ELASTIC NONWOVEN SHEET
20230141900 · 2023-05-11
Assignee
Inventors
Cpc classification
B32B2262/16
PERFORMING OPERATIONS; TRANSPORTING
C08L23/16
CHEMISTRY; METALLURGY
B32B5/267
PERFORMING OPERATIONS; TRANSPORTING
B32B2262/14
PERFORMING OPERATIONS; TRANSPORTING
A61L15/24
HUMAN NECESSITIES
B32B2307/718
PERFORMING OPERATIONS; TRANSPORTING
B32B2307/54
PERFORMING OPERATIONS; TRANSPORTING
D04H3/16
TEXTILES; PAPER
B32B2250/20
PERFORMING OPERATIONS; TRANSPORTING
A61F13/15731
HUMAN NECESSITIES
B32B5/271
PERFORMING OPERATIONS; TRANSPORTING
B32B2250/40
PERFORMING OPERATIONS; TRANSPORTING
International classification
A61F13/15
HUMAN NECESSITIES
A61L15/24
HUMAN NECESSITIES
Abstract
The invention relates to elastically stretchable nonwoven sheets comprising an elastically stretchable nonwoven layer and a stretchable facing layer, and an in-line method for making such sheets.
Claims
1. An elastically stretchable nonwoven sheet comprising at least two layers of nonwoven materials, wherein one layer is an elastically stretchable nonwoven comprising spunbonded elastic fibers formed from a thermoplastic elastomer polymer material, wherein one layer is a stretchable facing layer comprising spunbonded crimped multicomponent fibers, and wherein adjacent layers are bonded together by embossed bonding points, wherein
at least one of the components of the crimped multicomponent fibers is a propylene-α-olefin copolymer material.
2. The sheet according to claim 1, wherein the elongation at break of the sheet in machine direction is greater 150% when measured according to WSP 100.4.
3. The sheet according to claim 1, wherein permanent deformation in machine direction, as measured according to ASTM D5459, after the first cycle is less than 15%.
4. The sheet according to claim 1, wherein the area between the increasing and decreasing machine-directional stress-strain curves of a hysteresis plot in a second cycle of an ASTM D5459 test, as expressed in the relative size of the area between the curves (A) in relation to the overall area under the initial increasing curve (A+B), expressed in% [A/(A+B)x100] is lower than 40%.
5. The sheet according to claim 1, wherein a further component of the crimped multicomponent fibers is a polypropylene homopolymer material.
6. The sheet according to claim 5, wherein the propylene-α-olefin copolymer is a poly(propylene-ethylene) random copolymer.
7. The sheet according to claim 1, wherein the molecular weight distribution of the propylene-α-olefin copolymer is broader than the molecular weight distribution of the other component(s) of the crimped multicomponent fibers.
8. The sheet according to claim 1, wherein the crimped multicomponent fibers are bicomponent fibers.
9. The sheet according to claim 1, wherein the thermoplastic elastomer polymer material forming for the elastic fibers is a thermoplastic polyolefin elastomer.
10. The sheet according to claim 1, wherein the sheet comprises a sandwich structure of the elastically stretchable nonwoven between at least one facing layer on either side thereof .
11. The sheet according to claim 1, wherein basis weight of each facing layer is between 5-40 g/m.sup.2 and/or wherein the basis weight of the elastic layer is between 10-140 g/m.sup.2.
12. A method for manufacturing an elastically stretchable nonwoven sheet according to claim 1, the method comprising the following in-line steps: (a1) spinning crimped multicomponent fibers, wherein at least one of the components of the crimped multicomponent fibers is a propylene-α-olefin copolymer, and laying them onto a moving spinbelt to form a web; (a2) spinning elastic fibers formed from a thermoplastic elastomer polymer material and laying them onto the surface of the web formed in step (a1) to form another web; (a3) optionally, spinning crimped multicomponent fibers, wherein at least one of the components of the crimped multicomponent fibers is a propylene-α-olefin copolymer, and laying them onto the surface of the web formed in step (a2) to form another web; (b) bonding the adjacent webs to form the elastically stretchable spunbonded nonwoven sheet.
