Unsaturated ethylenic polyether monomer for concrete water reducer and preparation method thereof
A technology of concrete water reducing agent and alkenyl polyether, which is applied in the field of building materials, can solve the problems of affecting product application performance, many side reactions, and low double bond retention rate, so as to avoid broadening of product molecular weight distribution and improve application effect , to avoid the effect of product performance degradation
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Embodiment 1
[0032] (1) Add 8 to 50 parts by weight of acetylenic alcohol and 0.01 to 0.22 parts by weight of a basic catalyst in the reactor, and react under a nitrogen atmosphere, the reaction temperature is 30 to 90 ° C, and the reaction time is 0.5 to 3.5 hours;
[0033] (2) Continue to heat up to 90-130°C with a heating rate of 0.5-2.0°C / min, and then continuously feed 45-210 parts by weight of ethylene oxide and / or propylene oxide into the reactor to maintain the temperature of the reactor. The pressure inside is 0.4~0.6MPa, continue to react for 4~10h after feeding, and then lower the temperature to 40~60℃, the cooling rate is 0.2~2.5℃ / min;
[0034] (3) Continue to add 0.01 to 0.22 parts by weight of the basic catalyst to the reactor, raise it to 90 to 130°C at a rate of 0.5 to 2.0°C / min, and react under a nitrogen atmosphere, and continuously feed 800 ~950 parts by weight of ethylene oxide and / or propylene oxide, to maintain the pressure in the reactor is 0.4 ~ 0.6MPa, continue to ...
Embodiment 2
[0038](1) Add 10 parts by weight of 2-propyn-1-alcohol and 0.05 parts by weight of sodium metal to the reactor, and react under a nitrogen atmosphere with a reaction temperature of 50°C and a reaction time of 3 hours;
[0039] (2) Continue to heat up to 90°C with a heating rate of 0.2°C / min, then continuously feed 50 parts by weight of ethylene oxide into the reactor to maintain the pressure in the reactor at 0.4MPa, and continue to React for 4 hours, then lower the temperature to 60°C at a cooling rate of 0.5°C / min;
[0040] (3) Continue to add 0.1 parts by weight of sodium metal to the reactor, and continuously feed 920 parts by weight of ethylene oxide into the reactor under a nitrogen atmosphere and a reaction temperature of 90°C (the heating rate is 0.2°C / min). Alkanes, in order to maintain the pressure in the reactor at 0.4MPa, continue to react for 6h after feeding, and then lower the temperature to 60°C, the cooling rate is 0.5°C / min;
[0041] (4) Add 0.1 parts by wei...
Embodiment 3
[0044] (1) Add 30 parts by weight of 2-methyl-3-butyn-2-ol and 0.01 parts by weight of sodium hydroxide to the reactor, and react under a nitrogen atmosphere, the reaction temperature is 30 ° C, and the reaction time is 3h ;
[0045] (2) Continue to heat up to 90°C with a heating rate of 0.8°C / min, then continuously feed 50 parts by weight of ethylene oxide into the reactor to maintain the pressure in the reactor at 0.5MPa, and continue to React for 6 hours, then lower the temperature to 60°C at a cooling rate of 0.2°C / min;
[0046] (3) Continue to add 0.05 parts by weight of sodium hydroxide to the reactor, and continuously feed 920 parts by weight of epoxy resin into the reactor under a nitrogen atmosphere and a reaction temperature of 90°C (heating rate is 0.8°C / min). Ethane, to maintain the pressure in the reactor at 0.5MPa, continue to react for 6h after feeding, and then lower the temperature to 60°C at a cooling rate of 0.2°C / min;
[0047] (4) Add 0.2 parts by weight ...
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