Preparation method of polyisobutene with low molecular weight and high activity
A technology of polyisobutylene and high activity, which is applied in the field of preparation of low-molecular-weight and high-activity polyisobutylene, can solve the problems of difficult control of polyisobutylene molecular weight, reduced selectivity of polymerization reaction, uneven concentration diffusion, etc., and achieves good product quality stability, High conversion rate, easy control of activity and stable effect
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Embodiment 1
[0023] Embodiment 1, the polymerized monomer adopts the concentrated mixed C4 from the catalytic cracking of the refinery, the isobutylene content is 90%, and the diene content is less than 0.05%, and the mixed C4 is continuously added at a speed of 500L / h by a 40L polymerization reactor with stirring , the speed of the stirrer is 150-200r / min; the catalyst A is continuously added at the speed of 150ml / h at the entrance of the polymerization reactor, and the catalyst B is continuously added at the speed of 100ml / h at the other entrance of the polymerization reactor, and then at -20 The polymerization reaction is carried out at ~30°C and 0.6~1.5Mpa for 15~18 minutes. Catalyst A is boron trifluoride isopropanol complex, the molar ratio of boron trifluoride to isopropanol is 0.5:1, and catalyst B is both boron trifluoride isopropanol complex, boron trifluoride and isopropanol Propanol molar ratio is 0.1:1.
[0024] The polymer material is continuously extracted from the outlet o...
Embodiment 2
[0025] Embodiment 2, the same polymerization device as in Example 1, the catalyst adopts a single catalyst A, which is added by the import of the polymerization device, the addition is constant, the polymerization conditions and the polymer post-treatment method are constant, and the raw material adopts the enrichment from the catalytic cracking of the refinery Mixed C4, isobutene content 90%, diene content ≤ 0.05%. The number-average molecular weight of the product obtained in the embodiment is 1200-1350, the molecular weight distribution is ≤2.0, the average conversion rate is 80%, and the α-terminal double bond content is 60%.
Embodiment 3
[0026] Embodiment 3, the same as the polymerization device of embodiment 1, add A+B mixed catalyst continuously at the speed of 250ml / h at the entrance of the polymerization reactor, the polymerization conditions and the post-treatment mode of the polymer are unchanged, and the raw material adopts catalytic cracking from the refinery Concentrated mixed C4, isobutene content 78%, diene content ≤ 0.05%. The number average molecular weight of the product obtained in the embodiment is 1250-1350, the molecular weight distribution is ≤2.0, the average conversion rate is 80%, and the α-terminal double bond content is 70%.
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