U.S. patent number 3,771,307 [Application Number 05/174,430] was granted by the patent office on 1973-11-13 for drawing and bulking polyester yarns.
This patent grant is currently assigned to E.I. du Pont de Nemours and Company. Invention is credited to Dennis G. Petrille.
United States Patent |
3,771,307 |
Petrille |
November 13, 1973 |
DRAWING AND BULKING POLYESTER YARNS
Abstract
Textured polyester yarn is prepared from multifilament yarn by
drawing at a draw ratio of 1.3 to 2.0, and false-twist texturing at
temperatures above 200.degree.C. in a continuous process.
Preparation of the starting yarn by melt spinning at 3,000 to 3,500
yards per minute is illustrated.
Inventors: |
Petrille; Dennis G.
(Naperville, IL) |
Assignee: |
E.I. du Pont de Nemours and
Company (Wilmington, DE)
|
Family
ID: |
22636121 |
Appl.
No.: |
05/174,430 |
Filed: |
August 24, 1971 |
Current U.S.
Class: |
57/288; 264/168;
264/288.8; 264/290.5 |
Current CPC
Class: |
D02G
1/0286 (20130101); D02G 1/026 (20130101) |
Current International
Class: |
D02G
1/02 (20060101); D02g 001/02 () |
Field of
Search: |
;57/34HS,157TS,14R |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Petrakes; John
Claims
I claim:
1. In a draw-texturing process for producing textured yarn from
feed yarn composed of synthetic linear ethylene terephthalate
polyester filaments, wherein the feed yarn is drawn as it passes
continuously to a false-twisting device and a heater is used for
setting twist backed up in the yarn by the false-twisting device;
the improvement for providing higher crimp development without
damage to filaments when using heater temperatures above
200.degree. C., wherein the improvement comprises draw-texturing at
1.3X to 2.0X draw ratio a feed yarn prepared by melt-spinning the
polyester at a windup speed of about 3,000 to 4,000 yards per
minute to have a structural integrity value (.epsilon..sub.0.2) of
0.3 to 1.0, a boil-off shrinkage of 40 percent to 60 percent and
less than 30 percent crystallinity.
2. The process defined in claim 1 wherein feed yarn having a
structural integrity value of about 0.5 to 0.6 is draw-textured at
a draw ratio of about 1.5X to 1.7X and a heater temperature above
215.degree. C.
Description
BACKGROUND OF THE INVENTION
This invention relates to production of false-twist textured yarn
from multifilament yarns of synthetic linear ethylene terephthalate
polyester; it is more particularly concerned with improvements in
the false-twist texturing process and feed yarn supplied for
texturing.
Conventional production of synthetic linear ethylene terephthalate
yarn for textile use involves melt-spinning the polyester into
filaments, cooling the filaments and drawing the filaments to
impart desired mechanical properties. To produce bulk and tactility
a crimping step is usually added. Crimp is provided in a variety of
ways depending on the use of the yarn. A particularly popular
method for continuous filament yarns is to twist the yarn, heat-set
the twisted configuration in the yarn, and then untwist the yarn,
using, for example, a false-twist spindle to twist and untwist the
yarn. The strains set in the yarn filaments cause the filaments to
curl when relaxed.
In a typical false-twist texturing process, yarn is passed
continuously from feed rolls over a hot plate to a rotating
false-twist spindle and is forwarded by take-off rolls at a rate
which maintains tension between the feed and take-off rolls. The
spindle is rotated at high speed to twist the yarn at least 40
turns per inch (1,575 turns/m.) [60 to 100 turns per inch (2,362 to
3,940 turns/m.) are generally used for yarns of 70 to 150 denier].
Since a spindle speed of at least 216,000 revolutions per minute is
required to provide a twist of 60 tpi. (2,362 turns/m.) when using
a feed rate of 100 yards per minute (91.4 meters/min.), relatively
low yarn feed rates are necessary because of practical limitation
in spindle speeds.
