement (or extrapolation) for 7 To improve the accuracy of the determination, absorption curves for several samples of a given polymer are generated and the intercepts of these curves with the surface-tension axis are averaged to define y to within about :1 dyne/cm. Preferably, 'y,, is determined from samples that yield an absorption rate curve that has a slope steeper than -0.005
rate of a test product, the results of the first run on a sample pad are always discarded. Additional runs are made until the results from three consecutive runs are substantially constant. Generally, a total of four runs is sufficient. Between runs, the pads are washed and then dried at 60 C. in a vacuum oven. At least three sample pads of the same product should be tested in this manner and the measured absorption rates from each sample averaged to obtain an accurate value for the initial absorption rate for the product under test.
' To characterize the liquid-absorption characteristics of the textile products, the absorption-rate tests described above are carried out with liquids of different surface tensions. These liquids are easily prepared from solutions of ethanol in water, calcium chloride in water or sodium nitrate in water, depending upon the surface tension desired. To isolate the effect of surface tension on liquid absorption, a correction is made for liquid viscosity by multiplying the absorption rates by the viscosity' of the liquids employed and dividing by the viscosity of water. This procedure gives viscosity-normalized initial absorption rates, -I,,'. Surface tensions for aqueous solutions of ethanol, calcium chloride, and sodium nitrate are given in Lan ges Handbook of Chemistry, 10th Edition, N. A. Lange, Editor, McGraw Hill, N.Y., 1967, pages 1664, 1666. Viscosities of ethanol-water solutions are given on page l679.-Viscosities of aqueous solutions of sodium nitrate are given in Ann. Physik Chem, 159, l35 (1876) and of calcium chloride in J. Timmermans, The Physico-Chemical Constants of Binary Systems in Concentrated Solutions, Vol. III, Interscience' Publishing, Inc., N.Y., 1960, p. 763.
The viscosity-normalized initial absorption rate, I is plotted on linear coordinates against the surface tension of the liquid used in the test. Such a plot is illustrated in FIG. 4 wherecurve a represents the absorp: tion-rate characteristics of a sample pad made from very fine denier filaments (not fibrillated) of an acrylonitrile terpolymer; curve b, a sample pad made from somewhat fibrillated material of the same terpolymer falling outside the scope of this invention; andc, a sam- 1 ple pad of well-fibrillated material of the same terpolymer falling within the scope of this invention. All three curves intersect the surface-tension axis at the same value of 80.3 dynes/cm. This value, where the curves intersect the axis, is the limiting surface tension (y characteristic of the polymer being tested.
All liquid absorption rates of the textile products of this invention provided herein are determined on pads ml./sec./dyne/cm.
The limiting surface characteristic of six polymers and cotton, determined in the above-described manner, are listed in the following Table l.
. TABLE I Limiting Surface Test Material Tension, y dynes/cm. Polyethylene 32. l Polyethylene terephthalate 57.7 6-6 nylon (polyhexamethylene adi- 64.7 pamide) 6 nylon (polycaproamide) 78.8 Acrylic terpolymer (acrylonitrile/ 80.3 methyl acrylate/sodium styrene sulfonate, 94/6/0.12) Acrylic copolymer (acrylonitrile/ 81.5 sodium styrene sulfonate, 94/6) Cotton 82.2
Of the materials listed in Table 1, those made from the first three polymers, no matter how well fibrillated, do not absorb water; those of the next three polymers, when in the well-fibrillated form of this invention, absorb water very rapidly; and, of course, the last material, cotton, also absorbs water very well. The limiting surface tension characteristic of all polymers that absorb water in these tests is greater than 72 dynes/cm., the surface tension of water. Polymers with limiting surface tension characteristics greater than 74 dynes/cm. are preferred. The 7,, can range up to or greater.
DETERMINATION OF FIBRIL CONCENTRATION AND SPECIFIC SURFACE It has been found that the rate at which'a textile product of this invention absorbs liquid depends not only on the (y -y) driving force and the viscosity (p.)-of the liquid, but also on fibril concentration (F) and specific surface (S). F may be visualized as being related to the number of capillary paths available to the liquid and S may be thought of as being related to, the surface available per path. These characteristics and tests used to measure them are described as follows:
Fibril Concentration (F) Fibril concentration (F) is defined as the number of ends per cm. oftextile product cross-section and can be determined by the following formula which applies to the sample pad used for the absorption-rate test:
[(L) (Y) (ml/rm (wn where L is the number of layers of product in the sample pad, Y is the number of turns per layer on the pad (i.e., Y is defined as the number of parallel lines of product). Thus, when yarn is employed, Y is the number of turns per layer and when a sheet or ribbon is used, Y is the number of sheets or ribbons that lie side by side in each layer of the sample pad. Whether yarn, bundles, sheets, strands, ribbons, filaments, etc., all will be referred to hereinafter as yarn. The number of fibrils per cross-section of yarn is n; the total thickness in cm. of the material while under load in the Buchner funnel of the absorption-rate apparatus (excluding the thickness of the Teflon form) is t; and the total width in cm. of the sample wound on the padis w. The number of fibrils or ends per yarn n, is determined from photomicrographs of the crosssection of the opened yarn (e.g., an opened plexifilamentary strand). Four representative cross-sectional samples, each microns thick, are taken from the length of the yarn and the photomicrographs of these cross-sections are prepared by standard procedures, well known in the art. Three fibril counts are made on each of the photomicrographs. The 12 counts are then averaged to obtain n. Care must be taken not to alter the yarn (e.g., by breaking tie points, breaking fibrils or joining fibrils) during this determination. The photomicrograph should provide a linea'l magnification of about SOOX. Each individual fibril appears as an independent particle on the photomicrograph. A representation of such a photomicrograph is shown in FIG. 6 where several types of fibrils are identified, as discussed further below.
To fall within the scope of this invention, F must be at least 5 X lO/cm. Below this value of F, the materials are coarse and unsuited for general textile use. In general, F can range up to 15 X l0/cm., or more.
Specific Surface (S) Specific surface (S) of a textile product is derived from optical measurements of the light scattering coefficient (s). High specific surface provides good covering power and promotes rapid absorption of liquid. It is known that a light scattering coefficient is a measure of the specific surface of a material (TAPPI, V0. 42, No. 12, December 1959, pages 986-994). Light scattering measurements are used to derive the specific surface of the textile products of this invention by the procedure described below.
A sample suitable for light reflectance measurements is prepared by winding a close-packed parallel warp of product, preferably in the form of yarns, on a rectangular frame (e.g., measuring about 10 cm. X 8 cm.). A yarn winder (e.g., Suter yarn evenness controller) is used to hold the frame and rotate it. A light tension (e.g., at about 2 grams) is maintained on the yarn to keep it essentially straight. The guide traverse controlling the number of threads per cm. is adjusted to provide a specimen with no gaps between the elements of the parallel warp. When the sample is in the form of a sheet or fabric, winding on a frame is not necessary; the flat planar sample may be used directly.
A Bausch and Lomb Opacimenter is adjusted to read absolute reflectance by calibration with a standard having an absolute reflectance of about 75 percent. Absolute reflectance is measured at ten points on the sample with the sample backed by a white body; then ten more measurements are made with the sample backed with a black body. The sample is placed over the opening of the instrument so that the yarns run parallel to a line 1961, pp. 322, 323 (namely, equations 48 and 55) are used to determine the scattering power K. The scattering coefficient s is then determined from the equation:
To convert this scattering coefficient into optical specific surface area, the following equation is used:
