[0001] The invention relates to a process for the production of patterned nonwoven fabrics
made from cotton, and to the patterned nonwoven cotton fabrics that are made thereby.
[0002] Nonwoven fabrics that are made by the fluid rearrangement of fibers have been in
commercial use for some time. For instance, Kalwaites, in U.S. Patent Nos. 2,862,251,
3,033,721, 3,193,436, and 3,769,659, and Griswold in U.S. Patent Nos. 3,081,515 and
3,025,585, describe various processes for producing nonwoven fabrics by the fluid
rearrangement of a fibrous web to which resin binder is added after the fluid rearrangement
to form a useful, coherent, nonwoven fabric. Still other nonwoven fabrics are made
by forming a web of fibers and treating it with high pressure jets to entangle the
fibers and produce a strong fabric that does not require the addition of binder to
be self-supporting and useful for many purposes. Such a technique is described by
Evans, in U.S. Patent No. 3,485,706.
[0003] In the processes taught by Kalwaites and Griswold, resin binder is added to the rearranged
fabric to produce a commercially useful nonwoven fabric. With the Evans process, although
binder need not be added, high pressure water jets are used to produce the nonwoven
fabric. The present invention relates to a process whereby cotton fibers can be fluid
rearranged to produce useful patterned nonwoven fabrics, without the necessity for
the use of any resin binder, and yet the fluid rearrangement takes place at relatively
low pressures.
[0004] French published patent application No. 1, 478, 115 concerns absorbent cotton felt
formed of cotton fibers welded and interlaced in all directions made by a process
consisting of successively cleaning and fleecing raw cotton fibers of all lengths
and then bleaching, washing and drying the fleece.
[0005] Bunting
et al., in U.S. Patents Nos. 3,493,462; 3,508,308; and 3,620,903, describe a process for
producing light-weight non-woven fabrics by treating an array of fibres to essentially
columnar streams of liquid jetted from orifices under high pressure. The jet streams
may be rapidly oscillated, which oscillation is done for the purpose of producing
a smooth fabric surface and to enhance the non-patterned structure of the non-woven
fabric.
[0006] In particular, Bunting
et al., in U.S. Patent No. 3,493,462 disclose a process in which a layer of fibrous material
is supported on a smooth supporting member and the layer on the smooth supporting
member is treated by jetting liquid. The liquid in the jets is supplied at a pressure
of at least 200 psig.
[0007] The smooth supporting member must be one which does not influence the arrangement
of the fibers into a pattern dependent on the supporting surface. The smooth supporting
member may be a solid plate, bar, roll or the like, or it may be a relatively smooth
screen of sufficiently fine mesh so that the fibers are not rearranged into any pattern
dependent on the screen pattern.
[0008] It is indicated that the invention disclosed in U.S. Patent No. 3, 493,462 is particularly
useful for nonfeltable fibers and filaments, i.e. synthetic and cellulosic fibers
and filaments, including cotton, rayon and cellulose derivatives.
[0009] In the process described in U.S. Patent No. 3,493,462, the liquid jets may be oscillated,
but where oscillating jets are used, a non-patterned fabric is produced.
[0010] In Figure 5 in US Patent No. 3,493,462 there is shown an apparatus for producing
a patterned fabric. The apparatus comprises a plurality of jets which are held stationary
and which produce longitudinal lines in the fabric. The apparatus also includes two
other jets which are traversed over the complete width of the layer to form transverse
lines in the fabric. The pattern in the fabric is not influenced by the smooth supporting
member. After the fabric has been treated by the liquid jets, Figure 5 shows it being
passed through a liquid bath wherein it is momentarily immersed. It is indicated that
this momentary immersion may be for shrinkage, dyeing, bleaching, etc.
[0011] The problem with the process disclosed in the US Patent No. 3,493,462 is that it
requires a high energy input into the fibrous layer in order to produce a satisfactory
product. This requires the use of expensive and complicated equipment. It is an aim
of the present invention to provide a process by which a coherent, patterned, nonwoven
fabric can be produced using relatively inexpensive and uncomplicated equipment.
