Technical Field
[0001] This invention relates generally to improved polyamide multi-filamentary yarns, more
particularly it relates to a polyamide yarn for use in cut pile carpets without requiring
ply-twisting and the process for making such yarns.
Background
[0002] Two or more bulked continuous filament nylon yarns to be used as pile in cut pile
saxony carpets are usually ply-twisted together then heat set while traveling on a
moving belt in a relaxed condition through an enclosure in which saturated steam under
pressure permeates the yarn. This treatment sets the yarns in the twisted configuration
so that they retain a substantial degree of twist after tufting, cutting. dyeing and
wear and give an appearance of compact. columnar tuft shafts. The appearance of compact.
columnar tuft shafts with well-defined tuft tips is desired for cut pile saxony carpets,
as opposed to cut pile velour carpets where the appearance of tuft integrity is not
desired.
[0003] Yarns which are not sufficiently twisted or heat-set lose their twist so that filaments
of one tuft intermingle with those of another, giving a matted appearance.
[0004] However, ply-twisting and heat setting are both slow and expensive operations. A
yarn meeting the same performance standards as ply-twisted heat-set yarn without requiring
twisting would be highly desirable.
Summary of the Invention
[0005] A multifilament polyamide yarn product that does not require ply-twisting and is
particularly suited for use as pile in cut pile fabric, including both carpets and
upholstery because it does not spread out and mat. has now been discovered. The yarn
comprises filaments in the range of about 5-40 denier per filament having an oriented
core portion and a deoriented skin portion characterized by a Skin Deorientation Index
of about 0.1 or greater and preferably less than about 0.5 and a thickness of the
deoriented skin portion of about 0.4-3.0 micrometers. The filaments may be crimped
by any of the known methods but crimps are preferably random in frequency. direction
and amplitude. The multifilament yarn is characterized by a bending rigidity ratio
(R/R
cfm) in the range of about 20-200 in the absence of adhesive or size, preferably in
the range of about 20-75. a lateral pull apart distance of about 4 cm., and the number
of filaments are less than about 500. with a portion of these being lightly bonded
together. Yarn having a bending rigidity ratio of 20-75 is generally suitable for
residential carpets while yarn at 75-200 can be used for heavy wear installations.
[0006] The yarn bundle may be substantially free of true yarn twist. This does not exclude
a small amount of twist which may occur incidentally in the handling of the yarn bundle,
such as by overend take off of the yarn bundle in a conventional manner from a stationary
package, as from a creel. A yarn bundle having no more than about one turn of true
twist per 3 cm is considered to be substantially twist free.
[0007] The improved properties are believed to arise in part from a deorientation of the
polymer molecules in the outer region or skin portion of the filaments and in part
from light bonding among the filaments. Evidence for deorientation can be obtained
from observation of the birefringence difference between skin and core or by observing
the general lack of anisotropy present in a mechanically delaminated section of "skin".
Evidence of light bonding among the filaments can be observed by physically pulling
the yarn apart by hand and also can be seen by following the procedures set out in
Example 5. Yarns of this invention are found to be significantly stiffer than yarns
that have not been subjected to the process of this invention as determined by a ratio
of the bending rigidity of the yarn bundle measured as described herein to the computed
rigidity of the same yarn bundle wherein the filaments are completely free to move
relative to each other. Yarns of the invention derive such stiffness from the heat
and moisture treatment accompanied by the compacting effects of the close-fitting
inlet and outlet passages of the steam treating chamber without the presence of adhesive
or size. The inlet passage has a diameter roughly the same size or smaller than the
diameter of the yarn bundle resulting in the crimped surface filaments of the yarn
bundle being slightly compressed in the inlet passage. It is indeed surprising that
yarns having stiffnesses characteristic of the present products can develop such a
high degree of bulk during carpet finishing. The bending rigidity ratio is a measure
of the degree of light bonding among the filaments. At too low a bending rigidity
ratio, there is too little bonding among the filaments in the yarn bundle and the
carpet made from such yarn bundle spreads out to give a matted appearance. At too
high a bending rigidity ratio too many strong bonds are formed and the carpet made
from the yarn bundle is harsh to the touch and the filaments are excessively fused.
