U.S. patent application number 10/859119 was filed with the patent office on 2004-11-04 for morphologically stable bulked continuous filaments and methods and systems for making the same.
This patent application is currently assigned to Honeywell International Inc.. Invention is credited to Ilg, Otto M., Sferrazza, Randall A..
Application Number | 20040219243 10/859119 |
Document ID | / |
Family ID | 25528355 |
Filed Date | 2004-11-04 |
United States Patent
Application |
20040219243 |
Kind Code |
A1 |
Ilg, Otto M. ; et
al. |
November 4, 2004 |
Morphologically stable bulked continuous filaments and methods and
systems for making the same
Abstract
BCF yarn is melt-spun, drawn and textured to provide
morphologically stable BCF yarns. The yarn texturizing includes a
relatively low efficiency fluid jet texturizer, that is a fluid jet
texturizer operating at a sufficiently low fluid jet velocity and a
sufficiently high fluid jet temperature to obtain a yarn skein
shrinkage of less than about 0.50 inch, more preferably about 0.25
inch or less. Most preferably, the BCF yarns are formed of nylon-6
and exhibit an alpha-crystalline content of less than about 45%,
and usually between about 45% to about 55%.
Inventors: |
Ilg, Otto M.; (Asheville,
NC) ; Sferrazza, Randall A.; (Farmington,
MI) |
Correspondence
Address: |
NIXON & VANDERHYE, PC
1100 N GLEBE ROAD
8TH FLOOR
ARLINGTON
VA
22201-4714
US
|
Assignee: |
Honeywell International
Inc.
Colonial Heights
VA
|
Family ID: |
25528355 |
Appl. No.: |
10/859119 |
Filed: |
June 3, 2004 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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10859119 |
Jun 3, 2004 |
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09981432 |
Oct 18, 2001 |
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6776943 |
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Current U.S.
Class: |
425/66 ;
425/382.2 |
Current CPC
Class: |
Y10T 428/2913 20150115;
D01D 5/082 20130101; D02G 1/161 20130101; D02G 1/20 20130101; Y10T
428/2969 20150115 |
Class at
Publication: |
425/066 ;
425/382.2 |
International
Class: |
D01D 005/08 |
Claims
1-13. (Canceled)
14. A system for making yarns of bulked continuous filaments
comprising: a spinning head for melt-spinning a polymeric material
to form multiple filaments thereof; a draw zone downstream of said
spin head for drawing the melt-spun filaments; and a texturing unit
downstream of the draw zone for texturing the melt-spun, drawn
filaments; wherein the texturing unit includes a fluid jet
texturizer operable at a sufficiently low fluid jet velocity and a
sufficiently high fluid jet temperature to obtain a yarn skein
shrinkage of less than about 0.50 inch.
15. The system of claim 14, further comprising a finish applicator
downstream of said spinning head to apply a liquid finish to the
filaments.
16. The system of claim 14, further comprising a winder downstream
of said texturing unit to wind the BCF yarn into a yarn
package.
17. The system of claim 14, wherein said texturizing unit imparts
an alpha-crystalline content in the BCF of at least about 45%.
18. A system for making yarns of bulked continuous filaments
comprising: a spinning head for melt-spinning a polymeric material
to form multiple filaments thereof; a draw zone downstream of said
spin head for drawing the melt-spun filaments; and a texturing unit
downstream of the draw zone for texturing the melt-spun, drawn
filaments; wherein the texturing unit including fluid jet
texturizer means operable at a sufficiently low fluid jet velocity
and a sufficiently high fluid jet temperature for imparting
alpha-crystalline content in the BCF of at least about 45% and a
yarn skein shrinkage of less than about 0.50 inch.
19. The system of claim 18, further comprising a finish applicator
downstream of said spinning head to apply a liquid finish to the
filaments.
20. The system of claim 18, further comprising a winder downstream
of said texturing unit to wind the BCF yarn into a yarn package.
