Continuous fiber nonwoven fabric
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example 1
[0053]A propylene polymer used was a propylene homopolymer (PP-1) having a MFR at 230° C. under 2160 g load of 24 g / 10 min [Achieve 3854 manufactured by Exxon Mobil Chemical, Mw / Mn: 2.3, Mz / Mw: 1.8, melting point (Tm): 148° C., produced with metallocene catalyst]. The propylene homopolymer was molten in an extruder (screw diameter: 75 mm) at a shaping temperature of 210° C. The molten polymer was spun with use of a nonwoven fabric manufacturing apparatus (a spunbonding apparatus, 320 mm in length perpendicular to the machine direction on a collecting surface) as illustrated in FIG. 3 which had a spinneret having nozzle pitches 4.5 mm in vertical direction and 4.0 mm in horizontal direction and orifices as illustrated in FIG. 1 capable of giving a fiber cross section as shown in FIG. 2, at a throughput of 0.6 g / min per orifice and a spinning rate of 2550 m / min. The fibers were cooled with 25° C. cooling air and deposited on a collecting belt. The web was thermally pressure treated wi...
example 2
[0056]A propylene polymer used was a propylene homopolymer (PP-2) having a MFR at 230° C. under 2160 g load of 65 g / 10 min [Mw / Mn: 2.6, Mz / Mw: 1.7, melting point (Tm): 155° C., produced with metallocene catalyst]. The propylene homopolymer was molten in an extruder (screw diameter: 75 mm) at a shaping temperature of 190° C.
[0057]The molten polymer was spun with use of a nonwoven fabric manufacturing apparatus (a spunbonding apparatus, 320 mm in length perpendicular to the machine direction on a collecting surface) as illustrated in FIG. 3 which had a spinneret having nozzle pitches 4.5 mm in vertical direction and 4.0 mm in horizontal direction and orifices as illustrated in FIG. 1 capable of giving a fiber cross section as shown in FIG. 2, at a throughput of 0.6 g / min per orifice and a filament velocity of 3158 m / min. The fibers were cooled with 25° C. cooling air and deposited on a collecting belt. The web was thermally pressure treated with an embossing roll (emboss area percenta...
example 3
[0059]A propylene polymer used was a propylene homopolymer (PP-3) having a MFR at 230° C. under 2160 g load of 65 g / 10 min [Mw / Mn: 2.8, Mz / Mw: 1.8, melting point (Tm): 155° C., produced with metallocene catalyst]. The propylene homopolymer was molten in an extruder (screw diameter: 75 mm) at a shaping temperature of 190° C. The molten polymer was spun with use of a nonwoven fabric manufacturing apparatus (a spunbonding apparatus, 320 mm in length perpendicular to the machine direction on a collecting surface) as illustrated in FIG. 3 which had a spinneret having nozzle pitches 4.5 mm in vertical direction and 4.0 mm in horizontal direction and orifices as illustrated in FIG. 1 capable of giving a fiber cross section as shown in FIG. 2, at a throughput of 0.6 g / min per orifice and a filament velocity of 2769 m / min. The fibers were cooled with 25° C. cooling air and deposited on a collecting belt. The web was thermally pressure treated with an embossing roll (emboss area percentage: 2...
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