where C is an instrument calibration constant and N is the fiber surface reflectivity. The calibration constant can be determined by measuring s for a variety of yarns of known specific surface (e.g., smooth round fibers). This calibration constant should not differ much from unity; in the measurements given here it generally is about 0.9. Fiber surface reflectivity N is calculated by the expression where H is the mean index of refraction of the fiber. If the fiber is birefringent and has two values for the index (n i. for parallel and i for perpendicular), then It should be recognized from the above discussion that some textile products could have large specific surface S principally due to extraneous effects, e.g., the presence of numerous closed-cell internal voids or pigments. Although such products might have the same specific surface values as products without closed-cell internal voids, they would not possess the same waterabsorption characteristics. For example, closed-cell voids would not generally be available to a liquid and would not contribute to water absorption even though they contribute to light scattering.
To distinguish these products having closed-cell internal voids from the products without such voids, the scattering coefficient may be measured on a wet specimen. Because water or any common liquid has an index of refraction closer to that of the polymer than does air, the surface reflectivity wet is less than when dry and the scattering coefficient correspondingly lower. In the ideal case where all of the available surface is wetted by liquid, the wet and dry scattering would be proportional to the wet and dry reflectivity. However, in the test procedure summarized below, the sample is not immersed when it is tested. It is only wetted. The sample is (l) soaked for 5 to 10 minutes in a water bath, (2) removed from the bath, (3) has one edge brought briefly into contact with a paper towel to eliminate excess liquid, and (4) then has its scattering coefficient determined as above. Under these test conditions, it is found that the products of this invention generally have a ratio of wet-to-dry scattering coefficient of much less than 0.4.
The textile products of this invention generally have a specific surface (dry) of at least 0.8 mF/gm. S can range up to 3 or more, but below 0.8, the covering power of the material is less than desiredIAn accepted 1968, p. 93 as 100 (R /R), and as recorded herein is normalized to a constant basis weight of 34 g. /m
Stability to Water I The products of this invention are also stable to repeated exposure to water. The term stable to repeated exposure to water means that the products do not change their structural characteristics (e.g., fibril concentration, specific surface or limiting surface tension) upon such repeated exposure, and that the products remain essentially unswollen, do not become slimy upon being wetted, and upon drying do not become stiff or hardened but rather remain essentially as pliable and soft as before wetting and drying. The products are durable and derive their water-absorption characteristics from their basic structure and not from an additive that may be present only temporarily or that might be effected or removed upon repeated use of solvents or detergents commonly employed in laundering and drycleaning operations. Thus, the term repeated is understood as not including any initial washings of the product which may wash out or extract such additives. Such additives which may be present in the products of this invention include the usual textile additives, e.g., dyes, pigments, antioxidants, ,delusterants, antistatic agents, adhesion promoters, ultraviolet stabilizers, and the like.
THE PRODUCTS AND THEIR PREPARATION The term textile products as used herein is defined as including strands, yarns, tapes, fabrics, ribbons, and the like. All these textile products are made of assemblies of fibrils. The non-cellulosic, synthetic organic polymers from which the textile products are prepared are defined herein as polymeric products of at least filmforming molecular weight which are man-made by polymerization or copolymerization of various organic monomer units. Polymers made by chemical modification of naturally occurring products are not included in this definition.
Preferably, the textile products of this invention are made from acrylonitrile or polyamide polymers. The term polymer as used herein includes both homopolymers and copolymers, including binary and terpolymers, and the like. Preferred polymers are the polyacrylonitriles, especially the acrylonitrile copolymers which contain major amounts of acrylonitrile units, and most preferably at least about 80 percent by weight acrylonitrile units. Comonomers with acrylonitrile include styrene, methyl acrylate, itaconic acid, sodium styrene sulfonate, vinyl acetate, vinyl pyridine, and the like. Useful polyamides include polycaproamide and its homologue polyhexamethylene urea, poly-1,4 benzamide and methylphenylene diamine isophthalic acid/terephthalic acid (70/30). Other polymers which may be used to make textile products capable of absorbing water are those containing large amounts of ionic groups (e.g., sulfonic or carboxylic acids) or hydrogen bonding sites (e.g., amide or hydroxyl groups).
Common polymers which do not permit absorption of water are polypropylene, polyvinyl chloride, polyethylene terephthalate, polystyrene and the polyacetals.
The "fibrils" of the fibril assemblies are fine elements which tend to lie roughly parallel to the major axis of the assembly. An-assembly or portion of an assembly of fibrils is shown in.FlG. 5 and in the photomicrograph of FIG. 6. A majority of the fibrils 30 are joined or interconnected to other fibrils to form a continuous structure. Each fibril penetrates the array of adjacent fibrils in a random fashion before terminating at a junction as indicated by points 31. The fibrils may be interconnected in a three-dimensional array. Thus, the fibrils may be thought of as an intermingled non-planar matrix of very thin film or ribbon-like elements that are interconnected (joined) at various points to form a web-like three-dimensional network or plexus.
The fibrils come in many irregular shapes and sizes as shown in FIG. 7 which is a drawing of an enlarged cross-section of an assembly of fibrils called a plexifilamentary strand. The rather irregular, convoluted, rolled up, or folded shape of most of the fibrils provides bulk to the strand and prevents excessively close packing of fibrils, which could block passages between fibrils thereby deleteriously affecting the wicking and the absorption of water.
Film-fibrils are the basic units from which the fibrils are built. Individual film-fibrils may have thicknesses averaging less than one or two microns, as measured with an interference microscope. The individual film-fibrils may occasionally appear as ribbons, such as the one labeled a in FIG. 7. More often, the film-fibrils are folded or rolled or convoluted about their axis, frequently appearing as multilayer laminates or aggregates (labeled b). Sometimes film-fibrils contain voids (labeled c). Any of these configurations, or combinations thereof, may constitute the fibrils defined above. It will be seen that the cross-section of the fibrils is irregular, thus lacking in symmetry and providing a rough fibril surface. It is believed that such an irregular surface promotes water absorption. Thus, the fibril may correspond to a single film-fibril but more usually corresponds to an aggregation of film-fibrils and may be one to several times as thick as the film-fibrils of which it is constituted. Thickness measurements can be made with an interference microscope by the methods discussed in Interference Microscopy, King, Rienitz and Schulz, translated by J. H. Dickson, published by Hilger and Watts, Ltd., 1964.
A preferred type of fibril assembly is a plexifilamentary strand. Plexifilamentary strands are a unitary or integral assembly of fibrils which because of their high degree of interconnection among fibrils form a continuous web or strand from one piece of polymer. The term continuous is used herein in the sense that the plexifilament is an integral structure (due to the joining) over lengths many times greater than the length of its individual fibril components (i.e., often many meters or longer). These continuous plexifilaments may, of course, be cut into staple fiber lengths (i.e., lengths suitable for conversion into yarn by established methods, usually 0.6 cm. or greater). They may also be combined intermingled or twisted together, and the like, to obtain higher denier.
