US3249591A - Homopolyamide of recurring bis (paraaminocyclohexyl) methane-azelamide units - Google Patents

Homopolyamide of recurring bis (paraaminocyclohexyl) methane-azelamide units Download PDF

Info

Publication number
US3249591A
US3249591A US199261A US19926162A US3249591A US 3249591 A US3249591 A US 3249591A US 199261 A US199261 A US 199261A US 19926162 A US19926162 A US 19926162A US 3249591 A US3249591 A US 3249591A
Authority
US
United States
Prior art keywords
yarn
filaments
polymer
pacm
methane
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
US199261A
Inventor
Gadecki Filon Alexander
Speck Stanley Brooke
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
Priority to US199261A priority Critical patent/US3249591A/en
Application granted granted Critical
Publication of US3249591A publication Critical patent/US3249591A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/26Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/60Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides

Definitions

  • This invention relates to fibers of linear polyamides. More specifically, this invention relates to polyamide fabrics having improved resilience and silk-like hand, combined with superior wash-wear performance.
  • Fibers from polyamides such as polyhexamethylene adipamide (66-nylon) and polycaprolactam (6-nylon) are well known for producing fabrics of excellent durability, high strength and good chemical resistance.
  • the fabrics are soft and flexible, but are not notably outstanding in resilience.
  • a test has been developed which can be applied to an individual fiber, by which wash-wear performance can be predicted. It has been found that the tensile strain recovery (abbreviated TSR for convenience) adequately predicts wash-wear performance of a fabric when sub- In one test, fibers are stretched 0.5 to 3% in 40 C. water, and are then allowed to recover in air at room temperature, without drying. The average recovery in percent gives a measure of D wash performance. In general, a TSR value of 40% is considered to be the minimum for acceptable wash-wear performance. Higher values are even more desirable.
  • a second fiber test, called washset recovery angle (abbreviated WSRA) correlates with C wash. It is described in detail hereinafter.
  • polyamides having certain molecular building blocks can be spun, drawn and subjected to an optional after-treatment thereby producing a yarn 0f specified structure, which may be woven to fabrics having both excellent resilience and superior washwear performance.
  • the required structure is identified by X-ray and optical parameters, or alternatively, by nuclear magnetic resonance (NMR).
  • the class of polymers useful for producing filaments "ice of this structure is among those disclosed in US. Patent No. 2,512,606 to Bolton and Kirk. These polymers are prepared from the diamine bis(para-aminocyclohexyl) methane, abbreviated PACM herein, for convenience.
  • PACM diamine bis(para-aminocyclohexyl) methane
  • This diamine due to its carbocyclic nature, is a mixture of isomers, having'trans-trans (tt) cis-trans (ct) and ciscis (cc) configurations. Hydrogenation conditions. used in preparing the diamine result in a mixture of isomers which may be either liquid or solid at room temperature, as disclosed in the above patent.
  • the patent describes preparation of filaments from the polymer of sebacic acid and either the liquid or the solid mixture of isomers. These filaments are disclosed to have a high tensile and torsion recovery.
  • PACM-10 polymer requires the use of sebacic acid, which is expensive and limited in supply, since it is derived from a natural product (castor oil).
  • the polymerization process is unduly expensive since the salt of PACM and sebacic acid is not water soluble enough to permit a water strike. It is usually prepared by reaction in methanol prior to polymerizing, which adds to the expense of the product.
  • the polymer from bis(para-aminocyclohexyl)methane and azelaic acid (PACM-9) does not suffer from these disadvantages, since azelaic acid is available from low cost intermediates. Moreover, the salt is water soluble.
  • the as-clrawn filaments from the polymer of liquid PACM with sebacic acid i.e., liquid PACM-l0
  • these treatments cause the filaments to shrink excessively and fuse. This limits their utility to fabrics Where such treatment is not required. Yarn from the polymer of solid PACM-l0 does not suffer from this deficiency.
  • An object of this invention is to produce a polyamide filament having low shrinkage and excellent silk-like resilience, and from which silk-like fabrics can be prepared. It is an additional object to provide such filaments from low cost intermediates by convenient processing. Fabrics produced from these filaments give superiod wash-and-Wear performance, requiring little or no ironing after washing.
  • a filament from a homopolyamide containing recurring bis(para-aminocyclohexyl)methane-azelarnide units as an integral part of the polymer chain, and having an inherent viscosity of at least 0.5, the fiber having an X-ray-optical factor of at least about 0.040 and an NMR loosening factor of less than about 2.5.
  • the para-aminocyclohexyl methane units of such a polymer preferably consist of at least 50% of the trans-trans-isomer, as identified by vapor phase chromatography of the diamine or X-ray melting point of the polymer.
  • the filaments of this invention are characterized by a low loosening factor, as measured by NMR.
  • This factor is a measure of the freedom of motion of the chain segments, and is related to the shrinkage of the yarn which must be held to a tolerable level in order for it to be processed acceptably, and not result in excessive fabric shrinkage.
