Composite spinneret and method of manufacturing composite fiber
A composite spinneret and polymer technology, applied in spinneret assemblies, fiber processing, textiles and papermaking, etc., can solve the problems of not being able to reach the nanometer level, the spacing between holes becomes larger, and the equipment cost is large, and it can prevent confluence. , the effect of high dimensional stability
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[0268] [Example 1]
[0269] Polyethylene terephthalate (PET melt viscosity: 120 Pa·s) having an intrinsic viscosity (IV) of 0.63 dl / g as an island component and 5 having an IV of 0.58 dl / g as a sea component polymer - PET (copolymerized PET melt viscosity: 140 Pa·s) copolymerized with sodium sulfonate isophthalic acid 5.0 mol% was melted at 290°C, respectively, and then measured and flowed into the assembly. Image 6 In the spinning package of the composite spinneret of the present embodiment shown, the sea-island composite polymer flow is discharged from the discharge hole of the spinneret. In addition, on the lowermost distribution plate, 1000 island component discharge holes were perforated at equal intervals for one discharge introduction hole for the island component polymer. The sea-island ratio was 50 / 50. The discharged composite polymer stream was cooled and solidified, oil was added, and it was wound up at a spinning speed of 1500 m / min to obtain an unstretched fiber...
Example Embodiment
[0271] [Example 2]
[0272] like figure 2 As shown, the same composite spinneret as in Example 1 was used, except that the arrangement of the island component discharge holes and the sea component discharge holes of the lowermost distribution plate was changed to Condition B of (2), and the island component polymer ratios were Except that Example 1 was large (the sea-island ratio was set to 20 / 80), the same polymer, the same fineness, and spinning conditions were spun as in Example 1, and 13,500 multifilaments were obtained.
[0273] Here, in the composite spinneret used in Example 2, the radius R1 of the imaginary circumferential line C1 was 0.4 mm, the radius R2 of the imaginary circumferential line C2 was 0.8 mm, and the radius R4 of the imaginary circumferential line C4 was 0.8 mm. An island component discharge hole and a sea component discharge hole with a hole diameter of 0.2 mm were provided. As described in Table 1, the island component has a triangular cross-sectio...
Example Embodiment
[0274] [Example 3]
[0275] like image 3 As shown, the same composite spinneret as in Example 1 was used, except that the arrangement of the island component discharge holes and the sea component discharge holes of the lowermost distribution plate was changed to Condition C of (2), except that the sea-island ratio was Other than 20 / 80, spinning was carried out with the same polymer, the same fineness, and spinning conditions as in Example 1, and 15,000 multifilaments were obtained.
[0276] Here, in the composite spinneret used in Example 3, the radius R1 of the imaginary circumferential line C1 was 0.4 mm, the radius R2 of the imaginary circumferential line C2 was 0.8 mm, and the radius R4 of the imaginary circumferential line C4 was 0.693 mm. An island component discharge hole and a sea component discharge hole with a hole diameter of 0.2 mm were provided. As described in Table 1, the island component has a hexagonal cross section (angle of intersection of the straight li...
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