Crude polypropylene fiber and preparation method thereof
A polypropylene, crude fiber technology, used in fiber processing, fiber chemical characteristics, single-component polyolefin rayon, etc., can solve the problem of limited improvement in concrete toughness and crack resistance, and high price of thermotropic liquid crystal polymers , increase the cost of polypropylene fiber, etc., to achieve the effect of enhancing strength, reducing product cost, and simplifying production process
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[0043] Example 1:
[0044] Step (1). The attapulgite was vacuum dried at 200°C for 12h; then 8.5kg of polypropylene, 1.0kg of attapulgite, 0.45kg of maleic anhydride grafted polypropylene, 30g of antioxidant 1010, 20g The ultraviolet absorber UV-1 is mixed into a 10kg mixture;
[0045] Step (2). The mixture is extruded through a twin-screw extruder, and is spun from a spinneret, and then subjected to water cooling, hot water drafting, hot roll drafting, and heat setting to form coarse fibers;
[0046] The processing temperature of the twin-screw extruder is 180°C in the feeding section, 220°C in the plasticizing section, 240°C in the homogenizing section, the temperature of the spinneret is 250°C, the outlet shape of the spinneret hole is circular; the temperature of the water-cooled water bath It is 10℃; the water bath temperature of hot-water drawing is 60℃, and the drafting ratio is 2 times; the drafting temperature of the hot roll drafting is 150℃, and the drafting ratio is 6 ti...
Example Embodiment
[0050] Example 2:
[0051] Step (1). Dry the montmorillonite in vacuum at 150°C for 24 hours; then 9.9 kg of polypropylene, 10 g of montmorillonite, 70 g of acrylic grafted polypropylene, 10 g of antioxidant 264, and 10 g of ultraviolet absorber UV -326 is mixed into a 10kg mixture;
[0052] Step (2). The mixture is extruded through a twin-screw extruder, and is spun from a spinneret, and then subjected to water cooling, hot water drafting, hot roll drafting, and heat setting to form coarse fibers;
[0053] The processing temperature of the twin-screw extruder is: feeding section 185°C, plasticizing section 230°C, homogenizing section 250°C, the spinneret temperature is 260°C, the outlet shape of the spinneret hole is oval; water-cooled bath temperature It is 20°C; the temperature of the hot water bath is 70°C, and the drawing ratio is 2 times; the drawing temperature of the hot roll drawing is 130°C, and the drawing ratio is 2 times; the heat setting temperature is 130°C .
[0054]...
Example Embodiment
[0057] Example 3:
[0058] Step (1). Dry the zeolite in vacuum at 160°C for 15 hours; then mix 9.8 kg of polypropylene, 100 g of zeolite, 50 g of acrylamide grafted polypropylene, 20 g of antioxidant 168, and 30 g of ultraviolet absorber UV-327. Into a 10kg mixture;
[0059] Step (2). The mixture is extruded through a twin-screw extruder, and is spun from a spinneret, and then subjected to water cooling, hot water drafting, hot roll drafting, and heat setting to form coarse fibers;
[0060] The processing temperature of the twin-screw extruder is: 200°C in the feeding section, 240°C in the plasticizing section, 260°C in the homogenization section, the temperature of the spinneret is 270°C, and the outlet shape of the spinneret hole is cross-shaped; water-cooled bath temperature The temperature of the water bath for hot-water drawing is 80°C, and the drawing ratio is 4 times; the drawing temperature of the hot roll drawing is 140°C, and the drawing ratio is 5 times; the heat setting ...
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