  • the structure and property determinations used in characterizing the product of this invention are measured on yarn which has been drawn to a standard break elongation of about 15%. The measurements are made before the yarn has been subjected to annealing, relaxing or mock finishing treatments, unless otherwise specified.
  • the polyamide yarns of this invention are prepared by melt spinning using conventional procedures.
  • the desirable structure as already indicated, is in part a function of trans-trans (tt) content of the diamine, and to a lesser extent is dependent on the heat treatment the yarn receives subsequent to drawing.
  • the desirable structure is enhanced by a high temperature annealing treatment at constant length. Temperatures of 100 to- 200 C. are suitable; usually, the lower temperature range will be preferred for the lower tt isomer content polymers due to their lower heat stability. -It is believed that the most effective temperature range is in the vicinity or above the glass transition temperature, T which is about 160 C.
  • the yarn may be annealed on the package.
  • This may be accomplished by placing the package in an oven containing an inert gas, air or steam atmosphere. Times of from one minute to one hour are satisfactory, primarily controlled by the time required for all yarn to reach the desired temperature. Preferably, however, the annealing treatment is done on the running yarn, immediately after drawing. Heating is suitably accomplished by ya-rn contact with a hot plate, pin or tube,
  • Treatment should produce a yarn temperature of at least about 100 C. and preferably 150 C. Under these conditions, yarn contact time of 0.001 to seconds are suitable.
  • the annealing treatment may be combined with a second stage of drawing, which may be followed with a partial relaxation step if desired. These steps may be performed as separate operations, with packaging steps intervening, or as a continuous sequence.
  • yarn structure may be improved by relaxing treatments, which maybe employed to treat skeins of yarn batchwise, but preferably are carried out on the run immediately following drawing.
  • the heating means disclosed for annealing are suitable for relaxing.
  • Supen' heated steam or hot air injected into a tube as taught by Pitzl in U.S. Patent No. 3,003,222 is satisfactory.
  • the amount of relaxation should be controlled, and should be within the rangev of 5 to 20%.
  • the recovery properties (e.g., TSR) of fibers subjected to the relaxation step may appear inferior to the fibers subject to the annealing treatment. This does not necessarily indicate inferior fabric performance. Fabrics made from yarn by either process, after boil-off (which subjects the annealed yarn to a relaxation) are approximately equivalent.
  • filaments of the present invention are surprisingly different, in that they are not crystalline, even after the annealing or relaxing treatments. Indeed, it is important that heat treating conditions be limited so that theyarn will not crystallize, as shown in Example V. If crystallinity is induced by a high temperature treatment, filaments become weak, stiff and brittle. Thus, treating temperatures above 200 C. should be avoided for lower tt content polymers.
  • the TSR measurement used to predict C and D wash performance is conducted by mounting a 10 in. specimen in the yarn clamps of an Instron Tensile tester, immersing the specimen.in.40 C. water for two minutes and then extending to one of the elongations prescribed (0.5, 1.0, 1.5, 2.0, 3.0%); the clamp separation is maintained for a two minute period.
  • the immersion tank is removed from the specimen and the stress dropped to 0.042 g.p.d., and maintained for a two minute period.
  • the Instron clamps are then returned to the original separation. and the increase in yarn slack measured.
  • the difference between the amount of elongation imparted to the yarn and the amount of slack remaining after recovery is an indication of the recovery obtained at the specific elongation.
  • the test is repeated with a fresh sample for each elongation.
  • Recovery is plotted versus elongation, and the area under the curve is integrated; this indicates the average recovery value at 0.042 g.p.d. stress.
  • the final value recorded in the tables is the average of the determinations at the five different elongations.
  • the stress level of 0.042 g.p.d. is chosen to simulate the effect of fiber friction in a fabric.
  • the wash set recovery angle (WSRA) test is used to predict fabric performance in the C Wash.
  • single filament samples are wetted in hot water and dried at room temperature and low humidity while deformed under load. The samples are then allowed to recover and the degree of recovery is measured.
  • the sample is bent 360 around a 0.625 mm. mandrel and is loaded to 0.05 g.p.d. The loaded fiber is immersed for two minutes in a 0.15% aqueous minutes at 15% RH. and room temperature after which it is cut loose and allowed to recover overnight unrestrained at 15% RH, after which the recovery angle is measured. 360 is complete recovery (e.g., glass fiber) and is no recovery (wool).
  • the X-ray-optical orientation factor is the product of the X-ray orientation calculated from the intensity of an X-ray meridional diffraction spot, using the Lorentz polarization theory and the conventional birefringence measured microscopically by the use of a compensator of the Ba binet or Berek type.
  • Matrix rigidity is measured using the nuclear magnetic resonance equipment of Varian Associates, model V-4302 Dual Purpose Spectrometer and using their high temperature probe insert model No. V-4331-TWL and using 56.4 mc./s. radio frequency energy. Yarns are wrapped taut around very thin glass rods and the ends tied to prevent shrinkage during the heating experiment. This wrapping, therefore, provides a random placement of the.
