Mud resistant type water reducing agent and preparation method therefor
A water-reducing agent and anti-mud type technology, which is applied in the field of anti-mud-type water reducing agent and its preparation, can solve the problems of high price of cationic monomer, influence on the performance of water reducing agent, and increasing the comprehensive cost of concrete admixtures, etc. The effect of using less monomer, increasing steric hindrance, and good mud resistance
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Embodiment 1
[0046] In the reaction kettle with negative pressure conditions, start stirring, add dimethyl carbonate and sulfuric acid, slowly raise the temperature to 80-90°C, and double drop 1-butenol and hydroquinone into the reaction kettle. Wherein, the feeding molar ratio of the three reactants is: dimethyl carbonate: 1-butenol: hydroquinone = 1: 1.5: 1.5, and the catalyst addition is 0.2% of the total feeding mass. As the reaction proceeds, the product methanol is continuously discharged from the system. When the methanol no longer flows out, the temperature is lowered for 20 minutes and the material is discharged. According to the difference in boiling point, the product is subjected to vacuum distillation to separate by-products to obtain the starting agent.
[0047] 207 g of starter and 1.0 g of KOH were added to the high pressure reactor. Seal the device and replace it with nitrogen 3 times. Start stirring, heat up, and when the temperature reaches 110°C, feed 10g of ethylene ...
Embodiment 2
[0053] In the reaction kettle with negative pressure conditions, start stirring, add dimethyl carbonate and sulfuric acid, slowly raise the temperature to 80-90°C, and double drop 1-butenol and hydroquinone into the reaction kettle. Wherein, the feeding molar ratio of the three reactants is: dimethyl carbonate: 1-butenol: hydroquinone = 1: 1.5: 1.5, and the catalyst addition is 0.2% of the total feeding mass. As the reaction proceeds, the product methanol is continuously discharged from the system. When the methanol no longer flows out, the temperature is lowered for 20 minutes and the material is discharged. According to the difference in boiling point, the product is subjected to vacuum distillation to separate by-products to obtain the starting agent.
[0054] 207 g of starter and 1.0 g of KOH were added to the high pressure reactor. Seal the device and replace it with nitrogen 3 times. Start stirring, heat up, and when the temperature reaches 110°C, feed 10g of ethylene ...
Embodiment 3
[0060] In a reaction kettle with negative pressure conditions, start stirring, add dimethyl carbonate and sulfuric acid, slowly raise the temperature to 80-90°C, and double drop 2-methyl-heptenol and p-hydroxybenzyl alcohol into the reaction kettle. Wherein, the molar ratio of the three reactants is: dimethyl carbonate: 2-methyl-heptenol: p-hydroxybenzyl alcohol = 1:1.5:1.5, and the catalyst addition is 0.2% of the total mass of the feed. As the reaction proceeds, the product methanol is continuously discharged from the system. When the methanol no longer flows out, the temperature is lowered for 20 minutes and the material is discharged. According to the difference in boiling point, the product is subjected to vacuum distillation to separate by-products to obtain the starting agent.
[0061] 277 g of starter and 1.0 g of KOH were added to the high pressure reactor. Seal the device and replace it with nitrogen 3 times. Start stirring, heat up, and when the temperature reache...
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