13. The method of claim 12, further comprising an in-line or off-line step (c) of machine-directionally pre-stretching the sheet.
14. The method of claim 13, wherein, during step (c), the sheet is machine-directionally pre-stretched by 40-160% of its original dimension.
15. Use of an elastically stretchable nonwoven sheet according to claim 1 in the manufacture of hygiene articles .
16. The sheet according to claim 1, wherein permanent deformation in machine direction, as measured according to ASTM D5459, after the first cycle is less than 10%.
17. The sheet according to claim 1, wherein the area between the increasing and decreasing machine-directional stress-strain curves of a hysteresis plot in a second cycle of an ASTM D5459 test, as expressed in the relative size of the area between the curves (A) in relation to the overall area under the initial increasing curve (A+B), expressed in% [A/(A+B)x100] is lower than 30%.
18. The sheet according to claim 1, wherein the crimped multicomponent fibers are bicomponent fibers that are side-by-side bicomponent fibers.
19. The sheet according to claim 1, wherein the thermoplastic elastomer polymer material forming for the elastic fibers is a thermoplastic polyolefin elastomer comprising propylene-α-olefin copolymers.
20. The sheet according to claim 1, wherein the elongation at break of the sheet in machine direction is greater 200% when measured according to WSP 100.4.
Description
[0046] Further details and advantages of the invention will become apparent from the figures and examples described in the following. The figures show:
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[0059] An exemplary machine setup for making an elastically stretchable nonwoven sheet 100 according to the invention is shown in
[0060] The setup comprises a conveyor belt 10 and three spunbonding machines 20, 30 and 40 arranged in line on the conveyor belt.
[0061] In each of the spunbonding machines, a molten thermoplastic polymer is extruded through the holes of a die. The extruded fiber strands are then quenched and drawn / stretched to form endless fibers, which are then laid onto the conveyor belt 10 or a web that has been previously deposited thereon.
[0062] The first spunbonding machine 20 deposits a web of crimped bicomponent fibers on the conveyor belt 10. The two polymer feeds are symbolized at the top of the first spunbonding machine 20. The middle spunbonding machine 30 deposits a web of fibers formed from a thermoplastic elastomer on the previously formed web. The last spunbonding machine 40 deposits another web of again crimped bicomponent fibers on the elastic fiber web. Each of the spunbonding machines 20 and 40 is followed by a pair of pre-compaction rollers 21 and 41, respectively, for pre-compacting the respective webs.
[0063] The pre-compacted web is then calendered in a calendering unit 50 comprising a pair of counter-rotating embossing rollers 51, 52 to form a nonwoven sheet. The calendering is followed by an activation step in activation unit 60, which comprises a pair of counter-rotating activation rollers 61, 62 whose surfaces comprise interlocking structural elements, as described below in more detail. At the end of the overall in-line process, the product sheet is collected on the product roll 70.
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[0066] Even without being activated, using a combination of a polypropylene homopolymer with a relatively narrow molecular weight distribution and an ethylene-propylene random copolymer with a relatively broader molecular weight distribution in crimped bicomponent fibers has proven to deliver sheets that can be stretched without breaking in machine direction to a significant extent, in embodiments up to 300%. This is sufficient to meet any industry standard and to match the high elongation properties of an elastic nonwoven layer as used in the inventive sheets, which can in embodiments be elastically stretched for 400 to 500%.
[0067] The advantageous properties of the inventive sheets are demonstrated in the following examples.
[0068] A number of spunbonded facing layers using side-by-side bicomponent crimped fibers were prepared using the materials as specified below.
TABLE-US-00001 Materials Used Type Polymer 1 Polymer 2 Ratio Ex. 1 (comp.) PP/PP 511A 511A (60%) / HP522N (40%) 70/30 Ex. 2 PP/CoPP 511A RP248R 50/50 Ex. 3 PP/CoPP 511A QR674K 50/50
[0069] The 511A polymer is a polypropylene homopolymer from the company Sabic with a narrow polymer weight distribution (M.sub.w/M.sub.n is 3.8), a MFR of 25 g/10 min and a T.sub.m of 161° C.