[0008] The yarn bundle of this invention is radially compressed while passing through the
inlet and outlet passages of the steam treatment chamber forcing the filaments into
a more intimate arrangement than is characteristic of such filaments without such
compression and the filaments are lightly bonded where the filaments touch. Since
the filaments retain a substantial amount of their original crimp, these contact points
are of a limited area and the light bonding at the contact points substantially disappear
later when the yarn is flexed during tufting and carpet finishing. Nevertheless, the
combination of light bonding and the more intimate arrangement gives the product of
the present invention a desirable degree of stiffness and coherency which allow it
to be used in cut pile carpets without the cost of the usual ply-twisting and heat-setting.
The temporary nature of the light bonding and the retention of crimp recovery ability
permits the present yarns to recover bulk in final carpet form.
[0009] The process of forming light bonds between filaments and compactness of the present
product is particularly beneficial when unusually bulky feed yarns are used. Such
yarns may have such large filament loops extending from the yarn surface that they
cannot be fed satisfactorily through conventional yarn guides and needles of standard
carpet tufting machines. When such yarns are processed in accordance with the present
invention with adjustments of apparatus dimensions to suit the product in accordance
with the disclosures herein, the surface loops are found to be compressed onto the
yarn bundle sufficiently for the yarn to feed satisfactorily through tufting, yet
they unfold and expand during carpet finishing to recover their desired bulk and texture.
[0010] The product is made by a process of passing one or more crimped multi-filamentary
polyamide yarns under tension through a close-fitting inlet wherein the length is
5.1 cm or more. subjecting them to saturated steam substantially free of entrained
water and impinged on the axis of the yarn bundle and exposing it to the steam for
a time of 150 milliseconds or less, preferably about 30 to 70 milliseconds in a chamber
of sufficient size to allow the filaments to spread and be treated individually by
the steam which is maintained at elevated pressure equivalent to saturation at the
specific temperature of the steam, and passing the filaments through a close-fitting
outlet similar to the inlet preferably of the same diameter to about 0.7 of the inlet
diameter, at a ratio of outlet to inlet tension of 1.1 to 1 or greater, and winding
on a package.
BRIEF DESCRIPTION OF THE DRAWINGS
[0011]
Fig. 1 is a schematic representation of an apparatus for practicing the process of
the invention.
Fig. 2 is a longitudinal section taken along lines 2-2 of Fig. 1.
Fig. 3 is a schematic representation showing the fringe shift which characterizes
skin-core orientation differences and skin thickness.
Fig. 4a and 5a are interference micrographs of a cross-section of a filament showing
the fringe shift which characterizes skin-core orientation differences and skin thickness.
Fig. 4b and 5b are schematic cross-section representations of the filament position
from which the micrographs of Fig. 4a and 5a were taken.
Fig. 6 is a schematic representation of a cross-section of a trilobal filament.
Fig. 7 is a schematic diagram of an instrument for measuring bending rigidity of yarn
samples.
Fig. 8 is a photograph of a cross-section of the yarn of this invention.
DETAILED DESCRIPTION OF THE DRAWINGS
[0012] Referring to Fig. 1. one or more crimped continuous filament yarns 10 are taken from
supply packages 12. combined into a yarn bundle 14 at guide 16 and led through steam
treatment device 18 where the yarn is treated by impinging saturated steam at elevated
pressure on the yarn bundle. Saturated steam is supplied from a source (not shown)
and enters the steam treatment device 18 through pipe 20. Treated yarn 22 then passes
through forwarding rolls 24 to windup package 26.
[0013] Fig. 2 shows a longitudinal cross section of the steam treatment device 18 in Fig.
1. wherein yarn bundle 14 enters inlet 28. an elongated tube having a close-fitting
passage 30 through which the yarn bundle passes to chamber 32 where a portion of the
saturated steam from chamber 32 travels countercurrent to the direction of yarn movement
and begins to heat yarn bundle 14. As the yarn bundle enters chamber 32. saturated
steam from orifice 34 impinges on the longitudinal axis of the chamber and the yarn
bundle. separating the filaments, and heating them individually on all sides, after
which the yarn passes out of chamber 32 through close-fitting passage 36 of outlet
38.
