U.S. patent number 3,630,816 [Application Number 04/845,075] was granted by the patent office on 1971-12-28 for nonwoven sheets made from rectangular cross section monofilaments.
This patent grant is currently assigned to Chevron Research Company. Invention is credited to Phillip H. Parker.
United States Patent |
3,630,816 |
Parker |
December 28, 1971 |
NONWOVEN SHEETS MADE FROM RECTANGULAR CROSS SECTION
MONOFILAMENTS
Abstract
Nonwoven sheets of continuous synthetic polymer, e.g.,
stereoregular polypropylene, monofilaments which have elongated,
e.g., rectangular, cross sections with aspect ratios of at least
about 3:1 and are disposed randomly and are substantially discrete
from each other except at crossover points in the sheet. These
sheets may be made by extruding the polymer through appropriately
shaped orifices, partially cooling the resulting monofilaments,
drawing them with a pneumatic jet and depositing them on a
collecting device.
Inventors: |
Parker; Phillip H. (San Rafael,
CA) |
Assignee: |
Chevron Research Company (San
Francisco, CA)
|
Family
ID: |
25294338 |
Appl.
No.: |
04/845,075 |
Filed: |
July 25, 1969 |
Current U.S.
Class: |
428/221; 428/397;
264/177.13; 442/337 |
Current CPC
Class: |
D04H
3/00 (20130101); Y10T 442/611 (20150401); Y10T
428/2973 (20150115); Y10T 428/249921 (20150401) |
Current International
Class: |
D04H
3/00 (20060101); D01d 005/22 (); D01d 007/00 ();
B32b 027/02 () |
Field of
Search: |
;264/177F,179
;161/150,157,177,72,89,92,252,165 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Ansher; Harold
Claims
I claim:
1. Nonwoven sheet of continuous synthetic polymer monofilaments,
said monofilaments having elongated cross sections in which the
aspect ratio is in the range of 3:1 to 8:1, and said monofilaments
being disposed randomly and substantially discrete from each other
except at crossover points.
2. The nonwoven sheet of claim 1 wherein the cross sections of the
monofilaments are substantially rectangular.
3. The nonwoven sheet of claim 1 wherein the individual
cross-sectional areas of the monofilaments are about 0.00005 to
0.008 mm..sup.2.
4. The nonwoven sheet of claim 1 wherein the polymer is
substantially crystalline, stereoregular polypropylene.
5. The nonwoven sheet of claim 1 wherein the polymer is
substantially crystalline, stereoregular polypropylene, the cross
sections of the monofilaments are substantially rectangular and
have individual areas of about 0.00005 to 0.008 mm..sup.2 and the
aspect ratio is in the range of 3:1 and 8:1.
Description
FIELD OF THE INVENTION
This invention concerns nonwoven sheets made from continuous
synthetic polymer monofilaments which have elongated cross
sections. More particularly, it relates to such sheets in which the
monofilaments have substantially rectangular cross sections and are
discrete from each other except crossover points.
BACKGROUND OF THE INVENTION
Nonwoven articles of continuous oriented monofilaments have been
made and used for a variety of textile and related uses. Primarily,
they have been used as carpet backings, insulation and disposable
clothing. In general, such articles have been made by spinning
continuous monofilaments of spinnable synthetic polymers, drawings
the freshly spun filaments and depositing then on a collecting
surface. A large portion of the art relating to these articles
concerns the way in which the freshly spun filaments are drawn to
improve the tensile strengths of the filaments. The strengths of
such freshly spun monofilaments have been improved by drawing then
between rolls rotating at different speeds. More recently they have
been drawn by "spin drawing" techniques. In "spin drawing"
partially cooled, partially crystalline filaments are fed into a
pneumatic jet. The jet works on the ejector principle. That is, the
expanding gaseous medium passing through the jet carries and
accelerates the filaments causing then to be drawn or oriented.
Developments concerning methods for depositing the drawn filaments
have been directed towards improving the isotropic properties of
the finished, nonwoven product made from the filaments. Such
developments have usually concerned particular patterns for laying
the drawn filaments down on the collecting surface for keeping the
filaments discrete, i.e., not entangled or bundled.
