US3299171A - Fibers of modified polypivalolactone - Google Patents

Fibers of modified polypivalolactone Download PDF

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US3299171A
US3299171A US360956A US36095664A US3299171A US 3299171 A US3299171 A US 3299171A US 360956 A US360956 A US 360956A US 36095664 A US36095664 A US 36095664A US 3299171 A US3299171 A US 3299171A
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fiber
yarn
fibers
percent
polypivalolactone
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Fred W Knobloch
William O Statton
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EIDP Inc
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EI Du Pont de Nemours and Co
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Priority to US360956A priority Critical patent/US3299171A/en
Priority to NL6504055A priority patent/NL6504055A/xx
Priority to DE19651494719 priority patent/DE1494719A1/de
Priority to GB16317/65A priority patent/GB1046994A/en
Priority to LU48414A priority patent/LU48414A1/xx
Priority to CH545565A priority patent/CH494827A/de
Priority to CH1389466A priority patent/CH473263A/de
Priority to FR13800A priority patent/FR1461386A/fr
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    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
    • D01F6/625—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters derived from hydroxy-carboxylic acids, e.g. lactones
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/06—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from hydroxycarboxylic acids
    • C08G63/08—Lactones or lactides
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
    • C08L67/04—Polyesters derived from hydroxycarboxylic acids, e.g. lactones

Definitions

  • This invention relates to novel fibers exhibiting exceptionally high levels of work recovery and tensile recovery, and to a novel process for making the new high recovery fibers.
  • the performance of a textile fiber is related to its ability, when deformed by the application of stress, to return to its initial configuration when the stress is removed.
  • the fibers in a carpet are required to recover rapidly from compression; otherwise, the carpets exhibit footprints and other marks. Limited ability of fibers to recover from deformation in fabrics results in wrinkles when the fabrics are creased or otherwise deformed.
  • a measure of the ability of a fiber to recover from deformations ordinarily encountered in textile applications is its work recovery from elongation, designated herein by the symbol WR
  • WR As shown by Beste and Hoffman (Textile Research Journal, vol. XX, No. 7, July 1950, pages 441-453), the ability of a fabric to recover from creasing is dependent upon the work recovery of the fibers from which it is made. Although most fibers exhibit only a relatively low level of "work recovery, with WR values of less than 50%, a few fibers having higher work recovery are known.
  • Drawn polypivalolactone fibers prepared as described by Alderson in his United States Patent 2,658,055 and Reynolds and Vickers in their British Patent 766,347 have a WR up to about 74%.
  • the new high recovery fiber comprises a polypivalolactone fiber having a novel physical structure.
  • the structural elements in terms of which the novel fiber is characterized are discussed fully hereinbelow, but in summary they are as follows:
  • the novel fiber comprises a highly oriented polypivalolactone fiber predominantly in the a crystalline form and particularly characterized by the high order of length of its on crystallites parallel to the fiber axis, as measured by a value of not more than 040 for the radial breadth of the low angle meridional X- ray peak.
  • novel fiber thus ditfers fundamentally in structure from the previously known types of polypivalolactone fibers: (A) a substantially unoriented polypivalolactone fiber in the on crystalline form, in which both the length and width of the a crystallites are of relatively low order, and (B) an oriented polypivalolactone fiber which has a substantial degree of B crystalline structure, the latter fiber being obtained by orientation of the former.
  • the high recovery fiber of the invention comprises a highly crystalline polypivalolactone fiber having an inherent viscosity, n of at least about 0.75; said fiber being highly oriented as characterized by an orientation angle less than the numerical value given by the expression,
  • novel fiber of the invention exhibits WR values ranging from 80% as a minimum to more than The novel fiber also exhibits outstanding tensile recovery at 5% elongation, designated herein 'by the symbol TR Values for TR range from about 92% up to about 98%.
  • the high recovery fiber of the invention is produced by a novel process which comprises heating an oriented polypivalolactone fiber having an inherent viscosity, of at least about 0.75 and an orientation angle, determined from its X-ray diffraction pattern, having a numerical value less than to a temperature of at least C. until its on ratio is at least 1.70, its on crystallite size transverse to the fiber axis is at least 85 A., and the radial breadth of its low angle meridional X-ray peak is reduced to a value of not more than 0.40.
  • the oriented polypivalolactone fiber is heated to a temperature of at least C.
  • the fibers to which the process of the invention is applied are readily prepared by conventional melt-spinning techniques with orientation of the fibers to an orientation angle having a numerical value less than
  • the required orientation may be developed during the spinning step alone simply by taking up the fibers on a forwarding roll or windup roll at a high spin-stretch factor, i.e., with a ratio of spinning speed at windup to the jet speed of the polymer stream issuing from the capillary orifice sufficient to orient the fiber to the
  • the orientation of the spun fibers is readily increased (lower orientation angle) by drawing them immediately following the spinning step.
  • the spun fibers usually have a high degree of a crystalline character as shown by a high a ratio, frequently even when they have received substantial orientation by spinning at a high spin-stretch factor, although the length of the or crystallites is low, and the a crystallite size transverse to the fiber axis is also low.
  • the drawn fibers typically have a substantial degree of [3 crystalline structure, as characterized by an a ratio less than 1.70.
  • the conditions required for conversion of oriented polypivalolactone fibers to the novel fibers of the invention exhibiting high levels of work recovery vary somewhat, depending upon the method used to prepare the oriented fibers. In general, optimum results are achieved by heating within the temperature range of 170-200 C. The fibers may be free of tension, but best results are obtained by holding them taut.
  • the minimum heating time is of the order of one second or less, especially at ⁇ higher temperatures; although this statement is not intended to be limiting owing to the difficulty in estimating the time required for the fiber to reach the desired temperature when heat is applied and the rapidity of cooling when the heat treatment is stopped.
  • the heating step is prolonged, and if desired may be prolonged for several hours or days. If desired, the steps of orienting and heating the fiber may be combined, with the fiber being heated hot enough for a sufiicient exposure time during and immediately following orientation to achieve the structure of the novel fiber of the invention exhibiting high work recovery.
  • the novel high recovery fiber of the invention may be produced by heating the initial oriented fiber at a temperature of 135 C. for about an hour, although for other samples of oriented polypivalolactone fiber a minimum heating temperature of 150 C. may be required.
  • the temperature reached within the fiber during the application of heat should, of course, be maintained below the melting point of the polymer, preferably at least C. below the melting point of the polymer.
  • the melting point of polypivalolactone, in the absence of any copolymeric modifiers, is 238 C.
  • the heating may be carried out in two or more stages. -In fact, when the fibers are intended for conversion into fabrics, it is preferred that achievement of the maximum degree of the high-recovery structure be deferred until the fibers are in fabric form.
  • the oriented polypivalolactone fibers may be heated at 150 C. for one minute to convert them to the high-recovery structure, after which the fibers may be processed to fabric form and given a further heat treatment at 170 C. or higher for a more prolonged period to develop further their a crystalline character and increase their level of work recovery.