[0014] The passage 30 should preferably have a cylindrical bore of small enough inside diameter
that no substantial amount of steam escapes from the upstream inlet 28 under the particular
operating conditions selected. On the other hand. it should not be so small that friction
between the yarn bundle and inlet imposes excessive tension on the yarn. The degree
of crimp in the filaments, the denier and number of the filaments and other factors
may influence the diameter selected. Steam condensing on the incoming filaments assists
in minimizing leakage as do higher yarn speeds.
[0015] Chamber 32 in which steam impinges on the yarn should be of large enough inside diameter
so that the filaments can spread apart to be treated on all sides by the steam. Surprisingly,
this diameter may actually be less than that of passage 30 under some modes of operation.
The tension on the filaments is higher in the chamber than in passage 30 due to the
increasing drag between yarn and inlet wall as the yarn progresses, and this tension,
coupled with the increasing filament temperature, straightens the filaments temporarily.
Thus. they occupy considerably less space than previously and have much greater freedom
to move about while being steam treated.
[0016] The diameter of chamber 32 should not be so large that the yarn bundle can avoid
the direct impingement of steam from orifice 34. A maximum chamber diameter of about
1.5 X the diameter of passage 30 is preferred.
[0017] In chamber 32, the filament surfaces reach their maximum temperature approaching
that of the steam. The water vapor lowers the melting point of polyamide yarns drastically,
causing the surfaces or skin of the filaments to molecularly deorient and reach a
"tack point" at which they may form light bonds. The limited penetration of the water
vapor prevents deorientation of the core of the filaments. thus preserving their desired
properties such as tenacity and their ability to recover crimp and bulk during carpet
finishing. The deoriented skin is a minor percentage of the total filament.
[0018] The steam treated yarn then passes into passage 36, which may be of about the same
inside diameter as passage 30 or smaller. In this portion of the apparatus, some leakage
of steam downstream may be desirable, since a substantial steam throughput is necessary
to give a high enough velocity of steam flowing through orifice 34 to separate and
treat the filaments adequately. Aside from leakage, a substantial quantity of steam
is carried downstream with the yarn. Therefore, the inside diameter of passage 36
may be the same size as passage 30 even though the yarn tension and temperature straightens
the crimp and makes the yarn somewhat less bulky than when it passes through inlet
28. Alternatively, the inside diameter of passage 36 may be about 0.7 of the diameter
of passage 30.
[0019] The sealing effect of the inlet and outlet passages depends on a combination of their
diameters as compared to the diameter of the yarn and lengths. A very short passage
would need to be very small to give adequate sealing, but this may impose excessive
tension on the yarn. For practical purposes, lengths of 2 inches or more as measured
from steam impingement orifice 34 are preferred. The outlet passage may preferably
be longer than the inlet.
[0020] The ratio of yarn tension downstream of the outlet to yarn tension upstream of the
inlet is a useful process control parameter. It is a measure of the frictional drag
imposed on the yarn during its passage through steam treatment device 18. This ratio
should be at least 1.1:1. since any lower reading indicates inadequate sealing against
steam leakage. While there is no definite upper limit, each product will have preferred
operating limits to avoid pulling out excessive amounts of crimp, bulk or entanglement.
[0021] Steam flashes off the yarn as it emerges from outlet 38 into atmospheric pressure.
The yarn may be cooled and dried adequately by the rotation of the windup package
or by extending the distance between steam treatment device 18 and windup package
26. If forced cooling is necessary, it should be performed in a manner which does
not separate the filaments, such as treating with cold air under confinement similar
to that in outlet 38 or by contact with a heat sink.
[0022] It is important that the saturated steam supplied through pipe 20 be substantially
free of entrained water, since the presence of liquid condensate causes variations
in the dye receptiveness of polyamide yarns. To this end. one or more condensate separators
40 may be installed in the supply line leading to pipe 20. and the line and pipe should
be maintained at the desired temperature by known means such as wrapping electric
heating cables 42 around the line or steam tracing.
[0023] When yarns of different dyeabilities or other different properties are employed,
the different components may not be affected equally by the processing conditions.