  • Data points are obtained about every five degrees while heating the yarn in the NMR instrument during an approximate 2-hour period.
  • the matrix rigidity value at 100 C. is obtained as an extrapolation of the straight line through the data points between room temperature and about 95-98 C. This value at 100 C. is subtracted from the matrix rigidity value of the soaked yarn at room temperature to obtain the loosening factor.
  • the standard tests used herein to simulate home laundering performance are to machine wash the fabric in a tumble type washing machine at a water temperature of 40 C. After the washing period, the fabric load is given a final spin to extract excess water.
  • C Wash test simulating washing and tumble drying, the
  • the inherent viscosity of the polymer is determined on a solution containing 0.5 gm. polymer in 100 ml. m-cresol.
  • a polymer is prepared in an autoclave from 50% aqueous solution of the salt of bis-(para-aminocyclohexyl) methane and azelaic acid.
  • the diamine consists of tt, 25% ct and about 5% cc isomers.
  • Yarn is spun and drawn from polymer of varying isomer content, according to the procedure of Example I. Yarn properties are measured after mock finishing. The column headed strength loss lists the strength reduction due to mock finishing Table II [Yarn properties after Mock Finishing] X-ray NMR TSR, Break Strength Isomer Sample optical loosening percent Ten., g.p.d. Elong, loss, Ratio.
  • Yarn is prepared from polymers of different isomer ratio and type of acid, according-to the procedure of Example I. Yarn properties before and after constant length annealing and after mock finishing are listed in the following table.
  • PACM9 and PACM-10 of 31% tt-isomer content are deficient in heat stability, as shown by high boil-off shrinkage and by fusing on mock finishing. At 45% tt-isomer content, PACM-lO is a satisfactory yarn, whilePACM-9 is too unstable.
  • EXAMPLE IV ADVANTAGES OF HEAT TREATMENT Filaments from PACM-9 polyamides of various isomer ratios are prepared as described in Example I. Immediately after drawing and before packaging, they are (a) passed through a steam tube as shown by Pitzl in US. 3,003,222, relaxing the yarn 13%, or (b) passed in multiple wraps around a hot plate (suitable design being that perat-ure gives some improved properties at higher ttisomer' level yarns; excessive temperatures should not be employed (see Example V).
  • the tenacity after removing all methanol is about 0.5 g.p.d., the yarn is brittle, and the crystallinity is much greater than that of sample G above. It is noted that the length of the structural repeating unit of the polymer is increased from 10 A. for the non-crystalline polymer to about 22 A. for all the crystalline samples. The predicted length of the PA- CM-9 unit is about 22 A.
  • filaments of the present invention have many properties which are unusual and I unexpected when compared to those of other polyamides.
  • the filaments can be employed in a variety of constructions such as taffeta, broadcloth, etc. which show Percent tt Temp. of X-ray opti- NMR TSR, Boil-oft Sample 180K181 Treatment medium, cal factor loosening percent shrink., 0. percent Nonecontrol 0. 031 3. 4 4. 2 82 45 Steam relax.-- 150 0. 031 3. 0 81 45 0. 038 3. 4 29 44 0. 041 2. 9 34 21 50 Hot anneal 150 0. 059 2. 4 47 12 50 do 175 0. 051 2. 0 34 8. 9 65 None-control- 0. 054 2. 1 51 12 65 Hot anneal 150 0. 077 49 10. 3 65 o 170 0.123 2.0 55 7.0
  • Samples G-I show that increasing the treatment temsilk show an unusual stitlening of the molecule in water
  • PACM-9 differs from silk in showing reversibility in matrix rigidity values as the fiber is cooled from high temperatures. Silk becomes more rigid on dry heating but becomes much less rigid on drying out from the boil. It is believed that this behavior may be related to the improved wash-wear performance of PACM-9 vs. silk.
  • the filaments of this invention are especially adaptable to making resilient silk-like fabrics which, unlike silk, give a high level of wash-wear performance.
  • Filaments from PACM-9 polymer of at least 0.5 inherent viscosity, from diamine in a preferred range of 55 to 70% tt isomer content will normally show a TSR of about 70%, after boil-off, but not heat set which is significantly above the minimum (60) for acceptable D wash performance.
  • TSR for silk is 40, and for 66-nylon is 60.
  • Trans-trans isomer content above 80% contributes little to fabric properties; do to high melt viscosity at conventional molecular weight, processing is very difficult.
  • the filaments of the invention are suitable for use in continuous filament form, as staple, crim'ped tow, fioc or the like. They may be used in fabrics of woven, knitted, tufted, pile, non-woven, or felted construction. They are useful for industrial yarn, especially where high modulus, high recovery fibers are required, such as for V- belts, tire cord, laminates and the like.
  • the filaments may be used alone or may be plied or blended with other natural, synthetic or man-made fiber.
  • the filaments of the invention may be dyed, printed, pigmented, bleached, grafted or the like. They may be textured, bulked, heat set, twisted, crirnped, or any combination of these processes.
  • the polymer composition used for the filaments of this invention may contain suitable heat stabilizers, antioxipara-aminocyclohexyl methane units are of the transtrans isomer, the filament having an X-ray optical factor of at least about 0.040 and a nuclear magnetic resonance loosening factor of less than about 2.5.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Artificial Filaments (AREA)

