EP0632147B1

EP0632147B1 - Fibers suitable for the production of nonwoven fabrics having improved strength and softness characteristics

Info

Publication number: EP0632147B1
Application number: EP94109404A
Authority: EP
Inventors: Millo Branchesi; Leonardo Spagnoli; Giancarlo Braca
Original assignee: Basell North America Inc
Current assignee: Basell North America Inc
Priority date: 1993-06-17
Filing date: 1994-06-17
Publication date: 2002-03-06
Anticipated expiration: 2014-06-17
Also published as: FI942890A0; EP0632147A3; KR950000939A; JPH07166416A; IT1264840B1; EP0632147A2; FI942890L; FI942890A7; DE69430026T2; ITMI931309A0; CA2126014A1; ITMI931309A1; KR100304296B1; DE69430026D1

Description

The present invention relates to polyolefin fibers suitable for the production of nonwoven fabrics by spun-bonding process, having improved strength and softness characteristics. The present invention also relates to a process for the production of said fibers, a process to produce nonwoven fabrics by spun-bonding using said fibers, and the nonwoven fabrics obtained by said process.
The definition of "fibers" includes also products similar to fibers, such as fibrils.
Nonwoven fabrics are widely used in various applications. They are used, for example, in the preparation of articles to be utilized in the agricultural field, and for domestic and industrial "throwaway" articles. For some specific uses said fabrics must possess good softness characteristics (which depend on the flexibility index of the fiber), strength (which depends on the thermowelding strength of the fiber) and resistance to yellowing. These characteristics are particularly important in the health and medical fields.
Polyolefin fibers which can be used for the preparation of nonwoven fibers possessing good aging and yellowing resistance are already known in the art. For example, fibers with the above mentioned properties are described in published European patent application EP-A-391438, in the name of the Applicant. Said patent application describes some combinations of stabilizers which can render the fibers particularly resistant to yellowing and aging.
Published European patent application EP-A-598 224 in the name of the Applicant describes nonwoven fabrics which have, among other things, good softness and strength properties (in the examples the maximum thermowelding strength of the fibers constituting the fabrics is slightly higher than 3 N).
Now some polyolefin fibers have been found which possess a high flexibility index and thermowelding strength, besides presenting good yellowing and aging resistance. These properties allow one to obtain nonwoven fabrics which offer good softness and strength.
One embodiment of the present invention is a process for the preparation of nonwoven fabrics which comprise said fibers and present both softness and strength properties.
Another embodiment of the present invention is a process used to prepare said fibers.
Yet another embodiment of the present invention relates to the nonwoven fabrics obtained with said process.
Accordingly the present invention provides a fiber for nonwoven fabrics having a thermowelding strength at 150°C or measured according to ASTM 1682 greater than 5 N and a flexibility index higher than 800, comprising a polymer material additivated with organic phosphites and/or phosphonites, HALS and optionally phenolic antioxidants, said polymer material being selected from:
1) isotactic propylene homopolymers having an isotactic index greater than 90;
2) random copolymers of propylene with ethylene and/or a C₄-C₈ α-olefin; and
3) blends of homopolymers (1) with copolymers (2), or blends of at least one of the above mentioned homopolymers and copolymers with heterophasic propylene polymers, said heterophasic polymers comprising (by weight):
A) from 10 to 60 parts of a propylene homopolymer, or a copolymer of propylene with ethylene and/or a C₄-C₈ α-olefin, containing over 80% of propylene and having an isotactic index greater than 80 (Fraction A);
B) from 1 to 25 parts of an essentially linear semicrystalline copolymer of ethylene with a C₃-C₈ α-olefin, insoluble in xylene at ambient temperature (Fraction B); and
C) from 15 to 87 parts of a copolymer fraction of ethylene with propylene and/or a C₄-C₈ α-olefin, and optionally minor quantity of diene, said copolymer Fraction containing from 10 to 80% of ethylene and being soluble in xylene at ambient temperature (Fraction C).;

240°-320°C for polymers (1) and (2), said polymers (1) and (2) having a MFR value ranging from 5 to 25 g/10 min; and
230°-300°C for polymer blends (3), said polymer blends (3) having a MFR value ranging from 5 to 40 g/10 min.