For the most part filaments which have been used to make nonwoven
sheets have had circular cross sections. Certain noncircular cross
section filaments have been suggested as equivalent to circular
cross section filaments for use in nonwoven materials. In the
related yarn art noncircular cross section monofilaments have been
used to simulate natural fiber shapes, provide a particular
appearance or increase covering power. Heretofore, it has not been
recognized that the cross-sectional shapes of the filaments may
materially affect the tensile properties of finished nonwoven
sheets made therefrom.
INVENTION DESCRIPTION
It has been found that nonwoven sheets of continuous oriented
synthetic polymer monofilaments having an elongated cross section
in which the aspect ratio is at least about 3:1 and in which the
monofilaments are deposited randomly and are substantially discrete
from each other except at crossover points have unexpectedly better
tensile properties than corresponding sheets of circular cross
section monofilaments. This finding is especially surprising in
view of the fact that individual monofilaments of circular cross
section and individual monofilaments of elongated cross section and
comparable denier have substantially similar tensile
properties.
Filaments having elongated cross sections are used to make the
unexpectedly strong nonwoven sheets of this invention. These
filaments are characterized as having an aspect ratio (the ratio of
cross section length of cross section width) of at least about 3:1
and usually in the range 3:1 and about 8:1. The shape of the cross
section of these filaments will usually be substantially
rectangular. Substantially rectangular cross sections include those
having two sets of essentially parallel flat surfaces which
intersect each other essentially at 90.degree. angles (true
rectangle) as well as those having two slightly rounded oppositely
disposed planar surfaces, the respective ends of which are joined
by rounded, smaller surfaces. These latter cross sections are
characterized as elliptical. The surfaces of these filaments will
be substantially regular. That is, they should be relatively smooth
and free of large bumps, protrusions or lobes.
The particular shapes of the elongated cross section monofilaments
used in this invention are dependent upon the shaped of the orifice
or die from which they are spun and extent to which they are
oriented or drawn. Oriented monofilaments of elliptical cross
sections are formed by extruding the polymer melt from orifices
having a substantially rectangular cross section. Such
monofilaments emerge from the orifices with rectangular cross
sections; but, as they are drawn their cross sections reshape to
ellipses. Oriented monofilaments which are substantially
rectangular are made by spinning the melt from a die of rectangular
cross section in which the longitudinal sides are somewhat concave.
When such monofilaments are drawn the concave sides of the
rectangle flatten so that they are substantially parallel. Devices
for making elongated cross section monofilaments are well known.
See for instance U.S. Pat. No. 3,179,770.
The freshly spun monofilaments are drawn from an original
cross-sectional area as the filament emerged from the die of about
0.004 to 4.0 mm..sup.2 down to a cross-sectional area of about
0.00005 to 0.008 mm..sup.2. In terms of a circular filament this is
equivalent to reducing the diameter from about 0.10-1.0 mm. down to
10-100 microns (1 to 60 denier). This drawing is done after the
filaments are partially cooled and while the polymer is in at least
a partially crystalline state.
When the filaments are made of substantially crystalline,
stereoregular polypropylene, after the drawing they will have
tenacities of about 2 to 5 g. per denier and elongations of about
50 to 400 percent, depending, of course, upon the particular
drawing conditions.
The drawing orients the polymer structure and greatly increases the
filament's tensile strength. While roll drawing or spin drawing may
be used, it is preferable to spin draw the monofilaments used to
make the unique, nonwoven sheets of this invention.
Accordingly, the freshly spun monofilaments are fed, usually in a
bundle of about 5-500, into the main chamber of a pneumatic jet.
Air, or other inert gases may be used as the gaseous drawing
medium. In order to draw the monofilaments sufficiently the air
velocity will usually be about 200-800 m. per sec. within the main
chamber. Air travelling at these velocities will pick up the
monofilament bundle and draw the filaments at speeds in excess of
1,500 m. per min. and up to the speed which causes the filaments to
break. The draw rate will preferably range between 2,500-5,000 m.
per minute. Particular jet designs may be used to keep the
individual monofilaments separate while they pass through the jet.