Description

jected to a standard C or D wash procedure.
United States Patent 3 249 591 HOMOPOLYAMIDE 6F RECURRING BIS(PARA- AMINOCYCLOHEXYL)METHANE AZELAMIDE UNITS Filon Alexander Gadecki and Stanley Brooke Speck, Wilmington, Del., assignors to E. I. du Pont de Nemours and Company, Wilmington, Del., a corporation of Delaware No Drawing. Filed June 1, 1962, Ser. No. 199,261
2 Claims. (Cl. 260-78) This invention relates to fibers of linear polyamides. More specifically, this invention relates to polyamide fabrics having improved resilience and silk-like hand, combined with superior wash-wear performance.
Fibers from polyamides such as polyhexamethylene adipamide (66-nylon) and polycaprolactam (6-nylon) are well known for producing fabrics of excellent durability, high strength and good chemical resistance. The fabrics are soft and flexible, but are not notably outstanding in resilience.
The synthetic fiber industry has long sought a fabric that would have the'hand, drape and other aesthetics of silk. Silk is noted for the almost explosive way in which it bursts from the 'hand after it has been crumpled into a tight ball. Attempts have been made to synthesize polyamides from which fibers having this resilience can be prepared. Such polyamides have usually contained aromatic or cycloaliphatic rings in the polyamide chain. Unfortunately, these polyamides are very intractable, being sometimes infusible, and almost always hard to extrude due to high melt viscosity and difficult to draw due to lack of polymer chain mobility.
While silk has desirable aesthetic properties, it is notably deficient in what has been termed ease of care or wash-and-wear performance. The modern demand is for fabrics which require a minimum amount of ironing, and which can be laundered in home laundry equipment, preferably requiring merely drip drying before'wearing, Although some synthetic fabrics meet this goal, for example, polyethylene terephthalate, the synthetic fibers, fail to provide fabrics with the rich hand of natural silk.
A test has been developed which can be applied to an individual fiber, by which wash-wear performance can be predicted. It has been found that the tensile strain recovery (abbreviated TSR for convenience) adequately predicts wash-wear performance of a fabric when sub- In one test, fibers are stretched 0.5 to 3% in 40 C. water, and are then allowed to recover in air at room temperature, without drying. The average recovery in percent gives a measure of D wash performance. In general, a TSR value of 40% is considered to be the minimum for acceptable wash-wear performance. Higher values are even more desirable. A second fiber test, called washset recovery angle (abbreviated WSRA) correlates with C wash. It is described in detail hereinafter.
Apart from desirable wash-and-wear characteristics, it is essential that modern fabrics be dyeable and heat settable by conventional procedures. Consequently they must be stable to aqueous boil and to dry heat setting at about 180 C.
It has been discovered that polyamides having certain molecular building blocks can be spun, drawn and subjected to an optional after-treatment thereby producing a yarn 0f specified structure, which may be woven to fabrics having both excellent resilience and superior washwear performance. The required structure is identified by X-ray and optical parameters, or alternatively, by nuclear magnetic resonance (NMR).
The class of polymers useful for producing filaments "ice of this structure is among those disclosed in US. Patent No. 2,512,606 to Bolton and Kirk. These polymers are prepared from the diamine bis(para-aminocyclohexyl) methane, abbreviated PACM herein, for convenience. This diamine, due to its carbocyclic nature, is a mixture of isomers, having'trans-trans (tt) cis-trans (ct) and ciscis (cc) configurations. Hydrogenation conditions. used in preparing the diamine result in a mixture of isomers which may be either liquid or solid at room temperature, as disclosed in the above patent. The patent describes preparation of filaments from the polymer of sebacic acid and either the liquid or the solid mixture of isomers. These filaments are disclosed to have a high tensile and torsion recovery.
One disadvantage of PACM-10 polymer is that it requires the use of sebacic acid, which is expensive and limited in supply, since it is derived from a natural product (castor oil). In addition the polymerization process is unduly expensive since the salt of PACM and sebacic acid is not water soluble enough to permit a water strike. It is usually prepared by reaction in methanol prior to polymerizing, which adds to the expense of the product.
The polymer from bis(para-aminocyclohexyl)methane and azelaic acid (PACM-9) does not suffer from these disadvantages, since azelaic acid is available from low cost intermediates. Moreover, the salt is water soluble. The as-clrawn filaments from the polymer of liquid PACM with sebacic acid (i.e., liquid PACM-l0) are not stable to dyeing and heat-setting treatments, since these treatments cause the filaments to shrink excessively and fuse. This limits their utility to fabrics Where such treatment is not required. Yarn from the polymer of solid PACM-l0 does not suffer from this deficiency. Unfortunately, experiment shows that neither the liquid nor the solid mixture of PACM isomers disclosed by Bolton and Kirk can be polymerized with azelaic acid to make a polyamide yarn which can be subjected to conventional finishing procedures. Both are too heat sensitive. When subjected to boiling water and dry heat setting, the filaments fuse into a brittle, unitary yarn which cannot be separated.
The adverse effect of conventional finishing procedures on filaments of liquid PACM-9 was not surprising in view of a similar effect on the filaments of homologousliquid PACM-10. However, the different behavior of the polymers from solid PACM-l0 and PACM-9 respectively, towards heat is indeed unexpected, especially since the polymers have the same X-ray melting point, and do not show even the normal variation in melting point observed with homologous polyamides having odd vs. even numbers of carbon atoms in the repeating unit. The present invention in providing a polyamide filament based on PACM and azelaic acid which is stable to conventional dyeing and finishing overcomes these difficulties.
An object of this invention is to produce a polyamide filament having low shrinkage and excellent silk-like resilience, and from which silk-like fabrics can be prepared. It is an additional object to provide such filaments from low cost intermediates by convenient processing. Fabrics produced from these filaments give superiod wash-and-Wear performance, requiring little or no ironing after washing.
These and other objects are attained in a filament from a homopolyamide containing recurring bis(para-aminocyclohexyl)methane-azelarnide units as an integral part of the polymer chain, and having an inherent viscosity of at least 0.5, the fiber having an X-ray-optical factor of at least about 0.040 and an NMR loosening factor of less than about 2.5. The para-aminocyclohexyl methane units of such a polymer preferably consist of at least 50% of the trans-trans-isomer, as identified by vapor phase chromatography of the diamine or X-ray melting point of the polymer.
