Liquid-crystalline polyester composition and molding
A liquid crystal polyester and composition technology, applied in the field of liquid crystal polyester composition and its molded products, can solve the problems of molded product deformation, mold release failure, difficult molded products, etc., and achieve the effect of good mold release properties
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[0108] The present invention is described in more detail by the following examples, which should not be construed as limiting the scope of the present invention.
[0109] Use the following release agents 1-4 as internal release agents.
[0110] Release agent 1: dipentaerythritol hexastearate, solubility parameter: 9.0 (cal / cm 3 ) 1 / 2 , 5% weight reduction temperature (TB): 260°C
[0111] Release agent 2: pentaerythritol tetrastearate, solubility parameter: 8.7 (cal / cm 3 ) 1 / 2 , 5% weight loss temperature (TB): 310°C
[0112] Release agent 3: triglycerin stearate (triglycerin stearate), solubility parameter: 6.7 (cal / cm 3 ) 1 / 2 , 5% weight loss temperature (TB): 340°C
[0113] Release agent 4: sorbitan tristearate, solubility parameter: 9.7 (cal / cm 3 ) 1 / 2 , 5% weight reduction temperature (TB): 280°C
[0114] The 5% weight loss temperature of the above release agents 1 to 4 was measured as described below.
[0115] Thermogravimetric analysis was carried out by using...
manufacture Embodiment 1
[0129] In a reactor equipped with a stirrer, torque meter, nitrogen inlet tube, thermometer and reflux condenser, 621 g (4.5 moles) of p-hydroxybenzoic acid, 279 g (1.5 moles) of 4,4'-dihydroxybiphenyl, 149.4g (0.9 mol) of terephthalic acid, 99.6g (0.6 mol) of isophthalic acid and 841.5g (8.25 mol) of acetic anhydride, after fully replacing the inside of the reactor with nitrogen, the reactor was decomposed under nitrogen flow for 30 minutes. Heat to 150°C and maintain reflux at this temperature for 30 minutes.
[0130] Thereafter, the temperature was raised to 315° C. in 3 hours and 30 minutes, while removing distilled by-product acetic acid and unreacted acetic anhydride, and the completion of the reaction was set at the moment when torque increase was observed to obtain a prepolymer.
[0131] The obtained prepolymer was cooled to room temperature, pulverized with a pulverizer to obtain a powder, and the powder was heated under a nitrogen atmosphere, raised from room tempera...
manufacture Embodiment 2
[0133] In a reactor equipped with a stirrer, torque meter, nitrogen inlet tube, thermometer and reflux condenser, 830.7 g (5.0 moles) of p-hydroxybenzoic acid, 465.5 g (2.5 moles) of 4,4'-dihydroxydihydro Benzene, 394.6g (2.375 moles) of terephthalic acid, 20.8g (0.125 moles) of isophthalic acid and 1153g (11.0 moles) of acetic anhydride were fully replaced with nitrogen inside the reactor, and the reaction was carried out under nitrogen flow for 15 minutes. The vessel was heated to 150°C and kept at reflux at this temperature for 30 minutes.
[0134] Thereafter, the temperature was raised to 320° C. in 2 hours and 50 minutes, while removing distilled by-product acetic acid and unreacted acetic anhydride, and the completion of the reaction was set at the moment when torque increase was observed to obtain a prepolymer.
[0135] The obtained prepolymer was cooled to room temperature, pulverized with a pulverizer to obtain a powder, and the powder was heated under a nitrogen atmo...
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