Method for restraining gelatin during preparation of conjugated diolefin and monovinyl aromatic hydrocarbons random polymers
A technology of conjugated diene and monovinyl arene, which is applied in the field of inhibiting gel, can solve the problems of limiting the application range of the gel inhibiting system, increasing the production cost and the like, and achieves the advantages of inhibiting the formation of gel, low cost and easy availability of raw materials. Effect
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Embodiment 1
[0038] The test was carried out in a 10-liter polymerization kettle by batch polymerization method. Under the protection of high-purity nitrogen, 4810g of mixed solvent (cyclohexane and n-hexane, weight ratio of 88:12), 225g of styrene, and additive THF11 were added to the kettle in sequence. .4g, the polymerization system was purified by high-purity N 2 After displacement and deoxidation, 624 g of 1,3-butadiene, 5.9 g of a coagulant 1-hexene, and 0.73 g of n-butyllithium were added, and then a copolymerization reaction was carried out. The polymerization initiation temperature is 50° C., and the reaction pressure is 0.1-0.3 MPa. When the polymerization temperature reaches 80° C., add 0.30 g of the second-step initiator n-butyllithium, and when the conversion rate reaches 100%, add 0.33 g of tin tetrachloride to the polymerization kettle to continue the coupling reaction. After the coupling reaction is finished, add 0.5 g of terminator isopropanol and anti-aging agent 2246 to...
Embodiment 2
[0040] The test was carried out in a 10-liter polymerization kettle by a batch polymerization method. Under the protection of high-purity nitrogen, 4810 g of mixed solvent (cyclohexane and n-hexane, with a weight ratio of 88:12), 225 g of styrene, and the additive THF were sequentially added to the kettle. 11.4g, the polymerization system was treated with high-purity N 2 After displacement and deoxidation, 624 g of 1,3-butadiene, 59 g of a coagulation inhibitor 1-hexene, and 0.73 g of n-butyllithium were added, and then a copolymerization reaction was carried out. The polymerization initiation temperature is 50° C., and the reaction pressure is 0.1-0.3 MPa. When the polymerization temperature reaches 80° C., add 0.30 g of the second-step initiator n-butyllithium, and when the conversion rate reaches 100%, add 0.33 g of tin tetrachloride to the polymerization kettle to continue the coupling reaction. After the coupling reaction, 0.5 g of terminator isopropanol and 10 g of anti...
Embodiment 3
[0042] The test was carried out in a 10-liter polymerization kettle by a batch polymerization method. Under the protection of high-purity nitrogen, 4810 g of mixed solvent (cyclohexane and n-hexane, with a weight ratio of 88:12), 225 g of styrene, and the additive THF were sequentially added to the kettle. 11.4g, the polymerization system was treated with high-purity N 2 After displacement and deoxidation, 624 g of 1,3-butadiene, 118 g of coagulation inhibitor 1-hexene, and 0.73 g of n-butyllithium were added, and then a copolymerization reaction was carried out. The polymerization initiation temperature is 50° C., and the reaction pressure is 0.1-0.3 MPa. When the polymerization temperature reaches 80° C., add 0.30 g of the second-step initiator n-butyllithium, and when the conversion rate reaches 100%, add 0.33 g of tin tetrachloride to the polymerization kettle to continue the coupling reaction. After the coupling reaction, 0.5 g of terminator isopropanol and 10 g of anti-...
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