Method for preparing polyester film for solar cell backsheet film
A technology of solar cells and polyester films, which is applied in circuits, photovoltaic power generation, electrical components, etc., can solve the problems of insufficient flame retardancy, difficulty in meeting the performance requirements of solar cell backplane films, and poor heat and humidity resistance, and achieve improvement Effects of crystallization performance, reduction of water vapor transmission rate, and increase of steric hindrance
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Embodiment 1
[0044] Production of modified polyester resin chips: 200 parts by mass of terephthalic acid, 50 parts by mass of 2,6-naphthalene dicarboxylic acid, 96 parts by mass of ethylene glycol, 0.01 parts by mass of adipic acid, 0.5 parts by mass of The pentaerythritol, the cobalt acetate of 0.09 mass parts, the antimony trioxide of 0.10 mass parts and the triphenyl phosphate of 0.02 mass parts are added to the pulping tank, start the mixer, after beating for 25 minutes with 60 rev / min speeds, gradually Add an esterification kettle, the esterification reaction is controlled at 250-255°C, the reaction is controlled within 3-4 hours, the temperature is kept at 250-265°C, and the pressure is kept at 1×10 5 ~2×10 5 Pa, about 30 minutes, when the water output reaches more than 95% of the theoretical water output, it is considered that the esterification is completed, and it is transferred to the diesterification kettle. Add 0.3 parts by mass of cis 9, cis 12, cis 15-octadecatrienoic acid, ...
Embodiment 2
[0048] Production of modified polyester resin chips: 400 parts by mass of terephthalic acid, 155 parts by mass of ethylene glycol, 5 parts by mass of 1,3-propanediol, 0.01 parts by mass of pentaerythritol, 0.07 parts by mass of Add cobalt acetate, 0.04 parts by mass of antimony trioxide and 0.03 parts by mass of phosphoric acid into the pulping tank, start the mixer to beat at a speed of 50 rpm for 30 minutes, then gradually add an esterification kettle, and the esterification reaction is controlled at 245- 255°C, the reaction is controlled within 3 to 4 hours, and the temperature is kept at 250 to 265°C, and the pressure is kept at 1×10 5 ~2×10 5 Pa, about 30 minutes, when the water output reaches more than 95% of the theoretical water output, it is considered that the esterification is completed, and it is transferred to the diesterification kettle. Add 1.0 parts by mass of cis 6, cis 9, cis 12-octadecatrienoic acid, start the mixer, stir at a speed of 50 rpm, keep the temp...
Embodiment 3
[0052] Production of modified polyester resin chips: 50 parts by mass of terephthalic acid, 350 parts by mass of 2,6-naphthalene dicarboxylic acid, 130 parts by mass of ethylene glycol, 2 parts by mass of neopentyl glycol, 0.1 parts by mass Parts of pentaerythritol, 0.1 parts by mass of 1,3,5 cyclohexanetriol, 0.08 parts by mass of cobalt acetate, sodium acetate mixture (cobalt acetate: sodium acetate=1:3), 0.09 parts by mass of trioxide Diantimony and 0.06 parts by mass of trimethyl phosphate are added to the pulping tank, the mixer is started, and after beating at a speed of 100 rpm for 15 minutes, they are gradually added to an esterification kettle. Finish adding within 3-4 hours, keep warm at 250-265°C, hold pressure 1×10 5 ~2×10 5 Pa, about 30 minutes, when the water output reaches more than 95% of the theoretical water output, it is considered that the esterification is completed, and it is transferred to the diesterification kettle. Add 0.03 parts by mass of cis 6, c...
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