Rare-earth catalyst and conjugated diene polymerization process
A rare earth catalyst and catalyst technology, which is applied in the field of polymerization of conjugated dienes, can solve the problems of reduced molecular weight and failure to meet the molecular weight requirements, and achieve the effects of small temperature fluctuations, easy control of the reaction, and stable catalytic performance
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Embodiment 1
[0023] at 50°C and N 2 Under protection, neodymium octanoate (0.05mmol), triisobutylaluminum (Al(i-Bu) 3 ) (0.78mmol), chloroform (1.7mmol), dichlorobutane (0.05mmol) and styrene (0.049mmol) were added to the dry catalyst preparation bottle, mixed evenly, and after aging for 26h, a light green transparent homogeneous catalyst solution.
[0024] in N 2 Under protection, add 30ml of butadiene / cyclohexane solution (wherein the monomer mass concentration is 12%) and the above-mentioned catalyst solution (catalyst / monomer=1.0mmol / mol) to start polymerization in the polymerization reactor at 10°C After reacting for 4 hours, an ethanol solution containing 0.1% by mass of 2,6-di-tert-butyl-p-cresol and hydrochloric acid was added to terminate the polymerization. After removing the solvent and unreacted monomers, the polymer product was obtained after repeated washing with ethanol / water and drying to constant weight. The weight average molecular weight of the product is 1.05×10 6 ...
Embodiment 2
[0026] at 50°C and N 2 Under protection, neodymium octanoate (0.09mmol), triisobutylaluminum Al(i-Bu) 3 (1.44mmol), chloroform (3.15mmol) and ethyl dichloroacetate (0.002mmol) were added to a dry catalyst preparation bottle, mixed uniformly, and after aging for 2h, a light gray blue transparent homogeneous catalyst solution was obtained.
[0027] in N 2 Under protection, add 40ml of butadiene and cyclohexane / raffinate (i.e. C 6 ~C 8 alkane mixed solution) (wherein the monomer mass concentration is 20%, cyclohexane / raffinate=1 / 1) and the above-mentioned catalyst solution (catalyst / monomer=0.9mmol / mol) start polymerization, after adiabatic reaction 4h, An ethanol solution containing 0.1% by mass of 2,6-di-tert-butyl-p-cresol and hydrochloric acid was added to terminate the polymerization. After removing the solvent and unreacted monomers, the polymer product was obtained after repeated washing with ethanol / water and drying to constant weight. The monomer conversion rate is 10...
Embodiment 3
[0029] at 40°C and N 2 Under protection, add neodymium octoate (0.08mmol), triisobutylaluminum (1.2mmol), trichloroethane (0.38mmol) into the dry catalyst preparation bottle, mix uniformly and age for 1.5h, a light gray blue color is obtained Transparent homogeneous catalyst solution.
[0030] in N 2 Under protection, add 30ml of butadiene and cyclohexane / raffin oil solution (wherein the monomer mass concentration is 20%, cyclohexane / raffin oil=1 / 1) and The above catalyst solution (catalyst / monomer = 1.0 mmol / mol) started the polymerization, and after 3.7 hours of reaction, an ethanol solution containing 0.1% by mass of 2,6-di-tert-butyl-p-cresol and hydrochloric acid was added to terminate the polymerization. After removing the solvent and unreacted monomers, the polymer product was obtained after repeated washing with ethanol / water and drying to constant weight. The weight average molecular weight of the product is 3.36×10 5 . The cis-1,4 structure content in polybutadi...
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