Description
FIELD OF THE INVENTION
[0001] The present invention relates generally to synthetic
filaments and to their processes and systems for manufacture. More
specifically, the present invention relates to processes and
systems for making melt-spun, synthetic polymeric yarns of bulked
continuous filaments (BCF), especially carpet yarns comprised of
nylon BCF.
BACKGROUND AND SUMMARY OF THE INVENTION
[0002] I. Definitions
[0003] As used herein, certain terms have the following
meanings:
[0004] "Filament" or "filaments" mean fibrous strands of extreme or
indefinite length. In contrast, "staple fibers" mean fibrous
strands of definite and short lengths.
[0005] "Yarn" means a collection of numerous filaments which may or
may not be entangled, twisted or laid together.
[0006] "One-step" means a process for making yarn whereby no
intermediate winding of the yarn occurs between the spinning,
drawing and texturing processes.
[0007] "Texturing" means any operation on filaments which results
in crimping, looping or otherwise modifying such filaments to
increase cover, resilience, bulk or to provide a different surface
texture or hand. A "bulked continuous filament" is therefore a
"filament" which has been subjected to one or more "texturing"
operation(s).
[0008] "Morphologically stable" means a bulked continuous filament
such that yarns of such filaments exhibit a skein shrinkage of less
than 0.50 inch, and more preferably about 0.25 inch or less.
[0009] II. Background of the Invention
[0010] One-step processes for manufacturing melt-spun polymeric
yarns of bulked continuous filaments (BCF) are known as evidenced
by the following U.S. Pat. Nos.: 5,804,115; 5,487,865; 4,096,226;
4,522,774; and 3,781,949 (the entire content of each cited U.S.
Patent being incorporated expressly hereinto by reference). In
general, such processes involve the continuous sequential
operations (i.e., without any intermediate winding of the yarn) of
spinning, drawing and texturing. The resulting BCF yarn is
thereafter wound on a package either sold as is or subjected to
further processing (e.g., coloration, entangling with other yarns,
fabric formation, and the like).
[0011] Conventional one-step BCF yarn production techniques
typically involve the melt-spinning of multiple polymeric filament
streams which, when cooled form the precursor (or undrawn)
filaments of the later BCF yarn. These undrawn filaments are then
typically immediately directed to separated pairs of godet rolls
(sometimes referred to as "duos" in art parlance) operating at
different rotational speeds. The BCF yarn will therefore be drawn
between such duos at a desired draw ratio dependent on the duo
speed differential, yarn temperature, yarn speed and the like. The
duos are typically heated to the same temperature in order to
elevate the filament temperature prior to texturing.
[0012] The thus drawn and heated yarn is then subjected to a
texturing operation, usually accomplished by feeding the drawn
continuous filament yarn into a fluid jet texturing unit at a rate
faster than the rate at which the textured yarn is drawn off and
subjecting the yarn in the unit to a turbulent region of a fluid
jet, usually at elevated temperature (e.g., a so-called fluid jet
texturing method). The resulting textured continuous filament yarn
exhibits increased bulk as compared to the non-textured yarn being
fed into the texturing unit to achieve the BCF yarn which may then
be wound up to form a yarn package.
[0013] Recently, in copending and commonly owned U.S. patent
application Ser. No. 09/599,458 filed on Jun. 22, 2000 (the entire
content of which is expressly incorporated hereinto by reference),
there are disclosed methods and systems for making melt-spun, drawn
and textured BCF yarns, wherein prior to texturing the yarn is
subjected to differential temperature condition. Most preferably,
such differential temperature condition is accomplished using the
duo rolls employed in drawing the BCF, such that one of the rolls
is maintained at a greater temperature as compared to the other of
the rolls. The morphology of the BCF yarn can thus be variably
controlled.
