Vinyl styrene-butadiene latex as well as preparation method and application thereof
A vinyl styrene-butadiene and latex technology, which is used in conjugated diene coatings, coatings, asphalt coatings, etc., can solve the problems that water-emulsion rubber asphalt waterproof coatings cannot be applied, and powder rubber cannot be added.
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Embodiment 1
[0036]Using a 2L polymerization kettle, the feeding amount is 1200g in total, first evacuated, then replaced with nitrogen, and 12.8 parts of aqueous solutions (mass concentration of 27%) of all emulsifier sodium rosinate, molecular weight regulator tertiary ten, are added to the polymerization kettle at one time. 0.4 part of hexaalkyl mercaptan, 0.3 part of aqueous solution of sodium naphthalene methylene sulfonate as diffusing agent (30% by mass), 0.6 part of radical stabilizer cetylamine polyoxyethylene ether oxide, electrolyte hydrogen carbonate 0.1 part of sodium and 155 parts of deionized water, start stirring, when the temperature of the reactor reaches 5-10 ℃, add 70 parts of butadiene, 30 parts of styrene, 2 parts of N-vinylpyrrolidone, initiator hydrogen peroxide 0.15 parts of mantle was continuously added dropwise into the reaction kettle, and the temperature was raised to 30°C after 4 hours of reaction to continue the reaction. When the conversion rate reached more ...
Embodiment 2
[0042] Using a 2L polymerization kettle, the feeding amount is 1200g in total, first evacuated, then replaced with nitrogen, and 13.8 parts of aqueous solutions (mass concentration of 25%) of all emulsifier sodium rosinate, molecular weight regulator tertiary ten, are added to the polymerization kettle at one time. 0.3 part of dialkyl mercaptan, 0.3 part of aqueous solution of sodium lignosulfonate as diffusing agent (25% by mass), 0.4 part of stearylamine polyoxyethylene ether oxide as radical stabilizer, 0.1 part of electrolyte potassium chloride 70 parts of butadiene, 30 parts of styrene, 5 parts of N-vinyl caprolactam, initiator hydrogen peroxide to montane 0.1 part was continuously added dropwise into the reaction kettle, and the temperature was raised to 40° C. to continue the reaction after 5 hours of reaction. When the conversion rate reached more than 96.0%, the latex was transferred to the degassing kettle. The vacuum degree in the degassing kettle was -0.10Mpa, and t...
Embodiment 3
[0046] Use a 2L polymerization kettle, the charging amount is 1200g, first evacuated, then replaced with nitrogen, in the polymerization kettle, 8.9 parts of aqueous solutions (mass concentration of 28%) of all emulsifiers potassium oleate, molecular weight regulator tertiary ten are added at one time in the polymerization kettle. 0.4 part of hexaalkyl mercaptan, 0.4 part of aqueous solution of sodium methylene dinaphthalene sulfonate as diffusing agent (32% by mass), 0.2 part of free radical stabilizer cetylamine polyoxyethylene ether oxide, electrolyte carbonic acid 0.2 parts of sodium hydrogen and 145 parts of deionized water, start stirring, when the temperature of the reactor reaches 5-10 ° C, 70 parts of butadiene, 30 parts of styrene, 3.5 parts of 1,4-cyclohexyl dimethanol divinyl ether 0.15 parts of cumene hydrogen peroxide and 0.15 parts of initiator cumene hydrogen peroxide were continuously added dropwise into the reaction kettle, and the temperature was raised to 45...
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