  • the initial heat treatment may be omitted, and the fabric may be prepared first with a subsequent heating step to convert the fibers to the novel high-recovery structure.
  • the fibers of the invention give excellent performance in both woven and nonwoven fabrics. They are highly useful in making carpets and as stufiing materials or reinforcing materials in pillows, sleeping bags, seat cushions, and other articles.
  • ELASTIC FIBERS In a variation of the novel polypivalolactone fibers having the structure described above and characterized by exceptionally high work recovery, the invention extends to comprehend fibers exhibiting good tensile recovery at very high elongation. At an elongation of 50%, such fibers exhibit a tensile recovery greater than 60% (tensile recovery from 50% elongation, measured on the second cycle after holding the fibers at 50% elongation for one minute, is designated herein by the symbol TR The fibers are thus elastic in character. The novel elastic fibers exhibit an exceptional degree of power, or modulus in the elongated state (measured on the second cycle at 50% elongation).
  • novel elastic fibers have a .high resistance to additional stretch in the elongated state, and correspondingly a high retractive force.
  • the power of the novel elastic fibers is actually more than twenty times the power of rubber and about ten times the power of commercially available spandex (segmented polyurethane elastomeric) fibers.
  • the novel elastic fiber comprises an oriented polypivalolactone fiber exhibiting a crystalline character to a very high degree and particularly characterized by the high order of width of its on crystallites across the fiber axis, as measured by a minimum a crystallite size transverse to the fiber axis of at least 140 A.
  • a portion of the entire range of novel fiber structures exhibiting elastic behavior coincides with the structural requirements defined above for high WR fibers, and these fibers exhibit elastic behavior as well as exceptional work recovery. Fibers in the remainder of the structural region associated with elastic behavior exhibit somewhat lower levels of work recovery, although still high as compared with most previously known fibers.
  • the elastic fiber of the invention comprises a highly crystalline polypivalolactone fiber having an inherent viscosity, of at least about 0.75; said fiber being oriented as characterized by an orientation angle less than the numerical value given by the expression said fiber having a crystalline character to a very high degree as characterized by an a ratio of at least 2.15 and well ordered in the direction of the fiber axis as measured by a value of not more than 0.50 for the radial breadth of the low angle meridional X-ray peak; and said fiber being particularly characterized by the high order of width of its at crystallites across the fiber axis, as measured by a minimum 0: crystallite size transverse to the fiber axis of at least 140 A.
  • the novel elastic fiber exhibits TR values ranging from 60% as a minimum to and above. Owing to their high degree of power, they find utility in core spun yarns for use in automobile seat covers and other stretchable fabrics, in which the novel elastic fibers are employed as the elastic core surrounded by a sheath of cotton, rayon, or other staple fibers.
  • the novel elastic fibers also exhibit high capacity to absorb energy, i.e., the amount of work required to break the fibers is of high order, for which reason the fibers find utility in the preparation of seat belts and other textile products requiring the ability to absorb large amounts of energy.
  • Elastic fibers exhibiting high work recovery-As defined by the present invention a class of elastic fibers which also exhibits excellent work recovery comprises a highly crystalline polypivalolactone fiber having an inherent viscosity, m of at least about 0.75; said fiber being highly oriented as characterized by an orientation angle less than the numerical value given by the expression ("Iinn+ said fiber having a crystalline character to a very high degree as characterized by an a ratio of at least 2.15; said fiber being particularly characterized by the high order of both the length and width of its on crystallites as measured by a minimum on crystallite size transverse to the fiber axis of at least 140 A. and a value of not more than 0.40 for the radial breadth of the low angle meridional X-ray peak.
  • novel high-recovery, elastic fibers defined above exhibit WR values ranging from 80% to more than 90%, TR values ranging from about 92% up to 98% and TR values ranging from 60% to more than 90%.
  • the high-recovery, elastic fibers are produced by a process which comprises heating an oriented polypivalolactone fiber having an inherent viscosity, of at least about 0.75 and an orientation angle less than the numerical value given by the expression to a temperature of at least 150 C. until its on ratio is at least 2.15, its or crystallite size transverse to the fiber axis is at least 140 A., and the radial breadth of its low angle meridional X-ray peak is reduced to a value of not more than 0.40".
  • the preferred temperature range is 170-200 C., optimum results being achieved by heating at about 190 C., at which temperature an exposure of only about a second, or at most a few seconds, is required.
  • a class of fibers which has excellent elastic behavior, but generally exhibits a somewhat lower level of work recovery than the exceptional level shown by the class of fibers defined just above comprises a highly crystalline polypivalolactone fiber having an inherent viscosity, of at least about 075; said fiber being oriented as characterized by an orientation angle at least equal to the numerical value given by the expression and less than the numerical value given by the expression said fiber having a crystalline character to a very high degree as characterized by an a ratio of at least 2.15 and well ordered in the direction of the fiber axis as measured by a value of not more than 0.50 for the radial breadth of the low angle meridional X-ray peak; and said fiber being particularly characterized by the high order of width of its at crystallites across the fiber axis, as measured by a minimum a crystallite size transverse to the fiber axis of at least 140 A.
  • novel elastic fibers defined in the preceding paragraph exhibit TR values ranging from 60% to more than 90% and WR values ranging from about 50% to about 80%. They are produced by a process which comprises selecting an oriented polypivalolactone fiber having an inherent viscosity of at least about 0.75 and an orientation angle having a numerical value at least equal to the numerical value given by the expression and less than the numerical value given by the expression 7inh+ 17 and heating said fiber to a temperature of at least 150 C. until its on ratio is at least 2.15, its a crystallite size transverse to the fiber axis is at least 140 A., and the radial breadth of its low angle meridional X-ray peak is reduced to a value of not more than 050.
  • the preferred temperature range is 170200 C.
  • FIGURE 1 is a schematic representation of the structure of a portion of a high recovery polypivalolactone fiber, taken in cross section along a plane containing the fiber axis;
  • FIGURE 2 is a typical X-ray ditfractometer scan, or equatorial intensity trace of the X-ray diffraction pattern, of the fiber of FIGURE 1, illustrating the method of determining the a ratio and the a crystallite size transverse to the fiber axis;
  • FIGURE 3 is a typical radial photometer intensity trace of a low angle X-ray diffraction pattern of the fiber of FIGURE 1, illustrating the method of determining the radial breadth of the low angle meridional X-ray peak;
  • FIGURE 4a is a representation of a proposed conformation of two repeating units of the polypivalolactone molecule in the ct crystalline form.
  • FIGURE 4b is a representation of a proposed conformation of two repeating units of the polypivalolactone molecule in the 13 crystalline form.
  • FIGURE 1 is a schematic representation of the structure of a portion of a high recovery polypivalolactone fiber in a plane which includes the fiber axis F.
  • crystallites of a crystalline form 1 are exemplified as aligned with the fiber axis F within the orientation angle 0.
