[0001] The present invention relates to a fiber comprising an ethylene copolymer, a non-woven
fabric comprising the fiber, the use of a specific ethylene copolymer for fiber production
and a process for preparing a fiber in accordance with the present invention.
Description of related art
[0002] Synthetic fibers are used over a broad range of applications and, in particular,
synthetic fibers comprising polyolefins have been developed in the recent past. One
specific type of synthetic fibers is bicomponent fibers, defining a fiber comprising
two different polymers of, for example, different chemical constitution or different
physical properties. Typically, these two different polymers are brought together
in the spinning process and thereby extruded into a bicomponent fiber.
[0003] The basic concept behind a bicomponent fiber is the desire to combine the properties
of two different polymers in order to widen the possible fields of application.
[0004] Typical bicomponent fibers are polypropylene/polyethylene fibers. These fibers comprise
a low melting temperature component (polyethylene) and a high melting temperature
component (polypropylene) which offers specific advantages, for example, when producing
a non-woven fabric. If the lower melting temperature component is employed, at least
partially as a component being present on the surface of the fiber, the non-woven
fabric can be bonded in a simple thermal bonding process requiring far less heat,
compared with a thermal bonding process employing pure polypropylene fibers. At the
same time, it is ensured that the polypropylene remains intact and provides the desired
product strength for the fabric. Typical advantages associated with the use of such
bicomponent fibers are non-woven fabrics with a soft handle which can be produced
without chemical binders. Furthermore, non-wovens can be obtained which show a desired
degree of bulkiness and the production process of such fabrics is simple and energy
efficient.
[0005] Various bicomponent fibers of this type are known in the art. The
European patent application EP 0696655 A1, for example, discloses a melt adhesive composite fiber which may be used for preparing
non-woven fabrics to be employed as surface material for medical supplies and paper
diapers. The melt adhesive composite fibers as disclosed in the above-mentioned European
patent application comprise a polypropylene as a first component and a polyethylene
as a second component, which is continuously present on at least a part of the fiber
surface along the length of the fiber.
[0006] Typical polyethylenes to be employed in such bicomponent fibers are LLDPE materials,
i.e. ethylene copolymers comprising α-olefins, as well as HDPE materials, which may
be homopolymers or copolymers. Examples of such HDPE materials are copolymers of ethylene
with 1-octene, which are, for example, disclosed in
WO 2005/111291 A1 as suitable component for a bicomponent fiber.
[0007] A commercially available ethylene polymer for use in bicomponent fibers is the polyethylene
grade Aspun 6811A of Dow, which is an LLDPE material.
[0008] However, a constant need still exists for further improvement with respect to materials
for bicomponent fibers, enabling in particular excellent spinning procedures, with
as few mechanical failures of the fibers as possible, enabling further broad windows
of manufacture and further processing while enabling a high non-woven strength.
Object of the present invention
[0009] In view of the above-outlined drawbacks of the prior art, the present invention aims
at providing an improved fiber, fulfilling at least one of the objectives as indicated
above. In this respect, the present invention provides the following.
Brief disclosure of the invention
[0010] The present invention provides an improved fiber as defined in claim 1. Preferred
embodiments of the fiber are defined in subclaims 2 to 9 as well as the following
description. The present invention furthermore provides a non-woven fabric comprising
the fibers in accordance with the present invention as well as processes for the preparation
of the fibers and the non-woven fabrics as defined in claims 10, 11 and 12. Finally,
the present invention provides the use of a specific ethylene copolymer for preparing
fibers as indicated in claim 13. Preferred embodiments are again derivable from the
present specification.
Detailed description of the present invention
[0011] As defined in claim 1, the present invention provides a fiber, comprising a first
polymer component and a second polymer component, wherein the first and the second
polymer component differ from one another at least with respect to one property, such
as chemical constitution or physical properties, and wherein the second component
is an ethylene-α-olefin copolymer having a density of from 0.945 to 0.965 g/cm
3 and having an MFR
2 of from 15 to 45 g/10 min.
[0012] The α-olefin as contained in the ethylene-α-olefin copolymer of the second polymer
component preferably is an α-olefin having from 3 to 20 carbon atoms, more preferably
from 4 to 10 carbon atoms, still more preferably from 4 to 6 carbon atoms and in particular
the α-olefin is 1-hexene.
[0013] The amount of α-olefin contained in the ethylene-α-olefin copolymer of the second
polymer component of the fiber in accordance with the present invention amounts to
about 1 to 7 wt%, preferably 1.25 to 3.5 wt%, and more preferably 1.75 to 3.0 wt%.
