Preparation method of ultrahigh molecular weight polyethylene monofilament
A technology of ultra-high molecular weight and polyethylene, which is applied in the direction of single-component polyolefin rayon, rayon manufacturing, and melting of filament raw materials, which can solve high production costs, insufficient solution concentration, production efficiency, and production costs. There are problems in environmental protection, etc., to achieve good uniformity, solve the difficulty of chimeric rearrangement, and environmental friendliness
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Embodiment 1
[0029] The composite modified material containing 98% polyethylene with a weight average molecular weight of 1 million is added to a 30MPa ultra-high pressure co-rotating conical twin-screw extruder for full mixing and melting. The working temperature of the twin-screw extruder is 230 ℃. Then, the above-mentioned molten material is further increased to 55MPa through the booster pump, and the working temperature is 250°C. At the same time, the melt is metered and output, and the molten material is quantitatively pressed into the spinning die or spinning box for extrusion. For spinning, the temperature of the spinning box is 265°C. Then cool in a hot water bath at 80°C to obtain the primary monofilament; then carry out secondary stretching with hot air at 90°C, the stretching ratio is 10, and finally go through 130°C heat setting, oiling, winding and other processes to obtain a diameter of 0.12mm , UHMWPE monofilament with tensile strength of 8.1cN / dtex and elongation of 15%. ...
Embodiment 2
[0031]The composite modified material containing 94% polyethylene with a weight average molecular weight of 2 million is added to a 35MPa ultra-high pressure co-rotating twin-screw extruder for full mixing and melting. The working temperature of the twin-screw extruder is 240 ℃. Then, the above-mentioned molten material is further increased to 60MPa through the booster pump, and the working temperature is 255°C. At the same time, the melt is metered and output, and the molten material is quantitatively pressed into the spinning die or spinning box for extrusion. For spinning, the temperature of the spinning box is 268°C. Then cool in a hot oil bath at 120°C to obtain the primary monofilament; then carry out three-stage hot air stretching at 90°C, with a draw ratio of 15, and finally go through 130°C heat setting, oiling, winding and other processes to obtain a diameter of 0.25mm , UHMWPE monofilament with tensile strength of 8.7cN / dtex and elongation of 17.6%.
Embodiment 3
[0033] The composite modified material containing 92% polyethylene with a weight average molecular weight of 2.5 million is added to a 42MPa ultra-high pressure co-rotating conical twin-screw extruder for full mixing and melting. The working temperature of the twin-screw extruder is 255 ℃. Then the above-mentioned molten material is further increased to 65MPa through the booster pump, and the working temperature is 260°C, and the melt is metered and output at the same time, and the molten material is quantitatively pressed into the spinning die or spinning box for extrusion For spinning, the temperature of the spinning box is 270°C. Then cool in a hot water bath at 90°C to obtain primary monofilament; then carry out hot air four-stage stretching at 100°C, with a draw ratio of 20, and finally undergo heat setting at 150°C, oiling, winding and other processes to obtain a diameter of 0.30mm , UHMWPE monofilament with tensile strength of 9.2cN / dtex and elongation of 20%.
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