Antipilling nitrilon and its production method
An anti-pilling acrylic fiber, production process technology, applied in textiles and papermaking, one-component synthetic polymer rayon, fiber chemical characteristics, etc. Poor durability, etc.
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Embodiment 1
[0023] Anti-pilling fiber pilot test:
[0024] The production of polymer A, the specific parameters of A polymer are shown in Table 4, and the reaction is carried out in a continuous reactor with a jacket of pure aluminum, and the feed amount of the reactant is accurately measured by a mass flow meter. The solid concentration is 28%, the reaction temperature is 65°C, the pH value in the kettle is 3.0, and the conversion rate is 85%. The jacket is cooled with chilled water to remove the heat generated by the reaction. Remove the monomer, wash it into the polymer and mix it;
[0025] For the production of polymer B, change the parameters of B set after 7 hours of production of polymer A to produce polymer B. The specific parameters are shown in Table 5. The preparation method and process conditions are the same as those of polymer A;
[0026] A and B two kinds of polymers are mixed in a mixing tank at a ratio of 1:1 to produce stock solution;
[0027] Dehydration and pulping s...
Embodiment 2
[0045] Acrylonitrile copolymer A with acrylonitrile content of 95%, vinyl acetate content of 5%, viscosity average molecular weight of 35000-50000 and acrylonitrile content of 85%, vinyl acetate content of 14%, viscosity average molecular weight of 50000-50000 For 60000 acrylonitrile copolymer B, the two polymers A and B are mixed in a ratio of 1:1.5.
[0046]The reactions were all carried out in a jacketed continuous reaction kettle of pure aluminum, the total monomer concentration of the feed was 35%, the reaction temperature was 55°C, the pH value in the kettle was 2.0, and the conversion rate was 75%. Chilled water is used for cooling to remove the heat generated by the reaction; the reacted polymer is terminated by reaction, the monomer is released, washed with water and mixed with the polymer; the mixed polymer is dehydrated and dissolved with sodium thiocyanate to prepare a polymer The raw material content is 13.5%, and the crude stock solution is extracted by air bubbl...
Embodiment 3
[0048] 91% acrylonitrile and 91% vinyl acetate? 9%, acrylonitrile copolymer A with a viscosity-average molecular weight of 35,000-50,000 and an acrylonitrile content of 91%, and a vinyl acetate content of ? 9%, an acrylonitrile copolymer B with a viscosity-average molecular weight of 50,000-60,000, and two polymers A and B in a ratio of 1:2.
[0049] The reactions were all carried out in a jacketed continuous reaction kettle of pure aluminum, the total monomer concentration of the feed was 30%, the reaction temperature was 60°C, the pH value in the kettle was 2.5, and the conversion rate was 80%. Chilled water is used for cooling to remove the heat generated by the reaction; the reacted polymer is terminated by reaction, the monomer is released, washed with water and mixed with the polymer; the mixed polymer is dehydrated and dissolved with sodium thiocyanate to prepare a polymer The raw material content is 13.5%, and the crude stock solution is released through air bubbles, ...
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