The textile products of this invention and especially the plexifilamentary strands, are prepared by flashextruding a uniform dispersion of the non-cellulosic synthetic organic polymer in water amounting to 25-40 percent by weight of the polymer through an orifice of about 0.02 to 0.75 mm. diameter. To maintain uniformity of the aqueous dispersion, particulate waterinsoluble stabilizers, comprising up to 15 percent (preferably 2 to 12 percent) based on weight of the polymer employed, may be used. Such stabilizers include: inorganic oxides, such as aluminum oxide; silicon compounds, such' as colloidal silica, aluminum silicate, ethyl orthosilicate; cellulose; and cross-linked vinyl polymers, for example, having sulfonic acid groups. The dispersion may also be mechanically stirred to aid in maintaining uniformity. The dispersion is heated and then extruded at temperatures between about 260 C. and about 280 C. and pressures of between about 50 atmospheres and about 110 atmospheres. The pH of the aqueous dispersion is maintained on the acidic side, usually by addition of sulfuric acid, and pHs of between and 6.0, depending on the stabilizer present, are most useful. It is generally also useful to hold the dispersion at its extrusion temperature for a short time before extruding, e.g., for about 1 to 5, 10, 15 or even minutes; and it is sometimes convenient to raise the temperature in two discrete and separate levels during the heating. Moreover, it is sometimes advantageous to employ a pressure let-down region immediately adjacent the extrusion orifice. If desired, when the polymer used is an acrylonitrile polymer, a mixture of water and acetonitrile may be employed as the dispersant medium and lower extrusion temperatures (e.g., 220 C.) may be used. The procedure, described in greater detail in the examples below, is preferred, particularly for use with the acrylonitrile polymers.
The textile products of this invention may also be prepared by flash spinning a solution of the noncellulosic synthetic organic polymer. In this procedure, the solvent employed is one that should have a boiling point below the flow temperature of the polymer and should be able to form a single-phase solution of the polymer at the extrusion temperature but form a twoliquid phase system at the same temperature when the pressure on the solution is reduced in a let-down chamber. The extrusion temperature employed should be within 40 C. of the critical temperature of the solvent; and a pressure of roughly 200-300 p.s.i. above the phase boundary at the extrusion temperature should be employed. Preferably, a let-down chamber is used and in this chamber the pressure is dropped to a value about 200 p.s.i. below the phase boundary. The polymer concentration in the solution to be flash spun can range from about 10-40 percent by weight of the solution.
EXAMPLES In all examples, the yarns obtained are characterized in accordance with the procedures described above after all additives, finishes or contaminants have been removed. For example, siliceous materials are removed from the textile products by washing in dilute aqueous hydrofluoric acid. Measured characteristics and some process conditions for all samples prepared in Examples I through 111 are given in Table II those of Examples IV and V, in Tables III and IV, respectively. Also, in the succeeding examples, L is the length and D is the diameter of a circular orifice or length of tubing or pipe.
EXAMPLE I In this example, 15 samples of textile products in the form of continuous plexifilamentary strands having interconnected fibrils of irregular shape are prepared in accordance with the details given below from an acrylic terpolymer comprising 94 parts acrylonitrile (AN), 6 parts methyl acrylate (MA) and 0.12 parts sodium styrene sulfonate (SSS).
Sample 1. A slurry comprising grams of the acrylic terpolymer, 2 grams of Cab-O-Sil colloidal silica and 79 ml. of water is prepared and adjusted to a pH of 4.8. A portion of this slurry is loaded into a cylindrical pressure vessel of about 15-cm. length and 2-cm. inside diameter which is fitted with a closed spinneret at one end and a piston at the other. Nitrogen pressure of 54.4 atm. is applied to the rear of the piston. The contents of the vessel are heated to 230 C., held at temperature for 5 minutes, and heated further to about 245 C. Total time of heating is about 20 minutes. The orifice, which measures 0.64 mm. D X 1.27 mm. L, is then opened and the sample is extruded.
Sample 2. A slurry is prepared as for Sample 1 except that 65 ml. of water is used. A lOO-gram portion is concentrated at 60 C. to a weight of 68 grams. A portion of this is extruded as per Sample 1, except that the temperatures are 250 and 270 C. and the orifice measures 0.51 mm. D X 0.64 mm. L.
Sample 3. A slurry is prepared as for Sample 1 except that ml. of water is used and a portion processed in the same manner except that a 4-minute hold at 250 C. and extrusion at 250 C. are used.
Sample 4. An aqueous slurry containing 29.5 percent of the acrylic terpolymer and 3.7 percent finely divided aluminum silicate is mixed continuously in a 208-1iter tank and pumped with a metering pump through 6.1 m. of steam-jacketed tubing of 6.35 mm. 1.D. (inside diameter) in which it is heated to about 150 to 170 C. The slurry is then raised to 280 C. and 83.3 atm. in an additional 6.1 m. of electrically heated, 7.72-mm. LD. tub- The slurry is passed through a 0.46 mm. D X 0.46 mm. L orifice into a pressure let-down chamber of 3.2-cm. volume, and finally through a 0.38 mm. D X 0.38 mm. L orifice to the atmosphere. In the let-down chamber, the temperature is 280 C. and the pressure is 63.9 atm. Total residence time in the heated zones is approximately 1 minute.
Sample 5. A slurry comprising 35 g. of the acrylic terpolymer, 0.14 g. of Cab-O-Sil silica, 6.0 g. of finely divided aluminum silicate, 11 ml. of water and m1. of acetonitrile is prepared. A portion of this slurry is processed in the same manner as for Sample 1 except that extrusion is at 255 C. through a 0.76 mm. D X 1.52 mm. L orifice.
Sample 6. An aqueous slurry containing 31 percent of the acrylic terpolymer and 4 percent finely divided aluminum silicate is processed continuously in the same equipment as used for Sample 4 except that (1) the slurry in the final heating stage reaches 279 C. and 85.7 atm., (2) the orifice at the entrance to the letdown chamber is 0.51 mm. D X 0.81 mm. L, and (3) the extrusion orifice, which measures 0.46 mm. D X 0.46 mm. L, is connected to a shroud comprising a cone opening into a cylindrical tube of 3.05 mm. D X 1.78 mm. L.
Sample 7. The same materials and apparatus as for Sample 6 are used except that: the slurry contains 31.5 percent acrylic terpolymer, is adjusted to a pH of 4.7, and finally heated to 272 C. and 91.8 atm.; the first orifice measures 0.51 mm. D X 0.51 mm. L, and steel wool is packed in the let-down chamber.
Sample 8. The same materials and apparatus as for Sample 6 are used except that: the slurry contains 31.5 percent acrylic terpolymer, is adjusted to a pH of 5.2, and is finally heated to 270 C. and 105.4 atm. infinal heating-stage tubing of M 18.3-meter length; and the shroud has a 40 entrance cone.
Sample 9. The same materials and apparatus as for Sample 7 are used except that: the slurry contains 31.5 percent acrylic terpolymer and 3 percent aluminum silicate, is adjusted to a pH of 4.8, and is finally heated to Sample 12. The same materialsand apparatus as for Sample 6 are used except that: the slurry contains 31.5 percent acrylic terpolymer and is finally heated to 270 Cfand 90.1 atm.; the entrance orifice to the let-down chamber is 0.38 mm. D X 0.38 mm. L; the extrusion orifice is 0.30 mm. D X 0.30 mm. L; and the tubular section of the shroud is 2.03 mm. D X 1.27 mm. L.
Sample 13. An aqueous slurry containing 31.4 percent of the acrylic terpolymer and 4.6 percent Cab-O- Sil colloidal silica is prepared and then processed in the same way as Sample 1, except that the temperature after the final heating is 260 C. and the extrusion orifice measures 0.064 mm. D X 0.127 mm. L.
. Sample 14. The same materials and apparatus as for Sample 6 are used except that: the slurry contains 32.5 percent acrylic terpolymer and 4.1 percent finely divided aluminum silicate, is adjusted to a pH of 4.0, is finally heated to 275 C. and 97.8 atm., and in the letdown chamber conditions are 273 C. and 91.1 atm.; the orifice at the inlet to the let-down chamber measures 0.76 mm. D X 0.89 mm. L; the extrusion orifice measures 0.33 mm. D X 0.33 mm. L; and the volume of the let-down chamber is 12.1 cm".
The extruded plexifilamentary yarn is passed through a 46-cm. long bath containing 95/5 water/ethylene carbonate at 34.3 cm./sec. at room temperature, then wrapped on a bobbin, and finally dried in an oven under vacuum at 80 C.
Sample 15. This sample is prepared the same way as Sample 14 except that the post-extrusion treatment bath contains 97.5/2.5 water/ethylene carbonate, the yarn speed in the bath is 10.7 cm./sec. and the yarn is dried by passage through a 60-cm.-long hot-tube oven held at 240 C.
