Preparation method of epoxy propane-carbon dioxide copolymer
A technology of propylene oxide and carbon dioxide, which is applied in the field of preparation of propylene oxide-carbon dioxide copolymer, can solve the problems of difficulty in large-scale production of polymerization, large heat release in the polymerization process, and difficulty in removing heat in time, so as to achieve low catalyst consumption , reduce production costs, and respond quickly
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Embodiment 1
[0027] A kind of preparation method of propylene oxide-carbon dioxide copolymer of the present invention comprises the following steps:
[0028] (1) Preparation of crude product
[0029] Add propylene oxide with a water content of less than 50ppm into the polymerization reactor, then add a quantitative multi-component catalyst, control the stirring speed in the polymerization reactor to 10 rpm, and then pass carbon dioxide gas with a purity higher than 99.95% into the polymerization reactor In the reactor, control the pressure in the polymerization reactor to 3.0MPag, then control the reaction temperature in the polymerization reactor to 70°C, and continue the reaction for 5 hours until the viscosity of the material in the polymerization reactor reaches 7×10 5 After CP, the temperature of the polymerization reaction was controlled to 65°C, and the reaction was continued for 5 hours until the viscosity of the material in the polymerization reactor reached 7×10 6 After CP, the ...
Embodiment 2
[0038] A kind of preparation method of propylene oxide-carbon dioxide copolymer of the present invention comprises the following steps:
[0039] (1) Preparation of crude product
[0040] Add propylene oxide with a water content of less than 50ppm into the polymerization reactor, then add a quantitative multi-component catalyst, control the stirring speed in the polymerization reactor to 30 rpm, and then pass carbon dioxide gas with a purity higher than 99.95% into the polymerization reactor In the reactor, control the pressure in the polymerization reactor to 3.2MPag, then cool it through the jacket and coil, control the reaction temperature in the polymerization reactor to 74°C, and continue the reaction for 4.5 hours until the viscosity of the material in the polymerization reactor reaches 7 ×10 5 After CP, the temperature of the polymerization reaction was controlled to 667°C, and the reaction was continued for 4.8 hours until the viscosity of the material in the polymeriz...
Embodiment 3
[0050] Same as Example 1, the difference is that in step (1), the stirring speed in the polymerization reactor is controlled to 50 rpm, the pressure in the polymerization reactor is controlled to 3.4MPag, and then the reaction temperature in the polymerization reactor is controlled to 77°C. Continue to react for 3.5 hours until the viscosity of the material in the polymerization reactor reaches 7×10 5 After CP, the temperature of the polymerization reaction was controlled to 68.5°C, and the reaction was continued for 4.2 hours until the viscosity of the material in the polymerization reactor reached 7×10 6 After CP, the temperature of the material is lowered to 52°C to obtain the crude product of propylene oxide-carbon dioxide copolymer; the amount of propylene oxide added is 1 / 2 of the volume of the polymerization reactor, and the amount of multi-component catalyst added is 1 / 2 of the mass of propylene oxide. 1.8%; the mass ratio of diethyl zinc, yttrium trichloroacetate and ...
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