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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Embodiment 1
[0044] Step (1). Vacuum dry the attapulgite 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 of The ultraviolet absorber UV-1 is mixed into a 10kg mixture;
[0045] Step (2). The mixture is extruded through a twin-screw extruder, and spun by a spinneret, and then subjected to water cooling, hot water drafting, hot roller drafting, and heat setting to form thick fibers;
[0046] The processing temperature of the twin-screw extruder is: feeding section 180°C, plasticizing section 220°C, homogenizing section 240°C, spinneret temperature 250°C, spinneret hole outlet shape is circular; water-cooled water bath temperature is 10°C; the water bath temperature of hot water drawing is 60°C, and the draw ratio is 2 times; the drawing temperature of the hot roller drawing is 150°C, and the draw ratio is 6 times; the heat setting temperature is 150°C .
[0047] Step (3). Carrying out indent...
Embodiment 2
[0051] Step (1). The montmorillonite was vacuum-dried at 150°C for 24h; then 9.9kg of polypropylene, 10g of montmorillonite, 70g of acrylic acid grafted polypropylene, 10g of antioxidant 264, and 10g of ultraviolet absorber UV -326 mixed into 10kg mixture;
[0052] Step (2). The mixture is extruded through a twin-screw extruder, and spun by a spinneret, and then subjected to water cooling, hot water drafting, hot roller drafting, and heat setting to form thick fibers;
[0053] The processing temperature of the twin-screw extruder is: feeding section 185°C, plasticizing section 230°C, homogenizing section 250°C, spinneret temperature 260°C, spinneret hole outlet shape is oval; water-cooled water bath temperature It is 20 ℃; the water bath temperature of hot water drawing is 70 ℃, and the drawing ratio is 2 times; the drawing temperature of the hot roll drawing is 130 ℃, and the drawing ratio is 2 times; the heat setting temperature is 130 ℃ .
[0054] Step (3). Carrying out i...
Embodiment 3
[0058] Step (1). Vacuum dry the zeolite at 160°C for 15 hours; then mix 9.8kg of polypropylene, 100g of zeolite, 50g of acrylamide grafted polypropylene, 20g of antioxidant 168, and 30g of UV absorber UV-327 into a 10kg mixture;
[0059] Step (2). The mixture is extruded through a twin-screw extruder, and spun by a spinneret, and then subjected to water cooling, hot water drafting, hot roller drafting, and heat setting to form thick fibers;
[0060] The processing temperature of the twin-screw extruder is: feeding section 200°C, plasticizing section 240°C, homogenizing section 260°C, spinneret temperature 270°C, spinneret hole outlet shape is cross-shaped; water-cooled water bath temperature is 30°C; the water bath temperature of hot water drawing is 80°C, and the draw ratio is 4 times; the drawing temperature of the hot roll drawing is 140°C, and the draw ratio is 5 times; the heat setting temperature is 140°C .
[0061] Step (3). Carrying out indentation treatment on the s...
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