Other techniques, such as charging the filaments, may also be used
to keep then from entangling.
The thus drawn monofilaments may be laid down onto a collecting
surface as they emerge from the pneumatic jet. If the filaments
have been drawn over rolls instead of spin drawn they may be passed
into a pneumatic filament-handling device. Such devices are well
known and operate on the same principle as the pneumatic
spindrawing jet. However, the gas velocities are below those which
stretch the filaments in the handling device. In order to keep the
gas emerging from the jet with the filaments from entangling the
filaments as they are deposited on the collecting surface or from
blowing them off the surface, the surface may be a wire screen or
other porous medium which allows the gas to pass through it.
Withdrawal and/or dissipation of the high-velocity gas emerging
from the jet may be facilitated by applying suction to the side of
the porous collecting surface opposite that on which the filaments
are being laid.
The collecting surface will move away from the zone in which the
bundles of nonentangled substantially parallel filaments are laid
down. This motion away from the lay down zone may be conveniently
achieved by using an endless moving screen belt as the collecting
surface. In order to form webs having substantially isotropic
tensile properties the rate at which the filaments are forwarded
onto the collecting surface will be several times that at which the
surface is moving away from the lay down zone. Usually, the
filament forwarding speed will be about 10-1000 times the speed at
which the surface is moved away from the lay down zone.
Filament patterns in the laid-down web will depend upon the
relative motion of the filaments and the collecting surface. By
moving the lay down device transverse to the direction of the take
away or by keeping the lay down device stationary and moving the
filaments either by oscillating the lay down device or baffling the
filaments, various filament patterns will be achieved. The pattern
should not be such as to affect substantially the isotropicity on
the laid-down web. It is within the scope of this invention to
incorporate within the nonwoven sheets a variable amount of
monofilaments having a nonelongated cross section shape; provided
such added filaments do not entirely eliminate the improved
strength properties obtained through the use of elongated cross
section fibers in accordance with this invention. Such fibers of
other shapes affect other properties of the sheet as well as the
strength of it. In particular, fibers having a round or circular
cross section may be incorporated into the nonwoven sheet. The
presence of such circular fibers improves the hand of the resulting
sheet by reducing the stiffness thereof. By a proper choice in the
ratio of round to elongated fibers, sheets having both improved
hand and high strength may be obtained.
The thus laid web of continuous monofilaments of elongated cross
section is dry--and even in this form has superior tensile
properties relative to corresponding webs of circular cross section
monofilaments.
Weight of the webs of this invention normally ranges from about 0.5
to 44 ounces per square yard. Their densities will usually be about
0.2 to 0.7 g. per cc. They will normally be 0.005 to 0.3 inch
thick.
This web or batt is useful as such for insulation, paper
reinforcement, nonwoven fabric reinforcement and filters. It may be
further treated if desired by needle punching, calendering, heat
sealing, sewing or knitting depending upon its intended end use.
This web is also susceptible to other conventional treatments such
as adhesive bonding. These bonded webs are useful as carpet
backing, sacking, paper and fabric reinforcement, felt carpets,
nonwoven fabrics, etc. As a general rule, the finished nonwoven
product with the elongated cross section filaments have superior
tensile properties to corresponding products made from conventional
monofilaments.
The synthetic polymers which may be used in this invention are
those which may be spun or otherwise formed into continuous
monofilaments. Such polymers include crystalline polypropylene,
crystalline polyethylene, poly-4-methyl-1-pentene, copolymers
thereof, polyvinylchloride, polyesters such as polyethylene
terephthalate, polyamides such as nylon and the like.
EXAMPLES
The following examples illustrate the nonwoven sheets of this
invention. These examples are not intended to limit the invention
in any manner. Unless otherwise indicated, percentages are by
weight.