The speed at which filaments can be melt-spun is limited only by
the rates at which the molten polymer can be pumped through the
spinneret assembly and the extruded filaments wound up. Although
windup speeds of up to 4,500 yards per minute (4,115 meters/min.)
are feasible, spinning speeds much higher than 1,000 ypm. (914.4
meters/min.) have been considered uneconomical because of the
increasing cost of equipment required for greater speeds.
In conventional processes, textile yarn is drawn about 3.5X to 4X
between feed and draw rolls driven at different speeds. This can be
done at high speed, and drawing can be coupled with melt-spinning
to provide drawn yarn in a continuous operation. However, the
greatly increased yarn windup speed required in a coupled spin-draw
process is a limitation on the spinning speed which can be
used.
It is economically desirable to combine the drawing with
false-twist texturing in a continuous process. However, previous
attempts to do so have not been successful when starting with
undrawn polyester yarn. The filaments produced in the melt-spinning
operation are substantially amorphous, and previously available
undrawn filaments having low molecular orientation are overheated
and break during stringup when subjected to conditions used in
modern false-twist texturing processes. Attempts to use lower
heater temperatures to avoid damaging the filaments have resulted
in products having poor crimp development. Separating the draw zone
from the texturing zone has not provided a solution to the stringup
problem. The products have still been inferior as to crimp
development and dyeing uniformity. Furthermore, ageing of the
undrawn yarn in storage and shipping has caused further decreases
in product quality.
SUMMARY OF THE INVENTION
The present invention provides an improved draw-texture process
wherein polyester yarn is drawn and false-twist textured at
temperatures high enough for outstandingly good crimp development.
The invention also provides feed yarn suitable for use in the
process.
The invention provides an improvement in the continuous process for
preparing false-twist textured yarn from multifilament yarn
composed of synthetic linear ethylene terephthalate polyester by
feeding the yarn to a false-twisting device and setting twist
backed up in the yarn with a heater having a temperature above
200.degree. C. The improvement in the process comprises
continuously drawing immediately prior to the false-twisting
device, a feed yarn characterized by (a) having a structural
integrity value (.epsilon..sub.0.2) of 0.3 to 1.0, (b) having a
voil-off shrinkage of 40 percent to 60 percent, and (c) being
composed of synthetic linear ethylene terephthalate polymer which
is less than 30 percent crystalline, the feed yarn being drawn
during the texturing process at a draw ratio of 1.3X to 2.0X.
The feed yarn preferably has a structural integrity value
(.epsilon..sub.0.2) of 0.4 to 0.9. A boil-off shrinkage of 53
percent to 58 percent is also preferred. The feed yarn can be
prepared in a substantially amorphous condition by a high speed
melt-spinning process, using windup speeds of 3,000 to 4,000 yards
per minute with controlled cooling of the filaments between
spinneret and windup.
The yarn is preferably twisted at least 7.34 .times. 10.sup.2
/.sqroot.D - 10 turns per inch in the improved process, where (D)
is the denier of the yarn before texturing, and this twist can be
heat-set with heater temperatures above 200.degree. C. to give a
crimp development (CD.sub.2.5) of at least 22-0.05 (D'), wherein D'
is the denier of the textured yarn. The feed yarn is quite stable
and can be stored in a warehouse for more than 60 days without
significant effect on the products of the process. The yarn draws
satisfactorily at ambient temperatures or at elevated temperatures
to give highly uniform products. No draw heater is required, even
when using a tandem draw-texturing arrangement wherein the drawing
operation is completed prior to the texturing machine heater. It is
surprising that adequate drawing is accomplished at the low draw
ratios of 1.3X to 2.0X. The examples illustrate that yarns having
structural integrity values of about 0.5- 0.6 can be drawn at draw
ratios of about 1.5X to 1.7X, false-twisted and heat-set with
heater temperatures above 215.degree. C. to give outstanding
products. Lower draw ratios can be used with lower values of
structural integrity.
BRIEF DESCRIPTION OF THE DRAWING
The single FIGURE of drawing is a diagrammatic representation of
the false-twisting process and suitable equipment.
