Colored special-shaped acrylic fiber as well as preparation method and application thereof
A technology of acrylic fibers and special shapes, which is applied in textiles and papermaking, chemical post-treatment of synthetic polymer rayon, single-component synthetic polymer rayon, etc. Dyeing old dude is not high, to achieve the effect of avoiding subsequent dyeing, high color fastness to washing, and green and environmentally friendly operation
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Embodiment 1
[0033] (1) Fiber forming: the solvent used is an aqueous sodium thiocyanate solution with a mass concentration of 50wt%, and dissolves the following monomers in parts by weight by a high-speed dissolving machine: 92 parts of acrylonitrile, 7.5 parts of methyl methacrylate and methacrylic acid 0.5 part of sodium is prepared into a spinning solution with a polyacrylonitrile polymer (the viscosity-average molecular weight of polyacrylonitrile in the polyacrylonitrile polymer is about 45,000-65,000) content of 7-12% after dissolving.
[0034] The spinning solution is heated to 85°C by a heater, and the heated spinning solution is extruded from the rectangular hole of the spinneret, and the as-spun fiber is formed by double diffusion in the coagulation bath. Among them, the aspect ratio of the extrusion hole of the spinneret nozzle is 15:1, the aspect ratio of the extrusion hole of the nozzle hole is 10:1, the hole length of the extrusion hole is greater than 0.1mm, the number of sp...
Embodiment 2
[0039] (1) Fiber forming: the solvent used is an aqueous solution of sodium thiocyanate with a mass concentration of 50 wt%, and dissolves the following monomers in parts by weight by a high-speed dissolving machine: 90 parts of acrylonitrile, 9 parts of methyl acrylate and 1 part of sodium propylene sulfonate, After dissolving, the spinning solution with a content of 10-12% of polyacrylonitrile polymer (the viscosity-average molecular weight of polyacrylonitrile in the polyacrylonitrile polymer is about 45,000-65,000) is prepared.
[0040] The spinning solution is heated to 85°C by the heater, and the heated spinning solution is extruded from the rectangular hole of the spinneret, and the primary fiber is formed by double diffusion in the coagulation bath, wherein the length and width of the extrusion hole of the spinneret The ratio of 10:1, the aspect ratio of the injection hole extrusion hole is 6:1, the hole length of the extrusion hole is greater than 0.3mm, the number of ...
Embodiment 3~8
[0045] The preparation steps of Examples 3-8 are the same as in Example 1, and most of its experimental parameters are also the same as in Example 1. The difference is that the length-to-width ratio of the nozzle hole of the spinneret and the length-to-width ratio of the extrusion hole are selected. The specific parameters are listed in Table 1. Comparing different spinnerets in the same coagulation bath forming conditions, the coagulation bath temperature is 2°C, the coagulation bath concentration is 12.5%, and the ratio of extrusion speed to traction roller speed is 1.8. The results are as follows:
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