EXAMPLE 1
Commercial, substantially crystalline, stereoregular polypropylene
with a melt flow rate of 4 was melted in an extruder with the final
extruder zone having a temperature of 320.degree. C. It was then
melt spun through a two-hole spinnerette having round holes with a
diameter of 1.0 mm. The spinnerette temperature was 300.degree. C.
The polymer was extruded at a rate of 4.1 g./hole/minute. The
resulting circular cross section filaments then fell 32 feet to a
pneumatic jet which accelerated the filaments to a linear velocity
of 2.400 yards per minute thereby drawing them. The filaments were
then collected on a screen with a vacuum behind it to form a web or
batt. This batt was slightly compressed between two rollers for
easier handling.
The tenacity of these filaments, the breaking strength of this web
or batt were determined by conventional ASTM tests. These
properties are tabulated in tables I and II, respectively.
EXAMPLE 2
Filaments and a batt were prepared under conditions similar to
those of example 1 except that the filaments were accelerated by
the pneumatic jet to 5,200 yards per minute after being melt spun.
The tenacity of these filaments and the break strength of this are
also shown in tables I and II.
EXAMPLE 3
Filaments and a batt were prepared under conditions similar to
those of example 2 except that the filaments were extruded at a
rate of 3.3 g./hole/minute and were accelerated by the pneumatic
jet to 5,300 yards per minute. The tenacity of these filaments are
shown in table I and batt breaking strength in table II.
EXAMPLE 4
Filaments and a batt were prepared under conditions similar to
those in example 1 except that the spinnerette had 3 rectangular
orifices which were 3.0 mm. long and 0.3 mm. wide. The filaments
were extruded at a rate of 2.8 g./hole/minute and were accelerated
by the pneumatic jet to 2,200 yards per minute. The filament
properties are shown in table I and batt properties in table
II.
EXAMPLE 5
Filaments and a batt were prepared under conditions similar to
those of example 4 except that the filaments were accelerated by
the pneumatic jet to 4,000 yards per minute. Filament properties
are shown in table I and batt properties in table II.
EXAMPLE 6
Filaments and a batt were prepared under conditions similar to
those of example 4 except the filaments were extruded at a rate of
3.3 g./hole/minute and accelerated by the pneumatic jet to 4,600
yards per minute. Filament properties are shown in table I and batt
properties in table II.
EXAMPLE 7
Filaments and a batt were prepared under conditions similar to
those of example 4 except that the spinnerette had 3 rectangular
orifices which were 2.0 mm. long and 0.5 mm. wide. The filaments
were extruded at a rate of 3.3 g./hole/minute and were accelerated
to 5,200 yards per minute by the pneumatic jet. Filament properties
are shown in table I and batt properties in table II.
EXAMPLE 8
The nonwoven batt of example 1 was passed through a needle loom to
produce a needled felt with about 200 needle penetrations per
square inch. The results of a breaking strength test on the
resulting fabric are shown in table III.
EXAMPLE 9
The nonwoven batt of example 4 was needle felted as in example 8.
The results of a breaking strength test on the resulting fabric are
shown in table III.
EXAMPLE 10
The nonwoven batt of example 3 was pressed in a hot calendering
machine at about 145.degree. C. to heat seal the fibers together.
The breaking strength of the heat-sealed nonwoven fabric is shown
in table IV.
EXAMPLE 11
The nonwoven batt of example 7 was heat sealed in a manner similar
to example 10. The breaking strength of the heat-sealed nonwoven
fabric is shown in table IV.
EXAMPLE 12
The nonwoven batt of example 6 was heat sealed in a manner similar
to example 10. The breaking strength of the heat-sealed nonwoven
fabric is shown in table IV. ##SPC1## ##SPC2## ##SPC3##
##SPC4##
The tenacity data in table I indicate there is no significant
difference in tenacity between round filaments and rectangular
filaments of comparable denier and orientation. In contrast the
strength data reported in tables II through Iv illustrate that
various types of nonwoven sheets made from rectangular cross
section monofilaments have substantially better breaking strength
than similar sheets made from comparable circular cross section
monofilaments.
* * * * *