and D wash). It is related to the optical characteristics,
polarizability, arrangement and orientation of the molecules themselves. High values of this parameter indicate high molecular orientation accompanied by a high degree of interchain bonding, resulting in greater stability. The shrinkage of this stabilized structure is therefore low, since the potential for molecular rearrangement, which is the basic mechanism of shrinkage, is greatly reduced.
'In addition, the filaments of this invention are characterized by a low loosening factor, as measured by NMR. This factor is a measure of the freedom of motion of the chain segments, and is related to the shrinkage of the yarn which must be held to a tolerable level in order for it to be processed acceptably, and not result in excessive fabric shrinkage.
It is believed that in order for a yarn to shrink, it must have a capacity for rearrangement of the molecular segments- Nuclear magnetic resonance measures motional constraint of segments, the degree being shown by the width of the broad absorption band. This motional constraint has been labeled matrix rigidity. Since the shrinkage measurement is the result of a boiling water treatment, the matrix rigidity is measured in water at room temperature and at the boil. The difference in these values may be termed the loosening parameter. 2
High values for this parameter. would indicate a large amount of loosening as the yarn is exposed to boiling water. Such a large value would be expected to accompany a high degree of shrinkage if there were internal stress within the fiber. Conversely, low values indicate a desirably low tendency to shrink in boiling water. The measurements are taken while the yarn is in the taut condition, under the assumption that this simulates the shrinkage tension that the yarn develops at the boil.
The structure and property determinations used in characterizing the product of this invention are measured on yarn which has been drawn to a standard break elongation of about 15%. The measurements are made before the yarn has been subjected to annealing, relaxing or mock finishing treatments, unless otherwise specified.
. The polyamide yarns of this invention are prepared by melt spinning using conventional procedures. The desirable structure, as already indicated, is in part a function of trans-trans (tt) content of the diamine, and to a lesser extent is dependent on the heat treatment the yarn receives subsequent to drawing. In general, the desirable structure is enhanced by a high temperature annealing treatment at constant length. Temperatures of 100 to- 200 C. are suitable; usually, the lower temperature range will be preferred for the lower tt isomer content polymers due to their lower heat stability. -It is believed that the most effective temperature range is in the vicinity or above the glass transition temperature, T which is about 160 C. The yarn may be annealed on the package. This may be accomplished by placing the package in an oven containing an inert gas, air or steam atmosphere. Times of from one minute to one hour are satisfactory, primarily controlled by the time required for all yarn to reach the desired temperature. Preferably, however, the annealing treatment is done on the running yarn, immediately after drawing. Heating is suitably accomplished by ya-rn contact with a hot plate, pin or tube,
or by heating in a radiant tube, fluid jet, molten metal or oil bath, fluidized bed, convection heated oven or the like. Treatment should produce a yarn temperature of at least about 100 C. and preferably 150 C. Under these conditions, yarn contact time of 0.001 to seconds are suitable.
The annealing treatment may be combined with a second stage of drawing, which may be followed with a partial relaxation step if desired. These steps may be performed as separate operations, with packaging steps intervening, or as a continuous sequence.
Alternatively, yarn structure may be improved by relaxing treatments, which maybe employed to treat skeins of yarn batchwise, but preferably are carried out on the run immediately following drawing. The heating means disclosed for annealing are suitable for relaxing. Supen' heated steam or hot air injected into a tube as taught by Pitzl in U.S. Patent No. 3,003,222 is satisfactory. The amount of relaxation should be controlled, and should be within the rangev of 5 to 20%.
The recovery properties (e.g., TSR) of fibers subjected to the relaxation step may appear inferior to the fibers subject to the annealing treatment. This does not necessarily indicate inferior fabric performance. Fabrics made from yarn by either process, after boil-off (which subjects the annealed yarn to a relaxation) are approximately equivalent.
When using steam as the treating fluid under such conditions that liquid water (condensate) remains on the yarn as it leaves the treatment zone, the yarn temperature will obviously be limited by the steam-water equilibrium temperature. Under these conditions, increasing steam temperature may fail to produce the expected improvement, as shown in some of the examples. This problem can be minimized by using superheated steam, pressure treatment cells, or a non-condensing fluid.
It is well known in the synthetic filament art to stabilize oriented filaments against shrinkage by heating them to induce crystallization (see for'example U.S. Patent No. 2,880,057). The filaments of the present invention are surprisingly different, in that they are not crystalline, even after the annealing or relaxing treatments. Indeed, it is important that heat treating conditions be limited so that theyarn will not crystallize, as shown in Example V. If crystallinity is induced by a high temperature treatment, filaments become weak, stiff and brittle. Thus, treating temperatures above 200 C. should be avoided for lower tt content polymers.
The TSR measurement, used to predict C and D wash performance is conducted by mounting a 10 in. specimen in the yarn clamps of an Instron Tensile tester, immersing the specimen.in.40 C. water for two minutes and then extending to one of the elongations prescribed (0.5, 1.0, 1.5, 2.0, 3.0%); the clamp separation is maintained for a two minute period. The immersion tank is removed from the specimen and the stress dropped to 0.042 g.p.d., and maintained for a two minute period. The Instron clamps are then returned to the original separation. and the increase in yarn slack measured. The difference between the amount of elongation imparted to the yarn and the amount of slack remaining after recovery is an indication of the recovery obtained at the specific elongation. The test is repeated with a fresh sample for each elongation.
