Preparation methods of alkaline polyether monomer and polycarboxylate water reducer
A technology of polycarboxylic acid and water reducer, which is applied in the field of concrete admixtures, and can solve problems such as increasing difficulty and reducing production efficiency
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Embodiment 1
[0068] Put vinyl glycol ether into a stainless steel high-pressure reaction kettle, the input amount is 564.46g, add 3.63g of potassium hydroxide solid, replace with nitrogen, then turn on the heating under stirring, and start to slowly pass into the reactor after the temperature rises to 110°C Add 2638.55g of ethylene oxide to carry out polymerization reaction, maintain the temperature at 110°C, and keep the pressure relatively constant at about 0.3MPa until all the ethylene oxide is added into the reactor and keep it warm for about 1 hour until the pressure of the reactor no longer drops. After vacuuming and degassing, the temperature was lowered to 80° C., and the material was discharged to obtain intermediate 1 with a molecular weight of 482.
Embodiment 2
[0070]Put diethylene glycol monovinyl ether into a stainless steel high-pressure reaction kettle, the input amount is 217.84g, add 1.15g of potassium hydroxide solid, replace with nitrogen, then turn on the heating under stirring, and start slowly to the reactor after the temperature rises to 110°C Introduce 935.97g of ethylene oxide into the reactor for polymerization, maintain the temperature at 110°C, and keep the pressure relatively constant at about 0.3MPa, until all the ethylene oxide is added into the reactor, and keep it warm for about 1 hour, until the pressure of the reactor no longer drops Time. After vacuuming and degassing, the temperature was lowered to 80° C., and the material was discharged to obtain intermediate 2 with a molecular weight of 675.
Embodiment 3
[0072] Put vinyl glycol ether into a stainless steel high-pressure reaction kettle with an input amount of 367.21g, add 3.81g of potassium hydroxide solid, replace with nitrogen, then turn on the heating under stirring, and start to slowly pass into the reactor after the temperature rises to 110°C Add 2974.06g of ethylene oxide to carry out polymerization reaction, maintain the temperature at 110°C, and keep the pressure relatively constant at about 0.3MPa until all the ethylene oxide is added into the reactor and keep it warm for about 1 hour until the pressure of the reactor no longer drops. After vacuuming and degassing, the temperature was lowered to 80° C., and the material was discharged to obtain intermediate 3 with a molecular weight of 768.
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