Carbonic diester, aromatic polycarbonate, production apparatus, and process for production
A manufacturing method, polycarbonate technology, applied in the reaction device of stainless steel alloy, the manufacture of novel aromatic polycarbonate, the manufacture of aromatic polycarbonate, the device field with specific oxide film layer, can solve the incomplete To solve problems such as to achieve the effect of excellent storage stability
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Embodiment 1
[0334] A raw material melting tank with a stirrer of the reaction device, wherein 99.5% of the normal-pressure gas in the distribution pipe placed directly in front of the raw material melting tank for supplying powdery aromatic dihydroxy compound to the raw material melting tank is nitrogen . The linear velocity is 5 cm / min, and the condenser whose internal temperature is maintained at 110° C. is connected to the exhaust port of the raw material melting tank, and the pressure of the gas phase part in the raw material tank is controlled at 0 MPa˜0.05 MPa. 2,2-Bis(4-hydroxyphenyl)propane and molten diphenyl carbonate were fed into the melting tank in a predetermined ratio of 1 mole of the former to 1.01 mole of the latter. After complete melting, the molten mixture was transferred to a raw material storage tank maintained at 150°C.
[0335] Next, at a speed of 60kg / hour, this molten mixture is continuously added to a vertical stirring tank equipped with a rectification tower, ...
Embodiment 2
[0338] Polymerization was performed in a similar manner to Example 1, except that a condenser whose internal temperature was kept at 90° C. was used and the gas phase pressure of the raw material melting tank was kept at 0 MPa to 0.01 MPa.
[0339] As a result, the quality of the polycarbonate was measured two days after production, and [η] was 0.35, and the b value was 0.01. Example 3
Embodiment 3
[0340] Polymerization was carried out in a manner similar to Example 1, except that the gas scrubber was used instead of the condenser and the gas phase pressure of the raw material melting tank was maintained at 0 MPa to 0.01 MPa.
[0341] As a result, the quality of the polycarbonate was measured two days after production, and [η] was 0.35, and the b value was -0.05. Comparative example 1
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