Recovery is plotted versus elongation, and the area under the curve is integrated; this indicates the average recovery value at 0.042 g.p.d. stress. The final value recorded in the tables is the average of the determinations at the five different elongations. The stress level of 0.042 g.p.d. is chosen to simulate the effect of fiber friction in a fabric.
The wash set recovery angle (WSRA) test is used to predict fabric performance in the C Wash. In this test, single filament samples are wetted in hot water and dried at room temperature and low humidity while deformed under load. The samples are then allowed to recover and the degree of recovery is measured. In the actual test, the sample is bent 360 around a 0.625 mm. mandrel and is loaded to 0.05 g.p.d. The loaded fiber is immersed for two minutes in a 0.15% aqueous minutes at 15% RH. and room temperature after which it is cut loose and allowed to recover overnight unrestrained at 15% RH, after which the recovery angle is measured. 360 is complete recovery (e.g., glass fiber) and is no recovery (wool).
The X-ray-optical orientation factor is the product of the X-ray orientation calculated from the intensity of an X-ray meridional diffraction spot, using the Lorentz polarization theory and the conventional birefringence measured microscopically by the use of a compensator of the Ba binet or Berek type.
Matrix rigidity is measured using the nuclear magnetic resonance equipment of Varian Associates, model V-4302 Dual Purpose Spectrometer and using their high temperature probe insert model No. V-4331-TWL and using 56.4 mc./s. radio frequency energy. Yarns are wrapped taut around very thin glass rods and the ends tied to prevent shrinkage during the heating experiment. This wrapping, therefore, provides a random placement of the.
fiber axis with respect to the magnetic field direction so that an average NMR spectrum is obtained at any temperature. As described in I. G. Powles, Polymer, 1, 219- 265 (1960), polymers give a broad absorption spectrum which can be characterized by a half width (peak to peak distance of the derivative output curve, expressed in gauss) herein called matrix rigidity. Values are obtained using 17 db attenuation of the RF field and with a sweep modulation of 1 gauss. To obtain values of the loosening factor, the yarns are soaked overnight in D 0 while Wrapped taut and then are heated while immersed in excess D 0. (D O'is used to prevent an NMR signal from the protons in H O). Data points are obtained about every five degrees while heating the yarn in the NMR instrument during an approximate 2-hour period. The matrix rigidity value at 100 C. is obtained as an extrapolation of the straight line through the data points between room temperature and about 95-98 C. This value at 100 C. is subtracted from the matrix rigidity value of the soaked yarn at room temperature to obtain the loosening factor.
Yarns which have been subjected to the mock finishing treatment have been boiled off in skeins at 4 mg./
denier tension, dried, and have'beensubjected to a dry heat treatment of one minute at 180 C., permitting only 2% shrinkage. These conditions give an adequate estimate of the response to be expected when fabrics are subjected to standard dyeing and finishing treatment.
The standard tests used herein to simulate home laundering performance are to machine wash the fabric in a tumble type washing machine at a water temperature of 40 C. After the washing period, the fabric load is given a final spin to extract excess water. For the C Wash test, simulating washing and tumble drying, the
fabric load is tumble dried at 77 C. For the D 1 Wash test, simulating washing and drip drying, the fabric load is removed and hung up todrip-dry for a period of several hours. The washed fabrics are evaluated subjectively, applying the following ratings: (1) excessive wrinkling; (2) considerable wrinkling,'unacceptable for wear; (3) wrinkling, may be worn; (4) some wrinkling, acceptable for Wear; (5) no wrinkling, looks freshly ironed.
The inherent viscosity of the polymer is determined on a solution containing 0.5 gm. polymer in 100 ml. m-cresol.
The following examples, in which percentages are by Weight unless otherwise indicated, further illustrate the invention.
EXAMPLE I A polymer is prepared in an autoclave from 50% aqueous solution of the salt of bis-(para-aminocyclohexyl) methane and azelaic acid. The diamine consists of tt, 25% ct and about 5% cc isomers.
It should be noted that regardless of the relative amounts of ft and ct isomers, the amounts of cc does not vary greatly from about 5%; thus, giving the tt content of any isomer mixture effectively identifies it.
As viscosity stabilizer,' 17.5 millimoles of acetic acid are added for every mole of the polyamide salt. The salt solution is heated under 350 lbs/in. pressure for two hours While the temperature is raised to 285 C. The pressure is then reduced to atmospheric While the temperature is raised to 315 C. and the polymer held under these conditions for one hour. It is then extruded and cut to flake. The polymer has an inherent viscosity of 0.82. The polymer is melted and filaments are extruded at a temperature of 315 C. through a 34-hole spinneret. The yarn (about 70 denier) is then drawn 3 times its extruded length over a snubbing pinat a temperature of C. The yarn is then subjected to a constant length anneal by passing over a plate heated to C. The contact time is 0.21 sec.
After boil-01f, without heat set, the yarn is also subjected to the WSRA test, with the results shown in the following table. The work recovery from 5% stretch (WR), and TSR are also listed. Corresponding data for other Well known fibers are also listed, as well as C wash results for fabrics made therefrom.
This example demonstrates the unexpected improvement in TSR, as the structure shown by the X-ray-optical factor and NMR loosening is improved by increasing the tt-isomer content of the PACM-9 polymer.
Yarn is spun and drawn from polymer of varying isomer content, according to the procedure of Example I. Yarn properties are measured after mock finishing. The column headed strength loss lists the strength reduction due to mock finishing Table II [Yarn properties after Mock Finishing] X-ray NMR TSR, Break Strength Isomer Sample optical loosening percent Ten., g.p.d. Elong, loss, Ratio.
factor percent percent percent tt 1 Yarn fused to brittle bundle.
It is apparent that yarn properties improve markedly when the X-ray-optical factor is above about 0.040, and when the NMR loosening factor is less than about 2.5.
v EXAMPLE III This example shows the surprising difference between the PACM-9 filaments of this invention, and the PACM- 10 filaments of the prior art.
Yarn is prepared from polymers of different isomer ratio and type of acid, according-to the procedure of Example I. Yarn properties before and after constant length annealing and after mock finishing are listed in the following table.
Table III Polymer PAOM-9 PACM-10 Isomer, ratio, percent tt 31 At room temp, isomer mix. is Liq. Solid Liq. Solid X-ray polymer melting point, 0..-- 248 268 2 2 Yarn tenacity, g.p.d 4. 4 3. 8 Modulus, g .d 42 43 Boil-oil shrinkage, percent 84 82 Percent ten. lost after anneal 150 C- .l 50 35 After mock finish:
