Polytrimethylene terephtalate conjugate fiber and method of preparing the same
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example 1
[0023] Using an extruder equipped with a spinning device as shown in FIG. 2, polytrimethylene terephtalate having an intrinsic viscosity (IV) of 1.0 at an amount of 50% by weight, which was used as PTT-H, and polytrimethylene terephtalate having an IV of 0.9 as PTT-L were spun at a spinning speed of 2000 m / min and at extruder temperatures of 260° C. and 265° C., respectively, using a side-by-side-type spinning nozzle, and then drawn at a draw ratio of 1.5, a draw temperature of 55° C. and a heat treatment temperature of 220° C. Cool air of 23° C. was supplied at a speed of 0.3 m / sec to a position of 5-120 cm under the nozzle, and oil pickup (OPU) was determined to 0.5 to 1.0 wt %. Using resulting fibers as warps and wefts, a woven fabric of weight of 100 g / m2 was processed and then stained at 105° C. A difference between intrinsic viscosities of the two polymers, PTT-H and PTT-L, was 0.1, and the ‘K’ value was 0.053.
examples 2 to 4
[0024] Woven fabrics were prepared and stained according to the method as in Example 1 except for change of extruder temperatures of polytrimethylene terephtalate having an IV of 1.0 as PTT-H and polytrimethylene terephtalate having an IV of 0.9 as PTT-L to temperatures as listed in Table 1, below.
examples 5 to 10
[0025] PTT-H and PTT-L having intrinsic viscosities and various combination ratios as shown in Table 2, below, were spun at a speed of 2000 m / min and at a spinning beam temperture of 265° C. using a side-by-side-type spinning nozzle, drawn at a draw ratio of 1.5, a draw temperature of 60° C. and a heat treatment temperature of 200° C.
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Abstract
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