DETAILED DESCRIPTION
In the drawing, polyester yarn 1 is fed continuously from package 2
by feed rolls 3 and 3', passes through texturing heater 4 and
false-twisting device 5, is pulled away by rolls 6 and 6', and is
wound up on package 7. The false-twisting device rotates at high
speed to insert "S" twist on one side and "Z" twist on the other.
The twist backs up to feed rolls 3 and 3' so that the yarn is
highly twisted as it passes through heater 4. The heat plasticizes
the polyester yarn and causes crystallization. Upon cooling, the
twisted configuration is locked in by the crystallized molecular
arrangement. The yarn untwists as it passes from the false-twisting
device to rolls 6 and 6'. Rolls 6 and 6' are driven at a higher
peripheral speed than the feed rolls 3 and 3' to provide a draw
ratio between 1.3X and 2.0X. Because the yarn is drawn in the twist
zone; i.e., between feed rolls 3 and 3' and rolls 6 and 6', the
latter set of rolls being preceded by the false-twist device 5,
this process is herein termed a "simultaneous" process. This
process can be carried out on commercially available false-twist
texturing machines by lowering the speed of rolls 3,3' and/or
increasing the speed of rolls 6,6' to provide the required draw
ratio. The machines used in the examples were modified by changing
gears to reduce the speed of rolls 3,3' relative to rolls 6,6'.
The yarn then passes to package 7, which is usually driven at a
somewhat slower peripheral speed than rolls 6 and 6' to provide a
package overfeed so that tension of the yarn will not be excessive
in the package. Another heating means may be used between the draw
rolls and the package to stabilize the textured yarn and decrease
its twist-liveliness. Illustrations of such later heating steps are
given in U.S. Pats. No. 3,131,528 and No. 3,316,705.
Optional rolls 8 and 8' are indicated in dotted lines between feed
rolls 3,3' and texturing heater 4. These rolls are used when it is
desired to separate a drawing zone from the twisting zone. Rolls 8
and 8' can be used as draw rolls when lower tensions are desirable
in the twist-texturing operation. A process wherein rolls 8,8' are
rotated at a higher peripheral speed than rolls 3,3' to draw the
yarn immediately prior to the twisting zone is herein termed a
tandem process. The relative speeds of rolls 3,3', rolls 8,8' and
rolls 6,6' can be adjusted to provide a process which combines
tandem and simultaneous drawing. If desired, a heater can be
inserted in the draw zone between rolls 3,3' and rolls 8,8', but no
draw heater is required for tandem drawing.
METHODS OF EVALUATION
Relative Viscosity of the terephthalate polyester is a measure of
its molecular weight. It is measured by either of the following two
methods reported herein; (a) RV is the ratio of the viscosity of a
solution of 2.15 gm. of polymer dissolved at 140.degree. C. in 20
ml. of fomal to the viscosity of the fomal itself, both measured at
25.degree. C. in a capillary viscometer and expressed in the same
units. Fomal is a mixture of 10 parts by weight of phenol and 7
parts by weight of 2,4,6-trichlorophenol, (b) HRV is the ratio of
the viscosity of a solution of 0.8 gm. of polymer dissolved at room
temperature in 10 ml. of hexafluoroisopropanol to the viscosity of
the hexafluoroisopropanol itself, both measured at 25.degree. C. in
a capillary viscometer and expressed in the same units.
