A kind of oleate modified silicone defoamer for coating and preparation method thereof
An organosilicon defoamer and oleate technology are applied in the field of oleate modified organosilicon defoamer for coating and its preparation, which can solve the problem of poor compatibility, high melting point and easy demulsification of paper coating and coating. and other problems, to achieve the effect of solving demulsification and defoaming, good chemical stability and simple production process
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Embodiment 1
[0041] 1) Put isooctyl alcohol and oleic acid with a molar ratio of 1:0.85 in the reactor and start stirring, add 0.1% methanesulfonic acid catalyst of the total mass of the system materials, start to heat up and at the same time open the vacuum to -0.08MPa, and heat up to Insulate and react at 140°C for 6 hours, then turn off the vacuum to end the reaction to obtain the esterified intermediate A;
[0042]2) Put the esterified product intermediate A with a molar ratio of 1:1.5 and the hydrogen-containing silicone oil with a hydrogen content of 0.05% into another reaction kettle and start stirring, and remove it at a vacuum degree of -0.090MPa and a temperature of 85°C. Water, removal of low-boiling point impurities, the treatment time is 30min, then turn off the vacuum, add 0.1% chloroplatinic acid catalyst of the total mass of the system material, in N 2 Under ambient conditions, the temperature was raised to 90°C for 6 hours to complete the reaction, and the oleic acid ester...
Embodiment 2
[0046] 1) Put isooctyl alcohol and oleic acid with a molar ratio of 1:1 in the reactor and start stirring, add 0.25% p-toluenesulfonic acid catalyst of the total mass of the system materials, start to heat up and at the same time turn on the vacuum to -0.085MPa, heat up Heat the reaction at 120°C for 3 hours, and then turn off the vacuum to end the reaction to obtain the esterified intermediate A;
[0047] 2) Put the esterified product intermediate A with a molar ratio of 1:1 and the hydrogen-containing silicone oil with a hydrogen content of 0.1% in another reactor and start stirring, and carry out at a vacuum of -0.090MPa and a temperature of 90°C Remove water, remove low boiling point impurity treatment, treatment time is 20min, turn off vacuum then, add the chloroplatinic acid catalyst of 0.25% of system material gross mass, in N 2 Under ambient conditions, the temperature was raised to 100°C for 4 hours to complete the reaction, and the oleic acid ester modified silicone ...
Embodiment 3
[0051] 1) Put isooctyl alcohol and oleic acid with a molar ratio of 1:1.15 in the reactor and start stirring, add 0.5% sulfamic acid catalyst of the total mass of the system materials, start to heat up and at the same time turn on the vacuum to -0.09MPa, and heat up to Insulate and react for 4 hours at 160°C, then turn off the vacuum to end the reaction to obtain the esterified intermediate A;
[0052] 2) Put the esterified product intermediate A with a molar ratio of 1:0.5 and the hydrogen-containing silicone oil with a hydrogen content of 0.36% in another reactor and start stirring at a vacuum of -0.090MPa and a temperature of 95°C. Remove water, remove low boiling point impurity treatment, treatment time is 25min, turn off vacuum then, add the 0.5% chloroplatinic acid catalyst of system material gross mass, in N 2 Under ambient conditions, the temperature was raised to 115°C for 2 hours to complete the reaction, and the oleic acid ester modified silicone defoamer active sub...
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