Hydrolysis resistant polyester resin composition and preparation method thereof
A technology of polyester resin and composition, which is applied in the field of polyester composition with hydrolysis resistance and its preparation, can solve the problems of easy hydrolysis of polyester material and inability to maintain material properties, etc., and achieves the effect of excellent hydrolysis resistance
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Embodiment 1
[0026] After polyethylene terephthalate (PET, F20S, Toray Corporation of Japan) was vacuum-dried at 150° C. for 6 hours, it was mixed with EPON 1001 (epichlorohydrin bisphenol A type solid epoxy resin) with 0.5% of PET mass. , Mn 1200) after dry blending, extruded by a twin-screw extruder to obtain blended chips. The temperature of the feeding section of the extruder is 210°C, the temperature of the remaining sections is 260°C, and the screw speed is 500 rpm. Analyze the change of the terminal carboxyl group concentration before and after the hydrolysis test of the obtained resin, and the results are shown in Table 1.
Embodiment 2
[0028] After polyethylene terephthalate (PET, F20S, Toray Corporation of Japan) was vacuum-dried at 150° C. for 6 hours, it was mixed with EPON 1001 (epichlorohydrin bisphenol A type solid epoxy resin) with 1% of PET mass. , Mn 1200) after dry blending, extruded by a twin-screw extruder to obtain blended chips. The temperature of the feeding section of the extruder is 210°C, the temperature of the remaining sections is 260°C, and the screw speed is 500 rpm. Analyze the change of the terminal carboxyl group concentration before and after the hydrolysis test of the obtained resin, and the results are shown in Table 1.
Embodiment 3
[0030] After polyethylene terephthalate (PET, F20S, Toray Corporation of Japan) was vacuum-dried at 150° C. for 6 hours, it was mixed with EPON 1001 (epichlorohydrin bisphenol A type solid epoxy resin) with 3% of PET mass. , Mn 1200) after dry blending, extruded by a twin-screw extruder to obtain blended chips. The temperature of the feeding section of the extruder is 210°C, the temperature of the remaining sections is 260°C, and the screw speed is 500 rpm. Analyze the change of the terminal carboxyl group concentration before and after the hydrolysis test of the obtained resin, and the results are shown in Table 1.
[0031] The resin hydrolysis test result of table 1 embodiment 1-3
[0032]
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