[0012] Accordingly, the present invention provides a process for producing a patterned,
nonwoven fabric which comprises:
(a) supporting a fibre layer comprising at least a major proportion of grey cotton
fibers, the fibres of which are in mechanical engagement with each other but capable
of movement under liquid forces, on a liquid pervious support member, having from
35 to 75 per cent open area, adapted to move in a predetermined direction and on which
fiber movement in directions both in and at an angle to the plane of said layer is
permitted in response to applied liquid forces;
(b) moving the supported layer in said predetermined direction through a fiber rearranging
zone within which streams of liquid under a pressure of about 100 to 600 psi (about
700 to 4,000 kPa) are projected directly onto said layer, wherein said streams are
oscillated in a direction transverse to said predetermined direction;
(c) permitting said streams of liquid to pass through said layer and said support
member to effect movement of said fibers to form a layer that resembles the negative
image of said liquid pervious support member and to effect sufficient interlocking
of said fibers that said layer becomes a self-supporting entangled fibrous web; and
(d) subjecting the self-supporting entangled fibrous web product of step (c) to a
conventional cotton bleaching step, thereby producing a coherent patterned nonwoven
fabric.
[0013] Preferably, the frequency of oscillation of said streams is from about 75 to about
200 cycles per minute, and the amplitude of said oscillation is from about 5 to about
50 millimeters.
[0014] Advantageously, the streams are columnar jets spaced at least 0.8 millimeters apart,
center-to-center.
[0015] In the accompanying drawings:
Fig. 1 is a schematic view in elevation of an arrangement of apparatus suitable for
carrying out the process of the invention;
Figs. 2 through 5 are photomacrographs, originally taken at 10X, of the nonwoven fabric
of Example 1 of this application;
Figs. 6 through 9 are photomacrographs, originally taken at 10X, of the nonwoven fabric
of Example 2 of this application; and
Fig. 10 is a top plan view of the manifold section looking in the direction of the
arrows 10-10 of Fig. 1.
[0016] Referring to Figs. 1 and 10, a carded web 12 of gray cotton fibers is produced by
a card 10, and is then passed onto a liquid pervious support member or forming belt,
such as an endless woven belt 14. The belt 14 carries the web 12 of fibers under a
series of manifolds 16 that are arranged in rows disposed transversely across the
path of travel of the belt 14 (i.e. they are disposed in the cross direction). On
the manifolds 16 are mounted spray heads or orifice strips for ejecting liquid 18
under moderate pressure down onto the carded web 12 of cotton fibers supported on
the belt 14. The liquid is provided from a source (not shown) of pressurized water,
through a main water duct 19, to a common supply manifold 21, and through flexible
hoses 23 into each manifold 16. The manifolds 16 are constructed and adapted so that
they can be oscillated transversely to the path of travel of the web 12 (see the arrows
"a" in Fig. 10, which show the direction of oscillation), with the frequency of oscillation
being, for instance, from about 1 to about 5 oscillations per second. There may be
a vacuum duct 20 attached to conventional vacuum means (not shown) pulling a vacuum
of, for example, up to 17 to 34 kPa (5 to 10 inches of mercury) beneath the belt 14,
with vacuum slots 22 being positioned directly under each manifold 16. The cotton
fibers in the web 12 are rearranged by the liquid jets or spray 18 as the liquid impinges
upon and passes through the fibrous web 12 and then through the belt 14. The rearranged
fibrous web 24 can be de-watered, as by passing it through a pair of squeeze rolls
28, and it is then carried to a conventional windup 26, still in the wet state, for
subsequent bleaching. The rearranged fibrous web 24 is preferably kept wet until it
has been bleached, in order to impart sufficient strength to the web 24 so that it
can be handled. The rearranged fibrous web is then bleached by conventional cotton
bleaching procedures, and is then rinsed and dried, to produce the cotton patterned
nonwoven fabric of the invention.
[0017] The process of the invention is employed with gray cotton staple fibers. While other
fibers can be blended with the cotton, the gray cotton must comprise at least a major
proportion of the web to be employed in the process of the invention. As used herein,
"gray cotton" refers to cotton that has not been bleached or scoured.
[0018] The cotton feed web can be formed by carding, air-laying, or other convenional web-forming
procedure. Typical feed web weights are from about 25 to about 200 grams per square
meter.