As shown in Table 11, Samples 1 through 13 are arranged in order of increasing fibril concentration. With the exception of Samples 1, 2 and 3, all samples of Example l absorbed wateras rapidly as, if not more rapidly than, cotton (see Example V). Samples 1, 2 and 3 each are outside the scope of this invention because of their low fibril concentration (i.e less than 5 X /cm?) Samples 14 and 15 show the general effect of how reducing specific surface, reduces the absorption rate.
specific surface to the values listed in Table 11 still absorb water as well as cotton, but Sample 14, which because of its very low specific surface, is outside the scope of this invention, and has poorer cover power than is desired for textile applications.
Samples 4 through 13 and 15 are examples of this invention. 1f such continuous plexifilamentary yarns are to be dyed to a dark hue, one would choose a sample with a small value of specific surface (e.g., Sample 15). 1f whiteness is desired, a plexifilamentary yarn of high specific surface with large light-scattering ability would be preferred.
EXAMPLE 11 In this example, four samples of textile products in the form of continuous plexifilament yarns falling within the scope of this invention are prepared from an acrylic copolymer comprising about 96 parts acrylonitrile (AN) and 4 parts sodium styrene sulfonate (SSS).
Sample 1. A slurry comprising 35 grams of the acrylic copolymer, ml. of water, and 9 grams of ethyl orthosilicate is prepared, and its pH adjusted to 1.4. A portion of this slurry is loaded into the same pressure vessel as used for Example 1, Sample 1. Nitrogen pressure of 54.4 atm. is applied to the piston. The vessel is then heated to 170 C., held at 170 C. for 5 minutes, and finally heated to 260 C. he contents are then passed through a 0.51 mm. D X 0.64 mm. L orifice into a 1.8 cm.- pressure let-down chamber, then through a 0.46 mm. D X 0.46 mm. L extrusion orifice which is attached to the same shroud as that described in Example l, Sample 6.
Sample 2. A slurry comprising 35 grams of the acrylic copolymer, 3 grams of Cab-O-Sil silica, and 65 ml. of water is prepared and the pH adjusted to 1.5. A portion of this slurry is processed as in Example 1, Sample 1, except that a 2-minute hold at 230 C. is used, and the extrusion orifice measures 0.46 mm. D X 0.46 mm.
Sample 3. A mixture of 4,620 grams of acrylic copolymer, 770 grams of Triton X- isooctyl phenoxy polyoxyethanol surfactant, 6,160 grams of acetonitrile, and 3,850 grams of water is heated in a stirred 18.9-liter autoclave to 222223 C. and 1 18 atm. Total heat-up time is 1 hour. The charge completely fills the vessel at the extrusion temperature and the pressure is internally generated by the confided liquid. The mixture is passed through a 100-mesh filter screen, then through a 0.61 mm. D X 0.64-mm. L orifice into a 1.27 cm. D X 8.4 cm. L pressure let-down chamber and finally through a 0.41 mm. D X 0.38 mm. L orifice to the atmosphere. Within the let-down chamber, the temper- These two samples, which were given a special postextrusion ethylene-carbonate treatment to reduce their ature is 222 C. and the pressure is atm. The resultant plexifilamentary yarn is drawn 2.8X at about 200 C. The Triton X-100 is removed by washing with water.
Sample 4. The same materials and apparatus as for Sample 3 are used except that: the temperature and pressure in the autoclave are 221 C. and atm.; the total heating time is 40 min.; the let-down chamber inlet orifice measures 0.86 mm. D X 0.64 mm. L and the extrusion orifice measures 0.58 mm. D X 0.51 mm. L; within the let-down chamber the temperature is 219 C. and the pressure is 102 to 103 atm.; and the extruded'plexifilamentary yarn is drawn 2.4X.
EXAMPLE in In this example, two samples of textile products of this invention in the form of plexifilamentary strands are made of 6 nylon (polycaproamide). Measured characteristics of these samples are also listed in Table 11.
Sample 1. A slurry comprising 35 grams of polycaproamide, 5.0 grams of Cab-O-Sil silica, and 65 ml. of water is mixed and a portion is loaded into the same pressure vessel as used for Example I, Sample 1. The pH of the mixture is 6.0. Nitrogen pressure of 54.4 atm. is applied to the piston and the vessel is heated to 230 C., held at 230 C. for minutes, and then heated further to about 260 C. Total heat-up time, including the hold, is about 20 minutes. The material is then extruded through an orifice measuring 0.64 mm. D X 1.27 mm. L.
Sample 2. A mixture comprising 35 grams of polycaproamide and 65 grams of 95 percent ethanol is heated to 200 C. in a cylindrical autoclave of about l-liter capacity, which is fitted with a piston which applies a pressure of 170 atm. to the mixture. Total heat-up time is about 35 minutes. The autoclave is connected to a twin autoclave by two square channels, each being about 6.25 mm. X 6.25 mm. X 13 cm. long, each having four 90 bends and the interior of each being connected to the other three times between their common entrances and exits. The heated charge is forced back and forth through this tortuous path to ensure good mixing. The charge is finally passed from one of the cylinders through a 0.64 mm. D X 0.64 mm. L orifice into a 1.7-cm. pressure let-down chamber, and then through a 0.46 mm. D X 0.51 mm. L extrusion orifice to atmospheric conditions.
TABLE II.CHARACTERISTICS H=Water wicking parameter, (yr-72) (F/10 (S)- Iw =Water absorption rate, ml.lsec.
w=Limiting surface tension, dynes/cm.
F =Fibri1 concentration, fibrils/cm.
ifilamentary yarns comprising continuous assemblies of fibrils, the fibrils being generally of irregular crosssection. The yarns are stable to repeated exposure to water, have a limiting surface tension (7 of greater than 72 dynes/cm., a specific surface (S) of greater than 0.8 m. /g., a fibril concentration (F) of greater than 5 X 10 /cm3, and an H parameter, ('y,,72)(F/10 (8), of greater than 6.
Sample l.'A slurry is prepared containing 13.3 grams of a copolymer comprising 94 parts by weight of acrylonitrile (AN), about 0.1 part sodium styrenesulfonate and 6 parts vinyl acetate (VA), 26 ml. of water, and 1.4 grams of Cab-O-Sil colloidal silica. The pH is adjusted to 4.0. The slurry is loaded into the same pressure vessel as used for Example 1, Sample 1. A pressure of 54.4 atm. is applied. The slurry is heated rapidly to 260 C., then passed through a filter comprising a 1.5- cm. thickness of stainless steel wool and a IOO-mesh screen, and finally extruded through a 0.63-mm. D X 0.63-mm. L orifice which is connected to a shroud having a cone of about 2-mm. length.
Sample 2. The same materials, apparatusjand cess as used for Sample 1 are employed for this sample, except that the slurry contains 1.4 g. of finely divided aluminum silicate in place of the Cab-O-Sil and the pH is adjusted t o 4 .5
OF TEXTILE PRODUCTS 1 S =Specific surface, mJ/gm. P =Extruslon pressure, atmospheres b '1 =Extrusion temperature, 0.
Product characteristics Extrusion Water conditions Contrast Absorption Sample Total Fibril Density, ratio,
Ex. No. No. Material P T denier c denier h gnu/cm. percent (I /10 S H Iw I 1 AN/MA/SSS94/6/0.12 54. 4 245 435 25. 6 0. l 80.3 0.07 0. 036 2 AN/MA/SSS94/6/0.12 54. 4 270 800 9. 3 0. 075 80. 3 0. 27 0. 024
3 AN/MA/SSS-94/6/0.12 54. 4 250 378 1. 2 0. 074 80. 3 0. 48 0. 05-1 4 ANIMA/SSS-94/6/0J2 B 63. 9 280 200 3. 5 O. 216 86 80. 3 1. 1 3.0 12 0. 15
5 AN/MA/SSS-94/6/OJ2 v 54. 4 255 532 1. 4 0. 074 69 80.3 1. 5 1. 3 12 0. 15
6 AN/MA/SSS94/6/0.12 62. 9 279 200 4. 4 0. 204 80 80. 3 2. 2 2. 1 19 0. 21
7 AN/MA/SSS94/6I0.12 e 59. 5 272 210 2. 2 0. 83 80. 3 3. 5 2. 5 28 0. 38
8 AN/MA/SSS-94/6/0.12 B 66. 6 270 229 3. 1 0. 179 78 80. 3 3. 7 1. 9 27 0. 40
9 AN/MA/SSS-94/6/0.12 280 134 2. 2 0. 158 80.3 4. 8 0.62
10 AN/MA/SSS94/6/0.12 e 76. 5 272 230 3. 2 0. 149 77 80.3 5. 9 1. 7 36 0.61
11 AN/MAISSS94/6/O.12 e 280 206 2. 1 0. 158 78 80. 3 6. 9 1. 9 42 0. 68
12 AN/MA/SSS-94/6/0J2 B 270 130 3. 5 0. 153 80 80. 3 7. 8 2. 1 47 0.69
13 AN/MA/SSS94/6/0.12 54. 4 260 130 0.22 0.096 82 80. 3 13. 4 2. 4 73 0. 94
14 AN/MA/SSS94/6/0.12 B 91. 1 273 3. 5 52 80. 3 1. 9 0.6 12 0. 11
15 AN/MA/SSS-94I6/0J2 91. 1 273 155 3. 5 59 80. 3 1. 9 0. 8 12 O. 13
II 1 AN/SSS-96/4 s 260 280 8.1 0. 097 71 81. 5 0. 76 1.- 4 9 0.089 2 AN/SSS-96/4 8 54. 4 260 351 5.6 0. 147 75 81. 5 1. 1 1. 7 12 0.21
3 AN/SSS-96/4 B 105 220 150 2. 3 0. 135 76 81.5 4. 2 1. 7 32 0. 45
4 AN/SSS-96I4 s 102 219 360 1. 5 0. 182 73 81. 5 5. 9 1. 5 40 0. 43
III l 6-Ny1on 54. 4 260 265 4. 3 0. 114 82 78. 8 2. 6 2. 3 18 0. 25 2 G-Nylon 200 450 1. 8 0. 079 73 78. 8 6. 1 1. 5 29 0. 35
B All samples are characterized by procedures of this application.
b Extrusion conditions are just upstream of the extrusion orifice or spinneret.
c Denier of as-extruded product after boiling treatment.
d Density (reciprocal of bulk) is based on the weight, width, length and thickness of the sample used in the absorption rate test while the pad is under the BOO-gram load.