[0014] III. Summary of the Invention
[0015] Broadly, the present invention is embodied in
morphologically stable BCF yarns, and the methods and systems for
making such BCF yarns. More specifically, according to the present
invention, the BCF yarn is melt-spun, drawn and textured, wherein
the yarn texturizing includes operating a fluid jet texturizer at a
sufficiently low fluid jet velocity and a sufficiently high fluid
jet temperature to obtain a yarn skein shrinkage of less than about
0.50 inch, more preferably less than about 0.25 inch. Especially
preferred embodiments of the present invention include filaments
formed of nylon-6 having an alpha-crystalline content of at least
about 45%, more preferably between about 45% to about 55%.
[0016] These and other aspects and advantages will become more
apparent after careful consideration is given to the following
detailed description of the preferred exemplary embodiments
thereof.
BRIEF DESCRIPTION OF THE ACCOMPANYING DRAWING
[0017] Reference will hereinafter be made to the drawing FIG. 1
which schematically represents a preferred system in accordance
with the present invention.
DETAILED DESCRIPTION OF THE INVENTION
[0018] Accompanying FIG. 1 schematically represents a particularly
preferred system 10 in accordance with the present invention. In
this regard, a conventional extruder 12 supplies molten polymeric
material via line 12-1 to a spinning head 14. The spinning head 14
includes spinnereftes (not shown) having multiple small orifices
through with the molten polymer material is extruded to form
streams 14-1, 14-2, 14-3 and 14-4 which are cooled and solidified
in the quench chamber 16 to form corresponding multi-filament
yarns. The now solidified yarns 14-1 through 14-4 may brought into
contact with a finish applicator 18-1, 18-2, 18-3 and 18-4,
respectively, whereby a liquid finish is applied onto the surface
of the yarns as may be desired.
[0019] It should be noted here that four yarns are shown only for
the purpose of illustration. Thus, more or less yarns may be spun
as desired for the finished yarn product.
[0020] The yarns 14-1 through 14-4 are then guided by guides 20-1,
20-2, 20-3 and 20-4 to a pretensioner godet 22. The pretensioner
godet 22 serves to prevent slippage of the filaments on the draw
rolls and stabilized filament movement. The pretensioned yarns are
then drawn in a draw zone 24 between separated pairs of duos 26-1,
26-2 and 28-1, 28-2, respectively. The tensioned yarns (now
collectively identified by TY in FIG. 1) may then be separately or
collectively subjected to texturing by a conventional texturing
unit 30. Most preferably, texturing unit 30 is a fluid jet
texturizer wherein a fluid jet at elevated temperature is brought
into contact with the drawn yarns to texturize the same. The
textured BCF yarns (identified by BCF in FIG. 1) are then wound
into a yarn package via winder 32.
[0021] In accordance with the present invention, fluid jet
texturizer of the texturing unit 30 exhibits relatively low
efficiency. That is, the orifice size of the fluid jet texturizer
is provided with a relatively larger size fluid jet orifice (i.e.,
as compared to higher efficiency texturizers) so as to operate at a
relatively lower fluid jet velocity. Operating at such a lower
fluid jet velocity, however, will not impart the desired cylinder
bulk (cc/g) properties. Therefore, in accordance with the present
invention, the fluid jet texturizer is operated also at a
relatively higher temperature so that comparable cylinder bulk
properties (i.e., as compared to higher efficiency texturizers) may
be obtained. Therefore, the texturing unit 30 includes, according
to the present invention, a fluid jet texturizer operable at
sufficiently low fluid jet velocity and at a sufficiently high
fluid jet temperature to obtain a yarn skein shrinkage of less than
about 0.50 inch (preferably about 0.25 inch or less). When nylon-6
is employed to form the filaments, the fluid jet texturizer will
operate at a sufficiently low fluid jet velocity so that the BCF
exhibit an alpha-crystalline content of at least about 45%
(preferably between about 45% to about 55%).