[0024] For example, lower-melting filaments may become excessively deoriented and fused,
creating an undesirably harsh and stiff product. Optimum processing conditions for
such products may be determined by experimentation.
[0025] A preferred product of this invention is made from two or more crimped yarns 10 of
at least two different colors or dyeabilities. at least one but not all of which is
interlaced and then all yarns are entangled together as described in Nelson U.S. Patents
Nos. 4.222.223 and 4.343.146. When the above-preferred product of the invention is
made into cut pile carpet, dyed and finished, the added cohesion given the yarn by
radial compression in outlet 38 persists during wear. effectively locking the fibers
into their positions relative to one another which existed at the time of processing.
Therefore. filaments of a given color remain substantially together, giving definite
spots of color and the appearance of tuft definition. Yarns described in Nelson U.S.
Patent 4.343.146 are particularly benefitted by processing in accordance with the
present invention. In a yarn where too few or no light bonds are formed, the filaments
of a given color separate and mingle with those of a different color giving a blurred
and indistinct appearance.
TEST METHODS
LATERAL PULL-APART TEST
[0026] The Lateral Pull-Apart Test directly measures the lateral bundle cohesiveness of
a yarn. Two hooks are placed at a randomly selected point in about the center of the
yarn bundle to separate it into two groups of filaments. The hooks are pulled apart
at a rate of 5 inches/min. (12.7 cm/min.) at a 90° angle to the yarn axis by a tensile
testing machine which measures the resistance to separation, such as an "Instron"
machine. The yarn is pulled apart by the hooks until a one-pound (454 gm.) force is
exerted, at which point the machine is stopped and the distance between the two hooks
is measured and recorded. Ten determinations are made and the average taken as the
pull-apart value. The test yarn lengths should be at least 4-6 inches (10-15 cm.)
long and selected randomly throughout a yarn package.
[0027] Normally, in yarns composed of two or more feed yarns, the component yarns are not
distinguishable and so a random placement of the hooks in the yarn gives a satisfactory
measurement of bundle cohesiveness. If component yarns can be distinguished. the hooks
should be inserted through at least two of the components.
MEASUREMENT OF "SKIN DEORIENTATION INDEX" (SDI)
[0028] When the fibers pass through the steam chamber their outer regions partially melt
and deorient producing a skin/core structure. Evidence for this deorientation can
be seen by observations of the fibers in core-matching refractive index fluids selected
as determined below for both refractive indices, n,, n,,. With the microscope set
to observe n, the fringes passing through the skin are displaced in a direction corresponding
to a higher refractive index relative to the core. Conversely, when n,, is examined,
the fringe displacement in the skin corresponds to a lower refractive index relative
to the core. The difference in refractive indices, i.e.. the birefringence, of the
skin is less than the birefringence of the core. Since birefringence reflects molecular
orientation, the skin is deoriented.
[0029] Other evidence for a deoriented skin can be observed with a polarizing microscope.
By carefully pulling apart two bonded fibers, portions of the skin can be examined.
When viewed in the 45° position. between crossed polars most of the skin appears isotropic.
[0030] SDI is an empirical measure of the deorientation in the skin. It is a value associated
with the difference in refractive indices between skin and core for light polarized
parallel to the fiber axis modulated by the skin thickness. It is deduced from the
observation of the fibers with a two beam Leitz transmitted light interference microscope
(Serial No. 592469) set for the fringe field mode. Illumination is provided by a mercury
arc lamp filtered to provide a wavelength of 546 nm. The fibers are observed in a
core-matching refractive index fluid (nominal value 1.572 at a wavelength of 589 nm
and at 25°C), manufactured by R. P. Cargille Laboratories. Inc., at a nominal magnification
of X500. The procedure for calculating the SDI entails measuring the fringe displacement
in the skin, d. relative to the inter-fringe spacing. D. as depicted in Figure 3.
This is determined with the aid of the drum compensator on the interferometer and
an eyepiece cross-hair reticle. D is an instrumental constant and for this instrument
corresponds to 210.5 divisions of the drumscale for a wavelength of 546 nm.