Crimp Development (CD) of textured yarns is a measure of their
crimp characteristics and is determined in the following manner: A
skein of yarn is wound on a denier reel the number of times
required to achieve a denier (in the looped skein) of 5,000 using
the formula:
n = 2,500/D
wherein n is the number of turns and D is the denier of the yarn. A
500 gm. weight is hung from the skein and the length of the skein
measured (L.sub.b). The 500 gm. weight is then replaced by a
suitable weight and the weighted skein is placed in a hot-air oven
for 5 minutes at 120.degree. C. The suitable weight may be 2.5 gm.
which would produce a load of 0.5 mg./denier, or some other desired
weight. In the examples which follow, loads of 0.5, 1.5, 2.5 and
5.0 mg./denier are used. The skein is removed and allowed to cool
with the weights still suspended therefrom. This length is measured
and recorded as L.sub.c. The weight is removed and the skein is
again loaded with 500 gm. (0.1 gm./denier) to remove the crimp and
the skein length is read after 15 seconds. This length is recorded
as L.sub.e. Crimp development is calculated by the following
formula:
CD.sub.w (%) = L.sub.e - L.sub.c /L.sub.e .times. 100
wherein w is the skein loading in mg./denier, during the
measurement of L.sub.c. All crimp development values expressed
herein are percentage values calculated by the above formula, %""T"
sign bein understood.
Skein Shrinkage is the decrease in length of a sample yarn under a
specified load caused by a specific heat treatment expressed as a
percentage of the length of the untreated sample. The same method
is used as described for CD. Calculations are as follows:
Skein shrinkage (%) = (L.sub.b - L.sub.e)/L.sub.b .times. 100
Boil-Off Shrinkage is obtained by suspending a weight from a length
of yarn to produce a 0.1 gm./denier load on the yarn and measuring
its length (L.sub.o). The weight is then removed and the yarn is
immersed in boiling water for 30 minutes. The yarn is then removed,
loaded again with the same weight, and it new length recorded
(L.sub.f). The percent shrinkage is calculated by using the
formula:
Shrinkage (%) = L.sub.o - L.sub.f /L.sub.o .times. 100
Structural Integrity Parameter (.epsilon..sub.0.2) is measured by
suspending a weight from a length of yarn to produce a 0.2
gm./denier load on the yarn and measuring its length (L.sub.o). The
yarn, bearing this load, is then immersed into 100.degree. C. water
for 2 minutes, then carefully removed and allowed to cool while
still under the load. The length is measured again (L.sub.f). The
following formula is used to calculate .epsilon..sub.0.2 :
.epsilon..sub.0.2 = L.sub.f - L.sub.o /L.sub.o
Conventional drawn yarns have a negative .epsilon..sub.0.2.
The heating means of a conventional false-twist texturing machine
is operated at a temperature of about 227.degree. C. As shown in
the examples, it is difficult and frequently impossible to string
up, under normal operating conditions, conventional as-spun
polyethylene terephthalate yarns having an .epsilon..sub.0.2
greater than 1.0.
The examples illustrate preparation of the feed yarns of the
present invention by melt-spinning at high spinning speeds, with
windup speeds of about 3,000 to 3,500 yards per minute (2,743 to
3,200 meters per minute). Higher windup speeds can be used.
Somewhat lower speeds can be used when the filaments in the
draw-textured product are to be less than about 4 dpf. Conventional
spinning conditions are suitable up to the point where the molten
polyester leaves the spinneret in the form of filaments. The
filaments are cooled as they are pulled away from the spinneret at
a speed which causes them to become greatly attenuated before
reaching the pulling means. The cooled filaments may be forwarded
to the windup by high speed pulling rolls or the like at
substantially the same speed as the filaments are wound up, i.e.,
the process does not require a conventional drawing step. The
cooled filaments may be interlaced as described in Bunting et al.
U.S. Pat. No. 2,985,995 before the windup or at any time prior to
texturing. The cooling conditions are preferably controlled to
provide an .epsilon..sub.0.2 value of 0.4 to 0.9. In the examples,
the cooling medium is room temperature air, free circulation of the
air takes place with the motion of the filaments, and the filaments
travel a distance of about 20 feet (6.1 meters) in the cooling
medium. The filaments can be cooled more quickly with a forced flow
of gas, e.g., 70.degree. F. air. Effective temperature and flow
conditions for the cooling medium selected, distance of travel in
the cooling medium, and filament speed (within the indicated range
of windup speeds), for producing suitable feed yarn, can readily be
determined by simply varying controllable conditions and measuring
the .epsilon..sub.0.2 values obtained.
