Dual-function catalyst system for preparing branched polyethylene through ethylene in-situ copolymerization and application of system
A technology of bifunctional catalyst and copolymerization catalyst, applied in physical/chemical process catalyst, organic compound/hydride/coordination complex catalyst, bulk chemical production, etc., can solve the problem of poor matching between oligomerization catalyst and copolymerization catalyst , poor catalyst matching, low catalyst activity, etc., to achieve the effects of high polymerization activity, simple preparation method and low catalyst cost
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Embodiment 1
[0040] The main catalyst (A1) of the oligomerization catalyst and the main catalyst (B1) of the copolymerization catalyst are as follows respectively, and the co-catalyst is MMAO (modified methyl aluminoxane).
[0041]
[0042] The 100ml polymerization bottle was pumped and baked for 3 times, replaced twice with high-purity nitrogen, and replaced with ethylene gas for the last time. Under 1 atm ethylene atmosphere, add 30ml of solvent toluene, control the reaction temperature at 25°C, add 10mmol of MMAO while stirring, continue After stirring for 10 minutes, add 4 μmol A1 and 1 μmol B1 to start the in-situ polymerization reaction. After 10 minutes of reaction, stop the reaction with 5% hydrochloric acid. The product was washed with hydrochloric acid aqueous solution, water and ethanol respectively, dried in vacuum, and weighed to calculate the activity; the properties and structure of the product were characterized by high-temperature GPC and high-temperature carbon spectrum...
Embodiment 2
[0044] The main catalyst of the oligomerization catalyst and the main catalyst of the copolymerization catalyst are A1 and B1 respectively, and the cocatalyst is MAO (methyl aluminoxane); the molar ratio of A1 and B1 is 2:1, and the polymerization reaction steps are as in Example 1, and other reactions Conditions, polymerization activity and product characterization results are shown in Table 1.
Embodiment 3
[0046] The main catalyst of the oligomerization catalyst and the main catalyst of the copolymerization catalyst are respectively A1 and B1, and the cocatalyst is] Ph3C]+[B(C6F5)4]-; the molar ratio of the sum of the cocatalyst and the main catalyst is 500:1, and the solvent It is hexane, the polymerization reaction steps are as in Example 1, other reaction conditions, polymerization activity and product characterization results are shown in Table 1.
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