Method for preparing diene-based rubber polymer, diene-based rubber polymer prepared thereby, core-shell structured acrylonitrile-butadiene-styrene graft copolymer comprising same
A technology of diene rubber and graft copolymer, which is applied in the field of acrylonitrile-butadiene-styrene graft copolymer, can solve the problems of reduced impact resistance, reduced transparency, reduced swelling index, etc., to achieve improved impact Strength properties, improvement of swelling index, effect of low gel content
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[0027] The present invention provides a kind of preparation method of diene rubber polymer, and described diene rubber polymer can have lower gel content and higher swelling index, has higher conversion rate simultaneously, therefore, described The polymer can be easily used as a rubber component of an acrylonitrile-butadiene-styrene graft copolymer of a core-shell structure.
[0028] The method for preparing a diene rubber polymer according to one embodiment of the present invention is characterized by comprising:
[0029] Add 50 parts by weight to 75 parts by weight of conjugated diene monomer, 1 part by weight to 4 parts by weight of emulsifier and 0.1 part by weight to 0.5 parts by weight of molecular weight control agent, and then make them undergo the first the step of aggregation (step 1);
[0030] At the point in time when the polymerization conversion rate in (step 1) is 10% to 40%, 25 parts by weight to 50 parts by weight of conjugated diene monomers are continuousl...
Embodiment 1
[0072] 1) Preparation of diene rubber polymer
[0073] Add 65 parts by weight of ion-exchanged water, 70 parts by weight of 1,3-butadiene, potassium rosinate of 1.5 parts by weight, potassium oleate of 0.8 parts by weight, 0.8 parts by weight of potassium carbonate (K 2 CO 3 ), 0.3 parts by weight of tertiary dodecyl mercaptan (TDDM) and 0.3 parts by weight of potassium persulfate (K 2 S 2 o 8 ), and then reacted at 70° C. until the polymerization conversion reached 30% (the first polymerization). Then, 30 parts by weight of 1,3-butadiene was continuously added over 6 hours, and then, from the time point of continuous addition, the reaction temperature was slowly raised over 10 hours until the reaction temperature reached 80° C. (second polymerization ). In this case, when the polymerization conversion rate reached 55%, 0.05 parts by weight of t-dodecylmercaptan was further added thereto and reacted. Then, when the polymerization conversion rate reached 93%, the reactio...
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