Method of producing thermotropic liquid crystalline copolyester, thermotropic liquid crystalline copolyester composition obtained by the same method, and molding made of the same composition
a technology of thermotropic liquid crystalline copolyesters and compositions, which is applied in the direction of group 5/15 element organic compounds, synthetic resin layered products, building components, etc., can solve the problems of corrosive film, serious problem of corrosive out-gases of such corrosive out-gases, etc., and achieve the effect of suppressing the generation of out-gases
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example 1
[0100] A polymerization reactor made of SUS316 as a material and having a double-helical stirring wing (manufactured by Nitto Koatsu Co.) was used. Nitrogen-substitution was carried out by repeating the process of "pressure reduction of the polymerization reactor and nitrogen injection into the reactor" five times. Then, 1,330.10 g (9.63 moles) of p-hydroxybezoic acid (HBA) manufactured by Ueno Seiyaku Co., 79.99 g (0.4815 moles) of isophthalic acid (IPA) manufactured by A.G. International Co., 453.29 g (2.7285 moles) of terephthalic acid (TPA) maufactured by Mitsui Sekiyu Kagaku Kogyo Co., 597.73 g (3.21 moles) of p,p'-biphenol (BP) manufactured by Honshu Kagaku Kogyo Co. and 0.35 g of magnesium acetate as a catalyst manufactured by Tokyo Kasei Co. were charged in the polymerization reactor and the monomers in the polymerization reactor were mixed by stirring at the rotation rate of the stirring wing of 50 rpm. 2 g of the monomer mixture in the polymerization reactor was taken out ...
example 2
[0107] A device which was similar to that used in Example 1 was employed. 1,330.10 g (9.63 moles) of p-hydroxybezoic acid (HBA), 79.99 g (0.4815 moles) of isophthalic acid (IPA), 453.29 g (2.7285 moles) of terephthalic acid (TPA), 597.73 g (3.21 moles) of p,p'-biphenol (BP) and 0.35 g of magnesium acetate as a catalyst were charged in the polymerization reactor. The temperature in the polymerization reactor was raised to 70.degree. C. and the process of "pressure reduction ad nitrogen injection" was repeated five times with rotating the stirring wing at 50 rpm, effecting the nitrogen substitution and the drying of the monomers in 2 hours. After the drying of the monomers was completed, 2 g of the monomer mixture in the polymerization reactor was taken out of the reactor and the water content therein was measured. 0.015 weight % of water content was detected in the monomer mixture. In other words, 0.37 g (0.02 moles) of H.sub.2O was present in the polymerization reactor.
[0108] The mo...
example 3
[0114] A device which was similar to that used in Example 1 was employed. Nitrogen substitution was carried out by repeating the process of "pressure reduction and nitrogen injection" of the polymerization reactor five times. 1,330.10 g (9.63 moles) of p-hydroxybezoic acid (HBA), 132.90 g (0.80 moles) of isophthalic acid (IPA), 400.37 g (2.41 moles) of terephthalic acid (TPA), 597.73 g (3.21 moles) of p,p'-biphenol (BP) and 0.35 g of magnesium acetate as a catalyst were charged in the polymerization reactor. The monomers in the polymerization reactor were mixed by stirring at the rotating rate of the stirring wing of 50 rpm. 2 g of the monomer mixture in the polymerization reactor was taken out of the reactor and the water content therein was measured. 0.200 weight % of water content was detected in the monomer mixture. In other words, 4.92 g (0.27 moles) of H.sub.2O was present in the polymerization reactor.
[0115] The monomer which had been taken out of the reactor for the measurem...
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