High productivity spandex fiber process and product
A technology of mixture and polyurethane urea, which is applied in the field of polyurethane urea, can solve the problems of limited application and achieve the effect of increased productivity and good product consistency
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Embodiment 1
[0060] with TERATHANE 1800 and ISONATE MDR prepared a polyurethane urea polymer typically used to make spandex at an end cap ratio of 1:1.69. The blocked diol had a %NCO of 2.6% and was diluted with DMAc to give a 45% solids solution. This solution is then contacted with a DMAc solution containing: a mixture of EDA and DYTEK A chain extender mixture (90 / 10 molar ratio); and diethylamine as a chain terminator in a ratio such that the resulting polymer solution has an intrinsic viscosity of 0.95, an initial solution viscosity of 2600 poise, and contains The solids were 34.8% and had a measured number of chain extender ends of 15 meq / kg polymer solids. A 40 denier, 3 filament spandex yarn was spun from the polymer solution at 950 yards per minute (ypm). The intrinsic viscosity of the spun yarn was 1.16.
Embodiment 2
[0062] The polyurethaneurea polymers of the invention are prepared from a mixture of diisocyanates containing 82% of ISONATE MDR and 18% MONDUR ML. with TERATHANE 1800 to prepare capped diols with a capping ratio of 1:1.69. The capped diol was diluted to 55% solids with DMAc and reacted with a mixture of ethylenediamine and diethylamine in DMAc in proportions to obtain a polymer solution with an intrinsic viscosity of 0.75 and an initial solution viscosity of 3300 poise, and a solids content of 45%, and a measured number of chain extender ends of 40 meq / kg polymer solids. A 40 denier, 3 filament spandex yarn was spun from the polymer solution at 950 yards per minute (ypm). The intrinsic viscosity of the spun yarn was 1.34.
Embodiment 3
[0064] Preparation of polyurethane urea polymers from a mixture of diisocyanates containing 82% ISONATE MDR and 18% MONDUR ML. with TERATHANE 1800 to prepare capped diols with a capping ratio of 1:1.69. The capped diol was diluted to 55% solids with DMAc and reacted with a mixture of ethylenediamine and diethylamine in DMAc in proportions to obtain a polymer solution with an intrinsic viscosity of 0.75 and an initial solution viscosity of 3300 poise, and a solids content of 45%, and a measured number of chain extender ends of 15 meq / kg polymer solids. A 40 denier, 4 filament spandex yarn was spun from the polymer solution at 950 yards per minute (ypm). The intrinsic viscosity of the spun yarn was 1.02.
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