  • Crystallites of the ⁇ 3 crystalline form 2 are shown dispersed within the fiber material.
  • a measure of the variation in length 3 of the ca crystallites or, ordered regions of 0c crystalline form parallel to the fiber axis, is given by the radial breadth of the low angle meridional X-ray peak.
  • the crystalline regions of the polypivalolactone are comprised of two forms: the a crystalline form, in which a sharp layer line having a 5.97 A. spacing appears on the wide angle X-ray diffraction pattern, and the ,8 crystalline form, in which a diffuse layer line having a 4.74 A. spacing appears.
  • a measure of the relative amount of the two forms is given by the or ratio.
  • a suitable method for determining the oc ratio involves the use of a reflection technique to record an equatorial intensity trace of the X-ray diffraction pattern with an X-ray dififractometer (employing a goniometer with a 17 cm.
  • an equatorial intensity trace is recorded from 7 to 22, 29, at a scanning speed of 1, 20 per min., a chart speed of 1 inch per min., and a time constant of 1; 20 being the angle between the undiifracted beam and the diffracted beam.
  • the full scale deflection of the recorder is set so that the peak with maximum intensity is at least 70% of the scale, which is a linear scale.
  • the difiraction peak located at 20 is due entirely to diffracted radiation from the a crystal structure and is the maximum peak for samples of high a content.
  • the diffraction peak located at approximately 17.8, 29, is due to diffracted radiation from both a and [3 crystal structure and is the maximum peak for the samples of high 5 content.
  • a base line is first established on the diffractometer scan by drawing a straight line between the points on the curve at 90 and 210, 20. Vertical lines are then drawn from points on the curve at 135 and 16.4", 20, to the base line.
  • FIGURE 2 illustrates a typical diffractometer scan and the guide lines drawn on it for calculation of the oc ratio. Using a planimeter, the area A of the diffraction peak between 9.0 and 13.5 20, is measured and recorded. The area B of the diffraction peak between 16.4 and 21.0, 26, is similarly determined.
  • the on ratio is then calculated from the equation A a Ratio Values for the a ratio as low as 0.2 are observed, but for the purposes of the present invention should be at least 1.70 for high work recovery fibers and at least 2.15 for elastic fibers. Observed values for the a ratio range up to about 4.1.
  • the a crystallite size transverse to the fiber axis is the degree of order of a crystalline character, or apparent average width of ordered regions of a crystalline form, transverse to the fiber axis; simply stated, it is the average width of the a crystallites. It is determined from the same difiractometer scan employed to calculate the a ratio, using the general method described by Klug and Alexander in their book, X-ray Diffraction Procedures, published by John Wiley & Sons, Inc., New York, 1954, pp. 491-538. A vertical line is dropped from the peak in the vicinity of 11.5 20, to the base line, and the midpoint C of the line between the peak and the base line is ascertained.
  • the oz crystallite size is then calculated from the equation H a Crystalhte S126,
  • CuKa radiation is used
  • I breadth at half-maximum peak height in degrees when calibrated by a metallic silicon standard (instrumental broadening).
  • Values for the u crystallite size as low as 30 A. are observed, but for the purposes of the present invention should be at least 85 A. for high work recovery fibers and at least 140 A. for elastic fibers. Observed values for the a crystallite size range up to about 300 A.
  • a measure of the degree of order of a crystalline character parallel to the fiber axis, or the apparent variation in the average length of ordered regions of 0c crystalline form in the direction of the axis, is given by the radial breadth of the low angle meridional X-ray peak, briefly designated herein as the radial breadth.
  • the radial breadth is measured by making a low angle X-ray diffraction pattern (transmission pattern), using a camera of the type described by W. O.
  • FIG- URE 3 illustrates a typical intensity trace, in which the diffraction spots are symmetrical.
  • a vertical center line Q is drawn between the peaks.
  • the center line is conveniently established by folding the trace so that the centers of the diffraction spots are superimposed and then creasing the trace at the position which is centered between these two peaks.
  • a straight base line is drawn beneath each peak.
  • a vertical line is dropped from one peak to the base line and the mid-point K between the peak and the base line is ascertained, determined logarithmically if the intensity scale is logarithmic, as in FIGURE 3.
  • a horizontal line across the peak through K is drawn and the distance L in mm. from the creased center line to the nearest peak edge is measured and recorded. Also the distance M in mm. from the creased center line to the farther peak edge is measured and recorded.
  • the corresponding diffraction angles 0 and 0 are calculated, and their difference yields a value for the radial breadth;
  • the orientation angle of the fiber is determined by the general method described by Krimm and Tobolsky, Textile Research Journal, vol. 21, pp. 805-22 (1951).
  • a wide angle X-ray diffraction pattern (transmission pattern) of the fiber is made, using CIJKa radiation, 21 fibersample thickness of 20 mils, a sample-to-film distance of 2.2 cm., and an exposure time of 5 minutes.
  • the fibers are aligned perpendicular to the X-ray beam. Crimped fibers are placed under sufficient tension to straighten the fibers, taking care not to impart additional orientation by drawing them.
  • the orientation angle should be less than the quantity, 10(21 +1), for useful elastic fibers; otherwise, the fibers are too brittle.
  • the orientation angle should be less than the quantity, 10(m +1). Decreasing orientation angles are indicative of increasing orientation of the polymer molecules in the fiber. Orientation angles as low as about 20, measured as described above, are indicative of a high degree of orientation. Values as low as about 12 are observed.
  • FIGURES 4a and 412 are proposed conformations of the polypivalolactone molecule in the a and B crystalline forms. In each case two full repeating structural units, plus certain adjacent groups, are shown. The repeat distance of 4.74 A. is close to that which would be expected (4.9 A.) for an extended planar zig-zag, and it is therefore hypothesized that in the p crystalline form of polypivalolactone the atoms comprising the main polymer chain lie substantially in a single plane, with only slight distortion. The 5.97 A.
  • repeat distance observed in the oc crystalline form is too large to be accounted for by a single repeating structural unit, and for two repeating structural units to be compressed to this distance it appears that the polymer chain must be folded or buckled in some nonplanar manner, perhaps into a type of spiral configuration.
  • inherent viscosity is defined as the polymer property determined in accordance with the following relationship:
  • the relative viscosity is calculated by dividing the flow time in a capillary viscometer of a dilute solution of the polymer by the flow time for the :pure solvent, trifluoroacetic acid.
  • concentration (c) used in the examples is 0.5 gram of polymer per 100 ml. of solution, and the measurements are made at 30 C.
  • a decrease in the inherent viscosity of a polymer is frequently noted when the polymer is extruded at high temperature through capillary orifices to form fibers. It has been found that there is a minimum inherent viscosity requirement of 0.75, measured when the polymer is already in fiber form, for both the elastic fibers of the invention and those exhibiting thigh work recovery. Inherent viscosity values up to 3 and higher are observed.
