Method for preparing highly uniform spandex fiber
A technology of spandex fiber and uniformity is applied in the field of high-uniformity spandex yarn dry-process spandex fiber and its preparation, and can solve the problems of not being able to meet the use requirements and the like
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[0021] The preparation method of high uniformity spandex fiber of the present invention comprises the following steps:
[0022] (1) Steps to improve the uniformity of spandex products in the polymerization solvent section: dry-process spandex fiber production can be carried out with different solvents, and the solubility of various solvents is very different, and the solvent with good solubility will reduce the impurities in the polymer , the polymer has high purity. At present, the main solvent used is DMF or DMAC. The impurity content indicators in the solvent, such as moisture, conductivity, and pH, also have a greater impact on the uniformity of spandex. At present, the indicators of general spandex manufacturers are: moisture 50-100PPM, conductance 0.3-0.4μS / cm, acid content ≤50-80PPM;
[0023] In the present invention, DMAC, a solvent with better solubility, is selected and purified by a special form of ion exchange resin to reduce impurities in DMAC and improve the puri...
Embodiment 1
[0033] In step 1, the solvent is 45PPM moisture, 0.12μS / cm conductance; DMAC with acid content 23PPM, in step 2, PTG with a molecular weight of 1805 and a molecular weight distribution of 2.02 is used for pre-polymerization, and the polymerization method adopts batch polymerization. In step 3, EDA, PDA, and DEA mixed amines are used as chain extenders, and the ratio of amines is EDA:PDA 4:1 for chain extension. In step 4, ordinary hot air is used for spinning in a square tunnel, and the spinning air volume is 9Nm 3 / min; produce 40D standard spandex products under the above process conditions.
Embodiment 2
[0035] In step 1, the solvent uses 85PPM of moisture and 0.35μS / cm of conductance; DMF with an acid content of 75PPM. In step 2, PTG with a molecular weight of 2006 and a molecular weight distribution of 1.52 is used for pre-polymerization. The polymerization method adopts static mixing, and step 3 EDA, PDA, DEA mixed amines are used as chain extenders, and the ratio of amines is EDA:PDA 4:1 for chain extension. In step 4, ordinary hot air is used for spinning in a square tunnel, and the spinning air volume is 9Nm 3 / min; produce 40D standard spandex products under the above process conditions.
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