Method and apparatus for continuously drip-free fire-retardant polyester
A technology of flame retardant and polymerization equipment, applied in the field of non-drip flame retardant polyester, can solve the problems of deterioration of the quality of the degraded blend, high cost, numerous procedures, etc., and achieves low production cost, simple method and uniform dispersion. Effect
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Embodiment 1
[0024] Use terephthalic acid and ethylene glycol as raw materials to carry out esterification reaction at 200-260°C, and then carry out recondensation reaction at 280-300°C under a vacuum lower than 300Pa to continuously produce poly(p-phenylene) with a viscosity of 0.655 Ethylene glycol diformate (abbreviated as: PET) melt. The polyethylene terephthalate melt in the continuous polymerization equipment 1 is input through the main pipeline 2 at a speed of 1000kg / h at a temperature of 220-300°C (for example, 220°C, 240°C, 280°C, 300°C). Co-mixing device 3, while branch pipe 4 inputs polyethylene terephthalate into screw mixer 5, and the supply rate is 5kg / h; silicon compound (Dow Corning 217 sheet resin, obtained by hydroxylation of 100% phenyl silicone resin) ) flame retardant powder (functional particles) into the screw mixer 5, the supply rate is 5kg / h. The mixture further enters the blending device 3 for blending treatment, and the blending temperature in the blending devic...
Embodiment 7
[0028] Use terephthalic acid and ethylene glycol as raw materials to carry out esterification reaction at 200-260°C, and then carry out re-condensation reaction at 280-300°C under a vacuum of less than 300 Pa to continuously produce poly(p-phenylene) with a viscosity of 0.655 Ethylene glycol diformate (abbreviated as: PET) melt. The polyethylene terephthalate melt in the continuous polymerization equipment 1 is input through the main pipeline 2 at a speed of 1000kg / h at a temperature of 220-300°C (for example, 220°C, 240°C, 280°C, 300°C). Co-mixing device 3, while branch pipe 4 inputs polyethylene terephthalate into screw mixer 5, and the supply rate is 5kg / h; silicon compound (Dow Corning 217 sheet resin, obtained by hydroxylation of 100% phenyl silicone resin) ) flame retardant powder and antioxidant IR1010 (or antioxidant 1076, antioxidant TNP, 168) are mixed and then added to the screw mixer 5, the supply rate is 5kg / h, and the mixture further enters the blending device 3 ...
Embodiment 8
[0030] Use terephthalic acid and ethylene glycol as raw materials to carry out esterification reaction at 200-260°C, and then carry out recondensation reaction at 280-320°C under a vacuum lower than 300Pa to continuously produce polyparaphenylene with a viscosity of 0.655. Ethylene glycol diformate (abbreviated as: PET) melt. Polyethylene terephthalate melt passes through the main pipeline from the continuous polymerization equipment 6 at a speed of 1000kg / h at a temperature of 220-320°C (for example, 220°C, 240°C, 280°C, 300°C, 320°C). 7 is fed into the blending device 8. On the other hand, polyethylene terephthalate chips with a viscosity of 0.655 supplied at a supply rate of 5 kg / h and silicon compound flame-retardant powder PEI (GE1010 series) supplied at a rate of 5 kg / h were mixed in a screw mixer 9 Mix in, and further enter the blending device 8 for blending treatment. Then use ordinary spinning machine to carry out conventional spinning and drawing process to make no...
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