[0022] The filaments may be formed of any synthetic fiber-forming
melt-spinnable materials, especially polyesters, polyamides and
polyolefins. Suitable polyesters include (but are not limited to)
polyethylene terephthalates, polybutylene terephthalates,
polytrimethylene terephthalates and copolymers and mixtures
thereof. Suitable polyamides include (but are note limited to)
nylon 6, nylon 6,6, nylon 6,9, nylon 6,10, nylon 6,12, nylon 11
nylon 12 and copolymers and mixtures thereof. Suitable polyolefins
include polypropylene, polypropylene derivatives and copolymers and
mixtures thereof.
[0023] The present invention will be further understood by
reference to the following non-limiting Examples.
EXAMPLES
[0024] In the following Examples, the "cylinder bulk", "alpha %"
and "skein shrinkage" data were obtained as follows:
[0025] Cylinder Bulk: "Cylinder bulk" of a BCF yarn is the specific
volume (cc/gm) of a yarn sample under a compression load of about 9
kg. The cylinder bulk is determined by compressing, within a PTFE
cylinder using the compression rod of an Instron gage, under a
compression load of about 9 kg, a yarn sample weighing 5 grams
which has been boiled previously in water for 30 minutes and
allowed to dry.
[0026] Alpha %: "Alpha %" is the percent of alpha crystallinity in
nylon-6 BCF yarn which is determined by infrared spectrometry with
a photoacoustic detector and a wire grid polarizer to collect
spectral data. The alpha % represents the percent alpha
crystallinity of an average of several yarn samples using their
respective peak heights at two characterized frequencies for known
alpha and gamma crystal absorbances.
[0027] Skein Shrinkage: A skein having an original skein length of
54 inches is formed from a fresh twisted, non-heatset yarn package
and is hung in a controlled atmosphere of 70.degree. F. and 65%
relative humidity. The skein length is measured at predetermined
time intervals. On the sixth day, a second skein is made from the
same yarn package and the procedures noted above are repeated. The
skeins are then subjected to 200.degree. F. saturated steam using a
Kusters dye line and the length after such heat-treatment is
measured and noted as the skein shrinkage (inches).
[0028] Bulked continuous filament (BCF) nylon 6 (ULTRAMID.RTM.
nylon commercially available from BASF Corporation) carpet yarn
samples were run on a one position RieterJO/I0 spin-draw-texture
machine similar to that depicted schematically in FIG. 1. A control
sample was made using standard production conditions for 1100d BCF
carpet yarns. The texturing jet used for the control sample was
then replaced with a less efficient jet utilizing about an 8%
higher cross sectional area. The lower efficiency texturing jet
produced less crimp, as evidenced by the position of the yarn plug
on the cooling drum. The amount of crimp was then adjusted by
increasing the draw duo temperature split so that the position on
the cooling drum was identical. For the purposes of these examples,
the term "draw duo temperature" is the temperature of the hotter
duo roll.
[0029] The results of these trials are listed in Table 1 below.
1 TABLE 1 Control Jet Low Efficiency Jet Draw Duo Temperature
(.degree. C.) 178 186 Cylinder Bulk (cc/g) 4.7 4.8 Crystallinity in
Alpha form (%) 42 45 Skein Shrinkage (inch) 1.25 0.25
[0030] As the data in Table 1 demonstrate, by using the lower
efficiency texturing jet, an 8.degree. C. higher draw duo
temperature was required to achieve substantially equivalent crimp
as evidenced by the cylinder bulk. For the final yarn, the
percentage of crystals in the alpha form increased by 7% while the
yarn skein shrinkage upon exposure to air over six days was reduced
by 80%.
[0031] While the invention has been described in connection with
what is presently considered to be the most practical and preferred
embodiment, it is to be understood that the invention is not to be
limited to the disclosed embodiment, but on the contrary, is
intended to cover various modifications and equivalent arrangements
included within the spirit and scope of the appended claims.
* * * * *