8 AN/MA/ SSS=94 parts acrylonitrile, 6 parts methyl acrylate, and 0.12 part sodium styrene sulfonate.
-Indicates no measurement for this item.
ANISSSB96 parts acrylonitrile and 4 parts sodium styrene sullonate.
EXAMPLE IV In this example, several other copolymers of acrylonitrile are used to make six samples of textile products of this invention. The products are in the form of plex- .me sq stqilmttPAQ- 1 tum-J1.-.
is preparedcontaining 10.0 grains of a copolymer comprising 95.5 parts acrylonitrile (AN) and 4.5 parts ethylene (E), 22 ml. of water and 1.5 grams of Cab-O-Sil. The pH is adjusted to 4.8.
The same process and apparatus as used for Sample 3 is used to prepare this sample except that the final tem-. perature before extrusion is 265 C. and the orifice this sample, except that the total time of heating is a .299t %=s Sample 6. A slurry is prepared containing 6.7 grams of a terpolymer comprising 88.8 parts acrylonitrile (AN), 5.8 parts methyl acrylate (MA) and 5.4 parts 2-methyl-5-vinyl-pyridine (MVP), 10 ml. of water and 0.7 gram of Cab-O-Sil. The same process and appamm as used fo r Sample 3 is used to prepare this samm./min. The yarn is drawn 4.5X- at 150 C. Four yarns are put together without twisting to make a bundle of forty 2-dpf. continuous filaments (dpf. denier per filament').
Sample 2. A 23 percent solution of the same acrylic terpolymer-used for Sample-l is dry spun through a 10- hole spinneret having 0.13-mm. diameter holes. Spinning pressure is 4.8 atm. and solution temperature is 45 C. The extrudate is collected at the rate of 272 10- m./min. with a spin-stretch factor of 10. The yarn is plied and steam drawn 13X. The final yarn has 2,000 filaments of 0.2 dpf.
Sample 3. This commercial continuous filament nylon yarn manufactured and sold by Allied Chemical Company, Hopewell, Virginia, as 200-l6-l.5Z-BW, is a bright 6-nylon (polycaproamide) yarn having 16 filaments totaling 200 denier. The yam has a Z twist of 1% turns per inch.
Samples 4, 5, 6, 7. These samples are conventional spun yarns of cotton (4, 5). Sample 6 is a spun yarn removed from a mans cotton T-shirt. Sample 7 is a spun yarn removed from a cotton towel. The yarns are charple. acterized after removal of all additives and finis hes. n
TABLE IV [Same nomenclature as Table 11] Water Contrast absorption ratio. Density,
Sample No. Material percent gm./cm. yo (F/lO) S H I 1 Acrylic terpolymer 24 0.272 80. 3 5. 9 0.21 19 0.0017 2 "d0 52 0.262 80.3 80. O 0. 64 185 0.0061 0. 315 78. 8 2. 9 0. 18 9 0. 0033 TABLE III PLEXIFILAMENTARY YARNS OF EXAMPLE lV Product Characteristics l'he numbers represent the respective parts by weight of each polymeric component, and
AN acrylonitrile VA vinyl acetate E ethylene MVP 2-methyl-5-vinylpyiidine MA methyl acrylate 2 Density of the textile product (in the water-absorption sample pad) in gram/cm 1,, is the water-absorption rate in ml/sec.
. V EXA LE V In this example, several yarns made from conventional fibers or filaments are tested in accordance with the procedures of this application for the purpose of comparing their water-absorption characteristics, bulk and cover power with those of the textile products of this invention. These yarns include two of acrylonitrile terpolymer, one of 6-nylon and four of cotton. Their characteristics are listed in Table IV.
Sample 1. A dimethyl formamide solution containing 65 26 percent of the acrylic terpolymer used in Example l is dry spun through a l0-hole spinneret having 0.16 mm.-diameter holes. Solution temperature is 80 C.
a d, rin nsgresurqisatmind-PP. ns ie 12 Even though Samples 1 and 2 of this example have very high apparent wicking parameters and are made of polymer that in the textile products of this invention absorb water very rapidly, these samples of continuous 40 filament yarns still exhibit very low water absorption rates. This distinction between the yarns of this example and the textile-product yarns of the invention is shown further in the graph of FIG. 1 which indicates about a l00-fold advantage in water absorption rate for the textile-product yarns of this invention over the conventional acrylic yarns and an even greater advantage over the 6-nylon yarn of Sample 3. Also, FIG. 1 showsthe products of this invention absorb water at least as well as and usually better than the conventional cotton yarns of this example (Samples 4-7). Comparison of Tables 11 and 111 shows the further advantage of the textile products of this invention over conventional yarns in cover power (i.e., contrast ratio of usually between and percent vs. 25-50 percent) as well as the satisfactory bulk (i.e., reciprocal density) of these products.
The textile products of this invention are intended for a wide range of textile uses. Because of the extraordinary ability to absorb large quantities of water rapidly, many can serve in end uses from which synthetic organic polymeric fibers have heretofore been excluded. In many instances, spun cotton yarns may be inferior to the preferred plexifilamentary strands of this invention, because cotton requires high amounts of twist to form a continuous load bearing structure while the preferred plexifilamentary strands are a continuous network as formed and require little or nor twist. High amounts of twist reduce the absorption rate of yarns. However, the
strands may be twisted or may be cut into staple lengths and spun into yarns as is cotton or may be converted into paper or processed into other nonwoven materials. The resultant products still provide acceptable water absorption rates along with satisfactory cover and bulk.
Fabrication of a terry-cloth towel completely from textile-product yarns of this invention is illustrated as follows: plexifilaments of acrylonitrile terpolymer are spun essentially in the same manner as those of Example 1, Sample 8. The plexifilaments are prepared into yarns and then fabricated into a terry-cloth towel. The towel contains a woven ground having 25.2 ends per cm. (in the warp direction) and 20.5 picks per cm. (in the fill direction); has a pile-to-ground-yarn weight ratio of 5.8/1, weighs 373 grams/m and measures 0.43 cm. in thickness. The ground yarns are of 260 to 265 denier and have a twist of two turns per cm. The yarn for the pile is passed at 15.2 m./sec. through an interlacing jet operating with steam at 9.5 atm. and 275 C. The pile yarn is 223 denier. The towel is very soft and highly effective in absorbing water.
The foregoing detailed description has been given for clearness of understanding only and no unnecessary limitations are to be understood therefrom. The invention is not limited to the exact details shown and described for obvious modifications will occur to those skilled in the art.
The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:
1. A textile product having water-absorbing characteristics comprising an assembly of fibrils, said assembly being of at least staple fiber length; said fibrils being of irregular cross-section and being composed of a noncellulosic, synthetic, organic polymer, with a majority of said fibrils being interconnected at various points to form a plexus; said product being stable to repeated exposure to water, and having a limiting surface tension (y greater than 72 dynes per centimeter, a specific ac o at least ab qu remetetp m") and a fibril concentration (F) of at least about 5 X 10 per square centimeter. said numerical values of y,,, S and F also being such that the parameter for said product is greater than 6.
2. The textile product of claim 1 wherein said product is a yarn.
3. The textile product of claim 1 wherein said product is a fabric.
4. The textile product of. claim 1 wherein said product is a continuous plexifilamentary strand.
5. The continuous plexifilamentary strand of claim 4 wherein said non-cellulosic synthetic organic polymer is an acrylonitrile polymer.
6. The continuous plexifilamentary strand of claim 5 wherein said acrylonitrile polymer is a copolymer wherein the major portion of the copolymer is composed of acrylonitrile units.
7. The continuous plexifilamentary strand of claim 6 wherein the acrylonitrile polymer is a terpolymer containing a major amount of acrylonitrile and minor amounts of methyl acrylate and sodium styrene sulfonate.
8. The continuous plexifilamentary strand of claim 6 wherein the acrylonitrile polymer is a copolymer containing a major amount of acrylonitrile and a minor amount of sodium styrene sulfonate.
9. The continuous plexifilamentary strand of claim 4 wherein said non-cellulosic synthetic organic polymer is a polyamide.
10. The continuous plexifilamentary strand of claim 9 wherein said polyamide is polycaproamide.
11. The textile product of claim 1 wherein the ratio of wet-to-dry scattering coefficient is less than 0.4.
12. The textile product of claim 11 wherein said product is a continuous plexifilamentary strand and said non-cellulosic synthetic organic polymer is an acrylonitrile polymer.

