A kind of high molecular weight unsaturated polyether macromonomer and its preparation method and application
A polyether macromonomer and high molecular weight technology, applied in the field of polyether macromonomers, can solve the problems of limited transportation distance, increased transportation costs, and increased production costs, and achieve low production costs, controllable molecular structure, and high double bond retention rate effect
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Embodiment 1
[0053] After adding 230 parts of allylamine to the reaction kettle at room temperature, add 1 part of potassium hydroxide solid to the reaction kettle, pass in nitrogen to replace the air in the reaction kettle, and then heat the reaction kettle to 70 °C, vacuumize to obtain the reaction starter with catalyst under vacuum conditions. When the material in the reactor was heated to 70°C, 1408 parts of ethylene oxide (EO) was slowly and continuously added to the reactor for polymerization reaction, and the reaction temperature was controlled at about 80°C to maintain a relatively stable pressure in the reactor. Until all ethylene oxide (EO) is added into the reactor, the aging reaction is carried out at a constant temperature of 80° C. for 60 minutes. When the pressure of the reactor no longer drops, the material is discharged to obtain a polyether intermediate.
[0054] Add 200 parts of intermediates to the high-pressure reactor, and then add 2 parts of potassium hydroxide soli...
Embodiment 2
[0056] After adding 300 parts of 2-methallyl alcohol to the reactor at room temperature, add 1 part of potassium hydroxide solid to the reactor, feed nitrogen into the reactor to replace the air, and then, under stirring conditions, The reaction kettle was heated to 90° C., and vacuumized to obtain a reaction starter with a catalyst under vacuum conditions. When the materials in the reactor were heated to 90°C, the mixture of ethylene oxide (EO) and butylene oxide (BO) was slowly introduced into the reactor (mass ratio butylene oxide (BO): ethylene oxide (EO)=21.5:100), the amount of feeding is 1804 parts to carry out the polymerization reaction, the reaction temperature is controlled to be about 100°C, and the pressure in the kettle is kept relatively stable. Until the mixture of ethylene oxide (EO) and butylene oxide (BO) is completely added into the reactor, the aging reaction is carried out at a constant temperature of 100° C. for 60 minutes. When the pressure of the reac...
Embodiment 3
[0059] After adding 280 parts of 2-methallyl alcohol into the reaction kettle at room temperature, add 1 part of sodium methoxide solid into the reaction kettle, pass in nitrogen to replace the air in the reaction kettle, and vacuumize to obtain Catalyst reaction starter. Start the heating, and when the materials in the reactor are heated to 95°C, start to slowly feed the mixture of ethylene oxide (EO) and propylene oxide (PO) into the reactor (mass ratio propylene oxide (PO): ethylene oxide Alkane (EO)=21.5:100), the feed rate is 1300 parts to carry out the polymerization reaction, the reaction temperature is controlled to be about 100°C, and the pressure in the kettle is kept relatively stable. Until the mixture of propylene oxide (PO) and ethylene oxide (EO) is completely added into the reactor, the aging reaction is carried out at a constant temperature of 100° C. for 60 minutes. When the pressure of the reactor no longer drops, the temperature is lowered to 80° C., and t...
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