  • TR tensile recovery from 5% elongation is a measure of the extent to which a fiber or yarn recovers its original length after being stretched, as determined from a stressstrain curve. In this test the sample is stretched at the rate of of its test length per minute until it has reached approximately 5% elongation, after which it is held at this elongation for 30 seconds and then allowed to retract at a controlled rate of 10% per minute, based on its original test length. The extension during elongation and the recovery during retraction are measured along the elongation axis. TR is then calculated as the percentage ratio of the amount of fiber retraction to the amount of its elongation.
  • WR work recovery from 5% elongation is a measure of the freedom from permanent re-alignment of the polymer molecules following stretching of the fiber or yarn.
  • the ratio of the work done by the polymer molecules in attempting to return to their original alignment following stretching to a predetermined elongation to the work done on the sample during stretching is termed the work recovery.
  • the work recovery is determined from the same stress-strain curve employed to measure the tensile recovery at 5% elongation.
  • WR is calculated as the percentage ratio of the area under the controlled relaxation curve to the area under the stretching curve.
  • the fiber sample In running the stress-strain curve for determination of TR the fiber sample is stretched at the rate of 100% of its test length per minute until it has reached approximately 50% elongation, after which it is held at this elongation for one minute and then all-owed to retract at the rate of 100% per minute, based on its original test length. The sample is reclamped to remove any slack. A second cycle is then carried out wherein the fiber sample is elongated at the rate of 100% per minute until it has reached 10 approximately 50% elongation, held for one minute, and then allowed to retract at the rate of per minute. The extension during elongation and the recovery during retraction are measured along the elongation axis. TR is then calculated as the percentage ratio of the amount of fiber retraction to the amount of its elongation.
  • polypivalolactone a linear condensation polyester consisting essentially, of recurring ester structural units of the formula
  • Alternative names for the polyester include poly(hydroxypivalic acid), poly(,B-oxypivaloyl), poly(2,2-dimethylhydracrylate), and poly(2,2 -dimethyl-3-hydroxypropionic acid) or poly(2,2-dimethyl-3-oxypropionoyl).
  • the polyester is readily prepared by the polymerization of hydroxypivalic acid or its esters as disclosed by Alderson in his US. Patent 2,658,055; or by the polymerization of pivalolactone, the intramolecular ester of hydroxypivalic acid, as disclosed by Reynolds and Vickers in their British Patent 766,347.
  • a fiber consisting essentially of polypivalolactone refers not only to fibers wherein the sole fiber-forming polymeric constituent is polypivalolactone but also to fibers formed from certain copolymers or polymer blends as indicated below.
  • copolymeric components may be present in amounts of up to about 10 mol percent and in some instances as high as 25 mol per- .cent so long as they do not prevent the fiber from assuming high orientation with well developed a crystalline character.
  • the copolymeric units be grouped in sequences alternating with long polypivalolactone sequences to form a segmented or block copolyester.
  • the lactones or hydroxyacids are particularly suited and especially ,B-propiolactones such as disclosed by Etienne and Fischer in French Patent 1,231,163.
  • copolymers consisting essentially of the following units CH CHz( )C 0 o With up to 25 mol percent of as derived from copolymerization of pivalolactone and a,a-diethylpropiolactone are herein contemplated.
  • Blends of polypivalolactone with up to about 10 percent or more by weight of polyamides as illustrated in Example XI or other polymers that do not materially affect the properties of the polypivalolactone are also suitable in the invention.
  • conventional additives as dyes, pigments, stabilizers, etc. may be present in the fibers.
  • Example I High work recovery, elastic fiber Molten polypivalolactone having an inherent viscosity of 2.6 and containing 0.1% 2,2-bis(4-hydroxyphenyl) propane by weight is extruded at 260 C. from a spinneret having a single orifice, 0.020 inch in diameter.
  • the extruded filament is passed through a cylindrical annealing tube 3 inches in diameter and 6 inches long having a surface temperature of 300 C., after which it is quenched by passing it through room temperature air. After passing it over a feed roll operated at 611 y.p.m. and drawing it at a draw ratio of 2.5x over a 190 C. hot plate with a 3-foot contact length, the filament is Wound up. It has a denier of 10.3.
  • the inherent viscosity of the polymer comprising the filament is 2.2.
  • a sample of the drawn filament wound taut on a bobbin is heated for 16 hours at 175 C. and is then boiled off by immersing it, free of tension, in boiling water containing 0.1% detergent for 30 minutes.
  • the yarn has a WR5 of and a TR50/1/2 of
  • the high work recovery, elastic heat-treated yarn has an a ratio of 3.27, an a crystallite size of 219 A., a radial breadth of 0.30, and an orientation angle of 21. Its tenacity is 2.5 g.p.d., its break elongation 76%, its initial modulus 28 g.p.d. and its TR 96%.
  • Example II.High work recovery, elastic fiber Polypivalolactone having an inherent viscosity of 1.54 is melt-extruded at 280 C. from a spinneret containing orifices, each 0.009 inch in diameter.
  • the extruded filaments are passed through a vertical Water-quench tube continuously fed by water maintained at 6 C. from a cylindrical pan surmounting the tube and maintained full of water.
  • the filaments are passed through a convergence guide and the yarn so formed is taken up by a roll at 900 y.p.m. and then passed to a draw roll at 1133 y.p.m. for a draw ratio of 1.26 after which the yarn is wound up at 1128 y.p.m.
  • the inherent viscosity of the polymer comprising the yarn is 1.23.
  • a sample of the drawn yarn wound taut on the bobbin is heated for 16 hours at 175 C. and is then boiled off for 30 minutes. After the heat treatment, the yarn has a WR of 90%.
  • the TR of a sample of heat-treated yarn is 72%.
  • elastic heat-treated yarn As characterized by X-ray measurement the high Work recovery, elastic heat-treated yarn has an a ratio of 2.26, an a crystallite size of 163 A., a radial breadth of 032, and an orientation angle of 15. Its tenacity is 4.36 g.p.d., its break elongation 85%, its initial modulus 34 g.p.d. and its TR 94%.
  • Example [IL-Illustration of critical structural limits Polypivalolactone having an inherent viscosity of 2.5 is extruded at 265 C. from a spinneret having 15 orifices, each 0.007 inch in diameter.
  • the extruded filaments are quenched by passing them through room temperature air and passed through a convergence guide, after which the yarn so formed is wound up.
  • the spinning speed is 200 y.p.m.
  • the yarn is subsequently oriented by drawing it at a draw ratio of 3.72 around a hot pin maintained at 130 C., after which it is again wound up.
  • the inherent viscosity of the polymer comprising the yarn is 1.44.
  • Table 1 are listed the structural parameters of the drawn yarn as determined by X-ray characterization, as Well as the physical properties of the yarn.
  • a sample of the drawn yarn wound taut on a bobbin is converted to a high work recovery yarn by heating it for two minutes at 170 C., after which the heat-treated yarn is boiled off for 30 minutes.