An especially preferred α-olefin content is in the range of from 2 to 2.6 wt%
[0014] The ethylene-α-olefin copolymer preferably is a mono-modal copolymer with respect
to the molecular weight distribution showing a rather narrow molecular weight distribution
(MWD) Mw/Mn of from 1 to 8, more preferably 2 to 5, even more preferably 3.5 to 4.5,
such as about 4.
[0015] The density of the ethylene-α-olefin copolymer typically amounts to from 0.945 to
0.965 g/cm
3, more preferably 0.945 to 0.960, even more preferably of from 0.947 to 0.955, and
in particular of from 0.948 to 0.954.
[0016] The ethylene-α-olefin copolymer displays an MFR
2 of from 25 to 45 g/10 min, more preferably of from 30 to 45 g/10 min and in particular
of from 35 to 42 g/10 min, such as about 39 g/10 min. Other highly suitable MFR
2 ranges are from 18 to 30 g/10 min, preferably from 20 to 28 g/10 min, such as about
20 or about 27 g/10 min.
[0017] Typically, the ethylene-α-olefin copolymer of the second polymer component of the
fiber in accordance with the present invention has not been subjected to any chemical
modification, such as grafting and/or irradiation, which are often employed in the
prior art in order to improve the bonding properties or the adhesion to the other
polymer component of a bicomponent fiber.
[0018] The fiber in accordance with the present invention preferably is a bicomponent fiber
which may be a bicomponent fiber of any type, including core-sheath types, side-by-side
types, hollow side-by-side types, orange types, island in sea types, layered types,
as well as others, including modifications, such as eccentric core-sheath types, hollow
orange types etc. Preferred in accordance with the present invention are bicomponent
fibers wherein the second polymer component as defined herein at least is partially
present at the surface of the fiber. Accordingly, core-sheath types are in particular
preferred, wherein the second polymer component in accordance with the present invention
constitutes the sheath. Also preferred, however, are side-by-side types as well as
orange types and layered types, since also these bicomponent fiber types ensure that
the second polymer component to be employed in accordance with the present invention
at least partially is present on the surface of the fiber.
[0019] In particular, preferred however are core-sheath types, wherein as identified above,
the second polymer component as defined herein constitutes the sheath.
[0020] As indicated above, the ethylene-α-olefin polymer to be employed in accordance with
the present invention as second polymer component preferably has not been subjected
to any further modification, such as grafting and/or irradiation. It is in particular
preferred if the ethylene-α-olefin copolymer is employed in the fiber without any
further additive beyond the basic stabilization, although it is possible to add typical
additives, such as additional stabilizers, coloring agents etc. in usual amounts.
[0021] The ethylene-α-olefin copolymer (HDPE) to be employed in accordance with the present
invention as second polymer component may be prepared using conventional polymerization
techniques, in particular employing Ziegler-Natta catalysts. Suitable polymerization
conditions and catalysts are known to the skilled person.
[0022] The first polymer component to be employed in accordance with the present invention
is not restricted and only has to differ at least with respect to one property from
the second polymer component. Typical and suitable examples for first polymer components
are polypropylene materials as well as ester materials, such as PET, commonly employed
for the preparation of synthetic fibers, in particular bicomponent fibers. No restriction
is given, however, with respect to the selection of first polymer component.
[0023] The first polymer component furthermore may be subjected to any desired kind of pretreatment,
such as grafting and/or irradiation in order to improve adhesion or bonding properties.
The first polymer component furthermore may be compounded, prior to the spinning process,
with any desired additives, such as stabilizers, coloring agents, processing aids
etc., in usual amounts.
[0024] The first polymer component and the second polymer component may be employed in any
desired ratio, depending from the desired end use of the fiber. Typical ratios are
weight ratios of from 10:90 to 90:10, such as 20:80 to 80:20 and 30:70 to 70:30, including
also weight ratios of 50:50 etc.
[0025] The fiber in accordance with the present invention may be prepared in any desired
thickness, again depending upon the desired end use. Typical thicknesses are known
to the skilled person and include in particular the range of from 0.5 to 100 denier,
such as from 1 to 50 denier.
[0026] The fibers in accordance with the present invention, after spinning, may be subjected
to any desired kind of post-treatment, such as stretching, crimping or cutting and
the fibers in accordance with the present invention in particular may be subjected
directly to a further process for preparing a non-woven fabric. However, the fibers
in accordance with the present invention also can be cut at any desired length or
may be wound up for any desired kind of post-treatment and/or storage, prior to the
further use thereof.
[0027] The present invention also provides a non-woven fabric prepared using the fiber in
accordance with the present invention. Such a non-woven fabric can be prepared in
accordance with standard techniques known to the skilled person.
