Method for preparing flame-retardant luminous polyethylene glycol terephthalate
A technology of polyethylene terephthalate and ethylene glycol, which is applied in the field of PET composite materials and preparation, and can solve problems such as flammability hazards
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Embodiment 1
[0015] Add 20% by weight zinc phosphate slurry in the esterification process of producing PET, wherein the zinc phosphate accounts for 5% by weight of the slurry, and the particle size is approximately normal between 1nm and 50nm distribution, the solvent is ethylene glycol. At the same time, 5% by weight of decabromodiphenyl ether was added to the reaction mixture. The esterification reaction temperature is 200-220° C., the reaction pressure is 0.1-0.25 MPa, and the reaction time is 1-2 hours. The product of the above-mentioned esterification process is then subjected to a polycondensation process to obtain a flame-retardant and luminous PET composite material. Among them, the polycondensation reaction temperature in the low vacuum stage is 200-240°C, the reaction pressure is 100,000-500Pa, and the reaction time is 10-30 minutes; the polycondensation reaction temperature in the high vacuum stage is 250-275°C, the reaction pressure is 500-50Pa, and the reaction time 1 to 1.5...
Embodiment 2
[0017] In the esterification process stage of producing PET, a slurry of 30% by weight of trivalent europium-activated yttrium-aluminum garnet is added to the reaction mixture, and the trivalent europium-activated yttrium-aluminum garnet in the slurry accounts for the weight percent of the slurry 30%, the particle size is approximately normal distribution between 5nm and 10um, and the solvent is ethylene glycol. At the same time, 7% by weight of the reaction mixture was added as a flame retardant 2-carboxyethylphenyl phosphoric acid. Wherein the esterification reaction temperature is 220-240° C., the reaction pressure is 0.2-0.6 MPa, and the reaction time is 1.5-2 hours. The product of the above-mentioned esterification process is then subjected to a polycondensation process to obtain a flame-retardant and luminous PET composite material. Among them, the polycondensation reaction temperature in the low vacuum stage is 230-250°C, the reaction pressure is 100,000-500Pa, the rea...
Embodiment 3
[0019] Adding divalent europium-activated strontium chlorophosphate slurry at 10% by weight of the reaction mixture in the esterification process stage of producing PET, wherein, divalent europium-activated strontium chlorophosphate accounts for 90wt% of the total amount of the additive, and the particles The diameter is approximately normal distribution between 5nm and 10um, and the solvent is ethylene glycol. Simultaneously, 10% antimony trioxide was added based on the weight percentage of the reaction mixture. Wherein the esterification reaction temperature is 220-240° C., the reaction pressure is 0.2-0.25 MPa, and the reaction time is 1.5-2 hours. The product of the above-mentioned esterification process is then subjected to a polycondensation process to obtain a flame-retardant and luminous PET composite material. Among them, the polycondensation reaction temperature in the low vacuum stage is 230-250°C, the reaction pressure is 100,000-500Pa, the reaction time is 20-30 ...
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Abstract
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