[0070] The HP552N polymer is a polypropylene homopolymer from the company LyondellBasell with a broad polymer weight distribution (M.sub.w/M.sub.n is 6.8), a MFR of 13 g/10 min and a T.sub.m of 161° C.
[0071] The RP248R polymer is an ethylene-propylene random copolymer from the company LyondellBasell with an MFR of 30 g/10 min, a medium molecular weight distribution (M.sub.w/M.sub.n is 5.2) and a T.sub.m of 148° C. It further contains a clarifier and a slip agent.
[0072] The QR674K polymer is an ethylene-propylene random copolymer from the company Sabic with an MFR of 40 g/10 min, a broad molecular weight distribution (M.sub.w/M.sub.n is 8.5) and a T.sub.m of 150° C. It also further contains a clarifier and a slip agent.
[0073] The melt flow rates (MFR) as used herein are to be understood as having been determined according to ISO 1133 with conditions being 230° C. and 2.16 kg.
[0074] The melting temperatures (T.sub.m) as used herein are to be understood as having been determined with DSC according to ISO 11357-3.
[0075] The values for molecular weight averages (M.sub.w and M.sub.n) and resulting values for molecular weight distribution (MWD, M.sub.w/M.sub.n) as used herein are to be understood as having been determined by GPC according to ISO 16014-1:2003, ISO 16014-2:2003, ISO 16014-4:2003 and ASTM D 6474-12 using the following formulae:
[0076] For a constant elution volume interval ΔV.sub.i, where A.sub.i, and M.sub.i are the chromatographic peak slice area and polyolefin molecular weight (MW), respectively associated with the elution volume, V.sub.i, where N is equal to the number of data points obtained from the chromatogram between the integration limits.
[0077] A high temperature GPC instrument, equipped with either infrared (IR) detector (IR4 or IR5 from PolymerChar (Valencia, Spain) or differential refractometer (RI) from Agilent Technologies, equipped with 3 × Agilent-PLgel Olexis and 1x Agilent-PLgel Olexis Guard columns was used. As the solvent and mobile phase 1,2,4-trichlorobenzene (TCB) stabilized with 250 mg/L 2,6-Di tert butyl-4-methyl-phenol) was used. The chromatographic system was operated at 160° C. and at a constant flow rate of 1 mL/min. 200 .Math.L of sample solution was injected per analysis. Data collection was performed using either Agilent Cirrus software version 3.3 or PolymerChar GPC-IR control software.
[0078] The column set was calibrated using universal calibration (according to ISO 16014-2:2003) with 19 narrow MWD polystyrene (PS) standards in the range of 0.5 kg/mol to 11 500 kg/mol. The PS standards were dissolved at room temperature over several hours. The conversion of the polystyrene peak molecular weight to polyolefin molecular weights is accomplished by using the Mark Houwink equation and the following Mark Houwink constants: [0079] K.sub.PS = 19 × 10.sup.-3 mL/g, a.sub.PS = 0.655 [0080] K.sub.PE = 39 × 10.sup.-3 mL/g, a.sub.PE = 0.725 [0081] K.sub.PP = 19 × 10.sup.-3 mL/g, a.sub.PP = 0.725
[0082] A third order polynomial fit was used to fit the calibration data.
[0083] All samples were prepared in the concentration range of 0.5 -1 mg/ml and dissolved at 160° C. for 2.5 hours.
[0084] Table 2 below shows properties that have been obtained for isolated 20 gsm spunbond facing sheets that have been obtained from these materials.
