A kind of preparation method of emulsifier and its use in preparing pesticide emulsifiable concentrate
An emulsifier and bimetallic catalyst technology, applied in chemical instruments and methods, botanical equipment and methods, applications, etc., can solve the problem of poor emulsification and dispersion effects of emulsifiers, inability to store stably for a long time, and the addition of emulsifiers and organic solvents. Large and other problems, to achieve the effect of less emulsifier and organic solvent, good emulsifying and dispersing effect, and good fluidity
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Embodiment 1
[0033] This embodiment provides a kind of preparation method of emulsifier, comprising,
[0034]S1. Using 100kg of n-hexanol as an initiator, the temperature was raised to 140°C after nitrogen replacement, and under the catalysis of 0.13kg of zinc-cobalt double metal cyanide complex catalyst, 2510kg of a mixture of propylene oxide and butylene oxide was added for reaction. The mass ratio of propylene oxide to butylene oxide is 0.6, the reaction temperature is 140° C., and the polymer intermediate is obtained after aging and degassing.
[0035] S2. Under the action of 18.4kg of sodium hydride, the polymer intermediate obtained in S1 is subjected to a capping reaction with 1673kg of ethylene oxide. The temperature of the capping reaction is 120°C, ripened and degassed, and then cooled to 70°C and then added with lactic acid Neutralization is carried out, and the pH after neutralization is 6, and finally 4283kg of emulsifier is obtained.
[0036] This embodiment also provides th...
Embodiment 2
[0038] This embodiment provides a kind of preparation method of emulsifier, comprising,
[0039] S1. Put 100kg of propanol as an initiator, put it into the reactor together with 0.06kg of zinc-cobalt double metal cyanide complex catalyst, replace it with nitrogen and raise the temperature to 120°C, add propylene oxide and butylene oxide into the reactor A mixture of 4230kg of alkanes was reacted, wherein the mass ratio of propylene oxide to butylene oxide was 0.1, and the reaction temperature was 120°C. After aging and degassing, a polymer intermediate was obtained.
[0040] S2, add 4kg metal sodium catalyst to the reaction kettle, under the catalysis of metal sodium, the polymer intermediate obtained in S1 is subjected to capping reaction with 3490kg ethylene oxide, the temperature of the capping reaction is 110°C, the aging After cooling to 60°C, add acetic acid for neutralization. After neutralization, the pH is 7, and finally 7820kg of emulsifier is obtained.
[0041] The...
Embodiment 3
[0044] This embodiment provides a kind of preparation method of emulsifier, comprising,
[0045] S1. Put 100kg of n-butanol as the initiator, and put it into the reactor together with 0.31kg of zinc-cobalt double metal cyanide complex catalyst. After nitrogen replacement, the temperature is raised to 180°C, and propylene oxide and epoxy are added to the reactor. A mixture of 3370 kg of butane was reacted, wherein the mass ratio of propylene oxide to butylene oxide was 1.2, and the reaction temperature was 180° C. After ripening and degassing, a polymer intermediate was obtained.
[0046] S2. Add 42.7kg of sodium hydroxide catalyst to the reactor, and carry out capping reaction with 1872kg of ethylene oxide with the polymer intermediate obtained in S1 under the catalysis of sodium hydroxide. The temperature of the capping reaction is 150°C , aging and degassing, after cooling down to 100°C, citric acid was added for neutralization, the pH after neutralization was 5, and finally...
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