[0031] The sample is prepared as follows: A plain microscope slide is halved and some fibers
are placed on both halves, immersed in a selected fluid. A cover slip is placed over
both slides. One slide preparation is placed on the sample stage of the microscope
and positioned so there is a fiber in the field of view. The other preparation is
placed on the microscope's reference stage with no fibers in the field of view. This
is a standard procedure to ensure that both beams of the interferometer have identical
path lengths. The interferometer is adjusted so that vertical fringes appear in the
field of view and one fiber is oriented perpendicularly to the fringes. The microscope's
analyzer is set to transmit light vibrating parallel to the fiber axis. The interferometer
is adjusted for maximum sharpness of the fringes. Preliminary observations are necessary
to select the core-matching refractive index fluid. The selection of this fluid is
determined by successively immersing the fibers in a series of refractive index fluids.
The core matching fluid is that fluid producing the smallest fringe displacement inside
the fiber. When hollow fibers are measured. regions corresponding to the hollow part
of the fibers are disregarded.
[0032] A region of the fiber is first selected where the fringe shift in the skin is clearly
delineated For example. in the case of a hollow, quasi-square cross-section, a proper
attitude relative to the light beam is required. A proper attitude is one for which
the fiber lays on one of its edges so that three voids are seen. This is illustrated
in Fig. 4a and 4b. If only two voids are observed, the fiber is laying on a face as
shown in Fig. 5a and 5b. In such a case the fringe pattern in the skin is obscured
by refraction effects and d cannot be measured. For fibers having a star cross-section,
e.g. trilobal. the measurement is obtained from a lobe whose skin isn't eclipsed by
another lobe. For an attitude as depicted in Fig. 6. the measurement would be taken
from lobe A: lobes B and C cannot be measured because their images are superimposed.
[0033] To measure d. the drum compensator is turned until the fringe pattern is positioned
so that a background fringe is superimposed on the vertical line of the reticle: the
corresponding compensator reading is noted. The pattern is then translated to bring
that region of the fringe where the displacement is maximum (i.e., in the skin) in
coincidence with the vertical line: the new compensator reading is noted. The absolute
value of the difference between the two readings is d. The SDI is calculated as follows:

Fibers of this invention have an SDI of at least 0.05.
SKIN THICKNESS
[0034] The approximate skin thickness can be obtained by photographing the fiber in the
fringe field mode at a nominal magnification of x500. The skin thickness is measured
from the micrograph with a x4 magnifier containing a reticles scale of 50mm incremented
in units of .lmm. The magnifier was calibrated from another x500 micrograph of a micrometer
slide (Carl Zeiss) ruled to .Olmm. The skin thickness is always less than 4µm.
BENDING RIGIDITY RATIO
[0035] The bending rigidity ratio (R/R
cfm) is determined by measuring the bending rigidity (R) of the yarns and dividing by
the computed rigidity of the same basic yarn wherein the fibers are completely free
to move relative to each other. (Rcfm), the subscript meaning "Complete Freedom of
Motion".
[0036] The yarn bending rigidity can be measured by a number of techniques such as by using
a Mitex Mk II Bending Tester manufactured by IDR. Needham. Massachusetts, U.S.A. In
this test. referring to Fig. 7, the yarn sample 60. which is about 2 inches (5.1 cm.)
long. is inserted as shown between pins 61 and 62 mounted on block 63 and between
pin 64 and arm 66. Then pin 64 mounted on micrometer 65 is adjusted to bring yarn
sample 60 into light contact with arm 66 of force transducer 67. The distance from
pin 62 to arm 66 is 1 inch. Block 63 moves to bend the sample into circular arcs of
progressively increasing yarn curvature (curvature - 1/radius of curvature). This
deformation is accomplished by movement of block 63. The maximum curvature is 1.5
in. 1. The outputs of the force transducers and a transducer which measures block
rotation are fed to an X-Y recorder. Since the bending moment on the sample equals
the force on the force transducer times the distance between pins 64 and 66 and the
curvature is proportional to the block rotation, the output plot gives the yarn moment-curvature
response.
