Soft extensible nonwoven webs containing fibers with high melt flow rates
a nonwoven web and high melt flow technology, applied in the field of soft extensible nonwoven webs, can solve the problems of significant challenge in the production of low denier fibers with high elongation, and achieve the effect of high extensibility, enabling the formation of nonwoven webs, and high extensibility
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example 1
[0048] This example demonstrates synergistic properties resulting from melt spinning a blend of a conventional spunbond grade polypropylene and a high melt flow rate polypropylene. Specifically, a 50:50 blend by weight of the polypropylenes from Comparative Example 1 and Comparative Example 2 is spun and bonded into nonwoven handsheets. The blend is pre-compounded in a twin-screw extruder prior to spinning. Table 1 shows the average strain at peak load for the handsheets made from the blend (1) are higher than that for either of the individual constituents (C1, C2), indicating synergistic elongation behavior.
TABLE 1Handsheets Made From Monocomponent Fibers - Neat PolypropyleneResins and a High MFR / Low MFR Polypropylene BlendSTRAIN ATEXAM-MFRPEAK LOADEXTENSIONPLE #RESIN(g / 10 min)(%)RATIOC1Profax PH8353572—C2Valtec HH44140098—150% Profax1181682.3PH835 50%Valtec HH441
[0049] The melt flow rate of a blend is calculated using the logarithmic additivity rule, such as described by Abraham...
example 2
[0052] This example illustrates the synergistic properties resulting from melt spinning a blend of a high melt flow rate polypropylene and a polyolefin copolymer. Specifically, an 80:20 blend by weight of the polypropylene from Comparative Example 2 and the polyolefin copolymer from Comparative Example 3 is spun and bonded into nonwoven handsheets. The blend is pre-compounded in a twin-screw extruder prior to spinning. Table 2 shows the average strain at peak load for the handsheets made from the blend (2) are higher than that for either of the individual constituents (C2, C3), indicating synergistic elongation behavior.
TABLE 2Handsheets Made From Monocomponent Fibers - Neat Polypropyleneand Polyolefin Copolymer Resins and Polypropylene / PolyolefinCopolymer BlendsSTRAIN ATEXAM-MFRPEAK LOADEXTENSIONPLE #RESIN(g / 10 min)(%)RATIOC1Profax PH8353572—C2Valtec HH44140098—C3Adflex Z104S25120—C480% Profax33880.7PH835 20%Adflex Z104S280% Valtec2301601.3HH441 20%Adflex Z104S
[0053] The melt flo...
example 3
[0055] This example demonstrates synergistic properties resulting from melt spinning a blend of a conventional spunbond grade polypropylene and a high melt flow rate polypropylene. Fibers of the present invention are prepared from a pre-compounded blend of 50 wt % ProFax PH835 and 50 wt % Valtec HH441 (400 MFR polypropylene resin available from Basell Polyolefins Company, Wilmington, Del.) at a mass throughput of 0.3 grams per hole per minute on a pilot-scale spunbond nonwoven line. Unbonded fiber bundles are collected for single fiber property evaluation. Table 3 shows the resultant diameters and average strain at break of the fibers. At equivalent or even at smaller diameters, fibers prepared from the blend of the present invention exhibit higher extensibility than fibers prepared from the neat 35 MFR polypropylene resin (C5).
TABLE 3Monocomponent Fiber Data - Neat Polypropylene Resin anda High MFR / Low MFR Polypropylene BlendDiameterStrain atExample #Resin(microns)Break (%)C5ProF...
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