The feed yarns of the present invention are molecularly oriented
and are not fully crystalline. Orientation and crystallinity can be
measured by conventional techniques.
It is highly surprising to find that as-spun yarn can be prepared
which is suitable for draw-texturing, under conventional conditions
with standard machines modified for drawing the yarn, to produce
textured yarn with improved crimp development and other properties
as compared with commercial textured yarn. The yarn has a low
degree of crystallinity which facilitates formation of the desired
crystalline structure when it is heat set. The yarn differs from
conventional undrawn yarn in having an .epsilon..sub.0.2 value of
less than 1.0.
The unusual feed yarns of this invention not only are easy to
texture in conventional high-speed operations but the final
textured yarns are found, unexpectedly, to possess higher crimp
development than conventional false-twist textured yarns processed
under similar conditions. Surprisingly, the lower the
.epsilon..sub.0.2 values of the starting yarn within reasonable
limits, the higher the crimp development of the final yarns
textured under similar conditions by either the tandem or the
simultaneous process. Higher throughput in the texturing operation
and improved dye uniformity are other advantages of yarns produced
according to this invention.
A further advantage of the new feed yarn is its stability in
storage compared to similar amorphous yarn having an
.epsilon..sub.0.2 of greater than 1. It has now been found that
polyester feed yarn of the present invention can be stored prior to
texturing for more than 60 days with no significant deterioration
of draw-texturing performance taking place whereas similar
amorphous yarn having an .epsilon..sub.0.2 of greater than 1
develops significant deterioration of draw-texturing performance
during the same period making it unsuitable for drawing and
texturing.
In the draw-texturing operation the minimum twist that should be
given to the yarn increases with decreasing yarn denier. The
draw-texturing machine is adjusted to produce a twist in the yarn,
in turns per inch, which is numerically equal to or greater than
7.34 .times. 10.sup.2 /.sqroot.D - 10 wherein D is the denier of
the yarn before texturing.
The textured yarns produced by the new process have a crimp
development under a load of 2.5 mg. per denier which is numerically
equal to or greater than 22-0.05 (D') wherein D' is the denier of
the textured yarn. Thus a 70-denier yarn would have a crimp
development (CD.sub.2.5) greater than 18.5 and a 400-denier yarn
would have a crimp development (CD.sub.2.5) greater than 2.
As in conventional false-twist texturing, a lubricating finish
should be applied to the feed yarn to facilitate the draw-texturing
operation.
The yarn polyester may contain minor amounts of the usual
delustrants, particulate matter, antistats, optical brighteners,
antioxidants and copolyester components, provided that the modified
yarn satisfies the requirements specified for the process
invention. In the examples which follow, the yarns contain one or
more of these agents.
The invention is further illustrated by the following examples,
which are not intended to be limitative.
EXAMPLE I
Polyethylene terephthalate of 27 RV is spun at 294.degree. C. using
a spinneret containing 34 round orifices of 15-mil (0.38 mm.)
diameter. The freshly spun filaments travel in air approximately 20
feet (6.1 meters) before they are wound-up at 2,000 yards per
minute (1,829 meters/minute) as 395-denier yarn. This first yarn
has an .epsilon..sub.0.2 of 1.53, a shrinkage (%) of 61, is
moderately oriented and substantially amorphous.
A second yarn is produced in similar fashion with the exception
that the second yarn is wound-up at 3,500 yards per minute (3,200
meters/minute) as 255-denier yarn. The second yarn is undrawn,
highly oriented, substantially amorphous, has an .epsilon..sub.0.2
of 0.5, and a shrinkage (%) of 54.
The second yarn is textured by the simultaneous process on a
commercial texturing machine of the type described previously. The
heater plate is at the conventional temperature of 227.degree. C.
Spindle speed of the false-twist means is 210,000 rpm to produce in
the yarn 60 turns per inch (2,362 turns/meter) in the twist zone.
