Catalytic system for preparing cycloolefine copolymer
A technology of cycloolefin copolymers and catalytic systems, applied in the field of catalytic systems, can solve the problems of limiting the heat resistance of cycloolefin copolymers, affecting the effective utilization rate of cycloolefin monomers, and the low insertion rate of cycloolefin monomers, etc., to achieve effective Effect of increased utilization rate, improved insertion rate, and improved heat resistance
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Embodiment 1
[0033] Dissolve 3.6 g of refined norbornene in 50 ml of refined toluene to form solution I. Solution I was added to a 100 ml Schlenk tube reactor previously flushed with nitrogen, and ethylene was pumped (1 atm) several times to saturate the solution with ethylene. Then 2 ml of a toluene solution of methylaluminoxane with a concentration of 1.72 mol / liter and 1.3 mg of isopropyl-(fluorenyl)-(cyclopentadienyl)zirconium dichloride were added successively. Polymerization was carried out at 50° C. and stirring at 250 r / min for 1 hour; during the polymerization process, ethylene was supplemented and metered, and the pressure was controlled at 1 atmosphere. After the reaction, the reaction solution was poured into ethanol for precipitation and filtered, and the filter cake was washed with ethanol and dried. The catalyst activity was 1.2×10 6 g / (mole zirconium·hour). The physical properties of the polymers are listed in Table 1.
Embodiment 2
[0035] Polymer is prepared by the method of embodiment 1, and the addition of refined norbornene is reduced to 0.7 gram by 3.6 gram, and catalyst activity 1.5 * 10 6 g / (mole zirconium·hour). The physical properties of the polymers are listed in Table 1.
Embodiment 3
[0037] The polymer is prepared by the method of Example 1, and the addition of refined norbornene rises to 5.4 grams from 3.6 grams, and the catalyst activity is 1.0×10 6 g / (mole zirconium·hour). The physical properties of the polymers are listed in Table 1.
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