[0028] With respect to the fiber and the non-woven fabric in accordance with the present
invention, the specific second polymer component as defined herein enables the preparation
of fabrics having improved values for tensile strength, compared with a non-woven
fabric prepared with the standard market product Aspun 6811A of Dow, which is widely
regarded as the best available polyethylene material for bicomponent fiber applications.
The fibers in accordance with the present invention furthermore provide the possibility
to tailor the bonding temperatures required for bonding of the fibers to produce a
non-woven fabric which provides the manufacturer of a fiber and a non-woven fabric
with a greater latitude for the bonding process, without encountering problems such
as sticking.
[0029] The specific ethylene-α-olefin copolymer to be employed in accordance with the present
invention furthermore enables problem-free spinning processes without fiber failures
due to gel particles.
[0030] In view of these advantages, the present invention also provides the use of an ethylene-α-olefin
copolymer as defined herein for the preparation of fibers, preferably bicomponent
fibers. The preferred embodiments as defined above in connection with the fiber and
the non-woven fabric also apply with respect to the use as defined herein.
[0031] The present invention finally also provides a process for preparing a fiber in accordance
with the present invention as well as a process for preparing a non-woven fabric as
defined herein. The process in accordance with the present invention comprises the
step of providing a first polymer component as defined herein and providing a second
polymer component as defined herein, melting the polymer components and extruding
the polymer components through a suitable die/spinnerette in order to combine the
two polymer components in a bicomponent fiber. Suitable process parameters and apparatuses
required therefor are known to the skilled person and reference in this respect can
be made to the Reicofil
® Bico Technology of Reifenhäuser as well as apparatuses developed and distributed
by Hills and Neumag.
[0032] Non-woven fabrics can be prepared from fibers in accordance with the present invention
by usual processes known to the skilled person, including in particular a treatment
step for bonding the fibers by suitable devices such as heated rolls or a calander.
A suitable process for preparing a non-woven fabric employing the fibers in accordance
with the present invention accordingly comprises the steps of providing fibers in
accordance with the present invention and bonding the fibers by means of a suitable
process as indicated above.
[0033] The following examples further illustrate the present invention.
Examples
[0034] Sheath/core fibers were produced employing a standard propylene homopolymer (STD
PP SB) spunbonded grade (MFR
2 25g/10min) as core component and employing either a commercially available reference
product Aspun 6811A of Dow as sheath component or an ethylene-α-olefin copolymer in
accordance with the present invention. Sheath/core fibers were produced with a weight
ratio of the two polymer components of 50:50 with a line speed of 56 m/min and other
process parameters as indicated in table 2 below. The ethylene-α-olefin copolymers
in accordance with the present invention were HDPE materials comprising 1-hexene,
having an MWD of about 4 and produced using a Ziegler-Natta catalyst. The ethylene-α-olefin
copolymers in accordance with the present invention as employed in the examples showed
MFR
2 values of 20.0, 27.0 and 38.6, respectively (E1, E2 and E3, respectively).
Table 1
|
E1 |
E2 |
E3 |
MFR (2,16kg,190°C) |
g/10min |
20,0 |
27,0 |
38,6 |
Density |
kg/m3 |
948,1 |
953,5 |
952,4 |
Comonomer |
- |
Hexene |
Hexene |
Hexene |
Comonomer content |
wt% |
2.1 |
2.0 |
2.6 |
[0035] The ethylene-α-olefin copolymers used in accordance with the present invention were
produced in a slurry process with a Z/N catalyst and tri-ethyl aluminium as cocatalyst.
Pressure was 42 bar and temperature was 95 °C, isobutane was used as diluent.
[0036] Mw, Mn, MWD: The determination of weight average molecular weight (Mw) and number average molecular
weight (Mn) and the molecular weight distribution (MWD = Mw/Mn) by size exclusion
chromatograhy (SEC): Mw, Mn and MWD (Mw/Mn) were determined with A Millipore Waters
ALC/GPC operating at 135 °C and equipped with two mixed bed and one 107 A TSK-Gel
columns (TOSOHAAS 16S) and a differential refractometer detector. The solvent 1,2,4-trichlorobezene
was applied at flow rate of 1 ml/min. The columns were calibrated with narrow molecular
weight distribution polystyrene standards and narrow and broad polypropylenes. Reference
is also made to ISO 16014.
[0037] MFR: The melt flow rates were measured according to ISO 1133 with a load of 2.16 kg at
230 °C for polypropylene and at 190 °C for polyethylene. The melt flow rate is that
quantity of polymer in grams which the test apparatus standardised to ISO 1133 extrudes
within 10 minutes at a temperature of 230 °C or 190 °C respectively, under a load
of 2.16 kg.
[0038] Density: densities are measured according to ISO 1183/D.
