A kind of loading method of metallocene catalyst
A metallocene catalyst and negative pressure technology, applied in the field of metallocene catalyst loading, can solve the problems of long loading time and low loading rate, and achieve the effects of improving polymer morphology, shortening preparation time, and being simple and easy to implement.
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Embodiment 1
[0017] 1) Take 6.0g of dried and processed specific surface is 305m 2 / g, the pore volume is 1.65cm 3 / g, with an average particle size of 45.3 μm, the silica gel carrier was put into a sealed reaction flask, and the interior of the reaction flask was replaced with nitrogen three times; vacuum was continuously evacuated for 15 minutes under (-0.085) MPa; 50ml12 was added to the flask by starting stirring % of the toluene solution of methylaluminoxane, keep the pressure (-0.065) MPa, and react at 20°C for 0.5 hours;
[0018] 2) Put 16ml of 12% methylaluminoxane toluene solution into another replaced flask, add 0.56g of diindenyl zirconium dichloride, start stirring to dissolve all the diindenyl zirconium dichloride;
[0019] 3) Add the dissolved bisindenyl zirconium dichloride / methylaluminoxane toluene solution into the silica gel, flush with nitrogen to keep the reaction flask under normal pressure, and react at 20°C for 0.5 hours;
[0020] 4) Wash with toluene for 3 times, ...
Embodiment 2
[0028] The reaction conditions are the same as in Example 1, except that 0.56 g of diindenyl zirconium dichloride is replaced by 0.76 g of (indenyl)(cyclopentadienyl) zirconium dichloride.
Embodiment 3
[0030] Reaction condition is the same as embodiment 1, and difference is only to replace 0.56g diindenyl zirconium dichloride with 0.76g two (butyl) (cyclopentadienyl) zirconium dichlorides, the reaction of the first step and the third step The temperature was lowered from 20°C to 5°C.
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