A kind of metallocene catalyst system and its method of catalyzing olefin polymerization
A metallocene catalyst and catalyst technology, applied in the field of olefin polymerization, can solve the problems of limited development and further application, high toxicity of toluene, low catalytic activity, etc., and achieve the effects of high molecular weight, reduced production cost, and high catalytic activity
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Embodiment 1
[0047] At 50°C, 10 wt% MMAO / heptane solution (component B) and 1,3-bis(2, 6-diisopropylphenyl)-iminoimidazoline-isooctanoic acid-cyclopentadienyl titanium chloride (component A) / hexane solution, wherein the moles of Al in component B and Ti in component A The ratio was 2000:1. After 30 minutes of polymerization, 5% ethanol solution of hydrochloric acid was added to terminate the reaction. The obtained copolymer was vacuum-dried at 40° C. to constant weight to obtain 3.7 g of binary copolymer. The catalyst activity is 1.5×10 6 g polymer mol -1 of Ti·h -1 , the weight average molecular weight of the copolymer (M w ) is 3.2×10 5 , molecular weight distribution index (M w / M n ) is 2.1; the ethylene content in the copolymer is 61wt%, and the propylene content is 39wt%.
Embodiment 2
[0049] At 50°C, add 10 wt% MMAO / heptane solution (component B) and component A and triisobutyl Aluminum (component C) is mixed for 1 minute and added to the polymerization system. The molar ratio of Al in component B to Ti in component A is 1000:1, and the molar ratio of Ti in component C to component A is 20: 1. The polymerization time was 30 minutes, and the termination process was the same as in Example 1 to obtain 2.8 g of binary copolymers. The catalytic activity is 1.1×10 6 gpolymer mol -1 of Ti·h -1 ; M of the copolymer w 3.8×10 5 ,M w / M n It is 2.0; the ethylene content in the copolymer is 66wt%, and the propylene content is 34wt%.
Embodiment 3
[0051] The polymerization process is as described in Example 2, except that the molar ratio of Al in component B to Ti in component A is 300:1, and the molar ratio of Ti in component C to component A is 100:1, 5.4 g of binary copolymer were obtained. The catalytic activity is 2.2×10 6 gpolymer mol -1 of Ti·h -1 . Copolymer M w 2.7×10 5 ,M w / M n It is 2.3; the ethylene content in the copolymer is 56wt%, and the propylene content is 44wt%.
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