A kind of copolymerization method of ethylene and terminal alkenyl silane/siloxane
A technology of terminal alkenyl silane and siloxane, which is applied in the field of copolymerization of ethylene and terminal alkenyl silane/siloxane, can solve the problems of low polymerization activity, inability to carry out copolymerization reaction, high price and the like, and achieves high polymerization activity, Broad industrial application prospects and the effect of increasing the content
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[0026] According to a preferred embodiment of the present invention, the main catalyst is selected from at least one of the following complexes,
[0027] Complex 1: R 1 =R 3 =R 4 =R 6 = Me,R 2 =R 5 = H, X = Br;
[0028] Complex 2: R 1 =R 3 =R 4 =R 6 =Et,R 2 =R 5 = H, X = Br;
[0029] Complex 3: R 1 =R 3 =R 4 =R 6 =iPr,R 2 =R 5 = H, X = Br;
[0030] Complex 4: R 1 =R 2 =R 3 =R 4 =R 5 =R 6 =Me, X=Br;
[0031] Complex 5: R 1 =R 3 =R 4 =R 6 = Me,R 2 =R 5 =Br, X=Br;
[0032] Complex 6: R 1 =R 3 =R 4 =R 6 = Me,R 2 =R 5 = Et, X = Br;
[0033] Complex 7: R 1 =R 3 =R 4 =R 6 =Et,R 2 =R 5 =Me, X=Br;
[0034] Complex 8: R 1 =R 3 =R 4 =R 6 =Et,R 2 =R 5 =Br, X=Br;
[0035] Complex 9: R 1 =R 3 =R 4 =R 6 = F, R 2=R 5 = H, X = Br;
[0036] Complex 10: R 1 =R 3 =R 4 =R 6 = Cl, R 2 =R 5 = H, X = Br;
[0037] Complex 11: R 1 =R 3 =R 4 =R 6 =Br,R 2 =R 5 = H, X = Br;
[0038] Complex 12: R 1 =R 3 =R 4 =R 6 = Me,R 2 =R 5...
Embodiment 1
[0099] The 1L stainless steel polymerization kettle equipped with mechanical stirring was continuously dried at 130°C for 6hrs, vacuumized while hot and heated with N 2 gas replacement 3 times; add 11.9 mg (10 μmol) of complex 3, then vacuumize and replace with ethylene 3 times; inject 500 mL of toluene, then add 6.5 mL of methylalumoxane (MAO) (1.53 mol / L toluene solution ), make Al / Ni=1000, 5mL allyltrimethoxysilane (28.7mmol), at 70°C, keep 10atm ethylene pressure, and stir for 30min. Finally, it was neutralized with an ethanol solution acidified with 5 volume % hydrochloric acid to obtain a polymer. The polymerization activity and the performance parameters of the polymer are shown in Table 1.
Embodiment 2
[0101] The 1L stainless steel polymerization kettle equipped with mechanical stirring was continuously dried at 130°C for 6hrs, vacuumized while hot and heated with N 2 gas replacement 3 times; add 11.9 mg (10 μmol) of complex 3, then vacuumize and replace with ethylene 3 times; inject 500 mL of toluene, then add 6.5 mL of methylalumoxane (MAO) (1.53 mol / L toluene solution ), make Al / Ni=1000, 5mL allyltrimethoxysilane (28.7mmol), at 100°C, keep 10atm ethylene pressure, and stir for 30min. Finally, it was neutralized with an ethanol solution acidified with 5 volume % hydrochloric acid to obtain a polymer. The polymerization activity and the performance parameters of the polymer are shown in Table 1.
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