A kind of rare earth isoprene rubber catalyst process method
A rare earth isoprene rubber and process method technology, applied in the field of synthetic rubber, can solve the problems of unstable quality of isoprene rubber products, difficult control of the reaction temperature and pressure of the first reaction kettle, blockage of the rubber conveying pipeline, and the like, so as to omit the catalyst The effect of preparation steps, saving equipment investment and stable product quality
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Embodiment 1
[0043]Under the protection of nitrogen, 562g of hexane and 102g of isoprene were added to a 2L reactor. After stirring and mixing evenly, 1.9 mL (0.1467 mol / L) neodymium neodecanoate hexane solution and 2.6 mL (1.865 mol / L) isobutylaluminum hexane solution were added. After stirring for 20 minutes and preheating to 40°C, add 2mL (0.4096mol / L) diisobutylaluminum hexane solution to initiate the polymerization reaction. The polymerization reaction temperature is controlled between 40°C-50°C and the reaction pressure is 0.2Mpa. After 3.5 hours of reaction, ethanol was added to terminate the reaction, and the yield was 78%.
[0044] Product structure analysis: cis-1,4-polyisoprene content mass percentage is 96.3%, 3,4-polyisoprene content mass percentage is 3.7%; weight average molecular weight is 88×10 4 , the molecular weight distribution is 2.4, and the Mooney viscosity is 90.
Embodiment 2
[0046] Under the protection of nitrogen, 562g of hexane and 102g of isoprene were added to a 2L reactor. After stirring and mixing evenly, add 1.9mL (0.1467mol / L) neodymium neodecanoate hexane solution and 2.6mL (1.865mol / L) isobutylaluminum and diisobutylaluminum hydride 1:1 hexane solution. After stirring for 30 minutes and preheating to 40°C, add 2mL (0.4096mol / L) diisobutylaluminum hexane solution to initiate the polymerization reaction. The polymerization reaction temperature is controlled between 60°C and 70°C, and the reaction pressure is 0.2MPa. After 3 hours of reaction, ethanol was added to terminate the reaction, and the yield was 72%.
[0047] Product structure analysis: cis-1,4-polyisoprene content mass percentage is 96.1%, 3,4-polyisoprene content mass percentage is 3.9%; weight average molecular weight is 52×10 4 , molecular weight distribution is 2.6, Mooney viscosity is 60.
Embodiment 3
[0049] Under the protection of nitrogen, 562g of hexane and 102g of isoprene were added to a 2L reactor. After stirring and mixing evenly, add 1.9mL (0.1467mol / L) neodymium naphthenate hexane solution and 2.6mL (1.865mol / L) 1:1 hexane solution of isobutylaluminum and diisobutylaluminum hydride. After stirring for 10 minutes and preheating to 30°C, add 2mL (0.4096mol / L) diisobutylaluminum hexane solution to initiate the polymerization reaction. The polymerization reaction temperature is controlled between 60°C-70°C, and the reaction pressure is 0.. 15MPa. After 3 hours of reaction, ethanol was added to terminate the reaction, and the yield was 72%.
[0050] Product structure analysis: cis-1,4-polyisoprene content mass percentage is 96.6%, 3,4-polyisoprene content mass percentage is 3.4%; weight average molecular weight is 55×10 4 , the molecular weight distribution is 3.0, and the Mooney viscosity is 63.
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