Supported single metallocene catalyst for ethylene polymerization
A single metallocene and ethylene polymerization technology is applied in the field of supported single metallocene catalysts for ethylene polymerization, can solve the problems of limited industrial application, low activity and high production cost, achieve high ethylene polymerization catalytic activity and simple preparation method , good particle shape
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Embodiment 1
[0051] (1) Preparation of chlorinated hydrocarbyl silicon / magnesium chloride support
[0052] Under the protection of nitrogen, take 5.62 grams of magnesium chloride carrier and add 100 ml of dried hexane to disperse into a suspension, add 1 ml of SiCl 2 (n-Bu) 2 , start stirring, heat up to 30° C., react for 4 hours, and dry in vacuum to obtain a solid powder with good fluidity.
[0053] (2) Preparation of alkyl aluminoxane / chlorinated hydrocarbyl silicon / magnesium chloride support
[0054] Under nitrogen protection, take 5.0 grams of the modified magnesium chloride carrier obtained above and add it to a glass reactor, add 60 milliliters of dried toluene, disperse into a suspension, and add 18 milliliters of 10 wt% MAO (methylaluminoxane) toluene solution , heated to 50 ° C, stirred for 4 hours, then washed three times with 50 ml × 3 toluene, then washed with hexane, and dried in vacuum to obtain a solid powder with good fluidity, that is, a magnesium chloride carrier conta...
Embodiment 2
[0063] (1) Preparation of chlorinated hydrocarbyl silicon / magnesium chloride support
[0064] With embodiment 1 step (1), only SiCl in embodiment 1 2 (n-Bu) 2 Change to SiCl 4 .
[0065] (2) Preparation of alkyl aluminoxane / chlorinated hydrocarbyl silicon / magnesium chloride support
[0066] Same as step (2) of Example 1.
[0067] (3) Preparation of supported metallocene catalyst B
[0068] Same as step (3) of Example 1 to obtain supported metallocene catalyst B. Characterized by ICP, in catalyst B, the weight content of Ti is 0.31%, and the weight content of Al is 11.30%.
Embodiment 3
[0070] (1) Preparation of chlorinated hydrocarbyl silicon / magnesium chloride support
[0071] With embodiment 1 step (1), only SiCl in embodiment 1 2 (n-Bu) 2 Change to CH 3 SiCl 3 .
[0072] (2) Preparation of alkyl aluminoxane / chlorinated hydrocarbyl silicon / magnesium chloride support
[0073] Same as step (2) of Example 1.
[0074] (3) Preparation of supported metallocene catalyst C
[0075] Same as step (3) of Example 1 to obtain supported metallocene catalyst C. Characterized by ICP, the weight content of Ti in catalyst C is 0.30%, and the weight content of Al is 11.18%.
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