  • a second sample of the drawn yarn wound taut on a bobbin is converted to a high work recovery, elastic yarn by heating it for 16 hours at 170 C., after which the yarn is boiled off for 30 minutes.
  • a third sample of the drawn yarn is boiled off for 30 minutes without previously heating the yarn at 170 C.
  • the drawn fiber has a relatively low degree of order of a crystalline character parallel to the fiber axis as illustrated by a radial breadth of 0.52, and its WR is only 68%. Its radial breadth value and work recovery are relatively unchanged upon boil-off.
  • the drawn yarn is heated for 2 minutes at 170 C. and boiled off, however, its radial breadth value drops to 0.37 and the WR rises to 81%.
  • the a crystallite size of this yarn is only 123 A. and the yarn is not considered elastic, the TR value being only 50%.
  • the u crystallite size rises to 171 A. and the TR value rises to 80%.
  • Example IV Additional illustration of critical structural limits.
  • Polypivalolactone having an inherent viscosity of 1.61 and containing 0.1% TiO is extruded at 275 C. from a spinneret having 15 orifices, each 0.009 inch in diameter.
  • the extruded filaments are quenched by passing them through a cold water quench-tube and formed into a yarn by passage through a convergence guide.
  • the yarn is taken up by a feed roll operated at a peripheral speed of 900 y.p.m., passed to a draw roll at a draw ratio of 1.3x, and then wound up.
  • the inherent viscosity of the polymer comprising the yarn is 1.35.
  • Table 2 are listed the structural parameters of the drawn yarn as determined by X-ray characterization, as well as the physical properties of the yarn.
  • a sample of the drawn yarn wound taut on a bobbin is converted to a high work recovery yarn by heating it for 5 minutes at 175 C.
  • a second sample of the drawn yarn Wound taut on a bobbin is converted to a high work recovery, elastic yarn by heating it for 5 minutes at 200 C.
  • X-ray data as well as physical properties for each of these yarns, determined in this instance on yarn samples not subjected to boil-off treatment, are listed in Table 2. Data are also listed for a control comprising a third sample of the drawn yarn boiled ofi? for 30 minutes without previously heating the yarn.
  • the drawn fiber has a low a ratio and at crystallite size.
  • the X-ray pattern for radial breadth is too faint to be measured.
  • the fiber has only a low degree of order of c: crystalline character parallel to the fiber axis as illustrated by a radial breadth of 0.59".
  • the WR is only 69%.
  • the radial breadth value drops to 039 and the WR rises to 80%.
  • the u crystallite size is only 114 A. and the TR is only 25%.
  • the or crystallite size rises to 150 A. and the TR /1 /2 value rises to 77%.
  • Example V.-Criticalness of the orientation angle Polypivalolactone having an inherent viscosity of 1.25 is extruded at 260 C. from a spinneret having 15 ML fices, each 0.005 inch in diameter, the extruded filaments being quenched by passing them through room temperature air.
  • the yarn is wound up at a spinning speed of 650 y.p.m.
  • the inherent viscosity of the spun yarn is 1.10, and its structural and physical properties are as follows:
  • orientation angle for high work recovery yarns is above the limit for high work recovery yarns as calculated by the expression
  • the critical nature of the orientation angle for high work recovery yarns will be further appreciated by comparing the 27 orientation angle of the above yarn with the 16 orientation angle of the elastic yarn of Example IV, which exhibits a WR value of 83%.
  • the latter yarn which exhibits substantially the same a crystallite size as the above yarn and generally similar values for a ratio and radial breadth, is made by a process which introduces greater orientation into the yarn.
  • Another sample of the spun yarn is converted to an elastic yarn by heating it, free of tension, for 35 minutes at 197 C. After the relaxed heat treatment, the yarn has the following structural and physical properties:
  • the boiled-off yarn has the following structural and physical properties:
  • Example VI.-High work recovery fibers Polypivalolactone having an inherent viscosity of 2.6 is extruded at 280 C. from a spinneret having 15 orifices, each 0.007 inch in diameter. The filaments are passed through a cold water quench-tube at a spinning speed of 550 y.p.m. and through a convergence guide, after which the yarn so formed is taken up by a feed roll, passed to a draw roll at a draw ratio of l.25 and then wound up. The inherent viscosity of the polymer comprising the yarn is 1.36.
  • the structural and physical properties of the drawn fiber are as follows:
  • a sample of the drawn yarn wound taut on a bobbin is converted to a high work recovery yarn by heating it for one minute in C. air; however, the rate of heating is such that the temperature of the bobbin surface rises 15 above 150 C. only after about 30 seconds of the heating time have elapsed. After the one-minute heat treatment, the yarn is boiled off for 30 minutes.
  • the structural and physical properties of the heat-treated fiber are as follows:
  • Example VII.Hig/z work recovery, elastic fiber A sample of the drawn yarn of Example VI is heated, free of tension, at 170 C. for 16 hours to convert it to a high work recovery, elastic yarn.
  • the structural and physical properties of the fiber after this relaxed heat treatment are as follows:
  • Example VI Another sample of the drawn yarn of Example VI is wound taut on a bobbin and converted to a high work recovery elastic yarn by heating it for 64 hours in 170 C. air, followed by treatment in boiling water for 30 TR percent Example VIII.C0mpressi0/zal recovery of staple pellets
  • Molten polypivalolactone having an inherent viscosity of 1.82 is extruded at 285 C. from a spinneret containing 15 orifices, each 0.009 inch in diameter.
  • the extruded filaments are passed through a vertical water quench tube continuously fed by water maintained at 13 C. from a cylindrical pan surmounting the tube and maintained full of water.
  • the filaments are passed through a convergence guide and the yarn so formedis taken up by a roll at 1,000
  • the yarn is plied (30 ends) at 70 yards per minute and heat set by passing it at the same speed over a roll heated to 175 C., the contact time being 0.5 second.
  • the yarn is then padded with a 5% aqueous solution of an anionic textile finishing agent, the pick-up of finishing agent on the yarn being about 1% after which a sheet of 23 plied ends is fed into a stuffer box crimper and crimped.
  • the crimped yarn is cut to give 3-inch staple fibers, which are then scoured for one hour at 35 C. in a 0.1% detergent solution, rinsed, and air-dried.
  • the staple fibers so prepared are designated as Control Sample A.
  • a portion of Control Sample A is heated, free of tension, for 10 minutes at 175 C., and the resulting staple fibers are designated as Control Sample B.
  • a second portion of Control Sample A is heated, free of tension, for 16 hours at 175 C., and the resulting staple fibers are designated as the Test Sample.
  • the structural parameters of each of these yarns as determined by X-ray characterization, as well as the physical properties of the yarns, are listed in Table 3.
  • the apparatus used in the Busse test is described in Textile Research Journal, 23, 84 (1953). The test is performed at 65% relative humidity and at 70 F.
