Liquid crystal polymer, preparation method thereof and liquid crystal polymer film
A liquid crystal polymer, polycondensation reaction technology, applied in liquid crystal materials, chemical instruments and methods, etc., can solve the huge difference in mechanical properties of liquid crystal polymer films, the difference in mechanical properties of molded products or films, and the low tensile strength of liquid crystal polymers. and other problems, to achieve good batch stability, excellent mechanical properties, and good batch stability.
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[0055] The present invention also provides a preparation method of the liquid crystal polymer described in the above technical solution comprising the following steps:
[0056] a) monomer I', monomer II', monomer III' and an acetylating agent are mixed for acetylation reaction to obtain an acetylated product;
[0057] b) the acetylated product undergoes a polycondensation reaction to form a liquid crystal polymer;
[0058]
[0059] in:
[0060] R 1 for C n h 2n , n is 1~6;
[0061] R 2 for C m h 2m , m is 1~6;
[0062] Regarding step a):
[0063] In the present invention, the structures of monomer I' (i.e. dihydric alcohol containing anthracene group), monomer II' (i.e. dibasic alkyl carboxylic acid containing anthracene group) and monomer III' (i.e. p-hydroxybenzoic acid) As shown above. Among them, in monomer Ⅱ', R 1 for C n h 2n , n is 1 to 6, preferably 2 to 5, and in some embodiments of the present invention, n is 2; R 2 for C m h 2m , m is 1-6, prefer...
Embodiment 1
[0082] S1. Mix 2mol of monomer I' and 5mol of monomer II' (R 1 for C 2 h 2 , R 2 for C 2 h 2 ), 3mol of monomer III' was added to the reaction vessel with a stirring paddle, and then 11mol of acetic anhydride was added to the reaction vessel as an acetylating agent. The reaction vessel was evacuated and argon was repeatedly operated for more than 5 times, so that the reaction mixture was protected by an inert gas, and then the temperature was raised to 150° C., and the acetylation reaction was carried out under stirring conditions for 4 hours.
[0083] S2. After the acetylation reaction in step S1 is completed, a small flow rate of argon gas is introduced into the reaction vessel, and the by-product acetic acid and excess acetic anhydride vapor are taken out of the reaction vessel under the action of 15 mL / min air flow.
[0084] S3. Raise the temperature of the reaction vessel to 360° C. to cause the reaction mixture to undergo a solid-phase melting condensation reaction....
Embodiment 2
[0090] S1, 3mol monomer Ⅰ', 4mol monomer Ⅱ'(R 1 for C 2h 2 , R 2 for C 2 h 2 ), 3mol of monomer III' was added to the reaction vessel with a stirring paddle, and then 11mol of acetic anhydride was added to the reaction vessel as an acetylating agent. The reaction vessel was evacuated and argon was repeatedly operated for more than 5 times, so that the reaction mixture was protected by an inert gas, and then the temperature was raised to 150° C., and the acetylation reaction was carried out under stirring conditions for 4 hours.
[0091] S2. After the acetylation reaction in step S1 is completed, a small flow rate of argon gas is introduced into the reaction vessel, and the by-product acetic acid and excess acetic anhydride vapor are taken out of the reaction vessel under the action of 15 mL / min air flow.
[0092] S3. Raise the temperature of the reaction vessel to 360° C. to cause the reaction mixture to undergo a solid-phase melting condensation reaction. After 6 hours, ...
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