Copolyester containing aromatic secondary amine structure and its preparation method and application
A technology of aromatic secondary amines and copolyesters, which is applied in the field of copolyesters containing aromatic secondary amine structures and its preparation and application, can solve the problems of destroying polyester mechanical properties and spinnability, and achieve good organic smoke volatilization , Improve the mechanical strength, smoke suppression and anti-droplet effect
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Embodiment 1
[0046] 582.0 g of dimethyl terephthalate, 400.0 g of ethylene glycol, 47.0 g of 5-anilinocarbonyl-1,3-isophthalic acid dimethyl ester, 0.2 g of zinc acetate and 0.3 g of antimony trioxide were added to the In the reaction kettle, nitrogen is charged to remove the air in the kettle; the reaction is carried out under normal pressure at 180-220°C for 2-6 hours, and the transesterification reaction is completed; after that, the low-vacuum polycondensation reaction is carried out at 220-240°C for 0.5-1.5h, and then the reaction is carried out under high vacuum for 0.5-1.5 hours. (pressure<80Pa) at 250~270℃ for 1~4 hours of polycondensation reaction, discharging and water cooling.
[0047] The intrinsic viscosity [η] of the copolyester is 0.95dL / g; the limiting oxygen index is 25.0%; the vertical combustion grade is V-2, and there are droplets in the test, but the droplet phenomenon is obviously improved; The peak heat release rate p-HRR in thermal test is 608kW / m 2 , the total smo...
Embodiment 2
[0049] 582.0g of dimethyl terephthalate, 400.0g of ethylene glycol, 140.9g of 5-phenylaminocarbonyl-1,3-dimethyl isophthalate, 0.25g of isopropyl titanate were added to the reactor, After carrying out the transesterification and polycondensation reaction according to the steps and conditions given in Example 1, the material is discharged.
[0050] The intrinsic viscosity [η] of the copolyester is 0.80dL / g; the limiting oxygen index is 30.2%; the vertical combustion grade is V-0, and no droplets are produced in the test; the peak heat release rate in the cone calorimetry test p-HRR is 340kW / m 2 , the total smoke emission TSR is 954m 2 / m 2 ; The tensile strength is 90.6MPa.
Embodiment 3
[0052] 498.0g of terephthalic acid, 250.0g of ethylene glycol, 68.7g of 3,5-dihydroxy-N-phenylbenzamide, 0.3g of germanium dioxide were added to the reaction kettle, and nitrogen was charged to remove the air in the kettle. Pressurize to 0.1MPa, heat up to 220~240℃ to start the esterification reaction, control the pressure in the kettle to be 0.3~0.4MPa, after maintaining for 2~4h, gradually reduce the pressure to normal pressure, and the esterification reaction ends; after that, gradually heat up To 250°C, polycondensate in low vacuum for 0.5-1.5h, then perform polycondensation at 250-270°C for 1-4h in high vacuum (pressure < 80Pa), then discharge and cool with water.
[0053] The intrinsic viscosity [η] of the copolyester is 1.20dL / g; the limiting oxygen index is 28.0%; the vertical combustion grade is V-2, and there are droplets in the test, but the droplet phenomenon is obviously improved; Peak heat release rate p-HRR in thermal test is 575kW / m 2 , the total smoke emissio...
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