Preparation method of monomer-terminated amine ether for synthesizing early-strength polycarboxylate superplasticizer
A technology of capping amine ether and polycarboxylic acid, which is applied in the field of polycarboxylate superplasticizer monomer polyether synthesis, can solve the problems of large air-entraining volume, achieve the effects of reducing air-entraining volume, excellent product performance, and wide application range
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Embodiment 1
[0024] ①Synthesis of crude block monomer amine ether: Add 110g of N-methallylamine and 1.34g of catalyst KOH to 1# reactor (2L), and the catalyst accounts for 0.09% of the total feed. Use high-purity N2 to replace the air in the reactor three times, keep the nitrogen pressure in the reactor at 0.3-0.5 MPa, raise the temperature to 95° C., and feed 42.3 g of ethylene oxide. After the reaction is initiated successfully, set the reaction temperature T=110-130°C, keep the temperature and under the condition of reaction pressure P<0.8MPa, continuously feed the first stage of ethylene oxide 643.1g into the reaction kettle, the first stage The amount of ethylene oxide (comprising the amount of initiation) that passes into the section is 76% of the total feed amount of ethylene oxide, and slaking is carried out after the feeding is completed; in the reactor, feed propylene oxide 528.8g continuously, The mass ratio of propane to ethylene oxide is 1:1.6, and after the feed is completed,...
Embodiment 2
[0028] ①Synthesis of crude block monomer amine ether: Add 95g of N-methallylamine and 1.72g of catalyst KOH to 1# reactor (2L), and the catalyst accounts for 0.11% of the total feed. Use high-purity N2 to replace the air in the reactor three times, keep the nitrogen pressure in the reactor at 0.3-0.5 MPa, raise the temperature to 95° C., and feed 49.1 g of ethylene oxide. After the reaction is initiated successfully, set the reaction temperature T=110-130°C, keep the temperature and under the condition of reaction pressure P<0.8MPa, continuously feed the first stage of ethylene oxide 785.3g into the reaction kettle, the first stage The amount of ethylene oxide (comprising the amount of initiation) that passes into the section is 80% of the total feed amount of ethylene oxide, and is matured after the feeding is completed; then continuously feeds 490.8g of propylene oxide in the reactor, The mass ratio of propane to ethylene oxide is 1:2, after the feeding is completed, it is m...
Embodiment 3
[0032] ①Synthesis of crude block monomer amine ether: Add 100g of N-methallylamine and 2.1g of catalyst KOH to 1# reactor (2L), and the catalyst accounts for 0.12% of the total feed. Use high-purity N2 to replace the air in the reactor three times, keep the nitrogen pressure in the reactor at 0.3-0.5 MPa, raise the temperature to 95° C., and feed 58.9 g of ethylene oxide. After the reaction is initiated successfully, set the reaction temperature T=110-130°C, keep the temperature and under the condition of reaction pressure P<0.8MPa, continuously feed the first stage of ethylene oxide 1001.8g into the reactor, the first stage The amount of ethylene oxide (comprising the amount of initiation) that passes into the section is 85% of the total feed amount of ethylene oxide, and aging is carried out after the feeding is completed; The mass ratio of propane to ethylene oxide is 1:2.5, and after the feeding is completed, it is matured; finally, 176.8 g of the second stage of ethylene ...
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