Draw ratio and crimp development values for this yarn are shown in
Table 1. The first yarn could not be textured at the machine
settings shown because it melted on contact with the heater.
A commercially available, semi-dull, drawn polyethylene
terephthalate yarn having a denier of 150 and containing 34
filaments is textured in the manner shown for the second yarn. The
draw ratio (in texturing) and crimp development values for this
commercial yarn are shown in Table 1.
TABLE 1
Yarn Draw Ratio CD.sub.0.5 CD.sub.1.5 CD.sub.2.5 CD.sub.5.0 Second
yarn 1.67 55 38 26 11 Commercial 0.98 69 46 25 9
EXAMPLE II
Polyethylene terephthalate of 26 RV is spun at 290.degree. C. using
a spinneret containing 34, 15-mil (0.38-mm.) diameter, round
orifices. The freshly spun filaments travel in air approximately 20
feet (6.1 meters) before they are wound-up at 3,430 yards per
minute (3,136 meters/minute). The .epsilon..sub.0.2 of this test
yarn is approximately 0.56 and the denier is 255. The yarn is
undrawn, highly oriented, and substantially amorphous.
As a control, the same type polymer is spun at 803 yards per minute
(734 meters/minute) as a 34-filament yarn, forwarded to feed rolls,
then to an aqueous draw bath at 95.degree. C. and then to enclosed
heated draw rolls maintained at 128.degree. C. and rotating at
3,000 yards per minute (2,743 meters/min.) to produce a draw ratio
of 3.73. The filaments are then forwarded directly to a windup and
the total denier of the yarn is 150.
Both yarns are textured by the simultaneous process on the same
type machine as used in Example I using a spindle speed of 210,000
rpm, to produce 60 turns per inch (2362 turns/meter) twist in the
twist zone, 227.degree. C. hot-plate temperature, and 12 percent
top overfeed. Top overfeed is the relationship between the draw
roll peripheral speed and the speed of the yarn as it is wound on
the final package. By regulating top overfeed, the "tightness" of
the yarn on the package is regulated in conventional fashion. Draw
ratio (in the texturing process) and crimp development values of
these yarns are shown in Table 2.
TABLE 2
Draw Ratio in Yarn Texturing CD.sub.0.5 CD.sub.1.5 CD.sub.2.5
CD.sub.5.0 CD.sub.10.0 Test 1.64 71.0 50.0 36.0 11.0 3.8 Control
drawn 72.0 50.0 30.0 8.0 2.8 previously
From these results, it can be seen that the yarn drawn and textured
simultaneously compares favorably to conventional textured yarn and
even shows superior crimp properties under relatively high
restraints such as would be encountered in fabric structures.
EXAMPLE III
This example shows the criticality of the .epsilon..sub.0.2
parameter.
Example I is repeated with the following exceptions: 3 yarns are
made, each yarn consisting of 34 filaments. Yarn 1 is wound-up at
2,800 yards per minute (2,560 meters/minute) and has an
.epsilon..sub.0.2 of about 1.05; yarn 2 is wound-up at 3,000 yards
per minute (2,743 meters/minute) and has an .epsilon..sub.0.2 of
about 0.85; yarn 3 is wound up at 3,500 yards per minute (3,200
meters/minute) and has an .epsilon..sub.0.2 of about 0.6.
The texturing machine for each yarn is a Leesona No. 555, similar
to the machine of the preceding examples and the simultaneous
process is used. The spindle speed is 210,000 revolutions per
minute to produce 58 turns-per-inch (2,283 turns/meter) twist in
the yarn in the twist zone, the temperature of the heater plate is
set at 227.degree. C., and the top overfeed is 12 percent. Table 3
shows the as-spun denier, draw ratio in the texturing process, and
crimp development values of the yarns. ##SPC1##
Yarn 1 (.epsilon..sub.0.2 about 1.05) could not be strung up in
spite of intense effort on the part of two experienced operators
because it melted.