Claims (11)

  1. 2. The textile product of claim 1 wherein said product is a yarn.
  2. 3. The textile product of claim 1 wherein said product is a fabric.
  3. 4. The textile product of claim 1 wherein said product is a continuous plexifilamentary strand.
  4. 5. The continuous plexifilamentary strand of claim 4 wherein said non-cellulosic synthetic organic polymer is an acrylonitrile polymer.
  5. 6. The continuous plexifilamentary strand of claim 5 wherein said acrylonitrile polymer is a copolymer wherein the major portion of the copolymer is composed of acrylonitrile units.
  6. 7. The continuous plexifilamentary strand of claim 6 wherein the acrylonitrile polymer is a terpolymer containing a major amount of acrylonitrile and minor amounts of methyl acrylate and sodium styrene sulfonate.
  7. 8. The continuous plexifilamentary strand of claim 6 wherein the acrylonitrile polymer is a copolymer containing a major amount of acrylonitrile and a minor amount of sodium styrene sulfonate.
  8. 9. The continuous plexifilamentary strand of claim 4 wherein said non-cellulosic synthetic organic polymer is a polyamide.
  9. 10. The continuous plexifilamentary strand of claim 9 wherein said polyamide is polycaproamide.
  10. 11. The textile product of claim 1 wherein the ratio of wet-to-dry scattering coefficient is less than 0.4.
  11. 12. The textile product of claim 11 wherein said product is a continuous plexifilamentary strand and said non-cellulosic synthetic organic polymer is an acrylonitrile polymer.
US00259175A 1970-09-11 1972-06-02 Hydrophilic textile products Expired - Lifetime US3774387A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US7158270A 1970-09-11 1970-09-11
US25917572A 1972-06-02 1972-06-02

