Production method of polyphenylene ether
A manufacturing method and polyphenylene ether technology, which are applied in the manufacturing field of polyphenylene ether, can solve problems such as unstable state and undisclosed variety changes, and achieve the effects of reducing production volume and stabilizing operation.
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[0178] Hereinafter, although an Example and a comparative example are given and this embodiment is demonstrated concretely, the scope of this embodiment is not limited to these Examples.
[0179] First, measurement methods for physical properties and characteristics applied to Examples and Comparative Examples are shown below.
[0180] (1) PPE concentration in PPE mixture
[0181] The PPE mixture solution after solution polymerization or concentration process was metered and dispensed to an aluminum tray, and dried at room temperature for 60 minutes. The sample whose surface was in a dry state was placed in a vacuum dryer together with an aluminum pan, the temperature of the vacuum dryer was set to 180° C., the pressure was reduced to 10 torr, and vacuum drying was carried out in this state for 120 minutes. The PPE concentration (mass %) in the PPE mixed liquid was calculated from the sample amount before and after drying.
[0182] (2) Reduced viscosity
[0183] For the 0.5...
manufacture example 1
[0192] In a 40-liter jacketed polymerization tank (the bottom of the polymerization tank is equipped with a nozzle for introducing oxygen-containing gas, a turbine impeller and a baffle, and the exhaust line on the upper part of the polymerization tank is equipped with a reflux condenser), one side is filled with 0.5 L Nitrogen gas was blown in at a flow rate of 4.57 g, 24.18 g of 47 mass % hydrogen bromide aqueous solution, 11.00 g of di-tert-butylethylenediamine, 62.72 g of di-n-butylamine, 149.92 g of butyldimethylamine, 20.65kg of toluene and 3.12kg of 2,6-dimethylphenol were stirred until a uniform solution was formed and the inner temperature of the polymerization tank was 25°C.
[0193] Next, dry air was introduced from the nozzle into the polymerization tank at a rate of 32.8 NL / min to initiate polymerization. Dry air was blown for 140 minutes to obtain a polymerization mixture. In addition, during polymerization, internal temperature was controlled to 40 degreeC. Th...
manufacture example 2
[0198] A PPE polymerization liquid was produced in the same manner as in Production Example 1 except that the ventilation time of the dry air was 90 minutes. The PPE concentration in the obtained PPE polymerization solution was 13.1% by mass. The obtained PPE polymerization liquid is referred to as PPE polymerization liquid (2).
[0199] The reduced viscosity of the polyphenylene ether particles in a dry state obtained in the same manner as in Production Example 1 from a portion of the obtained PPE polymerization solution (2) was 0.323 dL / g.
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