Rare earth catalyst and method for polymerizing conjugated diene by using same
A technology of rare earth catalysts and conjugated olefins, which is applied in the field of rare earth catalysts and their use in the polymerization of conjugated olefins, which can solve the problems of increased energy consumption and high price, and achieve the effect of high orientation and high catalytic activity
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Embodiment 1
[0040] Catalyst preparation and polymerization were carried out under nitrogen protection.
[0041] At 70°C, in a mixed solvent of n-hexane and isohexane (the volume ratio of the two is 6 / 4), mix 0.44mmol neodymium isooctanoate and 1.8mmol triphenylphosphine for 30min; at 50°C, in n-hexane, Mix 3.5mmol triisobutylaluminum, 7.0mmol chloroform and 0.03mmol ethanol for 3h; then mix and react the two for 1.5h to prepare a homogeneous catalyst system.
[0042] Add toluene, isoprene (monomer concentration = 2.7 mol / L) and the above catalyst system into the polymerization reactor, start the polymerization reaction at -40°C, and react under adiabatic conditions for 25 hours. The molar ratio of catalyst component A to monomer is 3.2×10 -3 . Add an ethanol solution containing 1% anti-aging agent 2,6-di-tert-butyl-p-methylphenol to terminate the reaction, wash with water and dry in a vacuum oven at 45°C until constant weight. The cis-1,4 content of the polyisoprene product is 97.2%, a...
Embodiment 2
[0044] Catalyst preparation and polymerization were carried out under nitrogen protection.
[0045] At 40°C, using hexane and cyclohexane (volume ratio: 9 / 1) as solvent, 10.5mmol triisobutylaluminum, 0.5mmol diisobutylaluminum hydride, 3.5mmol trichloromethane, 0.01mmol ethanol, 1.8 mmol of triphenylphosphine was mixed and reacted for 1 hour, and then mixed with 0.44 mmol of neodymium isooctanoate for 2 hours to prepare a homogeneous catalyst system.
[0046] Polymerization method and condition, termination reaction and aftertreatment method are all the same as embodiment 1, but the molar ratio of catalyst component A and total monomer is 2.0 * 10 -3 , Start polymerization at 30°C, and react under adiabatic conditions for 19h. Polyisoprene yield was 40%, M w 2.2×10 5,M w / M n is 3.2, and the cis-1,4 content is 97.3%.
Embodiment 3
[0048] Catalyst preparation and polymerization were carried out under nitrogen protection.
[0049] At 48°C, using hexane as a solvent, mix and react 0.26mol neodymium octanoate and 1.0mol triphenylphosphine for 18 hours, and mix and react 4.2mol triisobutylaluminum, 6.6mol trichloromethane and 0.11mol ethanol for 0.8h; They were mixed and reacted for 1.2h to prepare a homogeneous catalyst system.
[0050] Polymerization method and condition, termination reaction and aftertreatment method are all the same as embodiment 1, but the molar ratio of catalyst component A and total monomer is 2.5 * 10 -3 , Start polymerization at 0°C, and react under adiabatic conditions for 24h. Polyisoprene yield was 92%, M w 2.6×10 5 ,M w / M n is 2.5, and the cis-1,4 content is 97.0%.
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