Catalyst components and catalysts for olefin polymerization and their use and olefin polymerization process
A technology for olefin polymerization and catalysts, which is applied in the field of olefin polymerization catalysts and olefin polymerization, and can solve problems such as inability to prepare spherical carriers, poor stereospecificity, and carrier adhesion.
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preparation example 1
[0125] This preparation example is used to illustrate the spherical carrier of the olefin polymerization catalyst used in the present invention and the preparation method thereof.
[0126] In a 0.6L reactor, add 8.0g (0.08mol) magnesium chloride, 56mL (0.96mol) ethanol, 1g (0.03mol) α-sulfur, 1g PVP (polyvinylpyrrolidone) as a surfactant, and heat up to 90 ℃, after 2 hours of constant temperature reaction, add 38 mL (0.48 mol) of epichlorohydrin, continue the constant temperature reaction at 90 ℃ for half an hour, filter by pressure, wash the filter press product with hexane for 5 times, and finally vacuum dry the product to obtain olefin Polymerization catalyst spherical carrier Z1.
[0127] The olefin polymerization catalyst spherical carrier Z1 had an average particle diameter (D50) of 15 microns and a particle size distribution ((D90-D10) / D50) of 0.6. like figure 1 As shown, the olefin polymerization catalyst spherical carrier Z1 has a relatively regular particle morphol...
preparation example 2
[0131] This preparation example is used to illustrate the spherical carrier of the olefin polymerization catalyst used in the present invention and the preparation method thereof.
[0132] In the 0.6L reactor, add 300mL white oil, 8.0g (0.08mol) magnesium chloride, 28mL (0.48mol) ethanol, 0.3g (0.009mol) β-sulfur, 1g PVP (polyvinylpyrrolidone) as surfactant, The temperature was raised to 100 °C under stirring, and 12.5 mL (0.16 mol) of epichlorohydrin was added after the constant temperature reaction for 1 hour. After continuing the constant temperature reaction at 100 °C for 20 minutes, pressure filtration was performed, and the filter press product was washed with hexane for 5 times. Vacuum drying to obtain olefin polymerization catalyst spherical carrier Z2.
[0133] The olefin polymerization catalyst spherical carrier Z2 had an average particle diameter (D50) of 18 microns and a particle size distribution ((D90-D10) / D50) of 0.7. The particle morphology of the olefin polym...
preparation example 3
[0137] This preparation example is used to illustrate the spherical carrier of the olefin polymerization catalyst used in the present invention and the preparation method thereof.
[0138] In the 0.6L reactor, add 300mL white oil, 8.0g (0.08mol) magnesium chloride, 28mL (0.48mol) ethanol, 0.2g (0.006mol) α-sulfur, 1g PVP (polyvinylpyrrolidone) as surfactant, The temperature was raised to 100 °C under stirring, and 12.5 mL (0.16 mol) of epichlorohydrin was added after the constant temperature reaction for 1 hour. After continuing the constant temperature reaction at 100 °C for 20 minutes, pressure filtration was performed, and the filter press product was washed with hexane for 5 times. Vacuum drying to obtain olefin polymerization catalyst spherical carrier Z3.
[0139] The olefin polymerization catalyst spherical carrier Z3 had an average particle diameter (D50) of 20 microns and a particle size distribution ((D90-D10) / D50) of 0.8. The particle morphology of the olefin polym...
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