EXAMPLE IV
(a) Polyethylene terephthalate is melt-spun at 290.degree. C. using
a spinneret containing 34 round orifices of 15-mil (0.38 mm.)
diameter. The freshly spun filaments travel in air approximately 20
feet (6.1 meters) before they are wound up at 3,430 yards/min.
(3,136 meters/min.) as 248-denier yarn of 20.3 HRV. The yarn has an
.epsilon..sub.0.2 of about 0.55, a shrinkage of 57 percent and is
undrawn, highly oriented and substantially amorphous.
The yarn is textured by the tandem process on a Leesona 553 to
which a draw zone was attached immediately before the bottom feed
roll. The heater plate is at the conventional temperature of
227.degree. C.
Spindle speed is 210,000 rpm to produce in the yarn 60 turns per
inch (2,362 turns per meter) in the twist zone. The speed of the
feed rollers (similar to rolls 8 and 8' of the drawing) is set to
provide an overfeed of about 1 percent and the yarn is overfed to
the take-up package approximately 12 percent. In the draw zone the
yarn is drawn 1.64X while passing in the vicinity of a heater set
at 100.degree. C.
Item "a" in Table 4 shows spindle tensions during texturing and
final properties of this textured yarn.
(b) The process for producing Item "a" is repeated with the
exception that the spinning temperature is 285.degree. C. instead
of 290.degree. C., feed yarn is 110 denier instead of 248 denier,
the spindle speed is 240,000 rpm to produce in the yarn 72 turns
per inch (2,834 turns/meter) in the twist zone and the yarn is
overfed to the take-up package at 8 percent instead of 12 percent.
In the draw zone the yarn is drawn 1.53X. Item "b" in Table 4 shows
process conditions and final properties of this textured yarn.
(c) The process for producing Item "b" is repeated with the
exception that no heater is used in the draw zone. Item "c" in
Table 4 describes this yarn. Surprisingly, the properties of the
final textured yarn compare very favorably to Item "b" above which
employed a heater in the drawing step; whereas yarns having an
.epsilon..sub.0.2 of more than 1.0, if at all operable, are
nonuniform when drawn in the tandem process with no heater in the
draw zone.
(d) A commercially available, semi-dull, drawn polyethylene
terephthalate yarn having a denier of 70 and containing 34
filaments is textured in the same manner as for Item (b) with the
exception that the yarn is not drawn as illustrated but it is
processed according to customary conditions. Item "d" of Table 4
shows process conditions and final properties of this yarn. It is
easily seen that this yarn is inferior in crimp development to the
yarns of the present invention. Crimp development measured at loads
of 2.5 mg./denier or higher is especially indicative of the
performance of a yarn in a fabric.
EXAMPLE V
This example shows the surprising effect of .epsilon..sub.0.2 on
the crimp development of yarns processed according to this
invention.
Example IV is repeated for Item "b" with the exception that the
spinning temperature is 280.degree. C. instead of 285.degree. C.,
the HRV of the undrawn feed yarn is about 22 (except for item (d),
the HRV of which is 20), the spinning speeds and .epsilon..sub.0.2
values are as listed in Table 4, and the draw ratios, adjusted for
best physical properties, are 2.5X, 1.9X, 1.67X and 1.53X for items
"a" to "d," respectively. Spindle speed is 240,000 rpm and twist in
the twist zone is 72 turns/inch (2,834 turns/m.). In order to
draw-texture the feed yarns which are spun at 1,700 and 2,500
yards/minute (1,554 to 2,286 meters/min.) it is necessary to hold
them away from the texturing-machine heater during stringup and
during initial operation, a procedure causing undesirable effort
and waste product. Final properties and texturing process
conditions are shown in Table 4. Items a - c have crimp frequencies
of 35, 30 and 34 crimps/inch (about 13.8, 11.8 and 13.4
crimps/cm.), respectively. Crimp frequency is measured by
tensioning the fiber just enough to straighten it out and marking a
1-inch interval along the fiber while it is so tensioned. The fiber
is then relaxed and the number of crimps (peaks on one side of a
plane running along the helical axis of the fiber) is counted and
the number recorded as "crimp frequency."
