Flame-retardant anti-dripping copolyester based on high-temperature self-crosslinking as well as preparation method and application of flame-retardant anti-dripping copolyester
A technology of self-crosslinking and copolyester, which is applied in the manufacture of fire-resistant and flame-retardant filaments, single-component polyester artificial filaments, etc., can solve the problem of destroying the mechanical properties and spinnability of polyester, but cannot solve the problem of polyester smoke release , environmental pollution and health issues, to achieve the effect of suppressing the generation of molten droplets, excellent flame retardant and anti-droplet performance, and suppressing volatilization
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Embodiment 1
[0053] 498.0 g of terephthalic acid, 220.0 g of ethylene glycol, 7.98 g of 4-(phenylethynyl) phthalic acid, 36.6 g of 2,8-(2-hydroxyethoxy) potassium phenanthrene oxaphosphinate, Add 0.3g of antimony trioxide into the reaction kettle, fill with nitrogen to remove the air in the kettle, pressurize to 0.1MPa, raise the temperature to 240°C within 2 hours to start the esterification reaction, control the pressure in the kettle to 0.3-0.4MPa, and maintain 2 After ~4 hours, the pressure begins to drop to normal pressure, and the esterification reaction ends; then, the polycondensation reaction is carried out at 240°C for 0.5 to 2 hours in a low vacuum, and then the temperature is raised to 250~270°C, and the polycondensation reaction is carried out in a high vacuum (pressure<80Pa) for 1~2 hours. After 4 hours, the material was discharged and water-cooled.
[0054] The intrinsic viscosity [η] of the copolyester is 0.85dL / g; the limiting oxygen index is 27.0%; the vertical combustion...
Embodiment 2
[0056] 582.0g dimethyl terephthalate, 400.0g ethylene glycol, 159.6g 4-(phenylethynyl) phthalic acid, 25.2g (3-(2-hydroxyethoxy)-3-oxopropane Base) (phenyl) sodium phosphinate, 0.2g manganese acetate and 0.25g germanium dioxide were added to the reaction kettle, filled with nitrogen to remove the air in the kettle body; the reaction was carried out at 180-220°C under normal pressure for 2-6 hours, and the transesterification The reaction is completed; then polycondensation is carried out at 240-250° C. for 0.5-2 hours in low vacuum, and then at 250-270° C. for 1-4 hours under high vacuum (pressure < 80 Pa). The material is discharged and water-cooled.
[0057] The intrinsic viscosity [η] of the copolyester is 0.62dL / g; the limiting oxygen index is 30.5%; the vertical combustion rating is V-2; the peak heat release rate p-HRR in the cone calorimetry test is 312kW / m 2 , the total smoke release TSR is 801 m 2 / m 2 .
Embodiment 3
[0059] 388.0g dimethyl terephthalate, 194g dimethyl isophthalate, 400.0g ethylene glycol, 79.8g 4-(phenylethynyl) phthalic acid, 52.5g (3,5-bis(formyl Oxycarbonyl) phenyl) potassium phosphonate, 40.2g isophthalic acid-5-sodium sulfonate, 0.28g isopropyl titanate were added to the reaction kettle, and after esterification and polycondensation were carried out according to the steps and conditions of Example 2 ,Discharge.
[0060]The intrinsic viscosity [η] of the copolyester is 0.90dL / g; the limiting oxygen index is 31.0%; the vertical combustion rating is V-0, and no droplet is produced in the test; the p-HRR in the cone calorimetry test is 222kW / m 2 , TSR is 640m 2 / m 2 .
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