Polyimide precursor solution and manufacturing method thereof
一种聚酰亚胺前体、聚酰亚胺膜的技术,应用在涂层等方向,能够解决降低热膨胀系数、低热膨胀系数、无法达到塑料基板等问题,达到提高均匀度和收率、改善效率性、机械强度和柔韧性优异的效果
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Embodiment 1
[0151] TFMB(0.99) / PMDA(0.85)_6FDA(0.15)
[0152] In a stirrer with nitrogen flow, 100g of N,N-diethylacetamide (N,N-diethylacetamide) (DEAc) (distribution coefficient 0.32, density 0.9130g / cm 3 ), in a state where the temperature of the reactor was maintained at 25°C, 12 g of TFMB (2,2'-bis(trifluoromethyl)-4,4'-biphenylenediamine, 2,2` -bis(trifluoromethyl)-4,4`-biphenyl diamine). In the above TFMB solution, 7 g of PMDA (pyromellitic dianhydride, Pyromellitic Dianhydride) and 2.5 g of 6FDA (4,4'-(hexafluoroisopropylidene) diphthalic anhydride, 4,4 '-(Hexafluoroisopropylidene)diphthalic anhydride) was added at the same temperature, dissolved for a certain period of time and stirred. DEAc was added so that the solid content density|concentration of the polyimide precursor solution manufactured by the said reaction might become 10-10.5 weight%, and the polyimide precursor solution was manufactured. The viscosity of the said polyimide precursor solution was 6300cp.
Embodiment 2
[0153] TFMB(0.99) / PMDA(0.80)_6FDA(0.20)
[0154] 100 g of N,N-diethylacetamide (DEAc) was placed in a stirrer with nitrogen flow, and 12.7 g was dissolved while maintaining the temperature of the reactor at 25°C. TFMB (2,2'-bis(trifluoromethyl)-4,4'-biphenyldiamine, 2,2`-bis(trifluoromethyl)-4,4`-biphenyldiamine). In the above TFMB solution, 7g of PMDA (pyromellitic dianhydride, Pyromellitic Dianhydride) and 3.56g of 6FDA (4,4'-(hexafluoroisopropylidene) diphthalic anhydride, 4,4 '-(Hexafluoroisopropylidene)diphthalic anhydride) was added at the same temperature, dissolved for a certain period of time and stirred. DEAc was added so that the solid content density|concentration of the polyimide precursor solution manufactured by the said reaction might become 10-10.5 weight%, and the polyimide precursor solution was manufactured. The viscosity of the said polyimide precursor solution was 6800cp.
Embodiment 3
[0155] TFMB(0.99) / PMDA(0.75)_6FDA(0.25)
[0156]100 g of N,N-diethylacetamide (N,N-diethylacetamide) (DEAc) was placed in a stirrer with a nitrogen gas flow, and dissolved while maintaining the temperature of the reactor at 25°C. 13.56 g of TFMB (2,2'-bis(trifluoromethyl)-4,4'-biphenyldiamine, 2,2'-bis(trifluoromethyl)-4,4'-biphenyldiamine). In the above TFMB solution, 7g of PMDA (pyromellitic dianhydride, Pyromellitic Dianhydride) and 4.75g of 6FDA (4,4'-(hexafluoroisopropylidene) diphthalic anhydride, 4,4 '-(Hexafluoroisopropylidene)diphthalic anhydride) was added at the same temperature, dissolved for a certain period of time and stirred. DEAc was added so that the solid content density|concentration of the polyimide precursor solution manufactured by the said reaction might become 10-10.5 weight%, and the polyimide precursor solution was manufactured. The viscosity of the said polyimide precursor solution was 6200cp.
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