Tenacity loss, percent 100 82 Tenacity, g.p.d 0. 7
Modulus, and 13 TSR, percent. 4. 2 X-ray optical factor 0.030 0.031 NMR loosening 4. 3. 4
It is. apparent that both PACM9 and PACM-10 of 31% tt-isomer content are deficient in heat stability, as shown by high boil-off shrinkage and by fusing on mock finishing. At 45% tt-isomer content, PACM-lO is a satisfactory yarn, whilePACM-9 is too unstable.
EXAMPLE IV ADVANTAGES OF HEAT TREATMENT Filaments from PACM-9 polyamides of various isomer ratios are prepared as described in Example I. Immediately after drawing and before packaging, they are (a) passed through a steam tube as shown by Pitzl in US. 3,003,222, relaxing the yarn 13%, or (b) passed in multiple wraps around a hot plate (suitable design being that perat-ure gives some improved properties at higher ttisomer' level yarns; excessive temperatures should not be employed (see Example V).
EXAMPLE V HARMFUL EFFECT OF CRYSTALLINITY This example shows the harmful eifect of annealing treatment at temperatures sufficiently high to induce crystallization.
Filaments from PACM-9 polymer of 60% tt isomer content, 0.98 inherent viscosity, are prepared and annealed at various temperatures, according to the procedures of Examples I and IV. The X-ray crystallinity is also estimated, with the results shown in the table.
, Table V [Efiect of X-ray crystallization on yarnproperties] Sample Anneal. Crystallinity Tenacity, .WSRA, temp., C. g.p.d. percent 4. 1 265 3. 8 265 3. 7 278 3. 5 274 3. 4 262 227 Fairly well de 2. 9 236 veloped. 241 Well dcve1oped- 2. 0 200 In order to be sure that the effect observed is not heat degradation, a portion of sample A is treated with methanol at about 70 C.; methanol is a solvent which promotes crystallization. The tenacity after removing all methanol is about 0.5 g.p.d., the yarn is brittle, and the crystallinity is much greater than that of sample G above. It is noted that the length of the structural repeating unit of the polymer is increased from 10 A. for the non-crystalline polymer to about 22 A. for all the crystalline samples. The predicted length of the PA- CM-9 unit is about 22 A.
Filament characteristics.--The filaments of the present invention have many properties which are unusual and I unexpected when compared to those of other polyamides.
shown by Heighton in French Patent 1,244,789) at constant length. Contact time with the hot plate is about 0.2 sec.; the final yarn temperature is about 5 C. below that of the plate. Comparative data, without the heat treatment, are included in the following table. Contact time in the steam tube is about 0.01 second, and the final yarn temperature is believed to be about 100 C.
Table IV [Efiect of heat treatment] For example, the effect of shrinking these filaments is to produce an increase in X-ray orientation and an in: crease in matrix rigidity (as determined by NMR). It is also surprising that the matrix rigidity of the crystalline fibers is less than that of those which are amorphous.
The filaments can be employed in a variety of constructions such as taffeta, broadcloth, etc. which show Percent tt Temp. of X-ray opti- NMR TSR, Boil-oft Sample 180K181 Treatment medium, cal factor loosening percent shrink., 0. percent Nonecontrol 0. 031 3. 4 4. 2 82 45 Steam relax.-- 150 0. 031 3. 0 81 45 0. 038 3. 4 29 44 0. 041 2. 9 34 21 50 Hot anneal 150 0. 059 2. 4 47 12 50 do 175 0. 051 2. 0 34 8. 9 65 None-control- 0. 054 2. 1 51 12 65 Hot anneal 150 0. 077 49 10. 3 65 o 170 0.123 2.0 55 7.0
1 Too low to measure. 2 Not determined.
It is observed that hot annealing improves the structure and properties of the 45% t-t yarn (C vs. A), but even this treatment is insufiicient to produce an acceptable product. More severe heat treatments cannot be employed due to the thermal degradation of these low tt yarns, as shown in Example II.
It is noted that at 50% tt, the hot anneal at 150 C. (E) produces a 'suflicient improvement in structure and resulting yarn properties so that this yarn becomes acceptable. The decrease at 175 C. (F) is caused by degradation due to heat sensitivity at this isomer ratio.
Samples G-I show that increasing the treatment temsilk show an unusual stitlening of the molecule in water,
in extreme contrast to 66-nylon and polyethylene terephthalate which are loosened by water.
PACM-9 differs from silk in showing reversibility in matrix rigidity values as the fiber is cooled from high temperatures. Silk becomes more rigid on dry heating but becomes much less rigid on drying out from the boil. It is believed that this behavior may be related to the improved wash-wear performance of PACM-9 vs. silk.
It has been pointed out previously that the filaments of this invention are especially adaptable to making resilient silk-like fabrics which, unlike silk, give a high level of wash-wear performance. Filaments from PACM-9 polymer of at least 0.5 inherent viscosity, from diamine in a preferred range of 55 to 70% tt isomer content, will normally show a TSR of about 70%, after boil-off, but not heat set which is significantly above the minimum (60) for acceptable D wash performance. In contrast, TSR for silk is 40, and for 66-nylon is 60.
Trans-trans isomer content above 80% contributes little to fabric properties; do to high melt viscosity at conventional molecular weight, processing is very difficult.
The filaments of the invention are suitable for use in continuous filament form, as staple, crim'ped tow, fioc or the like. They may be used in fabrics of woven, knitted, tufted, pile, non-woven, or felted construction. They are useful for industrial yarn, especially where high modulus, high recovery fibers are required, such as for V- belts, tire cord, laminates and the like. The filaments may be used alone or may be plied or blended with other natural, synthetic or man-made fiber. The filaments of the invention may be dyed, printed, pigmented, bleached, grafted or the like. They may be textured, bulked, heat set, twisted, crirnped, or any combination of these processes.
The polymer composition used for the filaments of this invention may contain suitable heat stabilizers, antioxipara-aminocyclohexyl methane units are of the transtrans isomer, the filament having an X-ray optical factor of at least about 0.040 and a nuclear magnetic resonance loosening factor of less than about 2.5.
2. A novel wash-wear fabric containing filaments of poly[bis(para aminocyclohexyl)methane azelamide], said polymer having at least of the para-aminocyclohexyl methane units of the trans-trans isomer and the filaments having an X-ray-optical factor of at least about 0.040 and a nuclear magnetic resonance loosening factor of less than about 2.5.
References Cited by the Examiner UNITED STATES PATENTS 2,512,606 6/1950 Bolton et al. 26078 2,811,410 10/1957 Munch et a1. l854 2,880,057 '3/1959 Cuculo 26078 2,918,347 12/1959 Notarbartol-o et a1. 18-54 2,985,503 5/1961 Becker l8-54 3,003,222 10/1961 Pitzl 260-78 3,053,813 9/1962 Evans et a1. 26078 WILLIAM H. SHORT, Primary Examiner.
W. STEPHENSON, Examiner.