TABLE-US-00002 Properties obtained: Basis weight (gsm) Thickness* (mm) MD tensile at break** (N/50mm) Ex. 1 19.0 0.78 9.9 Ex. 2 18.6 0.61 14.3 Ex. 3 19.9 0.46 12.5
TABLE-US-00003 Properties obtained: MD elongation at break** (%) CD tensile at break** (N/50mm) CD elongation at break** (%) Ex. 1 167 6.3 199 Ex. 2 188 9.7 210 Ex. 3 270 8.2 278 *Determined according to WSP120.6 **Determined according to WSP 100.4
[0085] Notably none of the samples have even been activated in a mill as shown in
[0086] Example 1 is a comparative example. Examples 2-3 are inventive examples. The MD tensile (stress-strain) curves of the samples of comparative Examples 1-3 are shown in
[0087] As apparent from the values in Table 2 and the curves in
[0088] Next, as Example 4, three inventive sheets (Samples 4-1, 4-2 and 4-3) comprising an elastic spunbonded layer sandwiched between two inventively configured facing layers are manufactured on a line as shown in
TABLE-US-00004 Materials used / configuration in Example 4: Type Polymer 1 Polymer 2 Ratio Basis weight (gsm) 4-1 | 4-2 | 4-3 Facing layer 1 PP/CoPP 511A QR674K 50/50 20 | 15 | 10 Elastic layer Th-El. Vistamax 7050BF 40 | 30 | 20 Facing layer 2 PP/CoPP 511A QR674K 50/50 20 | 15 | 10
[0089] Both facing layers of the sheet of Sample 4-1 correspond to the facing layers as investigated in an isolated manner in Example 3. The bonding pattern was as described above for the isolated facing layers.
[0090] The elastic layer was made from a single commercially available TPE-o material Vistamaxx™ 7050FL from ExxonMobil, which is a propylene-based thermoplastic elastomer copolymer with an ethylene content of 13 wt.-% and a melt flow rate of 45 g/10 min. The bonding pattern, again, was as described above.
[0091] Table 4 below shows properties that have been obtained for the three samples of Example 4.
TABLE-US-00005 Properties obtained: Basis weight (gsm) Thickness* (mm) MD tensile at break** (N/50mm) Sample 4-1 77.8 0.78 30.5 Sample 4-2 63.2 0.68 24.1 Sample 4-3 44.8 0.56 18.7
TABLE-US-00006 Properties obtained: MD elongation at break** (%) CD tensile at break** (N/50mm) CD elongation at break** (%) Sample 4-1 249 20.8 321 Sample 4-2 203 16.6 270 Sample 4-3 192 7.5 274 *Determined according to WSP120.6 **Determined according to WSP 100.4
[0092] As a variant to Example 4, in another Example 5, the same materials as in Example 4 were produced, with the difference that they were machine-directionally pre-stretched and activated in an activation unit 60 as shown in
[0093] Table 5 below shows properties that have been obtained for the three samples of Example 5.
TABLE-US-00007 Properties obtained: Basis weight (gsm) Thickness* (mm) MD tensile at break** (N/50mm) Sample 5-1 76.8 0.88 28.3 Sample 5-2 61.2 0.75 26.3 Sample 5-3 42.3 0.60 17.2
TABLE-US-00008 Properties obtained: MD elongation at break** (%) CD tensile at break** (N/50mm) CD elongation at break** (%) Sample 5-1 209 12.7 295 Sample 5-2 202 11.2 346 Sample 5-3 188 6.0 325 *Determined according to WSP120.6 **Determined according to WSP 100.4
[0094] In addition to the inventive Examples 4 and 5, as Example 6, the isolated elastic layer of Example 4, sample 4-1 was also spun and investigated.
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[0097] The curves shown in
[0098] A further important parameter for the elastic materials herein is their permanent deformation as determined according to ASTM D5459. Permanent deformation is the increase in length, expressed as a% of the original length, by which an elastic material fails to return to the original length after subjected to the extensions prescribed in the test procedure in ASTM D5459. The lower the% of permanent deformation, the better is the elasticity property of the elastic material.
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[0100] Another important parameter is the area between the increasing and decreasing stress-strain curves of a hysteresis plot in a second cycle of an ASTM D5459 test, as expressed in the relative size of the area between the curves (A) in relation to the overall area under the initial increasing curve (A+B), expressed in% [A/(A+B)×100]. It is to calculate the% of the energy dissipated due to internal friction. When the plots during loading and unloading do not coincide, as usually observed in real life materials, this means that a certain amount of energy is lost. The lower the%, the better the elastic property of the material.
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