[0039] Comonomer content: Comonomer content is determined in a known manner based on Fourier transform infrared
spectroscopy (FTIR) determination calibrated with C13-NMR.
[0040] Trials were performed on a Reifenhäuser SMS Labline with a core-sheath configuration.
Extrusion temperatures were set to 235°C for the polypropylene component and 215°C
for the polyethylene materials.
[0041] The die temperature for both polymers was set to 235°C and the connection temperature
for the polypropylene and the polyethylene materials were identical to the extrusion
temperatures identified above. Fibers with a 2.5 denier thickness were produced and
non-woven fabrics of about 42 g/m
2 were prepared.
[0042] Mechanical parameters of the produced non-woven fabrics were tested according to
EN29073-1 and EN 29073-3. Strip measures were 50 * 200 mm. Distance between clamps
was 100 mm. Testing speed was 200 mm / min.
[0043] The results can be taken from the following table 2. The table clearly reveals that
the fibers in accordance with the present invention provide non-woven fabrics having
increased tensile strength values, compared with the comparative example employing
the reference market product. At the same time, the examples in accordance with the
present invention did not give rise to any problems during spinning, such as fiber
failure, for example, due to the occurrence of gel particles.

[0044] The examples as provided in Table 2 clearly show that, compared with the bicomponent
fibers employing Aspun 6811A as polymer 2, clear improvements with respect to tensile
strength values of the non-woven fabric, in machine direction (MD) as well as in cross
direction (CD) can be obtained only by employing an ethylene-α-olefin copolymer in
accordance with the present invention as second polymer component. In particular with
an ethylene-α-olefin copolymer having a rather high MFR
2 highly satisfactory tensile strength values can be obtained, employing a window of
about 10°C for the embossing roll temperature (127 to 136°C) showing the great latitude
provided by the fiber in accordance with the present invention. The two grades of
ethylene-α-olefin copolymer having lower MFR
2 values as tested in accordance with the present invention clearly show that also
these components enable highly satisfactory tensile strength values, again providing
a wide temperature window for the embossing temperature. The ethylene-α-olefin copolymer
with MFR
2 of 20.0, for example, enables a satisfactory bonding process with embossing roll
temperatures of from 124 to 142°C. Overall, it is therefore readily apparent hat the
present invention enables an improvement with respect to the mechanical properties
of a non-woven fabric produced using a fiber in accordance with the present invention
while, at the same time, the temperature window for the bonding process is suitably
wide providing the manufacturer with a great latitude concerning the process of forming
a non-woven fabric.
[0045] The values achieved with Aspun 6811A and given in the table are optimized with respect
to processing temperatures and speeds. They are the highest achievable with this polymer
under the chosen conditions.
1. Fiber, comprising a first polymer component and a second polymer component, wherein
the first and second polymer components differ at least with respect to one property,
and wherein the second polymer component comprises an ethylene-α-olefin copolymer
having a density of from 0.945 to 0.965 g/cm3 and a MFR2 of from 15 to 45 g/10 min.
2. Fiber in accordance with the present invention, wherein the α-olefin is 1-hexene.
3. Fiber in accordance with any of the preceding claims, wherein the ethylene-α-olefin
copolymer comprises from 1.75 to 3.0 wt% α-olefin.
4. Fiber in accordance with any one of the preceding claims, wherein the ethylene-α-olefin
copolymer has a MWD of from 3.5 to 4.5.
5. Fiber in accordance with any of the preceding claims, wherein the ethylene-α-olefin
copolymer has a density of from 0.947 to 0.955 g/cm3.
6. Fiber in accordance with any of the preceding claims, wherein the ethylene-α-olefin
copolymer has an MFR2 of 35 to 42, or from 18 to 30 g/10 min.
7. Fiber in accordance with any of the preceding claims, wherein the fiber is a bicomponent
fiber.
8. Fiber in accordance with claim 7, wherein the bicomponent fiber has a core/sheath
configuration.
9. Fiber in accordance with claim 8, wherein the second polymer component constitutes
the sheath.
10. Non-woven fabric comprising the fiber of any of claims 1 to 9.
11. Process for preparing a fiber in accordance with any of claims 1 to 9, comprising
the steps of providing the first polymer component and providing the second polymer
component, melting the first and second polymer component and extruding the first
and second polymer component through a spinnerette to produce a fiber.
12. Process for preparing a non-woven fabric in accordance with claim 10, comprising the
steps of providing a fiber in accordance with any one of claims 1 to 9 and bonding
in order to provide a non-woven fabric.
13. Use of an ethylene-α-olefin copolymer as defined in any one of claims 1 to 6 for the
preparation of a bicomponent fiber.