The terms "insoluble" in the definition of component B and "soluble" in the definition of component C are to mean "essentially insoluble" or "essentially soluble", respectively; preferably these terms are to mean "totally insoluble" or "totally soluble", respectively.
The C₄-C₈ α-olefins to be used for the preparation of the copolymers which can be present in random copolymers (2), Fraction A and Fraction C are linear or branched alkenes, and are preferably selected from the following compounds: 1-butene, 1-pentene, 1-hexene, 1-octene and 4-methyl-1-pentene. The 1-butene is the preferred α-olefin. The same applies to the C₃-C₈ olefins of fraction B which additionally include propylene.
The random copolymers (2) contain a quantity of comonomer ranging from 0.05 to 20% by weight. When the quantity of comonomer exceeds 5%, said copolymers must be blended with the propylene homopolymer.
Preferably Fraction A is present in the heterophasic polymer in quantities ranging from 10 to 50 parts by weight, and is made up of a propylene homopolymer with an isotactic index preferably greater than 90, more preferably from 95 to 98, or of the copolymer defined above, preferably containing over 85%, more preferably from 90 to 99% of propylene.
Preferably Fraction B is present in the heterophasic polymer in quantities ranging from 7 to 15 parts by weight and has a crystallinity ranging from about 20 to 60%, determined by way of DSC (Differential Scanning Calorimetry). The copolymer of said fraction is preferably selected from the following types of copolymers: ethylene/propylene, containing over 55% of ethylene; ethylene/propylene/C₄-C₈ α-olefin, containing from 1 to 10% of said α-olefin and from 55% to 98%, preferably from 80 to 95%, of ethylene plus said α-olefin; ethylene/C₄-C₈ α-olefin, containing from 55% to 98%, preferably from 80 to 95%, of said α-olefin.
Preferably Fraction C is present in the heterophasic polymer in quantities ranging from 30 to 75 parts by weight, and is made up of a copolymer selected from: an ethylene/propylene copolymer containing from 15% to 70% of ethylene, preferably from 20 to 60%; an ethylene/propylene/C₄-C₈ α-olefin copolymer, containing from 1 to 10% of said α-olefin, preferably from 1 to 5%, wherein the total quantity of ethylene plus α-olefin ranges from 20 to less than 40%; an ethylene/α-olefin copolymer, containing from 20 to less than 40%, preferably from 20 to 38%, more preferably from 25 to 38%, of said α-olefin. The dienes, optionally present in the copolymers of said Fraction are present in quantities equal to or less than 10%, and are preferably selected from: butadiene, 1,4-hexadiene, 1,5-hexadiene and 2-ethylidene-5-norbornene.
The heterophasic propylene polymers are prepared either by mechanically blending components (A), (B), and (C) in the molten state, or by using a sequential polymerization process carried out in one or more steps, and using highly stereospecific Ziegler-Natta catalysts.
Examples of the heterophasic polypropylene compositions mentioned above, as well as the catalysts and polymerization processes commonly used for their preparation, are described in published European patent applications 400333 and 472946.
The blends (3) are obtained by melting and pelletizing the polymers, or by blending them without melting. In these blends, the quantity of heterophasic polymer and/or random copolymer (2) containing over 5% of comonomer preferably does not exceed 30% of the total weight of the blend.
The stabilizers which are added to the polyolefins described above are the following:
a) one or more organic phosphite and/or phosphonites, preferably in quantities ranging from 0.01 to 0.5% by weight, more preferably from 0.02 to 0.15%;
b) one or more HALS (Hindered Amine Light Stabilizers), preferably in quantities ranging from 0.005 to 0.5% by weight, more preferably from 0.01 to 0.025;
c) optionally one or more phenolic oxidants, preferably in concentrations not exceeding 0.02% by weight.
The following compounds are examples of phosphites that can be used as additives for the polyolefins of the fibers of the present invention:
tris(2,4-di-tert-butylphenyl)phosphite, marketed by CIBA GEIGY under the trademark Irgafos 168; distearyl pentaerythritol diphosphite, marketed by BORG-WARNER CHEMICAL under the trademark Weston 618; 4,4'-butylidenebis(3-methyl-6-tert-butylphenyl-di-tridecyl)phosphite, marketed by ADEKA ARGUS CHEMICAL under the trademark Mark P; tris(monononyl phenyl)phosphite; bis(2,4-di-tert-butyl)pentaerythritol diphosphite, marketed by BORG-WARNER CHEMICAL under the trademark Ultranox 626.
The preferred organic phosphonite that can be used as additive for the polyolefins of the fibers of the present invention is tetrakis(2,4-di-tert-butylphenyl)4,4-diphenylene diphosphonite, marketed by SANDOZ under the trademark Sandostab P-EPQ.
Examples of HALS that can be added to the polyolefins of the fibers of the present invention are:
poly{[6-(1,1,3,3,-tetramethylbutyl)-imine] -1,3,5-triazine-2,4-diol] [2-(tetramethylpiperidyl)amine]hexamethylene- [4- (2,2,6,6-tetramethylpiperidyl)imine} (Chimassorb 944), Chimassorb 905, bis(2,2,6,6,-tetramethyl-4-piperidyl)sebacate (Tinuvin 770), Tinuvin 992, poly(N-β-hydroxymethyl-2,2,6,6,-tetramethyl-4-hydroxy-piperidyl succinate (Tinuvin 622), Tinuvin 144, Spinuvex A36, marketed by CIBA-GEIGY; Cyasorb UV 3346 marketed by AMERICAN CYANAMIDE.
Examples of preferred phenolic antioxidants to be used as additives in the polyolefins making up the fibers of the present invention are: tris(4-t-butyl-3-hydroxy-2,6-dimethylbenzyl)-s-triazine-2-4-6-(1H,3H,5H)-trione, sold by AMERICAN CYANAMID under the Cyanox 1790 trademark; calcium bi[monoethyl(3,5-di-tert-butyl-4-hydroxybenzyl)phosphonate] ; 1,3,5-tris (3,5-di-tert-butyl-4-hydroxybenzyl)-s-triazine-2,4,6(1H,3H,5H)trione; 1,3,5-trimethyl-2,4,6-tris (3,5-di-tert-butyl-4-hydroxybenzyl)benzene; pentaerythrityltetrakis[3-(3,5-di-tert-butyl-4-hydroxy-phenyl)propionate], sold by CIBA-GEIGY under the following trademarks: Irganox 1425, Irganox 3114; Irganox 1330; Irganox 1010; 2,6-dimethyl-3-hydroxy-4-tert-butyl benzyl abietate.
Besides the above mentioned stabilizers, one can add to the olefins which are consequently converted into the fibers of the present invention, the usual additives, such as pigments, opacifiers, fillers, UV stabilizers, and flame retardants.
The polymers (containing the necessary additives) which are converted in fibers according to the present invention have a melt flow rate (MFR) ranging from 5 to 40 g/10 min. In particular, the polymers of points (1) and (2) have a MFR preferably ranging from 5 to 25 g/10 min. The MFR is measured according to ASTM D 1238, condition L. High MFR values are obtained directly in polymerization, or by controlled radical visbreaking.
The process of controlled radical visbreaking is carried out using, for example, some organic peroxides, such as 2,5-dimethyl-2,5-di(tert-butylperoxy)hexane, during the pelletizing phase or directly in the fiber extrusion step.
The molecular weight distribution of the polymers making up the fibers of the present invention, expressed as Mw/Mn, ranges from 3 to 6, preferably from 3.5 to 4.5.
The polymers to be converted into the fibers of the present invention can be in the form of pellets or nonextruded particles, such as flakes, or spheroidal particles with a diameter ranging from 0.5 to 4.5 mm. Said particles are covered or impregnated, at least on the surface, with the stabilizers (or additives in general) mentioned above, and/or peroxides, if the latter should be necessary to obtain a molecular weight distribution within the range mentioned above.
Additives such as opacifiers, fillers and pigments can also be added while the fiber is being spun.
In order to obtain fibers which present both a high flexibility index (which is important to ensure nonwoven fabrics with good softness characteristics) and a high thermowelding strength (which is important to ensure nonwoven fabrics with good strength characteristics), the spinning process must be carried out at a die temperature ranging from 240°C to 320°C, and a hole flow-rate from 0.25 to 0.4 g/min/hole for polymers (1) and (2) having MFR ranging from 5 to 25 g/10 min., or it can be carried out at a die temperature ranging from 230°C to 300°C and a hole flow-rate from 0.25 to 0.4 g/min/hole for polymer blends (3) having a MFR ranging from 5 to 40 g/10 min. The fibers thus obtained have a flexibility index higher than 800 and a thermowelding strength at 150°C or measured according to ASTM 1682 higher than 5 N.