[0037] The slope of the moment-curvature plot equals the sample rigidity and has units of
force-length . The instrument is calibrated before measurements are made by measuring
the slope of a stainless steel strip of calculted rigidity. 0.001 inch (0.0025 cm.)
thick and 0.5 inch (1.27 cm.) wide inserted in place of the yarn. The rigidity of
the stainless steel strip is calculated by the following equation: R
c=w
c

E
c/12 where R
c = Rigidity of calibration strip w
c = width of calibration strip - 0.5 in. t
c = thickness of calibration strip - 0.001 in. E
c = Young's modulus of calibration strip = 30.000.000 psi. therefore: R
c = 1250 in
2lb.
[0038] The slope of the calibration strip plot is divided into the calibration strip's calculated
rigidity to give the calibration factor. The rigidity of any unknown yarn samples
equals its slope times the calibration factor.
[0039] Five yarn samples from each item are measured as above and the results are averaged
to give the values for R. The value of R
cfm is computed by multiplying the rigidity of a cylinder having the modulus of a fiber
by the number of fibers.
[0040] In terms of the combined "textile" and engineering units, the relation can be written
as: where:
K - 3.02 x 10-11 lb. in.2/(den)(cc)
Nf = No. of filaments in a yarn (calculated from ratio of yarn to filament denier)
Ef = Fiber modulus (g/denier)
wf = Filament Linear Density (denier)
df = Filament Density (g/cc)
R is then divided by R
cfm to give the bending rigidity ratio for each item.
EXAMPLES
Example 1
[0041] Various crimped multifilament yarns are entangled together by several processes and
are passed through a saturated steam treatment device under conditions shown in Table
1. Feed yarn A is 1225 denier 19 denier per filament cationic dyeable jet- bulked
continuous filament nylon 66 yarn, each filament having a cross section approximating
a square with rounded corners and a continuous void near each corner. Yarn B is the
same as yarn A except for being light acid dyeable. Yarn C is the same as yarn A except
for being deep acid dyeable and with the addition of 20 denier 3 filament yarn having
conductive carbon in the core for antistatic purposes as disclosed in U.S. Patent
3.803.453. Yarn D is 1750 denier nylon 6.31 denier per filament bulked continuous
filament yarn, each filament having a 6 void pentagon cross section. The jet entangling
process is in accordance with disclosures of the patents cited in Table 1.
[0042] Steam treatment device G consists of inlet 28 having a passage 30 eight inches (20.3
cm.) long and 0.070 inch (0.178 cm.) inside diameter, chamber 32 1.00 inch (2.54 cm.)
long of 0.062 inch (0.157 cm.) inside diameter and orifice 34 of 0.046 inch (0.117
cm.) diameter. and outlet 38 having a passage 36 twelve inches (30.5 cm.) long and
0.070 inch (0.178 cm.) inside diameter.
[0043] Steam treatment device H is similar to G except that the inside diameters of passage
30 and passage 36 are 0.052 inch (0.132 cm.). Steam temperature in pipe 20 is measured
by a thermocouple inserted into pipe 20 approximately 3 inches (7.6 cm.) upstream
of orifice 34. Steam temperature in chamber 32 is measured by a thermocouple inserted
in the wall of chamber 32 of device G flush with the inside bore of the chamber and
opposite to orifice 34.
[0044] Properties of the yarns are shown in Table 1. Item 2 which is not steam treated,
shows low bending rigidity ratio characteristic of untreated yarns and no filament
skin modification. Items 5. 6. 10 and 11 although steam treated. are below acceptable
levels of properties.
[0045] Item 12 has filament fusing within the limits of acceptability while Item 13 is more
heavily fused and many of the filaments cannot be separated. Items 10 through 13 are
nylon 6 which has a lower melting point than nylon 66.
[0046] The time during which the yarn is exposed to the steam is considered to be the total
time which the yarn spends within steam treatment device 18 of Fig. 1. This is determined
by dividing the overall length of the device from inlet 28 to outlet 38 by the yarn
velocity.
[0047] During the test no substantial amount of steam was observed escaping from the inlet.
Example 2
[0048] The yarns of Items 6 through 9 of Example 1 are tufted into carpet at 1/8 inch (3.18
mm) gauge and are tufted at a 5/16 (8 mm) inch cut-pile height. 32 oz./yd. (
1.
