Static cotton material and preparation method and application thereof
A technology of electrostatic cotton and raw materials, applied in the field of electrostatic cotton materials, can solve the problems of strong odor, obvious static attenuation, poor durability, etc., and achieve the effects of low high temperature filtration effect attenuation, strong charge retention ability, and beautiful cloth style
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Embodiment 1
[0054] The production of the embodiment of the present invention mainly includes the following steps:
[0055] Component A polymer is homopolypropylene, melting point 158~168℃;
[0056] The B-component polymer is a polyester chip treated with phosphorus-based flame retardant modification, with a melting point of 235-255°C and an oxygen index greater than 28%.
[0057] Parallel two-component matching ratio A: B=45:55 (mass ratio)
[0058] The two polymers mentioned above are polyolefin and polyester polymers. The former does not need to be baked by a single-screw extruder for direct melting and extrusion, while the latter requires a baking treatment at 155°C for 9 hours and then a single screw. The extruder performs melt extrusion.
[0059] The raw material of component A (containing 1.5wt% electret masterbatch) is melted through a single screw extruder, and its temperature zone is set to: 195℃, 205℃, 230℃, 230℃, 230℃, 230℃, 230℃, 225℃, melt temperature 225℃, screw pipe temperature 230...
Embodiment 2
[0063] The production of the embodiment of the present invention mainly includes the following steps:
[0064] Component A polymer is homopolypropylene, melting point 158~168℃;
[0065] The B-component polymer is a polyester chip treated with phosphorus-based flame retardant modification, with a melting point of 235-255°C and an oxygen index greater than 28%.
[0066] Parallel two-component collocation ratio A: B = 41:59 (mass ratio)
[0067] The two polymers mentioned above are polyolefin and polyester polymers. The former does not need to be baked by a single-screw extruder for direct melting and extrusion, while the latter requires a baking treatment at 155°C for 9 hours and then a single screw. The extruder performs melt extrusion.
[0068] The raw material of component A (containing 1.5% electret masterbatch) is melted through a single screw extruder, and its temperature zone is set to: 195℃, 205℃, 230℃, 230℃, 230℃, 230℃, 230℃, 225 ℃, melt temperature 225℃, screw pipe temperature...
Embodiment 3
[0072] The production of the embodiment of the present invention mainly includes the following steps:
[0073] Component A polymer is homopolypropylene, melting point 158~168℃;
[0074] The B-component polymer is a polyester chip treated with phosphorus-based flame retardant modification, with a melting point of 235-255°C and an oxygen index greater than 28%.
[0075] Parallel two-component matching ratio A: B=48:52 (mass ratio)
[0076] The two polymers mentioned above are polyolefin and polyester polymers. The former does not need to be baked by a single-screw extruder for direct melting and extrusion, while the latter requires a baking treatment at 155°C for 9 hours and then a single screw. The extruder performs melt extrusion.
[0077] The raw material of component A (containing 1.5% electret masterbatch) is melted through a single screw extruder, and its temperature zone is set to: 195℃, 205℃, 230℃, 230℃, 230℃, 230℃, 230℃, 225 ℃, melt temperature 225℃, screw pipe temperature 230℃...
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