As previously mentioned, the process for the production of the fibers is also an embodiment of the present invention. The process for the preparation of fibers according to the present invention is carried out by using extruders equipped with a die and without subjecting the fibers to a subsequent drawing. The die is characterized by a real or equivalent output hole diameter of less than 0.5 mm, preferably ranging from 0.2 to 0.48 mm. By "output diameter of the holes" is meant the diameter of the holes measured at the external surface of the die, i.e. on the front face of the die from which the fibers exit. Inside the thickness of the die, the diameter of the holes can be different from the one at the output. Moreover, the "equivalent output diameter" definition applies to those cases where the hole shape is not circular. In these cases, for the purposes of the present invention one considers the diameter of an ideal circle having one area equal to the area of the output hole, which corresponds to the above mentioned equivalent diameter. The temperature of both the extruder and the die during the processing of the polymers ranges from 230°C to 320°C; in particular it is best to operate at temperatures ranging from 240°C to 320°C when the fibers are obtained from polymers (1) and (2), while when using the polymer blends (3) the temperatures can range from 230°C to 320°C, preferably from 260°C to 300°C.
The dimensions of the fibers of the present invention if they are to be used for the preparation of nonwoven fabrics, have a count ranging from 1 to 10 dtex. In order to obtain said count, the hole flow-rate must range from 0.1 to 0.6 g/min/hole, preferably from 0.25 to 0.45 g/min/hole.
Tests were carried out on the polymer material and the fibers of the present invention to evaluate their characteristics and properties; the methods used for said tests are described below.
Melt Flow Rate (MFR): according to ASTM-D 1238, condition L.
Weight average molecular weight (Mw) : GPC (Gel Permeation Chromatography) in ortho-dichlorobenzol at 150°C.
Number average molecular weight (Mn): GPC (Gel Permeation Chromatography) in ortho-dichlorobenzol at 150°C.
Thermowelding strength: in order to evaluate the thermoweldability of staple fibers, one manufactures a nonwoven fabric with the fiber being tested by way of calendering under set conditions. Then one measures the strength needed to tear said nonwoven fabric when the stress is applied in directions which are both parallel and transversal to that of the calendering.
The thermoweldability index (ITS) is defined as follows: ITS = (TM • TC)1/2 where TM and TC represent the tear strengths of the nonwoven fabric measured according to ASTM 1682, for the parallel and transversal directions respectively, and expressed in Newton.
The value of the strength determined in this fashion is considered a measure of the capability of the fibers to be thermowelded.
The result obtained, however, is influenced substantially by the characteristics regarding the finishing of the fibers (crimping, surface finishing, thermosetting, etc.), and the conditions under which the card web fed to the calender is prepared. To avoid these inconveniences and obtain a more direct evaluation of the thermoweldability characteristics of the fibers, a method has been perfected which will be described below in details.
Some specimens were prepared from a 400 tex roving (method ASTM D 1577-7) 0.4 meter long, made up of continuous fibers.
After the roving was twisted eighty times, the two extremities were united, thus obtaining a product where the two halves of the roving are entwined as in a rope. On said specimen one produced one or more thermowelded areas by means of a thermowelding machine commonly used in a laboratory to test the thermoweldability of film.
A dynamometer was used to measure the average strength required to separate the two halves of the roving at each thermowelded area. The result, expressed in Newton, was obtained by averaging out at least eight measurements. The welding machine used was the Brugger HSC-ETK. The clamping force of the welding plates is 800 N; the clamping time was 1 second, and the temperature of the plates was 150°C.

