Wholly aromatic polyester, polyester resin composition, and polyester molded article
A technology of wholly aromatic polyester and polyester resin, applied in the direction of one-component polyester rayon, one-component copolyester rayon, etc. Problems such as cracks and insufficient heat resistance occur, resulting in less warpage deformation, good formability, and excellent flatness
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Embodiment 1
[0167] The following raw material monomers, a metal catalyst, and an acylating agent were put into a polymerization vessel equipped with a stirrer, a reflux column, a monomer inlet, a nitrogen inlet, and a decompression / outflow line, and nitrogen replacement was started.
[0168] (1) 4-hydroxybenzoic acid: 145g (48 mol%) (HBA)
[0169] (II) 6-hydroxy-2-naphthoic acid: 12g (3 mol%) (HNA)
[0170] (III) Terephthalic acid: 89g (24.7 mol%) (TA)
[0171] (IV) Resorcinol: 8g (3.5 mol%) (RES)
[0172] (V) 4,4'-Dihydroxybiphenyl 85g (20.8 mol%) (BP)
[0173] Potassium acetate catalyst: 15mg
[0174] Acetic anhydride: 229g
[0175] After feeding the raw materials, the temperature of the reaction system was raised to 140° C. and reacted at 140° C. for 3 hours. Then, the temperature was raised to 360° C. over 5.5 hours, and then the pressure was reduced to 10 Torr (that is, 1330 Pa) over 20 minutes, and melt polymerization was carried out while distilling acetic acid, excess acetic ...
Embodiment 2~3
[0179] Except that the kinds and charging ratios of the raw material monomers were as shown in Table 1, polymerization was carried out in the same manner as in Example 1, and the polymer was discharged from the lower part of the polymerization vessel. Table 1 shows the results of physical property measurements of the obtained polymers.
Embodiment 4
[0187] The following raw material monomers, a metal catalyst, and an acylating agent were put into a polymerization vessel equipped with a stirrer, a reflux column, a monomer inlet, a nitrogen inlet, and a decompression / outflow line, and nitrogen replacement was started.
[0188] (1) 4-hydroxybenzoic acid: 1061g (48 mol%) (HBA)
[0189] (II) 6-hydroxy-2-naphthoic acid: 90g (3 mol%) (HNA)
[0190] (III) Terephthalic acid: 657g (24.7 mol%) (TA)
[0191] (IV) Resorcinol: 62g (3.5 mol%) (RES)
[0192] (V) 4,4'-dihydroxybiphenyl 620g (20.8 mol%) (BP)
[0193] Potassium acetate catalyst: 110mg
[0194] Acetic anhydride: 1676g
[0195] After feeding the raw materials, the temperature of the reaction system was raised to 140° C. and reacted at 140° C. for 3 hours. Then, the temperature was raised to 360° C. over 5.5 hours, and then the pressure was reduced to 5 Torr (ie, 667 Pa) over 20 minutes, and melt polymerization was carried out while distilling acetic acid, excess acetic a...
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Abstract
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