A process for purifying polysulfone resin material by critical phase change extraction
A technology of polysulfone resin and extraction method, which is applied in the field of purification of polysulfone resin materials by critical phase change extraction method, can solve the problems of difficult recycling, high ash content of products, and decline in product performance, and achieve uniform product performance and The effect of low ash content and low production cost
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[0036] The preparation process of the polysulfone resin solution is as follows: the mixture of phenolic substance and sulfone substance is put into the reaction kettle as raw material, acid binding agent, solvent and water-carrying agent according to the proportion, and the reaction kettle is evacuated and nitrogen purged , The nitrogen standard is high-purity nitrogen, the total time of the polymerization reaction with water above 150℃ is 12~20h, the temperature in the kettle reaches 150~220℃, and the reaction is ended when the viscosity in the kettle reaches the requirement. The known range of the viscosity of the polysulfone material polymerization solution is 4000-12000 mpa.s, all of which are suitable for the purification process of the present invention.
[0037] After the reaction is completed, the polymerization solution in the reaction kettle is cooled and diluted to 80-90° C., and then the polysulfone resin solution is purified by the process of the present invention....
Embodiment 1
[0040] The process for purifying the polysulfone resin material by the critical phase change extraction method of the present embodiment specifically includes the following steps:
[0041] Add 8.78kg of 4,4'-dichlorodiphenylsulfone, 7.35kg of bisphenol S, 5.44kg of potassium carbonate, 60kg of solvent sulfolane, 15kg of xylene with water agent into the 100L polymerization reaction kettle, and vacuumize the kettle to ≤0.08MPa Then, nitrogen was introduced to make the pressure in the kettle reach ≥ 0.01MPa. After nitrogen replacement three times, the reaction at normal pressure in the kettle was maintained. The polymerization temperature was 200°C, the polymerization time was 14h, and the polymerization stirring speed was 100r / min. When the polyethersulfone resin solution reaches the target viscosity of 8000mpa.s, the reaction ends.
[0042] After the reaction is completed, the heating temperature of the heating medium in the kettle is lowered from 200 ° C to 90 ° C, and fresh s...
Embodiment 2
[0046] The process for purifying the polysulfone resin material by the critical phase change extraction method of the present embodiment specifically includes the following steps:
[0047] 9.2kg of 4,4'-dichlorodiphenyl sulfone, 6.41kg of bisphenol A, 5.27kg of potassium carbonate, 65kg of solvent dimethylacetamide, 20kg of water agent xylene were added to the 100L polymerization reaction kettle, and the kettle was evacuated After reaching ≤0.08MPa, nitrogen was introduced to make the pressure in the kettle reach ≥0.01MPa. After three nitrogen replacements, the reaction at normal pressure in the kettle was maintained. The polymerization temperature was 164°C, the polymerization time was 12h, and the polymerization stirring speed was 200r / min. When the polysulfone resin solution reaches the target viscosity of 6500mpa.s, the reaction ends.
[0048] After the reaction, the heating temperature of the heating medium in the kettle was lowered from 164°C to 85°C, and fresh dimethyla...
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