Amorphous wholly aromatic polyester amide composition
A polyester amide and fully aromatic technology, which is applied in the field of amorphous wholly aromatic polyester amide compositions, can solve the problems of poor adhesion of different polymers, concurrent gelation, and insufficient stretchability, etc.
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[0083] Hereinafter, the present invention will be described in more detail using examples, but the present invention is not limited by these examples. The methods of measuring physical properties in Examples are as follows.
[0084] [melting point, glass transition temperature]
[0085] The temperature was measured with a differential scanning calorimeter (DSC7 manufactured by Perkin-Elmer) at a temperature increase of 20°C / min.
[0086] [melt viscosity]
[0087] At a temperature of 250°C and a shear rate of 1000sec -1 Under the condition of , use a capillograph manufactured by Toyo Seiki using an orifice with an inner diameter of 1 mm and a length of 20 mm.
[0088] [Adhesive strength]
[0089] A 100 μm-thick sheet of Admer SF731 manufactured by Mitsui Chemicals was used as a bonding counterpart material, and after hot plate welding at a temperature of 220° C., a 15 mm-wide peel test piece was cut out to measure the maximum peel strength.
manufacture example 1
[0090] Production Example 1 (production of liquid crystalline polymer (a))
[0091] Into a polymerization vessel equipped with a stirrer, a reflux column, a monomer input port, a nitrogen introduction port, and a decompression / outflow line, the following raw material monomers and metal catalysts (30 ppm based on K1 relative to the produced polymer) were charged. , an acylating agent (1.02 times the equivalent of the total of the amino group and the hydroxyl group), and start nitrogen substitution.
[0092] (A) 4-hydroxybenzoic acid 59.22g (20mol%)
[0093] (B) 161.38 g (40 mol %) of 2-hydroxyl-6-naphthoic acid
[0094] (C) Acetoxy-4-aminophenol 71.23g (20mol%)
[0095] (D) 64.81g (20 mol%) of isophthalic acid
[0096] Potassium acetate catalyst 22.5mg
[0097] Acetic anhydride 178.6g
[0098] After charging the raw materials, the temperature of the reaction system was raised to 140°C, and reacted at 140°C for 1 hour. Then, the temperature was raised to 330° C. over 3.3 h...
manufacture example 2
[0100] Production Example 2 (production of liquid crystalline polymer (b))
[0101]Polymerization was carried out in the same manner as in Production Example 1, except that the charge amount of the raw material monomers was as follows.
[0102] (A) 4-hydroxybenzoic acid 122.8g (40mol%)
[0103] (B) 125.48 g (30 mol %) of 2-hydroxy-6-naphthoic acid
[0104] (C) Acetoxy-4-aminophenol 55.39g (15mol%)
[0105] (D) 50.39g (15 mol%) of isophthalic acid
[0106] Potassium acetate catalyst 22.5mg
[0107] Acetic anhydride 196.7g
[0108] The obtained liquid crystalline polymer (b) showed no melting point, had a glass transition temperature of 136.4°C, and a melt viscosity of 173.1 Pa·s.
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