  • a tuft of staple fibers weighing 0.3 gram is taken from a sliver or batt and placed in a metal cylinder which is 0.8 square inch in area.
  • the tuft of staple is formed into a loose pellet by compressing it with a light wooden rod at approximately 0.2 p.s.i. The initial height of the loose pellet is then measured under this load.
  • the wooden rod is then replaced with a steel rod and a loading force of 10,000 p.s.i. is applied to the pellet for one minute.
  • This compressed pellet of fiber is then removed from the cylinder and allowed to recover.
  • the recovery in percent is calculated from the ratio of the recovered pellet height to the initial pellet height. Because of the removal of the rod before the final measurement, the recovery may be greater in some cases than the initial height.
  • a sample of filamentary polyethylene terephthalate yarn is spun and drawn 2.46 at a draw speed of 2,750 y.p.m. through an aqueous bath maintained at a temperature of 90 C. and a draw roll temperature of 101 C. in accordance with the process described by Dusenbury in his US. Patent 3,091,805.
  • a sample of the drawn yarn boiled off for 30 minutes while held taut has a WR of 35%.
  • a sample boiled off free of tension for 30 minutes has a WR of 28%.
  • Another sample heated at 170 C. for 30 minutes While held taut and then boiled off free of tension for 30 minutes has a WR of 33%.
  • Example IX High work recovery copolyester fiber
  • benzene is refluxed in a 500-ml. threenecked flask equipped with stirrer and condenser with 1.0 ml. of a 0.1 N solution of the tetrabutylammonium salt of hexyldimethylacetic acid (mixture of C C trialkylacetic acids available commercially as Versatic acid from Shell Development Co.) inbenzene.
  • the resulting copolymer poly-(pivalolactone/a,a-diethylpropiolactone) (85/15 mol percent), is then coagulated by adding 200 ml. of alcohol, collected by filtration using more alcohol to wash the copolymer, and dried in a vacuum oven at 100 C.
  • the yield is 20.6 g. and the inherent viscosity is 1.47.
  • a plug of the copolymer is extruded at 250 C. from a single orifice having a diameter of 0.012 inch.
  • the filament is quenched in ice water and wound up at 1600 yards per minute.
  • a sample of the filament heated at 170 C. for 3.5 hours has the following structural and physical properties:
  • Example X -High work recovery, elastic copolyesler fiber
  • a mixture of 400 g. of pivalolactone and 13.4 g. of a,a-diethylpropiolactone is added to a refluxing solution of 4.1 g. of triethylenediamine and 0.41 g. of finely divided TiO in 1650 ml. of hexane.
  • An exothermic reac tion occurs, after which refluxing is continued for 2 hours.
  • the resulting copolymer, poly(pivalolactone/a,a-diethylpropiolactone) (97.5/ 2.5 mol percent) is collected by filtration and dried. The yield is 92% and the inherent viscosity is 1.5.
  • a sample of the copolymer is spun and drawn in general accordance with the procedure of Example II.
  • the inherent viscosity in yarn form is 0.94.
  • a sample of the drawn yarn Wound taut on the bobbin is heated for 16 hours' at 170 C. and is then boiled off for 30 minutes. After the heat treatment, the yarn has the following structural and physical properties:
  • Example Xl.High work recovery, elastic fiber of polypivalolactone/copolyamide melt blend A copolyamide derived from 10.96 g. of hexamethylenediarnine, 9.04 g. of adipic acid, 10.22 g. of sebacic acid, and 16.80 g. of caprolactam by slowly heating at 215245 C. with a final polycondensation step at 245 C. for one hour at 1 mm. of mercury has a molecular weight of 2450 by end group. titration.
  • Example X II .C0mparazive example Following the procedure of Alderson in his US. Patent 2,658,055 (Example 4), hydroxypivalic acid is polymerized to form a polymer having an inherent viscosity of 1.13. Filaments of the polymer are extruded at 250 C. and quenched in a. bath of kerosene maintained at 15 C., the spinning speed being 300 y.p.m. The yarn is drawn 3.5X and wound up. The inherent viscosity of the polymer comprising the yarn is 0.81.
  • the structural and physical properties of the yarn are as follows:
  • the orientation angles in the above example are determined by measurement of the diffraction spot at 11.5 20, as previously described. This diffraction spot is due entirely to diffraction radiation from the a crystalline structure and the technique accordingly yields the desired measure of the orientation of the a crystallites alone.
  • the orientation angle .for the sample of drawn yarn in the above example is additionally determined by measurement of the difiraction spot at 179, 20, and this value is 18. This value corresponds well with the 17 value observed by Alderson, who did not specify the diffraction spot employed.
  • the 179, 26, diffraction spot yields a mixed measure of a and ;& orientation.
  • Example XIV.-Higlz work recovery elastic fiber
  • a sample of the drawn yarn of Example XIII wound taut on the bobbin is converted to a high work recovery, elastic yarn by heating it for 16 hours at 170 C. and then boiling it in water for 30 minutes. After the heat treatment, the yarn has the following structural and physical properties.
  • WR percent 88 TR percent 88 0 Ratio 2.31 oz Crystallite size, A. 152 Radial breadth, degrees 0.35 Orientation angle, degrees 19 Tenacity (g.p.d.)/elong. (percent)/mod.
  • Example X V.C0mparative example Fibers of poly (m xdietlzylpropiolaclone) and poly(a-etlzyl-a-methylpropiolacrone) To a refluxing mixture of 8 liters of ethyl acetate, 3 g. of dried TiO and 1 g. of tetrabutylammonium hydroxide is added 1026 g. of a,a-diethylpropiolactone. Refiuxing is continued for 2.5 hours, after which the mixture is diluted with 8 l. of methanol and the precipitate is filtered, washed with methanol, and dried under vacuum. The product, poly-(a,a-diethylpropiolactone), is obtained in a yield of more than 90% and has an inherent viscosity of 1.42.
  • a sample of the polymer is extruded at 278 C. from a spinneret containing 14 orifices, each 0.009 inch in diameter.
  • the extruded filaments are passed through a vertical water-quench tube continuously fed by water maintained at a temperature of not more than 12 C. from a cylindrical pan surmounting the tube and maintained full of water.
  • the filaments are passed through a convergence guide and the yarn so formed is taken up by a roll at 400 y.p.m and then passed to a second roll at 700 y.p.m., after which the yarn is wound up.
  • the yarn is subsequently passed from a feed roll operated at a peripheral speed of 54 y.p.m. across a plate maintained at 165 C.
  • a sample of the drawn yarn wound taut on a bobbin is heated for 16 hours at 170 C. and is then boiled off for 30 minutes. After the heat treatment, the yarn has a WR of 51%.
  • a sample of the polymer is extruded at 130 C. from a press spinner through an orifice 0.009 inch in diameter and quenched in cold Water.
  • the spinning speed is 400 y.p.m.