The higher crimp development at the middle load of 2.5 grams per
denier which is an important number in predicting performance of
the yarn in a fabric, is readily apparent in the yarns which are
processed according to this invention as compared to yarns
processed otherwise.
This example is repeated with the same feed yarns. However, this
time the tandem process is not used but the yarn is drawn at the
twisting stage (simultaneous process) as in Example I. Again, it is
necessary to hold the feed yarns which are spun at 1,700 and 2,500
yards/minute (1,554 to 2,286 meters/min.) away from the
texturing-machine heater during stringup and initial operation.
Draw ratios for these items (e - h) of Table 4 are as follows:
2.5X, 1.9X, 1.67X, 1.53X, respectively. Process conditions and
final yarn properties are shown in Table 4. Overfeed to the take-up
package is approximately 8 percent for items e - h. Again, a rise
in crimp development at middle loads is seen for the yarns of the
present invention. ##SPC2##
EXAMPLE VI
Polyethylene terephthalate is melt spun at 290.degree. C. using a
spinneret containing 34 round orifices of 20-mil (0.50 mm.)
diameter. The freshly spun filaments travel in air approximately 20
feet (6.1 meters) before they are wound up at 3,400 yards per
minute (3,109 meters per minute) as 258-denier yarn. This undrawn,
highly oriented, substantially amorphous yarn (Yarn A) contains
about 0.3 percent TiO.sub.2, has an HRV of about 21, and an
.epsilon..sub.0.2 of about 0.53.
A second yarn (Yarn B) is produced in the same manner with the
exception that it is wound up at 2,000 yards per minute (1,829
meters/min.) instead of at 3,400 yards per minute (3,109
meters/min.). The denier of the second yarn is 362 and its
.epsilon..sub.0.2 is 1.43. It is substantially amorphous.
Each yarn is separately textured by the simultaneous process on a
commercially available false-twist texturing machine (Leesona
555/570). For Yarn A the draw ratio is 1.65, the spindle speed is
270,000 rpm to produce in the yarn 60 turns per inch (2,362
turns/m.), the bottom heater is at 216.degree. C., and the top
heater is at 213.degree. C., the package overfeed is -4 percent and
the second-heater overfeed is 14.5 percent. As in the conventional
process, the second heater (top heater) is used to set the yarn.
For Yarn B, the same texturing conditions are used with the
exception that the draw ratio is 2.45. The first two entries in
Table 5 show the bulk characteristics of these yarns.
The example is repeated with the exception that each yarn is
separately textured by the tandem process instead of by the
simultaneous process, the draw ratio for Yarn A is 1.75, the draw
ratio for Yarn B is 2.4, a heater at a temperature of 150.degree.
C. is used in the draw zone for Yarn B, the spindle speed is
240,000 rpm instead of 270,000 rpm and the spindle produces a twist
of 55 turns per inch (2,165 turns/m.) in Yarn A instead of 60 turns
per inch (2,362 turns/m.). The third and fourth entries of Table 5
describe these yarns.
The fifth entry (Yarn C) is a commercial Dacron Type 56 yarn of the
same type but which had been fully drawn before being textured
according to standard commercial practice.
In each process Yarn B has to be held off the heater of the Leesona
machine during stringup. In the simultaneous process Yarn B has
frequent broken filaments. Surprisingly, Yarn A does not require
heat in the draw zone in the tandem process.
TABLE 5
Spinning Speed of Feed Texturing Yarn Yarn .epsilon..sub.0.2
Process CD.sub.0.5 CD.sub.2.5 CD.sub.5.0 A 3400 0.53 Simultaneous
17.5 9.4 5.5 B 2000 1.43 Simultaneous 14.4 7.7 4.8 A 3400 0.53
Tandem 19.7 10.4 5.9 B 2000 1.43 Tandem 19.6 8.6 4.3 C Commercial
15.3 8.1 4.8
* * * * *