Flexibility index

The flexibility of the filaments is represented by an index defined in the following manner: IF= (1/W) • 100 where W is the minimum quantity in grams of a twisted roving specimen which when tested with the Clarks Softness-Stiffness Tester changes the direction of the flexion when the plane, on which the specimen is fixed in a perpendicular position, rotates alternatively of +/- 45° with respect to the horizontal plane.
The specimen has the same characteristics as the one used to measure thermowelding strength and is prepared using the same process described above.

Resistance to yellowing

Norm ISO/TC 38/SC1 at 60°C was applied to measure the resistance of the fibers to fading caused by gases produced by hydrocarbon combustion. In particular, the resistance to yellowing value referred to in the examples concerns the variation caused by gas fading measured at 60°C after 4 cycles.

Filaments' count

Measured according to ASTM D 1577-79.
The following examples are given in order to illustrate and not limit the present invention.

Example 1 (no longer comprised by the claim)

10 Kg of polypropylene pellets having an isotactic index of 96.5 (calculated as residue insoluble in xylene at 25°C), MFR of 35 g/10 min., Mw/Mn of 4.2, and containing 1000 ppm of the phosphite Irgafos 168 and 200 ppm of the HALS Chimassorb 944, have been prepared by extrusion at 220°C. The peroxide Lupersol 101 (marketed by Lucidol, Pennwalt Corp., USA) has been used to visbreak the polypropylene to a Mw/Mn of 4,2. The polypropylene pellets are spun using a spinning apparatus having the following characteristics:

extruder equipped with a screw having a 25 mm diameter, a length/diameter ratio of 25 and a capacity from 1 to 6 Kg/h;
die with 40 holes, said holes having a diameter of 0.4 mm and a length/diameter ratio of 5;
metering pump;
air quenching system at temperature from 18 to 20°C;
mechanical winding device with a velocity of up to 600 m/min, or air jet.

The spinning conditions and characteristics of the filaments obtained in this manner are shown on Table 1.

Example 2

Flake polypropylene, having a MFR of 2 g/10 min. and additivated with the same additives listed in Example 1, is visbroken with Lupersol until it reaches a MFR of 12 g/10 min, and a Mw/Mn of 4. 10 kg of said polymer are then subjected to spinning in the spinning apparatus described in Example 1.
The spinning conditions and characteristics of the filaments obtained in this manner are shown on Table 1.

Example 3

A polymer blend comprising: 90 parts by weight of polypropylene having a MFR of 5 g/10 min., and 10 parts by weight of heterophasic polymer having a MFR of 5 g/10 min, intrinsic viscosity of 2.6 dl/g, and the following composition: 55% by weight of ethylene/propylene random copolymer (containing 2.5% of ethylene), and 45% by weight of ethylene/propylene rubber at a 60/40 ratio is used.
The polymer blend, additivated with the same additives of Example 1 and visbroken with Lupersol 101 until a MFR of 35 g/10 min. is reached, is subjected to spinning, under the conditions listed in Table 1, in the spinning apparatus described in Example 1.
The properties of the fibers obtained are reported in Table 1.

Comparative example 1 (1c)

10 kg of polypropylene polymer flakes with an isotactic index of 96.5, MFR of 5 g/10 min., and Mw/Mn of 6, additivated with the same stabilizers as in Example 1, in the same quantities shown therein, and visbroken with Lupersol 101, used in such quantities as to visbreak the polymer to a MFR of 35 g/10 min (Mw/Mn equal to 3.8), are extruded at 220°C. The pellets obtained have been spun in a spinning apparatus having the same characteristics described in Example 1.
The spinning conditions and properties of the fiber obtained are shown on Table 1.