Publications (1)

Publication Number Publication Date
US3774387A true US3774387A (en) 1973-11-27

Family

ID=26752397

Family Applications (1)

Application Number Title Priority Date Filing Date
US00259175A Expired - Lifetime US3774387A (en) 1970-09-11 1972-06-02 Hydrophilic textile products

Country Status (1)

Country Link
US (1) US3774387A (en)

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3885014A (en) * 1971-06-01 1975-05-20 Oji Yuka Goseishi Kk Production of fine fiber mass
US3914354A (en) * 1970-09-25 1975-10-21 Oki Yuka Goeishi Kenkyujo Kk Process for producing fine fibrous structures
US3984601A (en) * 1971-10-14 1976-10-05 E. I. Du Pont De Nemours And Company Acrylonitrile polymer filaments
US3987139A (en) * 1972-03-20 1976-10-19 Crown Zellerbach Corporation Process of forming synthetic fibers
US4007247A (en) * 1972-09-26 1977-02-08 Imperial Chemical Industries Limited Production of fibrils
US4054625A (en) * 1972-08-30 1977-10-18 Crown Zellerbach Corporation Process for making fibers
US4094948A (en) * 1972-10-02 1978-06-13 E. I. Du Pont De Nemours And Company Improved acrylonitrile polymer spinning process
US4166091A (en) * 1973-04-17 1979-08-28 E. I. Du Pont De Nemours And Company Production of plexifilament strands
US4189455A (en) * 1971-08-06 1980-02-19 Solvay & Cie. Process for the manufacture of discontinuous fibrils
WO1980001391A1 (en) * 1978-12-29 1980-07-10 Du Pont Improved process for melt spinning acrylonitrile polymer hydrates
US4248812A (en) * 1977-07-18 1981-02-03 Japan Exlan Company Limited Process for producing a rush-like structure
FR2674542A1 (en) * 1991-03-27 1992-10-02 Korea Inst Science Technolo Short acrylic fibres resistant to heat and to chemical products and process for their manufacture without spinning
US5567486A (en) * 1993-08-03 1996-10-22 The Family Trust U/T/A Ribbon assembly
US5589264A (en) * 1992-10-01 1996-12-31 Korea Institute Of Science And Technology Unspun acrylic staple fibers
WO1997041281A1 (en) * 1996-05-01 1997-11-06 E.I. Du Pont De Nemours And Company Flash-spinning apparatus and process
WO1998007907A1 (en) * 1996-08-19 1998-02-26 E.I. Du Pont De Nemours And Company Flash-spun products
US5851936A (en) * 1996-08-19 1998-12-22 E. I. Du Pont De Nemours And Company Elongation for flash spun products
WO2016172707A1 (en) * 2015-04-24 2016-10-27 The Board Of Trustees Of The University Of Illinois Methods of extruding multilayer fibers