[0019] If desired, a reinforcing web such as a scrim or a reticulated plastic netting can
be used. Typically, the carded cotton fiber feed web is laid down on top of the reinforcing
web prior to the liquid rearranging.
[0020] The liquid pervious support member or forming belt that is employed to carry the
array of cotton fibers under the water spray can be a conventional plain weave belt
woven of polyester monofilament, bronze, or other conventional materials. The belts
will have from 35 to 75 per cent open area. Such belts are conventionally made from
monofilaments having a filament count of from about 11 to about 236 filaments per
10 centimeters (about 3 to 60 filaments per inch) in both directions. The use of a
support member having this open area, in conjunction with the other conditions of
the process, leads to the formation of the layer resembling the negative image of
the support member. The water that is jetted or sprayed onto the fibers is provided
at relatively low pressure of from about 100 to about 600 psi (that is, from about
700 to about 4,000 kpa). The water spray can be provided in the form of essentially
columnar jets, if desired, but can also be employed in the form of sprays with a relatively
wide angle of divergence, for instance, up to about 10 degrees.
[0021] The exact number of spray heads per unit width has not been found to be narrowly
critical. However, a much wider spacing can be used than is customarily employed with
the technique of Evans (U.S. Patent No. 3,485,706). When using columnar jets having
diameters of from about 76 to 254 µm (3 to 10 mils), the usual spacing is from about
0.79 to 3.9 jets per centimeter (2 to about 10 jets per inch). When using spray jets
instead of columnar jets, about 0.20 to 0.79 per centimeter (one-half to two per inch)
are typical. (Closer spacing would be difficult because of the size of the spray heads.)
[0022] The number of rows of jets (i.e. the number of jets in the machine direction or direction
of travel of the forming belt) has not been found to be narrowly critical. Typically,
there will be from about 10 to about 30 rows when spray jets are used, and from about
8 to about 20 rows when columnar jets are used.
[0023] For the conditions indicated above (i.e. typical web weights, jet liquid pressures,
jet spacings, and rows of jets), the usual speed of the forming belt is from about
5 to about 20 meters per minute.
[0024] An important feature of this invention is the provision of means to impart transverse
oscillation to the jets. Such oscillation can be effected by mounting the manifolds
16 in such a way that they are transversely movable (as by using roller bearings or
linear bearings), and employing a driven crank-shaft, rotating cams, eccentrically
mounted rotating circular disks, or other conventional oscillation-imparting means
(not shown), to engage the manifolds and oscillate them. The manifolds can be oscillated
either together (in phase with each other) or independently (out of phase with each
other).
[0025] In the embodiment schematically shown in the drawings, the manifolds 16 are ganged,
and are suspended from a stationary mounting plate 30. Upstanding projections or lugs
32 attached to the ganged manifolds 16 extend through slots 34 in the stationary mounting
plate 30. Roller bearings 36 mounted on the lugs 32 ride on the mounting plate 30
as the ganged manifolds 16 oscillate.
[0026] The oscillation used is a relatively low frequency oscillation, e.g. from about 75
to about 200 cycles per minute. The amplitude of the oscillation is not narrowly critical,
and it can vary, for instance, from about 5 millimeters to about 50 millimeters.
[0027] The rearranged web is subjected to a conventional cotton bleaching process (which
is illustrated below in the examples), and is then dried as by passing it over a set
of steam cans.
[0028] The examples below illustrate the practice of the invention.
Example 1
[0029] A carded web of gray cotton having a weight of 50 grams per square meter was laid
down onto a single layer of woven cotton gauze. The gauze was a plain weave scrim
having a warp thread count of 6.70 per centimeter (17 per inch) and a weft thread
count of 5.12 per centimeter (13 per inch), and weighed 15 grams per square meter.
The double layer web was then passed onto a woven belt having the following description.
[0030] The belt was a plain weave belt woven of polyester monofilaments. The warp and weft
threads had diameters of 500 µm, and the thread counts were 40 warp threads per centimeter
and 10 weft threads per centimeter.
[0031] The belt carrying the web of carded cotton plus scrim was passed under a series of
manifolds at a speed of 10 meters per minute. The manifolds contained spray nozzles
that were 55 millimeters apart (center-to-center) in the cross direction, and there
were 8 rows of nozzles in the machine direction. The spray nozzles used were designed
to deliver solid streams of water through orifices having diameters of about 203 µm
(8 mils).