Claims (1)

1. A NOVEL FILAMENT OF POLY(BIS(PARA-AMINOCYCLOHEXYL)METHANE-AZELAMIDE), WHEREIN AT LEAST 55% OF THE PARA-AMINOCYCLOHEXYL METHANE UNITS ARE OF THE TRANSTRANS ISOMR, THE FILAMENT HAVING AN X-RAY OPTICAL FACTOR OF AT LEAST ABOUT 0.040 AND A NUCLEAR MAGNETIC RESONANCE "LOOSENING" FACTOR OF LESS THAN ABOUT 2.5.
US199261A 1962-06-01 1962-06-01 Homopolyamide of recurring bis (paraaminocyclohexyl) methane-azelamide units Expired - Lifetime US3249591A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US199261A US3249591A (en) 1962-06-01 1962-06-01 Homopolyamide of recurring bis (paraaminocyclohexyl) methane-azelamide units

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US199261A US3249591A (en) 1962-06-01 1962-06-01 Homopolyamide of recurring bis (paraaminocyclohexyl) methane-azelamide units
US73623668A 1968-05-02 1968-05-02

Publications (1)

Publication Number Publication Date
US3249591A true US3249591A (en) 1966-05-03

Family

ID=26894610

Family Applications (1)

Application Number Title Priority Date Filing Date
US199261A Expired - Lifetime US3249591A (en) 1962-06-01 1962-06-01 Homopolyamide of recurring bis (paraaminocyclohexyl) methane-azelamide units

Country Status (1)

Country Link
US (1) US3249591A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3534541A (en) * 1969-07-15 1970-10-20 Du Pont Crimped yarn and process of making same
US3725358A (en) * 1971-04-12 1973-04-03 Phillips Petroleum Co Polyamide fibers from mixture of 1,3-bis-(4-piperidyl) propane and bis(p-aminocyclohexyl) methane
US3857819A (en) * 1973-03-05 1974-12-31 Du Pont Polyurea fibers based on poly(4,4{40 -methylenedicyclohexylene)urea
US4195164A (en) * 1977-08-18 1980-03-25 Bayer Aktiengesellschaft Transparent polyamides

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2512606A (en) * 1945-09-12 1950-06-27 Du Pont Polyamides and method for obtaining same
US2811410A (en) * 1952-08-06 1957-10-29 Perfogit Spa Spinning of polyamides into a low humidity environment
US2880057A (en) * 1958-01-22 1959-03-31 Du Pont Treatment of filaments to improve strength in tension
US2918347A (en) * 1956-05-18 1959-12-22 Snia Viscosa Process for melt-spinning polyamides into low humidity atmosphere
US2985503A (en) * 1958-09-24 1961-05-23 Becker Hermann Method for making a plastic thread
US3003222A (en) * 1958-11-17 1961-10-10 Du Pont Controlled relaxation of freshly drawn nylon
US3053813A (en) * 1959-04-21 1962-09-11 American Viscose Corp Hexamethyleneamide, p-xylyleneamide copolymers

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2512606A (en) * 1945-09-12 1950-06-27 Du Pont Polyamides and method for obtaining same
US2811410A (en) * 1952-08-06 1957-10-29 Perfogit Spa Spinning of polyamides into a low humidity environment
US2918347A (en) * 1956-05-18 1959-12-22 Snia Viscosa Process for melt-spinning polyamides into low humidity atmosphere
US2880057A (en) * 1958-01-22 1959-03-31 Du Pont Treatment of filaments to improve strength in tension
US2985503A (en) * 1958-09-24 1961-05-23 Becker Hermann Method for making a plastic thread
US3003222A (en) * 1958-11-17 1961-10-10 Du Pont Controlled relaxation of freshly drawn nylon
US3053813A (en) * 1959-04-21 1962-09-11 American Viscose Corp Hexamethyleneamide, p-xylyleneamide copolymers

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3534541A (en) * 1969-07-15 1970-10-20 Du Pont Crimped yarn and process of making same
US3725358A (en) * 1971-04-12 1973-04-03 Phillips Petroleum Co Polyamide fibers from mixture of 1,3-bis-(4-piperidyl) propane and bis(p-aminocyclohexyl) methane
US3857819A (en) * 1973-03-05 1974-12-31 Du Pont Polyurea fibers based on poly(4,4{40 -methylenedicyclohexylene)urea
US4195164A (en) * 1977-08-18 1980-03-25 Bayer Aktiengesellschaft Transparent polyamides

Similar Documents

Publication Publication Date Title
US3393210A (en) Polycarbonamides of bis (para-aminocyclohexyl)methane and dodecanedioic acid
US2199411A (en) Artificial structure and method for producing same
US3418199A (en) Crimpable bicomponent nylon filament
US2157117A (en) Steam treatment of polyamides
US3816486A (en) Two stage drawn and relaxed staple fiber
KR0130821B1 (en) Improvements to multifilament apparel yarns of nylon
JP5807456B2 (en) Polyamide 410 fiber and fiber structure comprising the same
Gupta Heat setting
US3039171A (en) Process of drawing filaments
JP2783460B2 (en) Copolyamide and fibers made therefrom
JP3232156B2 (en) Polyamide continuous spinning, stretching method and apparatus
US3044250A (en) Textile product
FI80079B (en) FOER FARING UTLOEPNING AV POLYESTERFILAMENT.
US3321448A (en) Nylon staple fiber for blending with other textile fibers
JP2619356B2 (en) Manufacturing method of high-strength polyester yarn
US3249591A (en) Homopolyamide of recurring bis (paraaminocyclohexyl) methane-azelamide units
CN109072491A (en) High heat-shrinkable Fypro and the combined yarn and fabric for having used the Fypro
US3090997A (en) Method of continuous treatment of as-spun birefringent polyamide filaments
US3322731A (en) Interpolymers of caprolactam, hexamethylene diamine, adipic acid and sebacic acid
US4721755A (en) Fibers and yarns from a blend of aromatic polyamides
USRE26614E (en) Sr xr re
AU2016351997B2 (en) Core-sheath composite cross-section fiber having excellent moisture absorbency and wrinkle prevention
US3598789A (en) Fiber-forming pacm-16
US3505165A (en) Bifilar polyamide yarns and filaments
US3088794A (en) Process for spinning and drawing polyalkylene isophthalamides