Drying method when preparing flexible adhesive-free polyimide copper-clad laminates by two-layer method
A technology of gluing polyimide and drying method, which is applied in the direction of coating, liquid coating device on the surface, pretreatment surface, etc., can solve the problems of poor dimensional stability, high cost, high energy consumption, etc., and prevent curl deformation Low requirements for stripping and coating equipment, and improved drying efficiency
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Embodiment 1
[0031] Such as figure 1 As shown, the production line for preparing flexible adhesive-free polyimide copper-clad laminates by the two-layer method of the present invention sequentially includes a reaction system 100 for preparing a polyamic acid solution, and a coating system 200 for coating the polyamic acid solution on copper foil. , A high-tension drying cylinder 300 for secondary drying the coated copper-clad laminate under high tension, and a special nitrogen high-temperature oven 400 for imidizing roll-shaped products.
[0032] The reaction system 100 and the coating system 200 for preparing the polyamic acid solution can adopt equipment in the prior art, wherein the coating system 200 can adopt equipment in the existing coating field; and the parameters of the high tension dryer 300 and the special The nitrogen high-temperature oven 400 is a special design for the present invention.
[0033] The high-tension drying cylinder 300 is connected to the end of the coating sy...
Embodiment 2
[0042] The content of Embodiment 2 is substantially the same as that of Embodiment 1. The difference is:
[0043] The aromatic amine solution in step 1) is the 3 substances in Example 1, the ratio is 4:4:1, cooled to a temperature of about -8 degrees Celsius, and equimolar biphenyltetracarboxylic acid dicarboxylate is added in 8 batches within 8 hours. Anhydride, maintained at about -8 degrees Celsius, the reaction time is 45 hours, the obtained polyamic acid has a solid content of 12 g / 100 ml, a molecular weight of 53000-69000, and a molecular weight distribution index of less than 1.4.
[0044] The thickness of the copper foil in step 2) is 12 mm, the coating speed is 9 m / min, the drying temperature is 130 degrees during coating, and 81% of the solvent is removed, and the diameter of the drying cylinder in step 4) is 2 meters. The surface drying temperature is 190 degrees Celsius, the speed is 3m / min, and the winding is 1500m / roll; during imidization, follow the temperature...
Embodiment 3
[0046] The content of embodiment 3 is substantially the same as that of embodiment 1. The difference is:
[0047] The aromatic amine solution in step 1) is the 3 substances in Example 1, the proportioning ratio is 6:6:1, the cooling temperature is -5 degrees Celsius, and equimolar 4-4 biphenyl ether dianhydride is added in 10 batches within 10 hours , maintained at -5 degrees Celsius and the reaction time is 50 hours, the solid content of the obtained polyamic acid is 13 g / 100 ml, the molecular weight is 51000-64000, and the molecular weight distribution index is less than 1.4.
[0048] The thickness of the copper foil in step 2) is 12 mm, the drying temperature is 160 degrees during coating, the speed is 12 m / min, and 80% of the solvent is removed; the diameter of the drying cylinder in step 4) is 2.5 meters, and it is dried on the surface of a high tension drying cylinder The temperature is 200 degrees, the speed is 2m / min, and the winding is 2000m / roll; during imidization,...
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