Low pressure resistant polyethylene terephthalate resin and producing method thereof
A technology of ethylene phthalate and production method, applied in the field of polyethylene terephthalate resin, can solve the problems of high post-processing cost, high price, unsuitability for soda water packaging, etc. cost effect
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Embodiment 1
[0037] Embodiment 1, this low pressure resistant polyethylene terephthalate resin contains: terephthalic acid, 1.7% isophthalic acid, 31.5% ethylene glycol, 0.3% diethylene glycol, Catalyst 230ppm, stabilizer 20ppm and the balance of terephthalic acid.
Embodiment 2
[0038] Embodiment 2, this low pressure resistant polyethylene terephthalate resin contains by raw material weight percentage: 2.0% isophthalic acid, 32% ethylene glycol, 0.5% diethylene glycol, catalyst 350ppm, stabilizer 40ppm and the balance of terephthalic acid.
Embodiment 3
[0039] Embodiment 3, this low pressure resistant polyethylene terephthalate resin contains by raw material weight percentage: 1.8% isophthalic acid, 32% ethylene glycol, 0.4% diethylene glycol, catalyst 290ppm, stabilizer 30ppm and the balance of terephthalic acid.
[0040] In the above embodiment: the catalyst can be antimony trioxide or antimony acetate or antimony glycol or germanium dioxide, and the stabilizer can be phosphoric acid or polyphosphoric acid or phosphorous acid or trimethyl phosphate or triphenyl phosphate.
[0041] The foregoing examples can be obtained by one of the following production methods:
[0042] The first step of beating: Put the required amount of terephthalic acid, isophthalic acid, ethylene glycol, diethylene glycol, catalyst and stabilizer into the slurry mixing tank and fully mix;
[0043] The second step of esterification reaction: when the esterification reaction pressure is 0.07MPa or 0.17MPa or 0.27Mpa, the esterification reaction tempera...
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