086 kg
/m
2) and are dyed under the same conditions. Item 6 shows some tuft distinction. Item
9 has tufts where the filaments appear cohesive with little intermingling of filaments
with adjacent tufts. yet the carpet is soft and springy without harshness. Items 7
and 8 are intermediate in tuft distinction.
Example 3
[0049] Three ends of cationic dyeable feed Yarn A are entangled and steam treated at the
conditions listed in Table 2. Feed yarn A is a copolymer of nylon 66 and the sodium
salt of sulfoisophthalic acid at about 2.2% by weight having a lower melting point
than yarns B and C, and therefore the filaments can be expected to bond to a greater
degree at similar conditions than Items 1. 2. 4 or 5-9 of Table 1. The yarns were
treated at a series of temperatures to demonstrate products ranging from insufficiently
to excessively bonded. This is a more extensive testing than Item 3.
[0050] It can be seen from the data in Table 2 that items 14-16 have bending rigidity ratios
below about 20 and have skin thickness and Skin Deorientation Index too low to measure
accurately.
Example 4
[0051] The yarns of Items 14 through 24 are tufted into carpet at 1/8 (3.18 mm) inch gauge
and 5/16 (8 mm) inch cut pile height. 32 oz/yd
2 (1.086 kg/m2) and are dyed under the same conditions. Items 14-16 have little cohesion
within the tufts, the filaments of each tuft spreading and intermingling with neighboring
tufts to give a uniform matted appearance. Items 17-22 have tufts where the yarns
appear cohesive with little intermingling of filaments with adjacent tufts, yet the
carpet is soft and springy without harshness. Items 23 and 24 are harsh and excessively
fused.
Example 5
[0052] This example demonstrates that the filaments are lightly bonded together. The yarn
was closely examined as described below.
[0053] To avoid disturbing the yarns' structures. yarns are embedded in an epoxy matrix
before cross-sectioning. To do this. the specimen yarn is placed in a mold. Epoxy
is poured around it and cured. The cured specimen block is removed from the mold.
shaped and sectioned in a microtome. Cross-sections, mounted on a microscope slide,
are photographed at suitable magnification.
[0054] The coated mold is sprayed lightly with release agent, and each cavity is lined with
cellophane tape. Small "pillovs" of double-faced masking tape (approximately 6 folds)
are placed at the ends of each cavity.
[0055] Before placing the yarn in the molds, the yarn is prepared as follows. Approximately
200 mm of yarn are taped at both ends using small pieces of masking tape. clamps are
attached to both ends.. and the yarn is hung on a rack hook. Sufficient weight is
added to the lower clamp to pull out any crimp, being careful not to stretch the yarn.
Using an eyedropper. clear acrylic lacquer is applied a few drops at a time down the
yarn. Approximately 10 applications about 3 minutes apart are made. then the sample
is allowed to dry about 2 hours.
[0056] The coated specimen is placed in the mold cavity on the "pillows" of tape such that
it lies below the mold surface but does not touch the bottom. The excess yarn is then
cut off.
[0057] Epoxy resin to fill -8 mold cavities is prepared by mixing the following:

The resin mixture is stirred slowly for about 5 minutes to prevent bubble formation.
Stirring should continue until the solution is clear.
[0058] The epoxy solution is then poured over each specimen. Bubbles can be eliminated by
manipulation of the specimen with a pair of forceps. If the sample sinks-to the bottom
or floats to the top of the mold. the yarn must be repositioned. The resin can be
cured at room temperature for 16 hours (or at 65°C for 3 hours).
[0059] After curing, the room temperature cured mold is placed on a warming table for about
15 minutes. By grasping the ends of the cellophane tape, the warm specimen block can
be removed from the mold. (Oven-cured specimens are removed from the mold immediately
after removal from the oven.) The specimen block is cooled on a flat surface and then
the cellophane tape is removed.
[0060] Each specimen block is shaped and then placed on a warming table for about 2 minutes
to relax filaments. The specimen block is then mounted in a Microtome (Rotary Model
820 - American Optical) and 7-micron thick cuts are made. The first few cuts are discarded.
A good cut (one with no obvious air bubbles or knife blade marks or tilt to the filaments)
is laid on a microscope slide thinly coated with Primol 335 (n - 1.5) or mineral oil
(n - 1.47). Once the cut has been inspected under the microscope and determined to
be satisfactory, a cover glass is placed over the specimen. Photographs are taken
at appropriate magnification.
