Synthesis of polyamic acid resin
A polyamic acid resin and a synthesis method technology, applied in the field of resin synthesis, can solve the problems of uneven surface, uneven color, high resin viscosity, etc., and achieve the effects of simple and feasible process method, reduced thickness deviation, and improved uniformity
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Embodiment 1
[0009] Embodiment 1 of the polyamic acid resin synthesis method adopts a jacketed reaction kettle, and cooling water is passed into the jacket. From the input of dianhydride, water at 10°C is continuously poured into the jacket of the reaction kettle and stirred, and the viscosity is detected during the feeding process. When the viscosity reaches 70,000 centipoise, the addition of dianhydride is stopped, and the stabilizer triphenyl phosphite is added. Ester, add-on is 0.1% of resin gross weight in the reactor, at this moment in the jacket of reactor, pass into the hot water of 45 ℃, the temperature of resin system rises to 60 ℃ after insulation and continue to stir for 5 hours. Obtaining the resin I that the viscosity is 60,000 centipoises at last is standby for the next operation.
Embodiment 2
[0011] The polyamic acid resin synthesis method embodiment 2 is similar to the method of embodiment 1, but the heating temperature is different. Starting from putting dianhydride into the reactor, water at 15°C is continuously poured into the jacket of the reactor and stirred. Viscosity detection is carried out during the feeding process. When the viscosity reaches 70,000 centipoise, stop adding dianhydride and add a stabilizer. Triphenyl phosphite, the addition amount is 0.3% of the total weight of the resin in the reactor. At this time, water at 50°C is introduced into the jacket of the reactor, and the temperature of the resin system rises to 65°C. Stir for 4 hours. Obtaining the resin II with a viscosity of 50,000 centipoise at last is standby for the next process.
Embodiment 3
[0013] The polyamic acid resin synthesis method embodiment 3 is similar to the method of embodiment 1, but the heating temperature is different. Starting from putting dianhydride into the reactor, water at 20°C is continuously poured into the jacket of the reactor and stirred. Viscosity detection is carried out during the feeding process. When the viscosity reaches 65,000 centipoise, stop adding dianhydride and add a stabilizer. Triphenyl phosphite, the addition is 0.2% of the total weight of the resin in the reactor. At this time, 55°C hot water is introduced into the jacket of the reactor, and the temperature of the resin system rises to 70°C. Stirring was continued for 3 hours. Obtaining the resin III with a viscosity of 45,000 centipoises at last is standby for the next process.
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