Polyether ketone ketone continuous production technology
A polyetherketone ketone and production process technology, applied in the field of polymer special engineering plastics, can solve the problems of inability to realize large-scale industrialized continuous production, short production cycle, low production cost, etc., achieve short production cycle, increase output, increase The effect of utilization efficiency
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Embodiment 1
[0034] The continuous production process of polyether ketone ketone comprises the following steps:
[0035] (1) 42.63kg of terephthaloyl chloride, 18.27kg of isophthaloyl chloride and 51.06kg of diphenyl ether are added to the mixing kettle, and then 100kg of dichloromethane is added for dissolving to obtain a mixed solution;
[0036] (2) Add 200kg of dichloromethane into the reactor, cool down to -15°C, then add 210kg of anhydrous aluminum chloride and 50kg of dimethylformamide to the reactor in batches for reaction to obtain a reaction solution;
[0037] (3) Add the mixed solution to the reaction solution, react at -15°C for 1h, and continue to react for 1h after heating up to 30°C to obtain a prepolymer;
[0038] (4) Add the prepolymer into the twin-screw reactor, control the reaction temperature at 40°C, and control the extrusion time at 30 minutes. After extrusion, the polymer is obtained, and the polymer is pulverized at the head of the twin-screw reactor. , while spray...
Embodiment 2
[0041] The continuous production process of polyether ketone ketone comprises the following steps:
[0042] (1) 36.54kg of terephthaloyl chloride, 24.36kg of isophthaloyl chloride and 51.06kg of diphenyl ether are added to the mixing kettle, and then 100kg of dichloromethane with a water content of 10-100ppm is added for dissolution to obtain a mixed solution ;
[0043] (2) Add 200kg of dichloromethane into the reactor, cool down to -15°C, then add 210kg of anhydrous aluminum chloride and 50kg of dimethylformamide to the reactor in batches for reaction to obtain a reaction solution;
[0044] (3) Add the mixed solution to the reaction solution, react at -15°C for 1h, and continue to react for 1h after heating up to 30°C to obtain a prepolymer;
[0045] (4) Add the prepolymer into the twin-screw reactor, control the reaction temperature at 40°C, and control the extrusion time at 30 minutes. After extrusion, the polymer is obtained, and the polymer is pulverized at the head of the...
Embodiment 3
[0048] The continuous production process of polyether ketone ketone comprises the following steps:
[0049] (1) 30.45kg of terephthaloyl chloride, 30.45kg of isophthaloyl chloride and 51.06kg of diphenyl ether are added to the mixing kettle, and then 100kg of dichloromethane with a water content of 10-100ppm is added for dissolution to obtain a mixed solution ;
[0050] (2) Add 200kg of dichloromethane into the reactor, cool down to -15°C, then add 210kg of anhydrous aluminum chloride and 50kg of dimethylformamide to the reactor in batches for reaction to obtain a reaction solution;
[0051] (3) Add the mixed solution to the reaction solution, react at -15°C for 1h, and continue to react for 1h after heating up to 30°C to obtain a prepolymer;
[0052] (4) Add the prepolymer into the twin-screw reactor, control the reaction temperature at 40°C, and control the extrusion time at 30 minutes. After extrusion, the polymer is obtained, and the polymer is pulverized at the head of t...
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