Preparation method of ultrahigh molecular weight polyethylene composite material
A low-molecular-weight polyethylene and ultra-high-molecular-weight technology, which is applied in the field of preparation of ultra-high-molecular-weight polyethylene composite materials, can solve problems such as poor uniformity of blended products, decreased mechanical properties, difficult untangle and dispersion, and achieve compensatory performance The effect of reducing, improving processing performance, balancing processing performance and use performance
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Embodiment 1
[0026] The reactor used in this example is a slurry polymerization reactor.
[0027] The reaction device was purged with high-purity nitrogen to remove air and water in the reaction device. 100ml toluene, 10ml concentration is 3.5×10 -4 The mol / l catalyst (A) toluene solution of diimide palladium catalyst and 5 g of POSS molecules with hydroxyl group and acrylate isobutyl group were added to the device, stirred for 4 hours, and then sent into the reactor. Set the temperature of the reactor at 20°C, the pressure at 30 bar, feed ethylene, stop the reaction after 20 minutes of polymerization, take a sample and analyze the resulting polyethylene with a branching degree of 340 / 1000C, a molecular weight of 10,234, a molecular weight distribution of 1.34, and POSS molecules at the end. Further add 100ml concentration to the reactor to be 3.5×10 -4 mol / l FI catalyst (titanium pyrrole imide catalyst) [3-t-Bu-2-O-C 6 h 3 CHdN(C 6 f 5 )] 2 TiCl 2 The toluene solution was stirred ...
Embodiment 2
[0029] The polymerization reactor was heated to 40°C and the pressure was 10 bar, and 5ml of trimethylaluminoxane (MAO), ethylene and 2ml of ethylene were added successively with a concentration of 3.5×10 -4 mol / l FI catalyst (titanium pyrrole imide catalyst) [3-t-Bu-2-O-C 6 h 3 CHdN(C 6 f 5 )] 2 TiCl 2 solution in toluene to start the polymerization reaction. After 30 minutes of polymerization, the reaction was stopped, and the obtained molecular weight was 4.255 million, the molecular weight distribution was 2.12, the product tensile strength was 55 g / d, and the melt viscosity was 45 g / d.
[0030] Others are as in Example 1.
Embodiment 3
[0032] The reaction device was purged with high-purity nitrogen to remove air and water in the reaction device. 100ml toluene, 10ml concentration is 3.5×10 -4 The mol / l catalyst (A) toluene solution of diimide palladium catalyst and 5 g of POSS molecules with hydroxyl group and acrylate isobutyl group were added to the device, stirred for 4 hours, and then sent into the reactor. Set the temperature of the reactor at 20°C, the pressure at 30 bar, feed ethylene, stop the reaction after 20 minutes of polymerization, take a sample and analyze the resulting polyethylene with a branching degree of 340 / 1000C, a molecular weight of 10,234, a molecular weight distribution of 1.34, and POSS molecules at the end. Further add 100ml concentration to the reactor to be 3.5×10 -4 mol / l catalyst TiCl 3 The toluene solution was stirred at 60°C for 4 hours, and the solvent was drained to obtain Catalyst B. The polymerization reactor was heated to 60°C and the pressure was 20 bar, and 5ml of t...
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