  • the filament is drawn 1.5x at C. It has a WR of 50%, a tenacity of 3.3 g.p.d., an elongation of 17% and an initial modulus of 42 g.p.d, The filament melts when heated to about C.
  • Example XVI Polypivalol actone having an inherent viscosity of 1.5 is melt extruded at 280 C. from a spinneret containing 30 orifices, each 0.007 inch in diameter.
  • the extruded filaments are passed through a vertical water quench tube continuously fed by water maintained at 14 C.
  • the filaments are passed through a convergence guide and the yarn so formed is taken up by a roll at 700 y.p.m. and is then passed to a draw roll at 816 y.p.m. for a draw ratio of 1.17 after which the yarn is wound up.
  • the drawn yarn has a denier of 70.
  • the inherent viscosity of the polymer comprising the yarn is 1.06.
  • Plain weave talfeta fabric havinga finished construction of 120 ends and 75 picks is woven from this yarn.
  • One sample of the fabric, designated Test Fabric is heated at 170C. for sixteen hours; and a second sample of the fabric, designated Control Fabric, is heated in boiling water for one hour. Filaments removed from the warp and filling of the Test Fabric are found to have a WR of 85%, while filaments similarly removed from the warp and filling of the Control Fabric are found to have a WR of 75%.
  • the Test Fabric exhibits superior recovery from wrinkling, under both wet and dry conditions, as compared with the Control Fabric.
  • Example XVII Po-lypivalolactone having an inherent viscosity of 1.6 is extruded at 280 C. from a spinneret having 25 orifices, each comprising three 0.003 inch x 0.012 inch slots intersecting in a Y configuration.
  • the filaments are quenched by a cross-flow stream of air at room temperature, supplied at the rate of 100 cubic feet per minute, after which they are gathered as a yarn and taken up by a forwarding roll at the rate of 800 y.p.m.
  • the yarn is then passed continuously under a draw pin immersed in a bath of water maintained at 90 C. and out of the bath via a pair of guides to a pair of draw rolls maintained at 100 C. and operated at a peripheral speed of 1,800 y.p.m.
  • the inherent viscosity of the polymer comprising the yarn is 1.5.
  • the yarns have a tenacity of 2.7 g.p.d., an elongation of 50%, an initial modulus of 40 g.p.d., and a WR of 65%.
  • the yarn is woven to form a taffeta fabric having a construction of 104 ends and 76 picks per inch.
  • the griege fabric is scoured at 35 C. and dried at room temperature.
  • One sample of the fabric is labelled Control Sample; while a second sample is heat set in a 175 C. oven for one hour, allowing 5% shrinkage in the fill direction, and designated as the Test Sample. Filaments removed from the warp and fill of the Control Sample have an average WR of 67%, while filaments removed from the warp and fill of the Test Sample have an average WR of 89%.
  • a wrinkle recovery test is carried out on both the Control Sample and the Test Sample.
  • a fabric sample is wrapped around a cylindrical form consisting of a coiled spring covered with a plastic-coated cloth so that the form is compressible in the direction perpendicular to the base of the cylinder.
  • the wrapped cylinder is compressed to one-half its original height and is held in this way for four minutes.
  • Pressure is removed and the fabric sample is hung vertically and is photographed at intervals while recovering from the wrinkling imparted during testing.
  • the Test Fabric has a markedly lower degree of imparted wrinkling than the Control Fabric; while the rate and degree of recovery from wrinkling of the Test Fabric is markedly superior to that of the Control Fabric.
  • the Test Fabric is also markedly superior in this test to a fabric of similar construction prepared from polyethylene terephthalate yarn.
  • Example XVIII Polypivalolactone having an inherent viscosity of 1.91 is extruded at 280 C. from a spinneret having 3 orifices, each 0.007 inch in diameter.
  • the extruded filaments are quenched by passing them through air at room temperature to a guide located sixty inches below the spinneret, after which they are passed to a wind-up at 600 yds./min.
  • the resulting l t-filament yarn has an inherent viscosity of 1.65, and the individual filaments have an average denier of 5.5.
  • the structural and physical properties of the spun yarn is as follows:
  • a sample of the spun yarn is converted to an elastic yarn by passing fifty wraps of the yarn at low tension between a roll maintained at 180 C. and a separator roll.
  • the yarn speed is 105 yds./min. and the contact time on the heated roll is 27 seconds.
  • the yarn After the heat treatment, the yarn has the following structural and physical properties:
  • Core-spun stretch yarns are prepared by the process of Humphreys in his US. Patent No. 3,038,295, using as core yarns the polypivalolactone yarns described above. The process is carried out on a conventional spinning frame. Roving having a weight of one pound per 840- yard hank and comprised of 70% acrylic bicomponent staple (Du Pont Orlon acrylic type 24 fiber) and 30% acrylic staple (Du Pont Orlon acrylic type 42 fiber) is spun to a 259 denier (20/1 cotton count) yarn twisted 18.2 turns per inch in the S direction with the introduction of the core yarn to which a draft of 1.8 is applied. The final wind-up speed is 10.6 yards per minute.
  • the heat-treated polypivalolactone yarn yields an elastic core-spun yarn having a core content of 5.5% and a modulus of 0.39 g.p.d. at 90% elongation.
  • the elastic core-spun yarn so prepared is useful for the preparation of stretchable fabrics.
  • a high work recovery fiber consisting essentially of polypivalolactone, said fiber having an orientation angle less than the numerical value given by the expression Where is the inherent viscosity of the polymer of the fiber, said viscosity being determined at a concentration of 0.5 gm. of polymer per 100 ml. of solution in trifluoroacetic acid, and at a temperature of 30 C. and is at least 0.75, the said fiber having an on ratio of at least 1.70, an a crystallite size transverse to the fiber axis of at least 85 A. and a radial breadth of not more than 040.
  • a novel fiber consisting essentially of polypivalolactone, said fiber having an orientation angle less than the numerical value given by the expression mnh-iwhere is the inherent viscosity of the polymer of the fiber, said viscosity being determined at a concentration of 0.5 gm. of polymer per 100 ml. of solution in trifluoroacetic acid, and at a temperature of 30 C. and is at least 0.75, the said fiber having an ratio of at least 2.15, an on crystallite size transverse to the fiber axis of at least 140 A. and a radial breadth of not more than 050.
  • An elastic fiber of high elongation consisting essentially of polypivalolactone, said fiber having an orientation angle that is greater than the numerical value given by the expression (mnn+ but less than 10(2n +1)
  • m is the inherent viscosity of the polymer of the fiber, said viscosity being determined at a concentration of 0.5 gm. of polymer per 100 ml. of solution in trifluoroacetic acid, and at a temperature of 30 C. and is at least 0.75
  • the said fiber having an a ratio of at least 2.15, an a crystallite size transverse to the fiber axis of at least 140 A. and a radial breadth of not more than 0.50.
  • novel fiber of claim 1 containing minor amounts of a polyamide blended with the said polypivalolactone.