[0061] After carpet processing (but before latexing) yarn from carpet tufts is cross-sectioned
as described by the above procedure with one exception. Because the yarn length is
so short (approximately 15 mm). it is not suspended and dropped with clear acrylic
lacquer. It is simply positioned in the center of the mold using the "pillows" of
tape to keep it from touching the top or the bottom of the mold.
[0062] Cross-sectional photographs of the yarns before and after carpet processing indicate
increasing fusion points with increasing steam temperature and the loss of fusion
points after carpet processing. Fusion is determined by examining the cross-sectional
photograph for loss of boundary definition between two touching filaments. This is
shown if Fig. 8 which is a cross-sectional photograph of Item 21 before processing.
Item 21 retains some fusion points after carpet processing and an increasing amount
of fusion points are retained as steam temperature is increased between Items 22 and
24.
Example 6
[0063] This example shows that above the temperature at which the light bonds are first
formed the amount and the strength of the bonds increases as the steam temperature
increases.
[0064] A length of yarn is held down on a block made from Teflon* tetrafluoroethylene resin.
A razor blade is held on the block at a 30° angle and drawn across the yarn twice
to cut a yarn segment approximately 5mm long. Care is taken not to disturb interfilament
bonds which may be present in the segment of yarn which is cut. The sample segment
should be cut from an area of the yarn which is of average visually apparent bundle
cohesion. It should not be cut from a section of yarn which is splayed or tightly
knotted. as in an "interlace node". A segment thus cut from a yarn having interfilament
bonds will remain substantially intact.
1. A substantially twist-free multifilament polyamide yarn, comprising a plurality
of crimped filaments having an oriented core portion and a deoriented skin portion,
said yarn being characterized by a bending rigidity ratio (R/Rcfm) of greater than about 20 and less than about 200, said filaments being characterized
by a Skin Deorientation Index of greater than about 0.05.
2. The yarn of Claim 1 characterized further by a thickness of the deoriented skin
portion of the filaments of greater than about 0.4 micrometer and less than about
4.0 micrometers.
3. The yarn of Claim 2 where the number of filaments is less than about 500 and the
denier per filament is greater than about 5 and less than about 40.
4. The yarn of Claim 1 where the Skin Deorientation Index is less than about 0.5.
5. The yarn of Claim 2 where R/Rcfm is greater than 20 and less than 75.
6. The yarn of Claim 5 characterized further by a lateral pull-apart distance greater
than about 0.25 cm. and less than about 10 cm.
7. The yarn of Claim 6 wherein the thickness of the deoriented skin portion of the
filaments is greater than 0.8 micrometers and less than 1.5 micrometers.
8. The yarn of Claim 1 where a portion of the filaments are lightly bonded together.
9. The yarn of Claim 1 where the multifilament polyamide yarn has a twist of from
about 0.33 to 2.0 twists per cm.
10. A process for treating a crimped multi-filament polyamide yarn bundle under tension
with saturated steam, said process comprising the steps of a) passing said yarn bundle
through a close-fitting inlet, b) then impinging the axis of the yarn bundle with
saturated steam supplied in a chamber for a time of greater than about 15 milliseconds
and less than about 150 milliseconds, said chamber being of sufficient size to allow
the filaments to spread and be treated individually by the steam, and c) passing the
filaments through a close fitting outlet.
11. The process of Claim 10 wherein the diameter of the outlet is greater than about
0.7 times the diameter of the inlet and less than about the 1.0 times the diameter
of the inlet.
12. The process of Claim 11 wherein the diameter of the Chamber is less than 1.5 times
the diameter of the inlet.
13. The process of Claim 12 wherein the ratio of outlet to inlet tension is greater
than about 1.1 to 1.
14. The process of Claim 13 wherein the saturated steam is substantially free of entrained
water.
15. The process of Claim 14 wherein the crimped multi-filament polyamide yarn is substantially
twist free.
16. The process of Claim 11 wherein the inside diameter of the inlet passage is small
enough so that no substantial amount of steam escapes from the upstream entrance.