Modified polyester and preparation method thereof
A modified polyester and copolymerization technology, which is applied in the field of modified polyester and its preparation, can solve the problems of low yield, easy to break, and high brittleness of PET film, etc., to improve yield, reduce brittleness, and increase shrinkage Effect
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[0022] The present invention also provides a kind of preparation method of modified polyester, comprises the following steps:
[0023] Mix isophthalic acid, 1,4-cyclohexanedimethanol, terephthalic acid and ethylene glycol, and carry out esterification reaction at 240°C~280°C to obtain esterified products;
[0024] The temperature of the esterification product is raised to 250° C. to 290° C. to carry out polycondensation reaction to obtain a modified polyester.
[0025] The invention uses terephthalic acid and ethylene glycol as raw materials and isophthalic acid and 1,4-cyclohexanedimethanol as modifiers to prepare modified polyester. In the present invention, firstly, isophthalic acid, 1,4-cyclohexanedimethanol, terephthalic acid and ethylene glycol are mixed, and the esterification reaction is carried out at 240°C to 280°C. In the present invention, after the esterification kettle is heated to 240°C, isophthalic acid, 1,4-cyclohexanedimethanol, terephthalic acid and ethylen...
Embodiment 1
[0039] Add 91.2g of terephthalic acid, 8.8g of isophthalic acid, 87.14g of ethylene glycol and 12.86g of 1,4-cyclohexanedimethanol into the slurry configurer, stir evenly to obtain a reaction mixture; raise the temperature of the esterification reaction kettle After reaching 250°C, add the above reaction mixture to it, raise the temperature and start stirring, control the temperature of the kettle between 240°C and 280°C, add the blueness agent, and slowly release the formed esterification reaction product; add the esterification reaction product to In the polycondensation kettle, heat up to 260°C and start slowly vacuuming, and finally carry out high-vacuum polycondensation reaction between 250°C and 290°C, and stir while polycondensation reaction. The stirring process is as follows: First, stir under the conditions of 50HZ and 0.6kW , when it reaches 2.1kW, reduce to 35HZ and continue stirring, when it reaches 2.0KW, reduce to 25HZ, when the stirring frequency reaches 1.8KW, ...
Embodiment 2
[0044] Add 87g of terephthalic acid, 13g of isophthalic acid, 85g of ethylene glycol and 15g of 1,4-cyclohexanedimethanol into the slurry configurer and stir evenly to obtain a reaction mixture; after the esterification reaction kettle is heated to 250°C Add the above reaction mixture to it, raise the temperature and start stirring, control the temperature of the kettle between 240°C and 280°C, add the blueness agent, and slowly release the generated esterification reaction product; add the esterification reaction product into the polycondensation kettle, Raise the temperature to 260°C and start to vacuumize slowly, and finally carry out high-vacuum polycondensation reaction between 250°C and 290°C, and stir while polycondensation reaction. When kW is reduced to 35HZ to continue stirring, when it reaches 2.0KW, it is reduced to 25HZ, and when the stirring frequency reaches 1.8KW, stop stirring; use nitrogen to increase the pressure of the polycondensation tank to 0.2MPa, open t...
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Abstract
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