A kind of extinction superfine high-strength and low-stretch viscose fiber and preparation method thereof
A high-strength, low-elongation, viscose fiber technology, which is applied in the field of textile fiber processing, can solve the problems of high cost and achieve the effects of improving brittleness, high elongation and fiber strength
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Embodiment 1
[0098] The matting superfine high-strength and low-elongation viscose fiber involved in this embodiment is made of pulp raw materials sequentially through impregnation, grinding, crushing, kneading, depolymerization, yellowing, dissolution, filtration, defoaming, aging, and spinning. Obtained after stretching and post-treatment, the high-strength low-stretch viscose fiber meets:
[0099]Denier 0.8~1.11 dtex;
[0100] Dry breaking strength ≥ 3.10 cN / dtex;
[0101] Wet breaking strength ≥ 1.60cN / dtex;
[0102] The strength required to produce 5% elongation in wet state is ≥0.55cN / dtex,
[0103] Dry elongation at break 11.0~19.0%;
[0104] Wet elongation at break 16.0~21.0%;
[0105] The radial water swelling degree is 22-26%;
[0106] The content of matting agent is 0.8-5%.
Embodiment 2
[0108] The difference between this embodiment and Embodiment 1 is that the extinction superfine high-strength low-elongation viscose fiber involved in this embodiment also satisfies:
[0109] Whiteness ≥ 85%;
[0110] Linear density deviation rate≤±11.0%;
[0111] Residual sulfur≤12.0mg / 100g;
[0112] Length deviation rate≤±11.0%;
[0113] Ultra-long fiber rate ≤ 0.5%;
[0114] Double-length fiber≤4.0mg / 100g;
[0115] Defect ≤ 4.0mg / 100g.
Embodiment 3
[0117] A preparation method of matting superfine high-strength low-elongation viscose fiber, the steps are as follows:
[0118] A: Immerse the pulp raw material in an immersion barrel filled with lye, and grind it with a grinder to make a pulp porridge with a concentration of 3%;
[0119] B: Send the pulp porridge prepared in step A to a press machine, and then send it to a pulverizer for crushing to obtain alkali cellulose, send the alkali cellulose to a kneading machine, and obtain a pulp porridge with a concentration of 30% after processing ;
[0120] C: Mix the porridge prepared in step B with lye and send it to the reactor, add pure oxygen to the reactor, and obtain alkali cellulose with a polymerization degree of 400 and a cellulose purity of 98.0% after depolymerization;
[0121] D: The alkali cellulose prepared in step C is sent to the yellowing machine, carbon disulfide is added in the yellowing machine, and after the yellowing reaction, the cellulose sulfonate obtai...
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Abstract
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