Oxygen absorbing type polyester resin, preparation method thereof, and high gas barrier product
A technology of polyester resin and polyester, which is applied in the field of oxygen-absorbing polyester resin and its preparation, can solve the problems of difficulty in controlling the dispersion uniformity of nanoparticles, high activity of nanoparticles, and high cost of nanomaterials, and it is easy to control the process conditions , simple process and flexible design
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Embodiment 1
[0054] The reaction device adopts a polyester reactor with a volume of 20 liters, and the reaction process is a direct esterification method. Adjust terephthalic acid (PTA), ethylene glycol (EG) and ethylene glycol antimony into slurry, wherein the molar ratio of ethylene glycol (EG) to terephthalic acid (PTA) is 1.3:1. The slurry enters the esterification reactor for esterification reaction to obtain esterified products, wherein the esterification reaction temperature is 260°C, the reaction pressure is 0.25Mpa, and the reaction time is 3 hours;
[0055] Add 5% epoxy-modified polyisoprene (that is, the amount of epoxy-modified polyisoprene / (the amount of epoxy-modified polyisoprene+the amount of esterified product) in the kettle after esterification finishes )=5%), the pressure in the kettle was slowly reduced to 1000Pa, and the reaction temperature was 260°C for pre-condensation, and the pre-condensation reaction time was 1 hour. After the pre-condensation, the reaction pres...
Embodiment 2
[0060] The reaction device adopts a polyester reactor with a volume of 20 liters, and the reaction process is a direct esterification method. Adjust terephthalic acid (PTA), ethylene glycol (EG) and ethylene glycol antimony into slurry, wherein the molar ratio of ethylene glycol (EG) to terephthalic acid (PTA) is 1.3:1. The slurry enters the esterification reactor for esterification reaction to obtain esterified products, wherein the esterification reaction temperature is 260°C, the reaction pressure is 0.25Mpa, and the reaction time is 3 hours;
[0061] Add 10% epoxy-modified polyisoprene (that is, the amount of epoxy-modified polyisoprene / (the amount of epoxy-modified polyisoprene+the amount of esterified product) in the kettle after esterification finishes )=10%), the pressure in the kettle is slowly reduced to 1000Pa, the reaction temperature is 260°C, and pre-condensation is carried out, and the pre-condensation reaction time is 1 hour. After the pre-condensation, the re...
Embodiment 3
[0063] The reaction device adopts a polyester reactor with a volume of 20 liters, and the reaction process is a direct esterification method. Adjust terephthalic acid (PTA), 1,4-butanediol, and tetraisobutyl titanate into slurry, wherein the molar ratio of 1,4-butanediol to terephthalic acid (PTA) is 1.3: 1. The slurry enters the esterification reactor for esterification reaction to obtain esterified products, wherein the esterification reaction temperature is 240°C, the reaction pressure is 0.15Mpa, and the reaction time is 3 hours;
[0064] Add 5% epoxy-modified polyisoprene (that is, the amount of epoxy-modified polyisoprene / (the amount of epoxy-modified polyisoprene+the amount of esterified product) in the kettle after esterification finishes )=5%), the pressure in the kettle was slowly reduced to 1000Pa, and the reaction temperature was 245°C for pre-condensation, and the pre-condensation reaction time was 1 hour. After the pre-condensation, the reaction pressure is low...
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