[0032] The belt was 15 millimeters under the tips of the nozzles. Water was sprayed through
the nozzles at a pressure of 3500 kPa. As the web was carried under the nozzles, the
manifolds in which the nozzles were mounted were vibrated at a frequency of 120 cycles
per minute and an amplitude of 37 millimeters. Vacuum slots under the belt below each
row of nozzles pulled a vacuum of about 17 kPa (5 inches of mercury). The fabric was
passed through the apparatus 10 times. The web was de-watered by passing it through
a pair of squeeze rolls, was collected on a windup while still wet, and was then bleached
under the following conditions.
[0033] The fabric is rolled onto a perforated spindle and is then placed in a bleaching
kier. The fabric is wet out with hot water and then drained. The kier is then filled
(to a level above the cloth) with an aqueous solution containing caustic soda, soda
ash, and soap, and allowed to circulate. Hydrogen peroxide is added and the kier is
sealed and heated to 120°C, where it is kept for 20 minutes. The kier is then cooled,
drained, and rinsed twice with cold water. Dilute acetic acid is added to a pH of
6.5 - 7.0, and then two more rinses are made. If the pH of the final rinse is 6.5
- 7.0, the cloth is removed and dried.
[0034] Photomacrographs of this fabric are shown in Figs. 2 - 5. Figs. 2 and 3 were made
with incident light and Figs. 4 and 5 were made with transmitted light. Figs. 2 and
4 show the top side of the fabric and Figs. 3 and 5 show the bottom or belt side (i.e.
the side that was next to the belt during the rearranging).
Example 2
[0035] By a procedure analogous to that described in Example 1, a cotton patterned fabric
was made from a web of carded gray cotton having a basis weight of 50 grams per square
meter. The forming belt was the same as that described in Example 1. The processing
conditions were as follows:
[0036] Belt speed - 10 meters per minute;
Spray pressure 3500 kpa; and
Manifold Oscillation:
2 cycles per second;
3.7 centimeter amplitude.
[0037] The wet, rearranged fabric was bleached and dried by a procedure analogous to that
of Example 1. Photomacrographs of the fabric are shown in Figs. 6-9. As with Example
1, the photomacrographs were taken both with incident light and with transmitted light,
and both the top and belt sides are shown.
[0038] The fabrics described in this application are useful as bandages, sponges, swabs,
primary dressings, secondary dressings, prepping swabs, and other absorbent products.
Examples 3 and 4
[0039] By a procedure analogous to that described in Example 1, a gauze reinforced fabric
was made from a web of gray cotton having a weight of 50 grams per square meter and
the scrim described in Example 1. Instead of using spray nozzles, the water was jetted
through the holes in an orifice strip, the holes being designed to produce essentially
columnar jets. The holes had diameters of 0.18 mm (0.007 inch), and there were 1.57
holes per centimeter (four holes per inch). There were 12 rows of nozzles. Only one
pass through the apparatus was used.
[0040] The processing conditions were the following:
Belt speed - 10 meters per minute;
Jet pressure - 3500 kpa; and
Manifold oscillation - 2.67 cycles per second
3.1 centimeter amplitude.
[0041] The webs were dewatered, bleached, and dried as described in Example 1.
[0042] The procedure was repeated, but without using the gauze reinforcement. Typical tensile
properties of both the gauze-reinforced and the non-reinforced fabrics are the following:
| Tensile Strengths |
| |
Non-Reinforced |
Gauze-Reinforced |
| MD Dry |
13.7 Newtons, minimum |
27.5 and 19.6 N., min. |
| MD Wet |
15.7 N., min. |
27.5 N., min. |
| CD Dry |
4.7 N., min. |
10.3 and 8.3 N., min. |
| CD Wet |
4.9 N., min. |
12.7 N., min. |
[0043] The tensile tests were carried out on an Instron tensile tester. Sample size was
25 x 130 mm. The initial distance between the jaws was 100 mm. The crosshead speed
was set at 200 mm/minute.
[0044] With the gauze-reinforced samples, there are two peaks in the stress/strain curve.
The higher numbers are the tensile strengths of the gauze reinforcement; the lower
are the tensile strengths of the entangled cotton.