Noncrystalline, wholly aromatic polyesteramide
A wholly aromatic, polyester amide technology, applied in the field of amorphous wholly aromatic polyester amide, can solve the problems of insufficient stretchability, unusability, poor adhesion of dissimilar polymers, etc.
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Method used
Examples
Embodiment 1
[0057] In the polymerization vessel that possesses stirrer, reflux column, monomer input port, nitrogen import port, decompression / outflow pipeline, pack following raw material monomer, metal catalyst (relative to the resin that produces in K + Nitrogen substitution was started with an acylating agent (1.02 times the total equivalent of the amino group and hydroxyl group) based on 30 ppm).
[0058] (A) 4-hydroxybenzoic acid 59.22g (20mol%)
[0059] (B) 161.38 g (40 mol %) of 2-hydroxyl-6-naphthoic acid
[0060] (C) Acetoxy-4-aminophenol 71.23g (20mol%)
[0061] (D) 64.81g (20 mol%) of isophthalic acid
[0062] Potassium acetate catalyst 22.5mg
[0063] Acetic anhydride 178.6g.
[0064] After charging the raw materials, the temperature of the reaction system was raised to 140°C and allowed to react at 140°C for 1 hour. Thereafter, the temperature was raised to 330° C. over 3.3 hours, and then the pressure was reduced to 10 Torr (that is, 1330 Pa) over 20 minutes. Melt poly...
Embodiment 2-10、 comparative example 2-6
[0076] The types and charging amounts of the raw material monomers are shown in Table 1-2, and polymerization was carried out in the same manner as in Example 1 except that. Tables 1-2 show these results. Regarding Comparative Examples 3 and 4, the melting point was high, and the melt viscosity and the like could not be measured under the above-mentioned implementation conditions. Regarding Comparative Example 5, the resin could not be polymerized.
[0077] Example
1
2
3
4
5
6
7
8
9
10
HBA (mol%)
20
40
40
30
26
34
20
40
40
40
HNA (mol%)
40
20
40
30
34
26
20
30
30
30
TA (mol%)
7.5
5
IA (mol%)
20
20
10
20
20
20
30
15
7.5
10
BP (mol%)
APAP(mo...
Embodiment 11
[0087] The manufacture of embodiment 11 inflation film
[0088] The polymer of Example 8 was melt-kneaded and pelletized using a twin-screw extruder (PCM30 manufactured by Ikegai Steel Co., Ltd.) at a cylinder temperature of 230° C., an extrusion rate of 8 kg / h, and a rotation speed of 150 rpm.
[0089] Next, a die with a die-core gap of 0.7 mm and a Φ25 mm was installed on Toyo Seiki's LABOPLASTMILL, and an inflatable film was produced at a resin temperature of 230°C and a die temperature of 230°C. At this time, while adjusting the amount of resin extruded, the pulling speed, and the air volume of the blower, the thickness of the wall can be reduced to the maximum within the range where the film can be stably formed, and the ratio of the film thickness to the die-core gap is obtained as a drawing. sexual indicators.
[0090] Winding speed(m / min)
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Abstract
Description
Claims
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