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB891943A (en) * 1957-06-11
GB891945A (en) * 1958-12-09 1962-03-21 Du Pont New synthetic polymer forms and paper and other sheet structures therefrom and processes for their production
US3081519A (en) * 1962-01-31 1963-03-19 Fibrillated strand
US3169899A (en) * 1960-11-08 1965-02-16 Du Pont Nonwoven fiberous sheet of continuous strand material and the method of making same
US3227784A (en) * 1961-12-07 1966-01-04 Du Pont Process for producing molecularly oriented structures by extrusion of a polymer solution
US3290207A (en) * 1962-08-22 1966-12-06 Du Pont Fibrillated fiber
GB1090478A (en) * 1964-05-21 1967-11-08 Monsanto Co Process and apparatus for preparing synthetic filamentary structures
GB1114151A (en) * 1964-07-17 1968-05-15 Monsanto Chemicals Fibre assemblies
GB1129831A (en) * 1965-02-11 1968-10-09 Courtaulds Ltd Fibrils of polyacrylonitrile

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB891943A (en) * 1957-06-11
GB891945A (en) * 1958-12-09 1962-03-21 Du Pont New synthetic polymer forms and paper and other sheet structures therefrom and processes for their production
US3169899A (en) * 1960-11-08 1965-02-16 Du Pont Nonwoven fiberous sheet of continuous strand material and the method of making same
US3227784A (en) * 1961-12-07 1966-01-04 Du Pont Process for producing molecularly oriented structures by extrusion of a polymer solution
US3081519A (en) * 1962-01-31 1963-03-19 Fibrillated strand
US3290207A (en) * 1962-08-22 1966-12-06 Du Pont Fibrillated fiber
GB1090478A (en) * 1964-05-21 1967-11-08 Monsanto Co Process and apparatus for preparing synthetic filamentary structures
GB1114151A (en) * 1964-07-17 1968-05-15 Monsanto Chemicals Fibre assemblies
GB1129831A (en) * 1965-02-11 1968-10-09 Courtaulds Ltd Fibrils of polyacrylonitrile

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3914354A (en) * 1970-09-25 1975-10-21 Oki Yuka Goeishi Kenkyujo Kk Process for producing fine fibrous structures
US3885014A (en) * 1971-06-01 1975-05-20 Oji Yuka Goseishi Kk Production of fine fiber mass
US4189455A (en) * 1971-08-06 1980-02-19 Solvay & Cie. Process for the manufacture of discontinuous fibrils
US3984601A (en) * 1971-10-14 1976-10-05 E. I. Du Pont De Nemours And Company Acrylonitrile polymer filaments
US3987139A (en) * 1972-03-20 1976-10-19 Crown Zellerbach Corporation Process of forming synthetic fibers
US4054625A (en) * 1972-08-30 1977-10-18 Crown Zellerbach Corporation Process for making fibers
US4007247A (en) * 1972-09-26 1977-02-08 Imperial Chemical Industries Limited Production of fibrils
US4094948A (en) * 1972-10-02 1978-06-13 E. I. Du Pont De Nemours And Company Improved acrylonitrile polymer spinning process
US4166091A (en) * 1973-04-17 1979-08-28 E. I. Du Pont De Nemours And Company Production of plexifilament strands
US4248812A (en) * 1977-07-18 1981-02-03 Japan Exlan Company Limited Process for producing a rush-like structure
US4238442A (en) * 1978-12-29 1980-12-09 E. I. Du Pont De Nemours And Company Process for melt spinning acrylonitrile polymer hydrates
WO1980001391A1 (en) * 1978-12-29 1980-07-10 Du Pont Improved process for melt spinning acrylonitrile polymer hydrates
FR2674542A1 (en) * 1991-03-27 1992-10-02 Korea Inst Science Technolo Short acrylic fibres resistant to heat and to chemical products and process for their manufacture without spinning
US5589264A (en) * 1992-10-01 1996-12-31 Korea Institute Of Science And Technology Unspun acrylic staple fibers
US5567486A (en) * 1993-08-03 1996-10-22 The Family Trust U/T/A Ribbon assembly
US5679415A (en) * 1993-08-03 1997-10-21 Southpac Trust International, Inc. Ribbon assembly
WO1997041281A1 (en) * 1996-05-01 1997-11-06 E.I. Du Pont De Nemours And Company Flash-spinning apparatus and process
WO1998007907A1 (en) * 1996-08-19 1998-02-26 E.I. Du Pont De Nemours And Company Flash-spun products
US5851936A (en) * 1996-08-19 1998-12-22 E. I. Du Pont De Nemours And Company Elongation for flash spun products
WO2016172707A1 (en) * 2015-04-24 2016-10-27 The Board Of Trustees Of The University Of Illinois Methods of extruding multilayer fibers

Similar Documents

Publication Publication Date Title
US3774387A (en) Hydrophilic textile products
US4496505A (en) Process for the production of a polyester fiber dyeable under normal pressure
Preston et al. Measuring the swelling of fibres in water
US5242644A (en) Process for making capillary channel structures and extrusion die for use therein
US3110151A (en) Process for producing compact interlaced yarn
US2353270A (en) Process for forming synthetic fibers
US5200248A (en) Open capillary channel structures, improved process for making capillary channel structures, and extrusion die for use therein
US6093491A (en) Moisture transport fiber
US3695025A (en) Fibrillated film yarn
US3623939A (en) Crimped synthetic filament having special cross-sectional profile
DE2510361A1 (en) Steamed, undrawn, spinned, polyhexamethylene adipic acid amide yarn and process for the manufacture of the same
US3088188A (en) Manufacture of shaped objects of acrylonitrile polymer by wet spinning
US4056652A (en) Monofilament of polyhexamethylene adipamide having a surface layer of reduced orientation relative to the orientation of the core
US4791026A (en) Synthetic polymer multifilament yarn useful for bulky yarn and process for producing the same
IE44939B1 (en) Hydrophilic bi-component threads
US3045315A (en) Apparatus for orienting continuous filament yarns
US3088793A (en) Spinning of acrylonitrile polymers
US5093061A (en) Deep dyeing conjugate yarn processes
US5458968A (en) Fiber bundles including reversible crimp filaments having improved dyeability
US3271943A (en) Process for stabilizing bulked yarns and product thereof
US3740940A (en) Plexifilimentary cellulose strand
US4228120A (en) Process for nylon 66 yarn having a soft hand
US3038239A (en) Crimpable composite filament
US3550369A (en) Steamed coupled-process nylon yarn
US3124629A (en) Manufacture of shaped objects of acrylonitrile