Claims

A fiber for nonwoven fabrics having a thermowelding strength at 150°C or measured according to ASTM 1682 higher than 5 N and a flexibility index greater than 800, comprising a polymer material additivated with organic phosphites and/or phosphonites, HALS and optionally with phenolic antioxidants, said polymer material being selected from:

1) isotactic propylene homopolymers having an isotactic index greater than 90;

2) random copolymers of propylene with ethylene and/or a C₄-C₈ α-olefin; and

3) blends of polymers (1) with copolymers (2), or blends of at least one of said homopolymers and copolymers with heterophasic propylene polymers, said heterophasic polymers comprising (by weight):

A) from 10 to 60 parts of polypropylene having an isotactic index greater than 80, or a copolymer of propylene with ethylene and/or a C₄-C₈ α-olefin containing over 80% of propylene and having an isotactic index greater than 80;

B) from 1 to 25 parts of an essentially linear semicrystalline copolymer of ethylene with a C₃-C₈ α-olefin, insoluble in xylene at ambient temperature; and

C) from 15 to 87 parts of a copolymer fraction of ethylene with propylene and/or a C₄-C₈ α-olefin, and optionally minor quantities of diene, said copolymer Fraction containing from 10 to 80% of ethylene and being soluble in xylene at ambient temperature;

said fiber being obtained by a spinning process operating with a real or equivalent output hole diameter of less than 0.5 mm and with a hole flow-rate ranging from 0.25 to 0.4 g/min/hole and in the absence of a drawing step; said process being carried out at a die temperature selected from:

240°-320°C for polymers (1) and (2), said polymers (1) and (2) having a MFR value ranging from 5 to 25 g/10 min ; and

230°-300°C for polymer blends (3), said polymer blends (3) having a MFR value ranging from 5 to 40 g/10 min.
The fiber of claim 1, obtained operating at a spinning temperature ranging from 260°C to 300°C using polymer blends (3).
The fiber of claim 1, comprising a blend of a homopolymer (1) and a heterophasic propylene polymer or random propylene copolymer containing more than 5% by weight of comonomer, said heterophasic propylene polymer or random propylene copolymer being in quantities greater than 30% by weight of the blend total weight.
The fiber of claim 1, containing from 0.01 to 0.5% by weight of one of more organic phosphites and/or phosphonites, from 0.005 to 0.5% by weight of one or more HALS, and not more than 0.02% by weight of one or more phenolic antioxidants.
A process for producing polyolefin fibers having a thermowelding strength at 150°C or measured according to ASTM 1682 higher than 5 N and a flexibility index greater than 800, wherein a polymer material additivated with organic phosphites and/or phosphonites, HALS and optionally phenolic antioxidants is subjected to spinning with a real or equivalent output hole diameter of less than 0.5 mm and a hole flow-rate from 0.25 to 0.4 g/min/hole and in the absence of a drawing step; said process being carried out at a die temperature selected from:

240°-320°C for polymers (1) and (2) having a MFR value ranging from 5 to 25 g/10 min; and

230°-300°C for polymer blends (3) having a MFR value ranging from 5 to 40 g/10 min, wherein the said polymer materials (1) to (3) are defined as follows:

1) isotactic propylene homopolymer having an isotactic index greater than 90;

2) random copolymers of propylene with ethylene and/or a C₄-C₈ α-olefin; and

3) blends of polymers (1) with copolymers (2), or blends of at least one of said homopolymers and copolymers with heterophasic propylene polymers, said heterophasic polymers comprising (by weight):

A) from 10 to 60 parts of polypropylene having an isotactic index greater than 80, or a copolymer of propylene with ethylene and or a C₄-C₈ α-olefin containing over 80% of propylene and having an isotactic index greater than 80;

B) from 1 to 25 parts of an essentially linear semicrystalline copolymer of ethylene with a C₃-C₈ α-olefin, insoluble in xylene at ambient temperature; and

C) from 15 to 87 parts of a copolymer fraction of ethylene with propylene and/or a C₄-C₈ α-olefin and optionally minor quantities of diene, said copolymer fraction, containing from 10 to 80% of ethylene and being soluble in xylene at ambient temperature.
A process for the production of nonwoven fabrics, wherein the fibers of claim 1 are subjected to spun-bonding.
Nonwoven fabrics obtained by the process of claim 6.