  • a process comprising incorporating oriented fibers into a fibrous structure, said fibers consisting essentially of polypivalolactone having an inherent viscosity mm of at least about 0.75, said viscosity being determined at a concentration of 0.5 gm. of polymer per 100 ml. of solution in trifiuoroacetic acid, and at a temperature of 30 C. and an orientation angle having a numerical value less than 8n +l5, and heating said fibrous structure at a temperature of at least 150 C. until the fibers have an a ratio of at least 1.70, an a crystallite size of at least A. and a radial breadth of not more than 0.40".
  • a process comprising incorporating oriented fibers into a fibrous structure, said fibers consisting essentially of polypivalolactone having an inherent viscosity of at least about 0.75, said viscosity being determined at a concentration of 0.5 gm. of polymer per ml. of solution in trifiuoroacetic acid, and at a temperature of 30 C. and an orientation angle having a numerical value less than 15 +17, and heating said fibrous structure at a temperature of at least 150 C. until the fibers have an a ratio of at least 2.15,.an 0c crystallite size of at least A. and a radial breadth of not more than 050.

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DE19651494719 DE1494719A1 (de) 1964-04-20 1965-04-14 Kunstfaden bzw. -faser und Herstellung des- bzw. derselben
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CH545565A CH494827A (de) 1964-04-20 1965-04-20 Verfahren zur Herstellung von Filamenten, die elastisch sind und/oder Arbeitserholungsvermögen aufweisen
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US3379001A (en) * 1965-04-09 1968-04-23 Du Pont Blends of cellulosic and polypivalolactone staple fibers
US3418393A (en) * 1966-05-19 1968-12-24 Du Pont Block copolymers of polypivalolactone and carboxyl group containing polymers
US3450664A (en) * 1965-10-13 1969-06-17 Du Pont Process for preparing delustered polypivalolactone
US3547891A (en) * 1969-04-02 1970-12-15 Eastman Kodak Co Heat formable polyester film
US3546756A (en) * 1967-08-17 1970-12-15 Kanebo Ltd Method for manufacturing textile products having improved crease resistance
US3626048A (en) * 1967-02-10 1971-12-07 Kanegafuchi Spinning Co Ltd Method for manufacturing molded articles of polypivalolactone resin which are superior in rigidity and toughness
US3775960A (en) * 1969-10-08 1973-12-04 Kanegafuchi Spinning Co Ltd Sewing thread and a method of preparing same
US4366270A (en) * 1977-03-10 1982-12-28 Chemische Werke Huls A.G. Process for uniformly blending additives into thermoplastic synthetic resins
US4481325A (en) * 1983-12-29 1984-11-06 General Electric Company Polyalkylenelactone modified polyetherimides
EP0211467A2 (fr) 1985-07-31 1987-02-25 Shell Internationale Researchmaatschappij B.V. Compositions de polymères résistant au choc
US4797447A (en) * 1985-08-16 1989-01-10 Shell Oil Company Impact resistant blends of thermoplastic polyesters and modified block copolymers
US4906687A (en) * 1987-12-31 1990-03-06 Shell Oil Company Blends of polar thermoplastic polymers and modified block copolymers
US4954568A (en) * 1985-08-16 1990-09-04 Shell Oil Company Impact resistant blends of thermoplastic polyesters and modified block copolymers
US5863466A (en) * 1997-02-06 1999-01-26 Mor; Ebrahim Electrostatic dissipative composition

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NL8202893A (nl) * 1982-07-16 1984-02-16 Rijksuniversiteit Biologische verdraagbaar, antithrombogeen materiaal, geschikt voor herstellende chirurgie.
NL8202894A (nl) * 1982-07-16 1984-02-16 Rijksuniversiteit Polyesterhoudend filamentmateriaal.

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US2658055A (en) * 1951-08-24 1953-11-03 Du Pont Orientable condensation polymers of hydroxypivalic acid and process for preparing them
GB766347A (en) * 1953-12-16 1957-01-23 Ici Ltd Synthetic polyester fibres
FR1231163A (fr) * 1959-04-08 1960-09-27 Kodak Pathe Nouveaux polyesters de grande masse moléculaire, procédé et intermédiaires pour leur fabrication et leurs applications industrielles

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US2658055A (en) * 1951-08-24 1953-11-03 Du Pont Orientable condensation polymers of hydroxypivalic acid and process for preparing them
GB766347A (en) * 1953-12-16 1957-01-23 Ici Ltd Synthetic polyester fibres
FR1231163A (fr) * 1959-04-08 1960-09-27 Kodak Pathe Nouveaux polyesters de grande masse moléculaire, procédé et intermédiaires pour leur fabrication et leurs applications industrielles

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3379001A (en) * 1965-04-09 1968-04-23 Du Pont Blends of cellulosic and polypivalolactone staple fibers
US3450664A (en) * 1965-10-13 1969-06-17 Du Pont Process for preparing delustered polypivalolactone
US3418393A (en) * 1966-05-19 1968-12-24 Du Pont Block copolymers of polypivalolactone and carboxyl group containing polymers
US3626048A (en) * 1967-02-10 1971-12-07 Kanegafuchi Spinning Co Ltd Method for manufacturing molded articles of polypivalolactone resin which are superior in rigidity and toughness
US3546756A (en) * 1967-08-17 1970-12-15 Kanebo Ltd Method for manufacturing textile products having improved crease resistance
US3547891A (en) * 1969-04-02 1970-12-15 Eastman Kodak Co Heat formable polyester film
US3775960A (en) * 1969-10-08 1973-12-04 Kanegafuchi Spinning Co Ltd Sewing thread and a method of preparing same
US4366270A (en) * 1977-03-10 1982-12-28 Chemische Werke Huls A.G. Process for uniformly blending additives into thermoplastic synthetic resins
US4481325A (en) * 1983-12-29 1984-11-06 General Electric Company Polyalkylenelactone modified polyetherimides
EP0211467A2 (fr) 1985-07-31 1987-02-25 Shell Internationale Researchmaatschappij B.V. Compositions de polymères résistant au choc
US4797447A (en) * 1985-08-16 1989-01-10 Shell Oil Company Impact resistant blends of thermoplastic polyesters and modified block copolymers
US4954568A (en) * 1985-08-16 1990-09-04 Shell Oil Company Impact resistant blends of thermoplastic polyesters and modified block copolymers
US4906687A (en) * 1987-12-31 1990-03-06 Shell Oil Company Blends of polar thermoplastic polymers and modified block copolymers
US5863466A (en) * 1997-02-06 1999-01-26 Mor; Ebrahim Electrostatic dissipative composition

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CH494827A (de) 1970-08-15
LU48414A1 (fr) 1966-10-17
DE1494719A1 (de) 1969-12-04
NL6504055A (fr) 1966-10-03
CH473263A (de) 1969-07-15
FR1461386A (fr) 1966-02-25
CH1389466A4 (fr) 1969-02-14
GB1046994A (en) 1966-11-02

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