Acetyl terminated polyester and preparation method thereof
A technology of acetyl-terminated polyether, which is applied in the field of acetyl-terminated polyether and its preparation, can solve the problems of increased hydroxyl value and lower capping rate, etc.
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Embodiment 1
[0026] A kind of preparation method of acetyl-terminated polyether of the present embodiment, comprises the steps:
[0027] Add 1600 parts of allyl alcohol atactic polyether (M=5000) and 82 parts of acetic anhydride into the reactor, connect it to a condensing reflux device, raise the temperature to 130°C to 140°C, and reflux for 2.5 hours. Connect to the distillation device, adjust the amount of nitrogen gas, at 120°C ~ 130°C, vacuum degree -0.080MPa ~ -0.085MPa, deacidify by bubbling for 2.5 hours. Cool down to 70°C, transfer to falling film evaporator, deacidify for 1.5 hours under the condition of temperature 100-120°C, vacuum degree ≤100Pa, cool down to 70°C, add 20 parts of heptane, , under the condition of vacuum degree of -0.097MPa, desolventize for 1 hour, and cool down to 60°C to obtain acetyl-terminated allyl alcohol random polyether, with a hydroxyl content of 15ppm, an acetic acid content of 30ppm, an acetic anhydride content of 0ppm, and a moisture content of is...
Embodiment 2
[0031] A kind of preparation method of acetyl-terminated polyether of the present embodiment, comprises the steps:
[0032] Add 1600 parts of allyl alcohol atactic polyether (M=7000) and 68 parts of acetic anhydride to the reactor, connect it to a condensing reflux device, raise the temperature to 130°C-140°C, and reflux for 2.5 hours. Connect to the distillation device, adjust the amount of nitrogen gas to make the vacuum degree be -0.085MPa~-0.090MPa, and deacidify by bubbling for 3.0 hours. Cool down to 70°C, transfer to a falling film evaporator, deacidify at a temperature of 110-130°C, vacuum ≤ 100Pa for 2.0 hours, cool down to 70°C, add 18 parts of octane, at a temperature of 110°C-120°C , under the condition of vacuum degree of -0.098MPa, desolventize for 1.5 hours, and cool down to 60°C to obtain acetyl-terminated allyl alcohol random polyether, with a hydroxyl content of 10ppm, an acetic acid content of 30ppm, an acetic anhydride content of 0ppm, and a moisture conten...
Embodiment 3
[0036] A kind of preparation method of acetyl-terminated polyether of the present embodiment, comprises the steps:
[0037] Add 1600 parts of allyl alcohol polyoxyethylene ether (M=400) and 530 parts of acetic anhydride into the reactor, connect it to a condensing reflux device, raise the temperature to 130°C to 140°C, and reflux for 3.0 hours. Connect to the distillation device, adjust the amount of nitrogen gas to make the vacuum degree be -0.085MPa~-0.090MPa, and deacidify by bubbling for 3.0 hours. Cool down to 70°C, transfer to falling film evaporator, deacidify for 2.0 hours at a temperature of 110-130°C, vacuum degree ≤100Pa, cool down to 70°C, add 30 parts of octane, , under the condition of vacuum degree of -0.098MPa, desolventize for 1.5 hours, and cool down to 60°C to obtain acetyl-terminated allyl alcohol polyoxyethylene ether, the content of hydroxyl is 32ppm, the content of acetic acid is 55ppm, the content of acetic anhydride is 0ppm, and the moisture content i...
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